DOC. APPENDIX 11F Emergency Response Plan

APPENDIX 11F Emergency Response Plan PDX/072550008.DOC Emergency Response Manual DRAFT (February 4, 2008) EMERGENCY RESPONSE MANUAL Table of C...
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APPENDIX 11F

Emergency Response Plan

PDX/072550008.DOC

Emergency Response Manual

DRAFT (February 4, 2008)

EMERGENCY RESPONSE MANUAL

Table of Contents Section

Page

INTRODUCTION ............................................................................................................. 1 1

2

ORGANIZATION AND CONTACTS.................................................................... 3 1.1

Normal Operating Organization ............................................................................... 3

1.2

Emergency Organization ........................................................................................... 3

1.3

Emergency Organization Team Responsibilities and Functions ........................... 4 1.3.1 Terminal Emergency Director .................................................................... 4 1.3.2 Public Information Contact......................................................................... 5 1.3.3 Emergency Response Team Leader............................................................ 6 1.3.4 Emergency Response Team........................................................................ 6 1.3.5 Security Shift Supervisor ............................................................................ 7 1.3.6 Security Force ............................................................................................. 7 1.3.7 Assembly Leaders....................................................................................... 8

1.4

Off-Site Emergency Organizations ........................................................................... 8 1.4.1 Coordination with Off-Site Organizations.................................................. 8 1.4.2 State and Local Emergency Organizations ................................................. 8

1.5

Contact Details .......................................................................................................... 11 1.5.1 Terminal Personnel Contact Details ......................................................... 11 1.5.2 Off-Site Emergency Organizations Contact Details ................................. 11 1.5.3 Other Off-Site Agency Contact Details .................................................... 12

RESPONSES TO EMERGENCIES WITHIN THE TERMINAL .................... 13 2.1

Emergency Classification......................................................................................... 13

2.2

Emergency Classification Determination ............................................................... 14 2.2.1 Controllable Emergency ........................................................................... 14 2.2.2 Uncontrollable Emergency ....................................................................... 14 2.2.3 Emergency Classification Summary......................................................... 16

2.3

Terminal Alarm System, Hazard Detection and Mitigation System and Shutdown System...................................................................................................... 16 2.3.1 Terminal Alarm System............................................................................ 16

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EMERGENCY RESPONSE MANUAL

Table of Contents Section

Page 2.3.2 2.3.3 2.3.4

3

Terminal Hazard Detection Systems ........................................................ 16 Terminal Shutdown Systems .................................................................... 17 Terminal Hazard Fire Control Equipment ................................................ 20

2.4

Communication Systems and Procedures .............................................................. 20 2.4.1 Communication Systems .......................................................................... 20 2.4.2 External Notifications ............................................................................... 21 2.4.3 Incident Reporting Requirements ............................................................. 22

2.5

Emergency Response Procedures............................................................................ 24

2.6

Emergency Response Procedures for LNG Carriers Berthed at the Terminal.. 25

2.7

On-Site Evacuation Procedures............................................................................... 25 2.7.1 Limited Area Evacuation Procedures ....................................................... 25 2.7.2 Total Terminal Evacuation Procedures..................................................... 26 2.7.3 Missing Personnel..................................................................................... 26 2.7.4 Emergency Evacuation Procedures for Visitors ....................................... 26 2.7.5 Emergency Evacuation Procedures for Contractors ................................. 27 2.7.6 Re-entry Into Previously Evacuated Areas ............................................... 27

EMERGENCY EVACUATION ADJACENT TO THE TERMINAL AND ALONG LNG CARRIER TRANSIT ROUTES .................................................. 28 3.1

Emergency Classification......................................................................................... 28 3.1.1 Controllable Emergency ........................................................................... 28 3.1.2 Uncontrollable Emergency ....................................................................... 29

3.2

Notifications .............................................................................................................. 29 3.2.1 Emergency Organization Notifications..................................................... 29 3.2.2 Federal Agency Notifications ................................................................... 30 3.2.3 Columbia River Pilots Notifications......................................................... 30 3.2.4 Residents and Recreational User Notifications......................................... 31 3.2.5 Contact Details.......................................................................................... 31

3.3

Emergency Procedures............................................................................................. 32 3.3.1 LNG Carriers in Transit ............................................................................ 32

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Table of Contents Section

Page 3.3.2 3.3.3

3.4

4

5

6

Evacuation of Areas Adjacent to the Terminal and LNG Carrier Transit Route ......................................................................................................... 33 Evacuation Zones, Routes and Methods of Egress................................... 33

Distribution of Public Information ......................................................................... 33

TRAINING AND DRILLS..................................................................................... 35 4.1

Emergency Response Plan Review.......................................................................... 35

4.2

Training Requirements ............................................................................................ 35 4.2.1 Emergency Response Plan Training. ........................................................ 35 4.2.2 Medical Training....................................................................................... 35 4.2.3 Fire Fighting Training............................................................................... 36 4.2.4 Local Fire Department .............................................................................. 36

4.3

Periodic Drills ........................................................................................................... 36

DOCUMENTATION OF REQUIRED CONSULTATION ............................... 37 5.1

Agencies and Emergency Organizations ................................................................ 37

5.2

Coordination Meetings............................................................................................. 37

COST SHARING PLAN ........................................................................................ 39 6.1

Direct Reimbursement ............................................................................................. 39

6.2

Capital Costs ............................................................................................................. 39

6.3

Annual Costs ............................................................................................................. 39

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EMERGENCY RESPONSE MANUAL Table of Appendices Page

Section Appendix A Oregon LNG Terminal Operations Maintenance Team Organization Chart Appendix B Terminal Hazard Detection Systems Plot Plans Appendix C Terminal Fire Control Equipment Matrix Appendix D Terminal Fire Control Equipment Plot Plans Appendix E Regulatory Agency Emergency Reporting Requirements Appendix F Emergency Response Procedures Appendix G Off-Site Emergency Evacuation Procedures Appendix H Off-Site Emergency Evacuation Zones, Routes and Maps Appendix I Documentation of Required Consultation Appendix J Cost Sharing Plan – Letter of Commitment

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EMERGENCY RESPONSE MANUAL

INTRODUCTION The Oregon LNG Import Terminal will be located on the East Skipanon Peninsula near the confluence of the Skipanon and the Columbia Rivers in Warrenton, Clatsop County, Oregon. The Terminal will be designed with a base-load natural gas sendout capacity of 1.0 billion standard cubic feet per day (“Bscfd”) and a peak of up to 1.5 Bscfd. The Project will receive LNG discharged from oceangoing LNG carriers, which will be stored in three (3) 160,000 cubic meter (“m3”) aboveground, full containment LNG storage tanks. LNG will be vaporized into natural gas, and sent out from the terminal via an approximately 121mile sendout pipeline. LNG carriers ranging in capacity from 70,000 m3 and 266,000 m3 will arrive at the Oregon LNG Project via marine transit through the Skipanon Channel In accordance with the requirements of the Draft Guidance for LNG Terminal Operator’s Emergency Response Plan issued by the FERC in September 2006, this Emergency Response Plan (ERP) has been prepared to establish the procedures for responding to specific emergencies that may occur at the Terminal as well as procedures for emergency situations that could affect the public along LNG carrier transit routes. Since emergency situations may require the involvement of federal, state and other local emergency organizations and agencies, this ERP has been prepared following consultation with appropriate agencies, including: •

Federal Energy Regulatory Commission;



United States Coast Guard;



Office of Homeland Security, Emergency Preparedness;



State Fire Marshal;



Columbia River Pilots;



Oregon State Police;



Local Sheriff Office;



Local Fire Department; and



Local Ambulance and Hospitals

The ERP defines the Oregon LNG Import Terminal Emergency Response Team, and also the actions that will be taken by the Emergency Response Team during an emergency situation. The ERP includes protocols to ensure close coordination with local area emergency response organizations, agencies and also with existing state and local Emergency Preparedness Plans. The ERP also addresses the reporting requirements compliant with the relevant provisions of local, state, and federal laws and regulations.

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EMERGENCY RESPONSE MANUAL An integral part of the ERP is a cost sharing plan that describe the mechanisms for funding all project specific costs that the Oregon LNG Import Terminal may impose on state and local agencies for security, safety/emergency management and emergency response if an emergency situation required the assistance of such organizations. The ERP establishes a base on which further plans, procedures, guidelines, arrangements, and agreements can be elaborated.

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EMERGENCY RESPONSE MANUAL

1 ORGANIZATION AND CONTACTS 1.1

Normal Operating Organization The Normal Operating Organization of the Oregon LNG Import Terminal consists of: •

Operations Personnel;



Maintenance Personnel;



Security Personnel;



Management and support personnel (normal working hours only); and



Contractor personnel (normal working hours only).

A copy of the Oregon LNG Import Terminal Organization Chart is included in Appendix A. During normal working hours, the Terminal Management Personnel will initiate the Emergency Response Plan. During off-normal working hours, Operations Personnel will initiate the Emergency Response Plan. 1.2

Emergency Organization When the Emergency Response Plan is put into effect, Terminal Personnel will assume designated positions, each with specific duties as depicted in the following chart.

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EMERGENCY RESPONSE MANUAL Figure 1.2 Emergency Organization

Terminal Emergency Director

Public Information Contact

Emergency Response Team Leader

Emergency Response Team

1.3

Security Shift Supervisor

Assembly Leaders

Security Force

Emergency Organization Team Responsibilities and Functions The positions and duties associated with each position depicted in figure 1.2 are as follows:

1.3.1 Terminal Emergency Director The Terminal Emergency Director is in command of the Terminal Emergency Organization. If the emergency occurs outside of normal business hours, the Shift Supervisor will assume the Terminal Emergency Director position until relieved by the Terminal Manager. The role of the Terminal Emergency Director involves interacting with both on-site groups (Terminal employees dealing with the emergency) as well as off-site groups (media and off-site emergency organizations). If the emergency continues for an extended period, then the Terminal Emergency Director position may be filled using different individuals. The Terminal Emergency Director is normally based in the Emergency Control Center, which will be located in the Administration Building. The specific duties of the Terminal Emergency Director position are: • Using information provided by the Emergency Response Team Leader, the

Terminal Emergency Director will assess the emergency and determine the appropriate Emergency Classification in accordance with Section 2.1 of this Emergency Response Plan.

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EMERGENCY RESPONSE MANUAL • Designate and direct the Terminal Public Information Contact or act as the

Terminal Public Information Contact until another individual is designated for that position. • Coordinate activities with off-site emergency organizations and, if acting as

the Public Information Contact request off-site assistance as required in accordance with Section 2.4.2.1 of this Emergency Response Plan. • Determine which resources are required and direct the call-in of additional

Terminal employees. • Direct on-site evacuation and provide recommendation for off-site evacuation,

as required and in accordance with the procedure described in Section 2.6 of this Emergency Response Plan. • Direct the Security Shift Supervisor. • Direct the Assembly Leaders. • Develop re-entry plans for any areas previously evacuated; and • Maintain the Terminal Emergency Control Center Status Board.

1.3.2 Public Information Contact In the event of an emergency at the Terminal, it is critical that information released to public agencies, the media, and ultimately the general public be accurate. During an emergency situation, the Terminal employees may be contacted by the media or by members of the general public regarding the emergency. In order to assure that accurate information rather than misinformation or speculation is disseminated, only the Public Information Contact is authorized to provide information to the media, local agencies or the public. Terminal employees will refer all persons with questions regarding the emergency to the Public Information Contact. Also, if Terminal employees are questioned about statements or speculations that arise, they will also refer the person to the Public Information Contact. The Public Information Contact is designated as the information point of contact by the Terminal Emergency Director and acts as the spokesperson for disseminating information to all media outlets and also local and state emergency organizations. The Public Information Contact, if not the Terminal Emergency Director, reports to the Terminal Emergency Director. The specific duties of the Public Information Contact include: • Contact off-site emergency organizations to request emergency support as

directed by the Terminal Emergency Director during an emergency condition • Provide off-site emergency organizations with the status of the emergency;

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EMERGENCY RESPONSE MANUAL • During General Emergencies, provide a liaison person to local emergency

organizations. The liaison will report to the Public Information Contact; and • Designate a media area, prepare news releases and disseminate information

to the media following established protocols. 1.3.3 Emergency Response Team Leader The Emergency Response Team Leader will be the on-duty Shift Supervisor or Lead Operator. The Emergency Response Team Leader will command the on-site Emergency Response Team and will report to the Terminal Emergency Director. Generally, the Emergency Response Team Leader is involved with directing the Operations Team and also the off-site emergency organizations while they are performing emergency actions at the Terminal. The specific duties of the Emergency Response Team Leader are: • Assess the emergency situation and assume the role of Terminal Emergency

Director until relieved by the Terminal Manager; • Identify the actual and potential hazards that the emergency situation will, or

may affect the Terminal, its personnel and / or areas adjacent to the Terminal; • Direct Emergency Response Team members; • Identify specific off-site resources that may be needed for the emergency; and • Provide the Terminal Emergency Director with the current situation status.

1.3.4 Emergency Response Team The Emergency Response Team reports directly to the Emergency Response Team Leader. The Emergency Response Team's responsibilities include the direct actions to bring the Terminal to a safe status. The Emergency Response Team consists of: • Operations Personnel; • Maintenance Personnel; • Selected contractor personnel as requested by the Emergency Response

Team Leader; and • Selected off-site emergency personnel requested by Emergency Response

Team Leader. The specific tasks that the Emergency Response Team is responsible for include: • LNG and flammable gas release control. This role will primarily involve the

Terminal Operations and Maintenance Personnel, who will implement those

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EMERGENCY RESPONSE MANUAL immediate actions required to terminate the release and mitigate the consequences of the incident; • Emergency recovery and restoration.

This role will primarily involve the Terminal Operations and Maintenance Personnel. These personnel will implement those immediate actions required to bring the Terminal to a safe condition and mitigate the consequences of the incident;

• Fire fighting.

This role will primarily involve off-site fire fighting personnel. The Terminal employees are also trained to fight fires;

• Re-entry into areas that were previously evacuated.

Re-entry will only be approved by the Terminal Emergency Director. Re-entry will primarily involve the Terminal Operations and Maintenance Personnel to search for unaccounted personnel, rescue trapped or injured personnel, perform maintenance or operations activities to terminate or mitigate the emergency, determine safe areas as well as personnel exclusion areas and determine the nature or extent of the emergency;

• Medical Aid.

This role will involve the Terminal employees, including the Safety and Health Coordinator, and off-site rescue squads as needed. The Terminal employees will perform this function until off-site rescue squad personnel arrive. As off-site rescue squad personnel arrive, Medical Aid activities will be taken over by rescue squad personnel to free the Terminal employees for Terminal recovery activities. The Medical Aid activities include transporting injured persons to a safe location, administering first aid, determining if transport off-site is needed and notifying hospital(s) of incoming injured, transport injured personnel to appropriate medical facilities, and maintaining accurate records of all first aid treatment; and

• Escort. Escort off-site emergency personnel as required.

1.3.5 Security Shift Supervisor The Security Shift Supervisor supervises the Security Force and reports directly to the Terminal Emergency Director. The Security Shift Supervisor is responsible for assuring the Security Force carries out their assigned duties. 1.3.6 Security Force The specific duties of Security Force Personnel are to: • Secure and maintain the Terminal perimeter; • Control access to the Terminal; • Ensure that Terminal access roads are clear for use by emergency vehicles

and essential personnel;

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EMERGENCY RESPONSE MANUAL • Coordinate and direct off-site emergency response teams to staging areas as

directed by the Emergency Response Team Leader; • Assist with on-site evacuations as directed by the Terminal Emergency

Director; • Assist with accountability activities; • Provide direct coordination with local law enforcement agencies; and • Identify the need for additional security requirements (i.e., local law

enforcement) to the Terminal Emergency Director. 1.3.7 Assembly Leaders The Assembly Leaders perform the accountability function as well as direct personnel safely to assembly areas. Assembly Leaders will assume their designated roles when a Terminal evacuation is ordered by the Terminal Emergency Director. Although the Assembly Leaders report to the Terminal Emergency Director, they will also communicate directly with the Emergency Response Team Leader. 1.4

Off-Site Emergency Organizations

1.4.1 Coordination with Off-Site Organizations Certain emergency actions will require emergency response from off-site emergency organizations. Effective emergency response planning and response is therefore dependent on close, ongoing coordination between the Terminal and those off-site emergency organizations. To assure effective coordination is maintained, there will be periodic meetings, drills and familiarization tours conducted for these organizations, ideally on at least an annual basis. In addition, the off-site emergency organizations will be encouraged to send new members to the Terminal for familiarization tours. 1.4.2 State and Local Emergency Organizations The development of this Emergency Response Plan has been coordinated with the United States Coast Guard (USCG) and the Office of Homeland Security, Emergency Preparedness (OHSEP) and will be compliant with the Oregon State Emergency Alert System Plan. A significant aspect of this Emergency Response Plan is the organization and staffing of state and local emergency response, including police, fire and other emergency response resources and personnel specific to the needs and action plans of the Oregon LNG Terminal. The following describes the key elements of

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EMERGENCY RESPONSE MANUAL emergency response planning that are to be identified and reviewed with the USCG, the Office of Homeland Security, Emergency Preparedness as well as other state and local resources. Section 6 of this Emergency Response Plan describes the Cost Sharing Plan that has been developed to fund project specific costs as well as safety and emergency management costs that may be imposed on state and local agencies and other organizations if an emergency situation were to exist that requires assistance from such state and local agencies or other organizations.

1.4.2.1

Office of Homeland Security, Emergency Preparedness (OHSEP) In response to a notification of an emergency situation from the Terminal Public Information Contact, the OHSEP will be responsible for implementing the Oregon State Emergency Alert System Plan.

1.4.2.2

United States Coast Guard In the event of an emergency, Oregon LNG has the primary responsibility of coordinating efforts in responding to and the mitigation of the emergency condition. The Captain of the Port or his designee will be contacted by the Terminal Manager assuring he is kept abreast of the emergency operations. He is authorized by the Ports and Waterways Safety Act of 1972 to direct emergency operations where the situation poses a threat to the port or nearby vessels. The Captain of the Port has the authority to assume coordination efforts when the situation is not being properly handled by the Oregon LNG Terminal. In response to a notification of an emergency situation from the Terminal Public Information Contact, the United States Coast Guard will be available to: • Control marine traffic in the vicinity of the Terminal; and • Assist with rescue or evacuation activities offshore.

1.4.2.3

State Fire Marshal's Office In response to a notification of an emergency situation from the Terminal Public Information Contact, the State Fire Marshal's Office may assist in: • Arson investigations; and • Bomb Threat response and disposition of bombs or suspected bombs. This will be

carried out in conjunction with the Oregon State Police and local Sheriffs Office as described in Section 1.4.2.5 of this Emergency Response Plan.

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EMERGENCY RESPONSE MANUAL 1.4.2.4

Columbia River Pilots The Columbia River Pilots will be notified of an emergency situation adjacent to the Terminal and / or along LNG carrier transit routes by the Pilot who has boarded the LNG carrier as it approaches the Terminal. The Pilot on board the Carrier will be notified of an emergency situation by the Terminal Public Information Contact and communication will be maintained via radio on VHF Channel TBD. The Pilot on board the LNG carrier will also notify the Terminal of any actual or potential emergency situation along the LNG carrier transit route. The Columbia River Pilots maintain communications with the USCG.

1.4.2.5

Oregon State Police and Local Sheriff's Office The Oregon State Police and Local Sheriff's Office are the local law enforcement agencies. In response to a notification of an emergency situation from the Terminal Public Information Contact, the Oregon State Police and Local Sheriff's Office will provide necessary law enforcement assistance if required, including: • Establishing an off-site command post in the vicinity of the Terminal during an

emergency; • Providing emergency communications; • Evacuating and excluding individuals from designated public and private areas; • Controlling vehicular and pedestrian traffic in to and out of designated areas; and • Bomb threat response and disposal of bombs or suspected bombs. This will be

carried out in conjunction with the State Fire Marshal’s Office as described in Section 1.4.2.3 of this Emergency Response Plan.

1.4.2.6

Local Fire Department The Local Fire Department will be the primary fire department and will provide the following emergency services: • Fire fighting; • First aid and medical assistance (including arranging ambulatory transportation); • Rescue; and • Assist with emergency communications.

Additionally, cooperative agreements allow the Local Fire Department to call other local fire departments if needed.

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EMERGENCY RESPONSE MANUAL 1.4.2.7

Local Ambulance and Local Hospitals Local hospitals are available to provide emergency room treatment for injured personnel.

1.5

Contact Details

1.5.1 Terminal Personnel Contact Details Figure 1.5.1 Terminal Personnel Contact Details Position / Group

Name

Telephone Number

Terminal Manager Operations Manager Health, Safety and Security Manager Environmental Manager Shift Supervisors Marine Safety Officer Security Supervisor Main Control Room Jetty Control Room

1.5.2

Off-Site Emergency Organizations Contact Details Figure 1.5.2 Off-Site Emergency Organization Contact Details Position / Group

Name

Telephone Number

Office of Homeland Security, Emergency Preparedness United States Coast Guard State Fire Marshal’s Office Oregon State Police Columbia River Pilots Local Law Enforcement Local Fire Department Ambulance Services Hospitals

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EMERGENCY RESPONSE MANUAL

1.5.3

Other Off-Site Agency Contact Details Figure 1.5.3 Other Off-Site Agency Contact Details Position / Group

Name

Telephone Number

Federal Energy Regulatory Commission DOT Office of Pipeline Safety (RSPA)

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EMERGENCY RESPONSE MANUAL

2 RESPONSES TO EMERGENCIES WITHIN THE TERMINAL 2.1

Emergency Classification Emergencies are categorized based on two distinct criteria: Can the Terminal Operations Personnel prevent harm to personnel or property by taking reasonable and prudent actions? This criterion determines whether the emergency is a Controllable Emergency or Uncontrollable Emergency; and If the emergency is an Uncontrollable Emergency, are, or can personnel or property off-site be affected? This criterion determines whether the emergency is a Terminal Site Emergency or a General Emergency. The categorization process is illustrated in Figure 2.1 below. Figure 2.1 Emergency Classification

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EMERGENCY RESPONSE MANUAL 2.2 2.2.1

Emergency Classification Determination Controllable Emergency This is an emergency in which the Terminal Operations Personnel can prevent harm to personnel or equipment by taking reasonable and prudent actions such as valve manipulations, shutting down equipment, or initiating the Emergency Shutdown System. Examples of Controllable Emergencies that may occur at the Terminal include: • LNG spills that are contained within the LNG spill containment system and

do not result in fire; • LNG spills that are contained within the LNG spill containment system and

result in a fire within the containment system; • Overpressure of gas or liquid process piping; • Collapse of buildings or systems and equipment that does not result in or

does not have the potential to result in the loss of containment of LNG or flammable gases; • Building fires that do not involve flammable gases; • Electrical fires that do not involve flammable gases; • Loss of electrical power; • Emergency LNG carrier departure – unexpected LNG carrier disconnect; • Vehicle accidents; • Severe weather conditions; and • Breaches of site security that do not result in or have the potential to result

in substantial damage to the Terminal. 2.2.2

Uncontrollable Emergency This is an emergency in which the Terminal Operations Personnel cannot prevent harm to personnel or equipment by taking reasonable and prudent actions such as valve manipulations, shutting down equipment, or initiating the Emergency Shutdown System. An Uncontrollable Emergency involves situations that have the potential to result in exposure of personnel or property to natural gas in a liquid, cold vapor, or gaseous state or may result in fire or explosion. Examples of Uncontrollable Emergencies that may occur at the Terminal include: • LNG spills that are not contained by the LNG spill containment system and

do not result in fire;

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EMERGENCY RESPONSE MANUAL • LNG spills that are not contained by the LNG spill containment system and

result in an unconfined fire; • Flammable gas leaks from significant failure of a pipeline or equipment; • Building or equipment fires that contain or have the potential to contain

flammable gases • Structural failure of an LNG storage tank; • Major fire aboard an LNG Carrier; • Bomb threats; and • Severe weather conditions that cause wide-scale damage to equipment

and systems that result in or have the potential to result in a loss of containment of LNG or flammable gases. In addition, a Security Breach that results in a high probability of substantial damage to the Terminal that may create an Uncontrollable Emergency will be considered an Uncontrollable Emergency, even if no damage has yet occurred. Examples of this situation include: • Discovery of an explosive device in close proximity to an LNG tank or

major LNG pipeline or natural gas pipeline; and • An act of sabotage that may result in structural failure of an LNG storage

tank or rupture of an LNG tank or major LNG pipeline or natural gas pipeline. An Uncontrollable Emergency is then further classified as a Terminal Site Emergency or a General Emergency.

2.2.2.1

Uncontrollable Emergency – Terminal Site Emergency This is an Uncontrollable Emergency that threatens Terminal personnel or equipment with exposure to natural gas (liquid, cold vapor, or gaseous state) or involves a fire or explosion of a magnitude that involves a large portion of the Terminal. A Security Breach that results in a high probability of substantial damage to the Terminal is considered a Terminal Site Emergency. At the instruction of the Terminal Emergency Director, emergency help will be requested by the Public Information Contact from off-site emergency organizations during a Terminal Site Emergency

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EMERGENCY RESPONSE MANUAL 2.2.2.2

Uncontrollable Emergency – General Emergency This is an Uncontrollable Emergency that threatens the public with exposure to natural gas (liquid, cold vapor, or gaseous state) or involves a fire or explosion of a magnitude that affects persons or property off-site. At the instruction of the Terminal Emergency Director, emergency help will be requested by the Public Information Contact from off-site emergency organizations during a General Emergency. Additionally, the Terminal Emergency Director may recommend an evacuation of the local community in accordance with Section 3.3.2 of this Emergency Response Plan.

2.2.3

Emergency Classification Summary In summary, there are ultimately three types of emergencies: • Controllable Emergency; • Uncontrollable Emergency resulting in a Terminal Site Emergency; or • Uncontrollable Emergency resulting in a General Emergency.

2.3

Terminal Alarm System, Hazard Detection and Mitigation System and Shutdown System. The following describes the hazard detection and mitigation system that is installed at the Terminal and which will be used to alert to and mitigate the impact from the Controllable Emergency and Uncontrollable Emergency situations listed in Section 2.2.1 and Section 2.2.2 of this Emergency Response Plan.

2.3.1

Terminal Alarm System Information will be provided when detailed design is complete, and issued for construction.

2.3.2

Terminal Hazard Detection Systems A Hazard Detection and Mitigation System (HDMS) is installed at the Terminal to prevent the occurrence of physical situations that have the potential to result in injury to personnel and/or damage to property and the environment. The HDMS accomplishes this by detecting and alerting operating personnel to the presence of fire and flammable gas leak hazards. The hazard detection system consists of a combination of heat detectors, flame detectors, smoke detectors, high and low temperature detectors and flammable gas leak detectors.

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EMERGENCY RESPONSE MANUAL Fire and flammable gas detection and protection of offices and other buildings is via networked fire panels located in individual buildings and networked to the main fire alarm control panel, which is located in the Main Control Room. The fire panels provide common alarms and status information to the Hazard Detection and Mitigation System. Plot plans illustrating the location of the hazard detection equipment are included in Appendix B. 2.3.3

Terminal Shutdown Systems An Emergency Shut Down System (ESD) is installed at the Terminal to initiate closure of valves and the shutdown of process drivers during emergency situations. All other shutdowns that are not ESD are designated as process related trips. Each major part of the Terminal has an ESD circuit, which consists of instrumentation that is independent and separate from instrumentation that is used for normal operations. LNG Carriers that arrive at the Terminal have their own ESD system, which will be connected to the Terminal ESD system through an umbilical link, which will be established prior to unloading LNG. The natural gas sendout system is also connected to the ESD system so that upon activation, the natural gas sendout pipeline will be isolated from the Terminal and vice versa. The Hazard Detection and Mitigation System described in Section 2.3.2 of this Emergency Response Plan interfaces with the ESD system and will initiate the ESD system. Figure 2.3.3 illustrates the general arrangement of the ESD system installed at the Terminal.

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EMERGENCY RESPONSE MANUAL Figure 2.3.3 Emergency Shutdown System – General Arrangement

Appendix D includes drawings that illustrates the areas that will be affected upon the initiation of the ESD system. The ESD system has three elements: •

ESD-1:

Shutdown of unloading operations and isolation of the pier



ESD-1-1:

Activates the Emergency Release Couplings (ERC) on all of the arms.



ESD-2:

Shutdown of LNG/NG sendout operations including ESD-1.

2.3.3.1

ESD 1: Marine Isolation and Emergency Shutdown. Actuation of ESD-1 leads to suspension of unloading operations, isolation of loading arms and vapor return arm and isolation of Pier/Shore transfer line. The following actions are performed on activation of ESD 1 for the Pier/Off-shore area: •

ESD valves on unloading arms and vapor return arm are closed.



Process valves on the off-shore piping with ESD function are closed.

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EMERGENCY RESPONSE MANUAL •

LNG unloading pumps on the ship trip and ship’s manifold valves are closed (through ship/ shore umbilical signal).



Pier/shore ESD isolation valves are closed.

ESD-1 is manually actuated by: •

ESD push buttons located in the Platform Control Room and the Main Control Room.



ESD push buttons centrally located close to the LNG unloading arms and vapor return arm.



ESD push buttons are located at the Pier/Shore interface.



The ship’s Cargo Officer.

ESD-1 is automatically operated on the following: •

Actuation of the 1st stage over-reach alarm (apex or slew angle) on any of the unloading arms or vapor return arm.



Activation of cross-zoned fire or spill detectors.



Activation of a cross-zoned gas detector’s HH limit alarm.

ESD-1 leads to complete shutdown of the platform unloading operation and isolation of process lines to/from the pier 2.3.3.2

ESD-1-1: Unloading Arm Breakaway Actuation of ESD-1-1 leads to the following actions: •

Activation of the Emergency Release Couplings (ERC) on all of the arms.



Activation of ESD-1.

ESD-1-1 is manually actuated through: •

ESD push buttons located (TBD during design).

ESD-1-1 is automatically operated on the following: •

2.3.3.3

2nd stage overreach of apex or slew angle alarm on any of the loading arms or vapor return arm. ESD 2: Balance of Terminal.

ESD-2 shuts down the operations on the process systems (LNG and NG) so as to minimize potential release of hydrocarbon in an emergency. Activation of ESD-2 automatically initiates ESD-1. Actuation of ESD-2 leads to the following actions: •

LP Pumps trip.

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EMERGENCY RESPONSE MANUAL •

The inlet and outlet valves to the LNG Tank close.



HP Pumps trip.



Vapor Return Blowers and BOG Compressors trip.



Valves on LNG inlet and outlet to the Condenser/HP Drum area close.



Valves on LNG inlet to vaporizers close.

ESD-2 action is initiated manually by activation of any single push button at the following locations:

2.3.4



Near the HP Pumps.



Near the Condenser.



Near the Compressor Building.



Near the Vaporizers.



Main Control Room.



On the pier and at other locations determined during review of the Fire Safety System.

Terminal Hazard Fire Control Equipment Matrices of fire protection equipment illustrating the type of equipment, tag number, location, system size and discharge conditions, and activation method are included in Appendix C. Drawings illustrating the location and arrangement of fire control equipment are included in Appendix D.

2.4

Communication Systems and Procedures

2.4.1

Communication Systems The following describes the on-site and off-site communications systems that will be used in response to the Controllable Emergency and Uncontrollable Emergency situations listed in Section 2.2.1 and Section 2.2.2 of this Emergency Response Plan.

2.4.1.1

On-Site Communications Shall be handled through the use of plant systems; Intrinsically safe plant radio’s, PA Speaker System, or telephone. Off-Site Communications Shall be provided through activation of the Emergency 911 systems.

February 4, 2008 20

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EMERGENCY RESPONSE MANUAL 2.4.2

External Notifications This section describes the notifications that will be made by the Public Information Contact following instruction from the Terminal Emergency Director during an emergency as well as notifications that must be made following an incident to satisfy regulatory requirements.

2.4.2.1

Emergency Notifications Emergency notifications are made by the Public Information Contact at the instruction of the Terminal Emergency Director to request off-site assistance as well as provide off-site organizations with the information needed to perform their emergency actions. Responses to specific emergency situations will require specific emergency notifications and are included in the procedures for responding to the emergencies situations described in Section 2.5 of this Emergency Response Plan. However, the following is a summary of the notifications that will be made in response to classifications of emergency situations. Controllable Emergency In a controllable emergency event that may be perceived by the public as a potential risk the Emergency 911 system will be activated for notification purposes only. Uncontrollable Emergency - Terminal Site Emergency Contact Emergency 911. The Emergency 911 system will implement notifications to emergency organizations. Uncontrollable Emergency - General Emergency Contact Emergency 911. The Emergency 911 system will implement notifications to emergency organizations.

2.4.2.2

Federal Notifications In the event of an emergency situation at the Terminal, at a minimum the following federal agencies will be notified: • National Response Center (NRC); • Federal Energy Regulatory Commission (FERC); and • United States Coast Guard

2.4.2.3

Dissemination of Public Information In the event of an emergency at the Terminal, it is critical that information released to public agencies, the media, and ultimately the general public be accurate. During an

February 4, 2008 21

DRAFT

EMERGENCY RESPONSE MANUAL emergency, the Terminal employees may be contacted by the media or by members of the general public regarding the emergency or the status of the Terminal. In order to assure that accurate information rather than misinformation or speculation is disseminated, only the Public Information Contact is authorized to provide information to the media, local agencies or the public during the course of the emergency. All Terminal employees shall refer all persons with questions regarding the emergency to the Public Information Contact. Also, if Terminal employees are questioned about statements or speculations that arise, they will also refer the person to the Public Information Contact. 2.4.3

2.4.3.1

Incident Reporting Requirements

Purpose and Scope Completion of an incident report form is the first step in the incident reporting process. Incident reporting includes near miss events. The reporting of near miss events or situations leads directly to accident prevention in a number of ways. In many instances, near miss reports uncover potential problems that need to be corrected and communicated to others. At times, near miss reports reveal misunderstandings or misconceptions that have the potential to eventually lead to undesirable consequences if left undiscovered. Whatever the situation or circumstance, near miss reporting continues to play a key role in accident prevention at all levels.

2.4.3.2

Incident Investigations Terminal employees who witness an incident will complete and forward an incident report to their supervisor. After reviewing, the supervisor will determine if the investigation can be completed by the supervisor and the reporting Terminal employee, or if a formal team investigation is warranted. If the supervisor and Terminal employee complete the investigation, the supervisor will forward a typed report to the Health, Safety and Security Manager and also the Operations Manager. If the supervisor investigating the incident determines that a formal investigation is required, the investigation will comprise a group appointed by the Terminal Manager or designee. The appointed group will include, as a minimum, a representative of the Health, Safety and Security department, Operations & Maintenance departments, and the Engineering department. Others may be appointed at the discretion of the Terminal Manager including outside personnel. Any incident that includes (i) an injury related to equipment failures, (ii) equipment damage or failures, (iii) a Hazmat release, (iv) activation of a fire suppression system; or (v) a “near miss” i.e., one of the incidents listed may have occurred if

February 4, 2008 22

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EMERGENCY RESPONSE MANUAL position or timing had been different, requires a formal, team investigation. The investigation must be initiated promptly and not later than 48 hours after the incident. In some cases, regulatory bodies may conduct their own investigations. The Terminal Manager and Health, Safety and Security Manager will coordinate responses to such investigations. 2.4.3.3

Investigation Reports Each incident report received by the Health, Safety and Security Manager will be placed on an agenda for discussion at regularly scheduled meetings of the Safety Committee. Immediate action will be taken to correct problems identified during the investigation process. At the conclusion of formal investigations, a report will be prepared and submitted to the Terminal Manager. As a minimum, the report will include the following information: • A brief summary of the entire incident including time, date, weather conditions,

etc. • Description of the incident; • Date investigation began; • Description of all damage, including off-site damage; • Cause and contributing factors; • Equipment failures; • Procedural errors; • Improper emergency action; • Intentional tampering; • Deficiencies in established procedures; • Photographic documentation; • Written statements from persons who were first to the scene of the emergency

and other witnesses; • Copy of printouts from Main Control Room equipment; • Summary of emergency response and actions; • List of all persons on the site; • List of organizations responding to the emergency; • List of all injured people and extent of their injuries;

February 4, 2008 23

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EMERGENCY RESPONSE MANUAL • Conclusions of the investigative group; • Recommendations resulting from the investigation; and • Critique of all response and follow-up activities.

A report of investigations containing the above information will satisfy Federal incident investigation reporting requirements. Additionally, the report of the investigation will be maintained on file for at least five years. When the initial investigation has been completed, cleanup procedures will begin, necessary repairs will be made and equipment will be checked and returned to service according to procedures in the Operations and Maintenance Manuals. 2.4.3.4

Regulatory Notifications and Reports It will be the responsibility of the Terminal Manager, Health, Safety and Security Manager, and the Operations Manager to ensure all regulatory notifications and incident reporting are initiated and completed. Appendix E includes a table that summarizes the Regulatory Agency Emergency Notifications. Department of Transportation (RSPA) regulations, 49 CFR, 193.2515 requires the investigation of any explosion, fire, or LNG spill or leak which results in any of the following: • Death or injury requiring hospitalization • Property Damage exceeding $10,000

OSHA regulations, 29 CFR 1910.119(m) requires an investigation after each incident that resulted in or could reasonably have resulted in a catastrophic release of LNG. The investigation must be initiated promptly, not later than 48 hours after the incident. An incident investigation report that includes the details described in Section 2.4.3.3 of this Emergency Response Plan will satisfy the RSPA and OSHA incident investigation reporting requirements. Since regulatory authorities may conduct their own independent investigation, the site of the incident will be maintained intact and undisturbed to the extent practical. 2.5

Emergency Response Procedures Emergency Procedures for the Controllable Emergency situations listed in Section 2.2.1 of this Emergency Response Plan and for Uncontrollable Emergency situations listed in Section 2.2.2 are included in Appendix F.

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EMERGENCY RESPONSE MANUAL

2.6

Emergency Response Procedures for LNG Carriers Berthed at the Terminal If an emergency has been declared within the Terminal and if there is the potential for the emergency situation to effect or spread to all portions of the Terminal, including the pier area, the Terminal’s person onboard the LNG carrier in the Cargo Control Room (CCR) will communicate to the Master or the Chief Mate, the emergency situation and event status. The Master will muster his crew to their stations, and standby if an emergency departure is required. The Master will commence emergency departure at his discretion or if the departure is requested by the Emergency Response Team Leader following the Emergency LNG Carrier Departure procedure as described in Appendix F. Likewise, if an emergency condition exists on board the LNG carrier, which endangers the Terminal, the carrier will be moved from the pier at the Master's direction or when requested by the Emergency Response Team Leader. Only the Terminal personnel assigned to the LNG Carrier Cargo Control Room may remain on-board the carrier during an emergency. All other Terminal personnel shall leave the carrier when an emergency onboard occurs and will stand-by to assist only as requested by the Emergency Response Team Leader. Terminal maintenance personnel assigned to carrier-related duties should assemble in the Platform Control Room awaiting instructions.

2.7

On-Site Evacuation Procedures The Terminal Emergency Director will declare either a Limited Area Evacuation or a Total Evacuation of the Terminal dependent upon the type and location of the emergency situation. The announcement for an evacuation will be made via the on-site communications systems described in Section 2.4.1.1 of this Emergency Response Plan.

2.7.1

Limited Area Evacuation Procedures The Terminal has the following zones that will be used for a limited area evacuation: • Marine Pier and Waterside Areas • LNG Storage Tanks • Process Area

Each zone will have a posted evacuation plan that will include: • Emergency Signals and Notification Procedures • Emergency Shutdown Procedures

February 4, 2008 25

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EMERGENCY RESPONSE MANUAL • Evacuation Plan with map showing primary and secondary exit routes • Assembly Areas

The primary assembly point for all personnel is the Administration Building. Secondary assembly areas are listed in the evacuation plans that will be posted within each of the above mentioned zones. Assembly Leaders will take a headcount at the assembly points. The headcount information will be verified and details of the headcount will be provided to the Terminal Emergency Director along with a listing of all on-site personnel that will be provided by the Security Shift Supervisor. 2.7.2

Total Terminal Evacuation Procedures If a total evacuation of the Terminal is ordered, personnel will use primary escape routes and will assemble at the Terminal Security Gate House for a headcount that will be taken by the Assembly Leader. In the event that the Security Gate House is not in a safe location, an alternate assembly point will be used.

2.7.3

Missing Personnel Upon completion of the headcount(s) by the Assembly Leaders and checks against the listing of all on-site personnel provided by the Security Shift Supervisor, if it is determined that there are person(s) unaccounted for then the Terminal Emergency Director and the Emergency Response Team Leader will be informed immediately. If a person is unaccounted for under normal headcount procedures, the Supervisor for that person will begin to interview other personnel to establish the last known location of the missing person. Information concerning injured or missing persons will not be given to anyone other than the Terminal Emergency Director or the supervisor of the injured or missing person.

2.7.4

Emergency Evacuation Procedures for Visitors All visitors to the Terminal will sign in at the Security Gate House before entering the Terminal and will sign out when leaving the Terminal. This will prevent an unnecessary search for individuals who are no longer inside the Terminal. Whenever an emergency situation is declared, visitors will be escorted to the Administration Building or Security Gate House assembly points, from where

February 4, 2008 26

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EMERGENCY RESPONSE MANUAL they will be escorted from the site after the headcount has been completed by the Assembly Leader(s). 2.7.5

Emergency Evacuation Procedures for Contractors The assembly area for contractors will be at the Security Gate House and supervisors of contractor personnel will report their headcount to the Security Shift Supervisor.

2.7.6

Re-entry Into Previously Evacuated Areas Personnel will only return to an evacuated area upon receipt of instructions from the Terminal Emergency Director.

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EMERGENCY RESPONSE MANUAL

3 EMERGENCY EVACUATION ADJACENT TO THE TERMINAL AND ALONG LNG CARRIER TRANSIT ROUTES 3.1

Emergency Classification Emergencies that occur or have the potential to occur at the Oregon LNG Import Terminal will be classified using the following flowchart. Figure 3.1 Emergency Classification

3.1.1

Controllable Emergency This is an emergency in which Operations Personnel can prevent harm to personnel or equipment by taking reasonable and prudent actions such as

February 4, 2008 28

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EMERGENCY RESPONSE MANUAL valve manipulations, shutting down equipment, or initiating the Emergency Shutdown System. 3.1.2

Uncontrollable Emergency This is an emergency in which Operations Personnel cannot prevent harm to personnel or equipment by taking reasonable and prudent actions such as valve manipulations, shutting down equipment, or initiating the Emergency Shutdown System. An Uncontrollable Emergency involves situations that have the potential to result in exposure of personnel or property to natural gas in a liquid, cold vapor, or gaseous state or may result in fire or explosion. An Uncontrollable Emergency is then further classified as a Terminal Site Emergency or a General Emergency.

3.1.2.1

Uncontrollable Emergency – Terminal Site Emergency This is an Uncontrollable Emergency that threatens Terminal personnel or equipment with exposure to natural gas (liquid, cold vapor, or gaseous state) or involves a fire or explosion of a magnitude that involves a large portion of the Terminal. A Security Breach that results in a high probability of substantial Terminal damage is considered a Terminal Site Emergency.

3.1.2.2

Uncontrollable Emergency – General Emergency This is an Uncontrollable Emergency that threatens the public with exposure to natural gas (liquid, cold vapor, or gaseous state) or involves a fire or explosion of a magnitude that affects persons or property off-site.

3.2 3.2.1

Notifications Emergency Organization Notifications Uncontrollable Emergency situations that are classified as General Emergencies will require the notification of various Off-Site Emergency Organizations. Emergency notifications will be made by the Terminal Public Information Contact at the direction of the Terminal Emergency Director to the following Off-Site Emergency Organizations to request assistance as well as provide offsite organizations with the information needed to perform their emergency actions.

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EMERGENCY RESPONSE MANUAL • Contact the Office of Homeland Security, Emergency Preparedness, who

will implement State Emergency Alert System Plan(s); • Contact the United States Coast Guard Captain of the Port, who will

control marine traffic in the vicinity of the Terminal and assist with offshore rescue or evacuation activities if required. In the event of an emergency, Oregon LNG has the primary responsibility for coordinating efforts in responding to and the mitigation of the emergency condition. The Captain of the Port or his designee will be contacted by the Terminal Manager assuring he is kept abreast of the emergency operations. He is authorized by the Ports and Waterways Safety Act of 1972 to direct emergency operations where the situation poses a threat to the port or nearby vessels. The Captain of the Port has the authority to assume coordination efforts when the situation is not being properly handled by the Oregon LNG Terminal; • Contact the State Fire Marshal’s Office, who will be available to assist in

arson investigations or bomb threat responses; • Contact the Oregon State Police and the local Sheriff’s Office if law

enforcement assistance is required; • Contact local Fire Department if fire fighting and rescue assistance is

required; and • Contact Local Ambulance and Local Hospitals if medical assistance is

required. The Public Information Contact will maintain periodic communications with the off-site emergency organizations and other assigned entities throughout the duration of the emergency by telephone and either fax or email. 3.2.2

Federal Agency Notifications In the event of an emergency situation at, or adjacent to the Terminal or along LNG carrier transit routes, the following federal agencies will be notified as a minimum: • National Response Center (NRC); • Federal Energy Regulatory Commission (FERC); and • United States Coast Guard

3.2.3

Columbia River Pilots Notifications The Pilot on board a LNG carrier that is in transit to the Terminal will serve as the Emergency Coordinator for that carrier. The Pilot will inform the Terminal (via VHF radio on Channel TBD) of any actual or potential emergency situation

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EMERGENCY RESPONSE MANUAL along the transit route that may affect the carrier. The Pilot will also contact the Columbia River Pilot’s Office. Information received by the Terminal from the Pilot on board an approaching LNG carrier will be communicated to the Terminal Emergency Director by the Terminal Emergency Response Team Leader. The Terminal Emergency Director will determine the classification of the emergency and initiate the appropriate actions. The Columbia River Pilot’s Office maintains communications with the USCG and 911 and will, therefore, inform the USCG and the Emergency 911 system of any actual or potential emergency situation along the transit route that may affect the carrier. Appropriate agencies will communicate directly with the Pilot on board the carrier via VHF Radio on Channel TBD. 3.2.4

Residents and Recreational User Notifications Upon receipt of notification of a General Emergency at the Terminal, the Emergency 911 system will notify the Oregon OHSEP who will activate existing systems to notify residents and other recreational users of the emergency situation and actions to be taken.

3.2.5

3.2.5.1

Contact Details

Terminal Contact Details Figure 3.2.5.1 Terminal Personnel Contact Details Position / Group

Name

Telephone Number

Terminal Manager Operations Manager Health, Safety and Security Manager Environmental Manager Shift Supervisors Marine Safety Officer Security Supervisor Main Control Room Jetty Control Room

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EMERGENCY RESPONSE MANUAL 3.2.5.2

Off-Site Emergency Organizations Contact Details Figure 3.2.5.2 Off-Site Emergency Organization Contact Details Position / Group

Name

Telephone Number

Office of Homeland Security, Emergency Preparedness United States Coast Guard State Fire Marshal’s Office Oregon State Police Columbia River Pilots Local Law Enforcement Local Fire Department Ambulance Services Hospitals

3.2.5.3

Other Off-Site Agency Contact Details Figure 3.2.5.3 Other Off-Site Agency Contact Details Position / Group

Name

Telephone Number

Federal Energy Regulatory Commission DOT Office of Pipeline Safety (RSPA)

3.3 3.3.1

Emergency Procedures LNG Carriers in Transit The Pilot of each LNG carrier will be the Emergency Coordinator for the carrier. The Pilot will communicate with the Columbia River Pilots Station on VHF Channel TBD and will also maintain contact with the Terminal. The Terminal will monitor Channel TBD as the LNG carrier approaches. The Pilot will activate sirens and other warning devices that are fitted to the LNG carrier when a General Emergency situation has been declared by the Terminal Emergency Director. The Terminal Emergency Director will consult with the Columbia River Pilot’s Office to determine the appropriate actions to be taken with a LNG carrier that is in transit to the Terminal. The Columbia River Pilot’s Office maintains

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EMERGENCY RESPONSE MANUAL communications with the USCG and will, therefore, inform the USCG of any actual or potential emergency situation along the transit route that may affect the carrier. 3.3.2

Evacuation of Areas Adjacent to the Terminal and LNG Carrier Transit Route

3.3.2.1

Initiating Event The initiating event for evacuation of areas adjacent to the Terminal and LNG carrier transit routes will be an Uncontrollable Emergency that has been categorized as a General Emergency by the Terminal Emergency Director because personnel or property off-site are, or may be affected.

3.3.2.2

Extent of Off-site Evacuation The Terminal Emergency Directory will determine the extent of the off-site evacuation and will instruct the Public Information Contact to recommend to the Office of Homeland Security, Emergency Preparedness that an off-site evacuation be ordered.

3.3.2.3

Evacuation Authority The authority to order an off-site evacuation rests with the Office of Homeland Security, Emergency Preparedness. The Terminal Emergency Directory only provides the recommendation that an off-site evacuation be ordered and the potential area affected.

3.3.2.4

Evacuation Procedures Evacuation Procedures are included in Appendix G.

3.3.3

Evacuation Zones, Routes and Methods of Egress Drawings that illustrate the off-site evacuation zones, evacuation routes and methods of egress are included in Appendix H.

3.4

Distribution of Public Information In the event of an emergency at the Terminal, it is critical that information released to public agencies, the media, and ultimately the general public be accurate. During an emergency, the Terminal employees may be contacted by the media or by members of the general public regarding the emergency or the status of the Terminal. In order to assure that accurate information rather than misinformation or speculation is disseminated, only the Public Information Contact is authorized to provide information to the media, local agencies, or the public. All Terminal employees will refer all persons with questions regarding the

February 4, 2008 33

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EMERGENCY RESPONSE MANUAL emergency to the Public Information Contact. Also, if Terminal employees are questioned about statements or speculations that arise, they will also refer the person to the Public Information Contact.

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EMERGENCY RESPONSE MANUAL

4 TRAINING AND DRILLS 4.1

Emergency Response Plan Review The Emergency Response Plan will be reviewed on an annual basis by the following organizations •

Oregon LNG Import Terminal;



Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshal;



Columbia River Pilots;



Oregon State Police;



Local Sheriff’s Office; and



Local Fire Department.

It is the responsibility of the Oregon LNG import Terminal to issue the Emergency Response Plan for review, coordinate the receipt of review comments, update the Emergency Response Plan and reissue as required. 4.2 4.2.1

Training Requirements Emergency Response Plan Training. All new Terminal employees will be trained on the Emergency Response Plan and will attend refresher training a minimum of 8 hours once every year. All Off-Site Emergency Organizations and other Off-Site Agencies will be invited to attend the Emergency Response Plan training and refresher training courses. It is the responsibility of the Oregon LNG Terminal to issue training schedules to the off-site emergency organizations and other off-site agencies.

4.2.2

Medical Training. All new Terminal employees will be trained and qualified in CPR and First Aid.

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EMERGENCY RESPONSE MANUAL

4.2.3

Fire Fighting Training Terminal employees assigned to operations and maintenance groups and volunteers will be trained for dealing with incipient fires and also fires involving natural gas vapors and will receive refresher training at least 8 hours of refresher training once every year.

4.2.4

Local Fire Department Local Fire Departments are the primary local fire/rescue organizations serving the Terminal. The Fire Departments will be invited on-site for Terminal familiarization training that will include: • Terminal layout; • Terminal firefighting equipment and firefighting equipment locations; and • Locations of major sources of potential fires and LNG fire fighting training.

They will also be asked to participate in routine emergency exercises. It is also anticipated that the Local Fire Departments will attend specialized fire training that will focus on LNG and natural gas. 4.3

Periodic Drills Annual emergency response drills will be held to: •

Maintain proficiency in the Emergency Response Plan;



Integrate new equipment, practices, or procedures into the emergency response effort;



Familiarize new Terminal employees and new members of off-site emergency organizations with their Emergency Response Plan duties; and



Correct any deficiencies or weaknesses noted in Emergency Exercises.

The annual drills will include as many of the emergency response activities as practical. The type of drill may vary. The Oregon LNG Import Terminal is responsible for developing the schedule of drills with the off-site emergency organizations and other off-site agencies.

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EMERGENCY RESPONSE MANUAL

5 DOCUMENTATION OF REQUIRED CONSULTATION In accordance with the requirements of the Energy Policy Act of 2005, the DOT regulations and the Commission Order(s) authorizing LNG Terminals, the owners of LNG Import Terminals are required to consult with appropriate agencies and emergency organizations while developing the Emergency Response Plan. This section of the Emergency Response Plan provides documentation demonstrating discussions that have been held between Oregon LNG and the appropriate agencies and other emergency organizations in the development of this Emergency Response Plan. 5.1

Agencies and Emergency Organizations The following is a listing of those agencies and other emergency organizations that have been consulted in the preparation of this Emergency Response Plan.

5.2



United States Coast Guard;



Office of Homeland Security, Emergency Preparedness;



State Fire Marshall;



State Police;



Local Sheriffs Office;



Oregon River Pilots;



Local Ambulance Services; and



Local Fire Departments.

Coordination Meetings Appendix I includes minutes and notes of coordination meetings that have been held with agencies and other emergency organizations who have been consulted in the preparation of this Emergency Response Plan. The following table 5.2 summarizes the occurrence of each coordination meeting.

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EMERGENCY RESPONSE MANUAL Table 5.2 Emergency Response Plan Coordination Meetings

Meeting Date

Attendees

Meeting Agenda

38

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EMERGENCY RESPONSE MANUAL

6 COST SHARING PLAN The Energy Policy Act of 2005 and Commission Orders authorizing LNG Terminals require that the Emergency Response Plan include a Cost Sharing Plan identifying the mechanisms for funding all project specific security costs and safety / emergency management costs that would be imposed on state and local agencies. This section of the Oregon LNG Terminal Emergency Response Plan details the Cost Sharing Plan that will be developed with and agreed to by the applicable agencies and emergency response organizations and specifies: •

What Oregon LNG will provide to cover the cost of resources required to manage the security of the Terminal and LNG carriers that visit the Terminal; and



What Oregon LNG will provide to cover the cost of state and other, local resources required for safety and emergency management.

Appendix J to this Emergency Response Plan will include a Letter of Commitment for the Cost Sharing Plan signed by Oregon LNG and acknowledged by the appropriate agencies and other emergency organizations. 6.1

Direct Reimbursement Oregon LNG will negotiate direct reimbursement costs that will be paid by Oregon LNG to the applicable agencies and emergency organizations for any per transit security and / or emergency management costs.

6.2

Capital Costs Oregon LNG will negotiate reimbursement and / or payment of capital costs that will be paid by Oregon LNG to applicable agencies and emergency organizations for any security / emergency management equipment specific to the needs of this Emergency Response Plan.

6.3

Annual Costs Oregon LNG will negotiate the payment of annual costs for providing specialized training and for conducting drills and other exercises specific to the needs of this Emergency Response Plan.

39

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EMERGENCY RESPONSE MANUAL

Appendix A Oregon LNG Terminal Operations and Maintenance Team Organization Chart

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix B Oregon LNG Terminal Hazard Detection Plot Plans

February 4, 2008 DRAFT

Oregon LNG Warrenton, OR Hazard Detection Equipment List

Job No. 07902 Doc No. 07902-LI-600-001, Rev: 0 Page 1 of 15

HAZARD DETECTION EQUIPMENT LIST By H H C H H

REV NUMBER: ISSUE PURPOSE: DATE: BY: CHECKED: APPROVED:

CH·IV International

0 Issued for Client Review 01/11/08 TOA OOA RCT

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Unloading Platform

Area 1

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Activation of Hazard Control Equipment

High Sensitivity Smoke Detector

Platform Control Room

XNHS-601A

--

XNHA-601A

Alarm in Platform Control Room and Main Control Room

High Sensitivity Smoke Detector

Platform Control Room

XNHS-601B

--

XNHA-601B

Alarm in Platform Control Room and Main Control Room

Gas Detector

Platform Control Room HVAC Intake

GD-601

Pre-alarm GAH-601 = 20%

Alarm GAHH-601 = 40%

Alarm in Platform Control Room and Main Control Room, shutdown HVAC Intake

Gas Detector

Inside Platform Control Room

GD-602

Pre-alarm GAH-602 = 20%

Alarm GAHH-602 = 40%

Alarm in Platform Control Room and Main Control Room, shutdown HVAC Intake

Gas Detector

Unloading Platform, arm L-101A

GD-603A

Pre-alarm GAH-603A = 20%

Alarm GAHH-603A = 40%

Gas Detector

Unloading Platform, arm L-101B

GD-603B

Pre-alarm GAH-603B = 20%

Alarm GAHH-603B = 40%

Gas Detector

Unloading Platform, arm L-101C

GD-603C

Pre-alarm GAH-603C = 20%

Alarm GAHH-603C = 40%

Gas Detector

Unloading Platform, arm L-102

GD-603D

Pre-alarm GAH-603D = 20%

Alarm GAHH-603D = 40%

Gas Detector

Platform Drum D-103

GD-604

Pre-alarm GAH-604 = 20%

Alarm GAHH-604 = 40%

Alarm in Platform Control Room and Main Control Room

Low Temp Detector

Unloading Platform, arm L-101A

TE-603A

--

TALL-603A Set point = -75 deg F

Low Temp Detector

Unloading Platform, arm L-101B

TE-603B

--

TALL-603B Set point = -75 deg F

Low Temp Detector

Unloading Platform, arm L-101C

TE-603C

--

TALL-603C Set point = -75 deg F

Low Temp Detector

Unloading Platform, arm L-102

TE-603D

--

TALL-603D Set point = -75 deg F

Heat Detector

Located above hydraulic lines on LNG unloading arm L-101A

XHS-603A

--

XHA-603A Alarm = 135 deg F

Shuts down the Unloading Arm L-101A Alarm in Platform Control Room and Main Control Room, ESD-1 Shuts down the Unloading Arm L-101B Alarm in Platform Control Room and Main Control Room, ESD-1 Shuts down the Unloading Arm L-101C Alarm in Platform Control Room and Main Control Room, ESD-1 Shuts down the Vapor Arm L-102 Alarm in Platform Control Room and Main Control Room, ESD-1 Shuts down the Unloading Arm L-101A Alarm in Platform Control Room and Main Control Room

Heat Detector

Located above hydraulic lines on LNG unloading arm L-101B

XHS-603B

--

XHA-603B Alarm = 135 deg F

Shuts down the Unloading Arm L-101B Alarm in Platform Control Room and Main Control Room

Heat Detector

Located above hydraulic lines on LNG unloading arm L-101C

XHS-603C

--

XHA-603C Alarm = 135 deg F

Shuts down the Unloading Arm L-101C Alarm in Platform Control Room and Main Control Room

Heat Detector

Located above hydraulic lines on LNG vapor return arm L-102

XHS-603D

--

XHA-603D Alarm = 135 deg F

Shuts down the Vapor Arm L-102 and Unloading arms L-101A/B/C Alarm in Platform Control Room and Main Control Room

Page 2

Alarm in Platform Control Room and Main Control Room, ESD-1

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Pier

Area 2

Date: 01/11/2008 Revision: 0

Area or Equipment Monitored

Type

Activation Point

Tag Number

Low Temp Detector

Pier, start of piperack

TE-605A

--

TALL-605A Set point = -75 deg F

High Temp Detector

Pier, start of piperack

TE-605B

--

TAHH-605B Set point = 165 deg F

Low Temp Detector

Pier

TE-606A

--

TALL-606A Set point = -75 deg F

High Temp Detector

Pier

TE-606B

--

TAHH-606B Set point = 165 deg F

Low Temp Detector

Pier

TE-607A

--

TALL-607A Set point = -75 deg F

High Temp Detector

Pier

TE-607B

--

TAHH-607B Set point = 165 deg F

Low Temp Detector

Pier

TE-608A

--

TALL-608A Set point = -75 deg F

High Temp Detector

Pier

TE-608B

--

TAHH-608B Set point = 165 deg F

Low Temp Detector

Pier

TE-609A

--

TALL-609A Set point = -75 deg F

High Temp Detector

Pier

TE-609B

--

TAHH-609B Set point = 165 deg F

Low Temp Detector

Pier

TE-610A

--

TALL-610A Set point = -75 deg F

High Temp Detector

Pier

TE-610B

--

TAHH-610B Set point = 165 deg F

Low Temp Detector

Pier

TE-611A

--

TALL-611A Set point = -75 deg F

High Temp Detector

Pier

TE-611B

--

TAHH-611B Set point = 165 deg F

Low Temp Detector

Pier

TE-612A

--

TALL-612A Set point = -75 deg F

High Temp Detector

Pier

TE-612B

--

TAHH-612B Set point = 165 deg F

Low Temp Detector

Pier

TE-613A

--

TALL-613A Set point = -75 deg F

High Temp Detector

Pier

TE-613B

--

TAHH-613B Set point = 165 deg F

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector

Pier, start of piperack Pier Pier Pier Pier

GD-605 GD-606 GD-607 GD-608 GD-609

Pre-alarm GAH-605 = 20% Pre-alarm GAH-606 = 20% Pre-alarm GAH-607 = 20% Pre-alarm GAH-608 = 20% Pre-alarm GAH-609 = 20%

Page 3

Activation of Hazard Control Equipment

ESD-1 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 mins.

Alarm GAHH-605 = 40% Alarm GAHH-606 = 40% Alarm GAHH-607 = 40% Alarm GAHH-608 = 40% Alarm GAHH-609 = 40%

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Pier

Area 2

Piperack (On-shore)

Area 2

Flare

Area 2

Date: 01/11/2008 Revision: 0

Area or Equipment Monitored

Type

Activation Point

Tag Number

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Low Temp Detector

Pier Pier Pier Pier Piperack Piperack Piperack Piperack Piperack Piperack

GD-610 GD-611 GD-612 GD-613 GD-614 GD-615 GD-616 GD-617 GD-618 TE-614A

Pre-alarm GAH-610 = 20% Pre-alarm GAH-611 = 20% Pre-alarm GAH-612 = 20% Pre-alarm GAH-613 = 20% Pre-alarm GAH-614 = 20% Pre-alarm GAH-615 = 20% Pre-alarm GAH-616 = 20% Pre-alarm GAH-617 = 20% Pre-alarm GAH-618 = 20% --

Low Temp Detector

Piperack

TE-615A

--

Low Temp Detector

Piperack

TE-616A

--

Low Temp Detector

Piperack

TE-617A

--

Low Temp Detector

Piperack

TE-618A

--

High Temp Detector

Piperack

TE-614B

--

High Temp Detector

Piperack

TE-615B

--

High Temp Detector

Piperack

TE-616B

--

High Temp Detector

Piperack

TE-617B

--

High Temp Detector

Piperack

TE-618B

Gas Detector

Flare

GD-622

Flame Detector

Flare

NS-622

-Pre-alarm GAH-622 = 20%

--

Page 4

Activation of Hazard Control Equipment

ESD-1 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 mins.

Alarm GAHH-610 = 40% Alarm GAHH-611 = 40% Alarm GAHH-612= 40% Alarm GAHH-613 = 40% Alarm GAHH-614 = 40% Alarm GAHH-615 = 40% Alarm GAHH-616 = 40% Alarm GAHH-617 = 40% Alarm GAHH-618 = 40% TALL-614A Set point = -75 deg F TALL-615A Set point = -75 deg F TALL-616A Set point = -75 deg F TALL-617A Set point = -75 deg F TALL-618A Set point = -75 deg F TAHH-614B Set point = 165 deg F TAHH-615B Set point = 165 deg F TAHH-616B Set point = 165 deg F TAHH-617B Set point = 165 deg F TAHH-618B Set point = 165 deg F Alarm GAHH-622 = 40%

Alarm in Main Control Room.

NI-622 (UVIR)

Alarm in Main Control Room.

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Full Containment Tanks

Area 3

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Gas Detector

FCT Tank T-201A

GD-623A

Pre-alarm GAH-623A = 20%

Alarm GAHH-623A = 40%

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Flame Detector

FCT Tank T-201A FCT Tank T-201A FCT Tank T-201A FCT Tank T-201A FCT Tank T-201A FCT Tank T-201A, Platform

GD-624A GD-625A GD-626A GD-627A GD-628A NS-623A

Pre-alarm GAH-624A = 20% Pre-alarm GAH-625A = 20% Pre-alarm GAH-626A = 20% Pre-alarm GAH-627A = 20% Pre-alarm GAH-628A = 20% --

Alarm GAHH-624A = 40% Alarm GAHH-625A = 40% Alarm GAHH-626A = 40% Alarm GAHH-627A = 40% Alarm GAHH-628A = 40% NI-623A (UVIR)

Flame Detector

FCT Tank T-201A, Platform

NS-624A

--

NI-624A (UVIR)

Flame Detector

FCT Tank T-201A, Relief Valve

NS-201AA

--

NI-201AA (UVIR)

Flame Detector

FCT Tank T-201A, Relief Valve

NS-201AB

--

NI-201AB (UVIR)

Flame Detector

FCT Tank T-201A, Relief Valve

NS-201AC

--

NI-201AC (UVIR)

Low Temp Detector

FCT Tank T-201A

TE-632AA

--

Low Temp Detector

FCT Tank T-201A

TE-633AA

--

Low Temp Detector

FCT Tank T-201A

TE-634AA

Gas Detector

FCT Tank T-201B

GD-623B

Pre-alarm GAH-623B = 20%

TALL-632AA Set point = -75 deg F TALL-633AA Set point = -75 deg F TALL-634AA Set point = -75 deg F Alarm GAHH-623B = 40%

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Flame Detector

FCT Tank T-201B FCT Tank T-201B FCT Tank T-201B FCT Tank T-201B FCT Tank T-201B FCT Tank T-201B, Platform

GD-624B GD-625B GD-626B GD-627B GD-628B NS-623B

Pre-alarm GAH-624B = 20% Pre-alarm GAH-625B = 20% Pre-alarm GAH-626B = 20% Pre-alarm GAH-627B = 20% Pre-alarm GAH-628B = 20% --

Alarm GAHH-624B = 40% Alarm GAHH-625B = 40% Alarm GAHH-626B = 40% Alarm GAHH-627B = 40% Alarm GAHH-628B = 40% NI-623B (UVIR)

Flame Detector

FCT Tank T-201B, Platform

NS-624B

--

NI-624B (UVIR)

Flame Detector

FCT Tank T-201B, Relief Valve

NS-201BA

--

NI-201BA (UVIR)

Flame Detector

FCT Tank T-201B, Relief Valve

NS-201BB

--

NI-201BB (UVIR)

Flame Detector

FCT Tank T-201B, Relief Valve

NS-201BC

--

NI-201BC (UVIR)

Low Temp Detector

FCT Tank T-201B

TE-632BA

--

Low Temp Detector

FCT Tank T-201B

TE-633BA

--

Low Temp Detector

FCT Tank T-201B

TE-634BA

--

TALL-632BA Set point = -75 deg F TALL-633BA Set point = -75 deg F TALL-634BA Set point = -75 deg F

--

Page 5

Activation of Hazard Control Equipment

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Full Containment Tanks

Area 3

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Gas Detector

FCT Tank T-201C

GD-623C

Pre-alarm GAH-623C = 20%

Alarm GAHH-623C = 40%

Gas Detector

FCT Tank T-201C

GD-624C

Pre-alarm GAH-624C = 20%

Alarm GAHH-624C = 40%

Gas Detector

FCT Tank T-201C

GD-625C

Pre-alarm GAH-625C = 20%

Alarm GAHH-625C = 40%

Gas Detector

FCT Tank T-201C

GD-626C

Pre-alarm GAH-626C = 20%

Alarm GAHH-626C = 40%

Gas Detector

FCT Tank T-201C

GD-627C

Pre-alarm GAH-627C = 20%

Alarm GAHH-627C = 40%

Gas Detector

FCT Tank T-201C

GD-628C

Pre-alarm GAH-628C = 20%

Alarm GAHH-628C = 40%

Flame Detector

FCT Tank T-201C, Platform

NS-623C

--

NI-623C (UVIR)

Flame Detector

FCT Tank T-201C, Platform

NS-624C

--

NI-624C (UVIR)

Flame Detector

FCT Tank T-201C, Relief Valve

NS-201CA

--

NI-201CA (UVIR)

Flame Detector

FCT Tank T-201C, Relief Valve

NS-201CB

--

NI-201CB (UVIR)

Flame Detector

FCT Tank T-201C, Relief Valve

NS-201CC

--

NI-201CC (UVIR)

Low Temp Detector

FCT Tank T-201C

TE-632CA

--

TALL-632CA Set point = -75 deg F

Low Temp Detector

FCT Tank T-201C

TE-633CA

--

TALL-633CA Set point = -75 deg F

Low Temp Detector

FCT Tank T-201C

TE-634CA

--

TALL-634CA Set point = -75 deg F

Page 6

Activation of Hazard Control Equipment

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Piperack

Area 4

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Activation of Hazard Control Equipment

Gas Detector Gas Detector Gas Detector Gas Detector

Piperack Piperack Piperack Under BOG Drum D-203

GD-619 GD-620 GD-621 GD-672

Pre-alarm GAH-619 = 20% Pre-alarm GAH-620 = 20% Pre-alarm GAH-621 = 20% Pre-alarm GAH-672 = 20%

Alarm GAHH-619 = 40% Alarm GAHH-620 = 40% Alarm GAHH-621 = 40% Alarm GAHH-672 = 40%

Gas Detector Gas Detector

Under BOG Condenser E-207 Under Gas Make-Up Vaporizer E-206

GD-673 GD-674

Pre-alarm GAH-673 = 20% Pre-alarm GAH-674 = 20%

Alarm GAHH-673 = 40% Alarm GAHH-674 = 40%

Gas Detector

Piperack - Beneath HP Pump Drum D208 Piperack

GD-635

Pre-alarm GAH-635 = 20%

Alarm GAHH-635 = 40%

Low Temp Detector

TE-619A

--

TALL-619A Set point = -75 deg F

Low Temp Detector

Piperack

TE-620A

--

TALL-620A Set point = -75 deg F

Low Temp Detector

Piperack

TE-621A

--

TALL-621A point = -75 deg F

Set ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the BOG Condenser are active at the same time or if a single alarm is active for 30 min.

Low Temp Detector

Piperack - Under BOG Condenser E207

TE-624A

--

TALL-624A point = -75 deg F

Set ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the BOG Condenser are active at the same time or if a single alarm is active for 30 min.

Low Temp Detector

Piperack - Under HP Pump Drum D208

TE-625A

--

TALL-625A point = -75 deg F

Set ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the HP Pump Drum are active at the same time or if a single alarm is active for 30 min.

Low Temp Detector

Piperack - Under BOG Drum 203

TE-626A

--

TALL-626A point = -75 deg F

Low Temp Detector

Piperack - Under Gas Make-Up Vaporizer E-206

TE-627A

--

TALL-627A point = -75 deg F

Set ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the BOG Drum are active at the same time or if a single alarm is active for 30 min. Set ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the Gas Make-Up Vaporizer are active at the same time or if a single alarm is active for 30 min.

High Temp Detector

Piperack

TE-619B

--

TAHH-619B Set point = 165 deg F

High Temp Detector

Piperack

TE-620B

--

High Temp Detector

Piperack

TE-621B

--

TAHH-620B Set point = 165 deg F TAHH-621B Set point = 165 deg F

D-

Page 7

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min. ESD-2 Shutdown immediately if two or more adjacent alarms in the second section of the Piperack or around the BOG Condenser are active at the same time or if a single alarm is active for 30 min.

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

LNG Spill Containment Basin

Area 4

Compressor Building

HP Pump Structure

Area 4

Area 5

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

TE-622A

Activation of Hazard Control Equipment

Low Temp Detector

Water Removal Pump P-607

--

TALL-622A Set point = -75 deg F

High Temp Detector

Water Removal Pump P-607

Low Temp Detector

Low Point Drain Drum D-211

TE-622B

--

TE-623A

--

TAHH-622B Set point = 165 deg F TALL-623A Set point = -75 deg F TAHH-623B Set point = 165 deg F Alarm GAHH-630 = 40% Alarm GAHH-631 = 40% Alarm GAHH-632A = 40% Alarm GAHH-632B = 40% Alarm GAHH-633A = 40% Alarm GAHH-633B = 40% NI-631 (UVIR)

High Temp Detector

Low Point Drain Drum D-211

TE-623B

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Flame Detector

Water Removal Pump P-607 Low Point Drain Drum D-211 Upper Level Upper Level Upper Level Upper Level Open Side

GD-630 GD-631 GD-632A GD-632B GD-633A GD-633B NS-631

Flame Detector

Lower Level

NS-632

--

NI-632 (UVIR)

Flame Detector

Lower Level

NS-633

--

NI-633 (UVIR)

Smoke Detector

Open Side

XNS-631

--

XNA-631

Smoke Detector

Lower Level

XNS-632

--

XNA-632

Smoke Detector

Lower Level

XNS-633

--

Gas Detector

Close to grade

GD-634

Low Temp Detector

Below HP Pumps

TE-628A

--

Low Temp Detector

Below HP Pumps

TE-629A

--

Low Temp Detector

Below HP Pumps

TE-630A

--

Flame Detector

HP Pump Structure

NS-634

--

TALL-628A Set point = -75 deg F TALL-629A Set point = -75 deg F TALL-630A Set point = -75 deg F NI-634 (UVIR)

Flame Detector

HP Pump Structure

NS-635

--

NI-635 (UVIR)

Flame Detetctor

HP Pump Structure

NS-636

--

NI-636 (UVIR)

-Pre-alarm GAH-630 = 20% Pre-alarm GAH-631 = 20% Pre-alarm GAH-632A = 20% Pre-alarm GAH-632B = 20% Pre-alarm GAH-633A = 20% Pre-alarm GAH-633B = 20% --

Pre-alarm GAH-634 = 20%

Page 8

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Alarm in Main Control Room

XNA-633 Alarm GAHH-634 = 40%

ESD-2 Shutdown immediately if two or more adjacent alarms in the HP Pump Structure are active at the same time or if a single alarm is active for 30 min.

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Piperack From HP Pump Structure to First Stage Vaporizer Area

Area 5

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Gas Detector Low Temp Detector

Piperack Piperack

GD-636 TE-631A

Pre-alarm GAH-636 = 20% --

High Temp Detector

Piperack

TE-631B

--

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-637

--

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-638

--

NI-638 (UVIR)

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-639

--

NI-639 (UVIR)

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-640

--

NI-640 (UVIR)

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-641

--

NI-641 (UVIR)

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-642

--

NI-642 (UVIR)

--

Alarm GAHH-636 = 40% TALL-631A Set point = -75 deg F TAHH-631B Set point = 165 deg F NI-637 (UVIR)

Flame Detector

Pipeway in First Stage Vaporizer Area

NS-643

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-637

Pre-alarm GAH-637 = 20%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-638

Pre-alarm GAH-638 = 20%

Alarm GAHH-638 = 40%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-639

Pre-alarm GAH-639 = 20%

Alarm GAHH-639 = 40%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-640

Pre-alarm GAH-640 = 20%

Alarm GAHH-640 = 40%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-641

Pre-alarm GAH-641 = 20%

Alarm GAHH-641 = 40%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-642

Pre-alarm GAH-642 = 20%

Alarm GAHH-642 = 40%

Gas Detector

Pipeway in First Stage Vaporizer Area

GD-643

Pre-alarm GAH-643 = 20%

Alarm GAHH-643 = 40%

Page 9

Activation of Hazard Control Equipment

ESD-2 Shutdown immediately if two or more adjacent alarms in the piperack or First Stage Vaporizer area are active at the same time or if a single alarm is active for 30 min.

NI-643 (UVIR) Alarm GAHH-637 = 40%

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Piperack From HP Pump Structure to First Stage Vaporizer Area

Area 5

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Flame Detector

First Stage Vaporizer Area

NS-644A

--

NI-644A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-644B

--

NI-644B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-645A

--

NI-645A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-645B

--

NI-645B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-646A

--

NI-646A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-646B

--

NI-646B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-647A

--

NI-647A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-647B

--

NI-647B(UVIR)

Flame Detector

First Stage Vaporizer Area

NS-648A

--

NI-648A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-648B

--

NI-648B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-649A

--

NI-649A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-649B

--

NI-649B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-650A

--

NI-650A (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-650B

--

NI-650B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-651A

--

NI-651A (UVIR)

--

NI-651B (UVIR)

Flame Detector

First Stage Vaporizer Area

NS-651B

Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector Gas Detector

First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area First Stage Vaporizer Area

GD-644A GD-644B GD-645A GD-645B GD-646A GD-646B GD-647A GD-647B GD-648A GD-648B GD-649A GD-649B GD-650A

Pre-alarm GAH-644A = 20% Pre-alarm GAH-644B = 20% Pre-alarm GAH-645A = 20% Pre-alarm GAH-645B = 20% Pre-alarm GAH-646A = 20% Pre-alarm GAH-646B = 20% Pre-alarm GAH-647A = 20% Pre-alarm GAH-647B = 20% Pre-alarm GAH-648A = 20% Pre-alarm GAH-648B = 20% Pre-alarm GAH-649A = 20% Pre-alarm GAH-649B = 20% Pre-alarm GAH-650A = 20%

Alarm GAHH-644A = 40% Alarm GAHH-644B = 40% Alarm GAHH-645A = 40% Alarm GAHH-645B = 40% Alarm GAHH-646A = 40% Alarm GAHH-646B = 40% Alarm GAHH-647A = 40% Alarm GAHH-647B= 40% Alarm GAHH-648A = 40% Alarm GAHH-648B = 40% Alarm GAHH-649A = 40% Alarm GAHH-649B = 40% Alarm GAHH-650A = 40%

Gas Detector

First Stage Vaporizer Area

GD-650B

Pre-alarm GAH-650B = 20%

Alarm GAHH-650B = 40%

Gas Detector

First Stage Vaporizer Area

GD-651A

Pre-alarm GAH-651A = 20%

Alarm GAHH-651A = 40%

Gas Detector

First Stage Vaporizer Area

GD-651B

Pre-alarm GAH-651B = 20%

Alarm GAHH-651B = 40%

Page 10

Activation of Hazard Control Equipment

Alarm in Main Control Room

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Second Stage Vaporizer Area and Auxiliary Building

Area 6

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Activation of Hazard Control Equipment

Gas Detector

Piperack

GD-652

Pre-alarm GAH-652 = 20%

Alarm GAHH-652 = 40%

Alarm in Main Control Room

Gas Detector

Piperack near Mixer

GD-653

Pre-alarm GAH-653 = 20%

Alarm GAHH-653 = 40%

Alarm in Main Control Room

Gas Detector

Second Stage Vaporizer, E-304A

GD-654A

Pre-alarm GAH-654A = 20%

Alarm GAHH-654A = 40%

Alarm in Main Control Room

Gas Detector

Second Stage Vaporizer, E-304B

GD-654B

Pre-alarm GAH-654B = 20%

Alarm GAHH-654B = 40%

Alarm in Main Control Room

Gas Detector

Second Stage Vaporizer, E-304C

GD-654C

Pre-alarm GAH-654C = 20%

Alarm GAHH-654C = 40%

Alarm in Main Control Room

Gas Detector

Fuel Gas Area

GD-655

Pre-alarm GAH-655 = 20%

Alarm GAHH-655 = 40%

Alarm in Main Control Room

Gas Detector

Auxiliary Building Ventilation Intake

GD-657

Pre-alarm GAH-657 = 20%

Alarm GAHH-657 = 40%

Alarm in Main Control Room and Shutdown Ventilation

Gas Detector

Fired Heater, B-401A

GD-659A

Pre-alarm GAH-659A = 20%

Alarm GAHH-659A = 40%

Alarm in Main Control Room

Gas Detector

Fired Heater, B-401B

GD-659B

Pre-alarm GAH-659B = 20%

Alarm GAHH-659B = 40%

Alarm in Main Control Room

Gas Detector

Fired Heater, B-401C

GD-659C

Pre-alarm GAH-659C = 20%

Alarm GAHH-659C = 40%

Alarm in Main Control Room

Gas Detector

Pressure Control Vent HTF Surge Drum, D-403

GD-402

Pre-alarm GAH-402 = 20%

Alarm GAHH-402 = 40%

Alarm in Main Control Room

Gas Detector

Pressure Safety Vent HTF Surge Drum, D-403

GD-403

Pre-alarm GAH-403 = 20%

Alarm GAHH-403= 40%

Alarm in Main Control Room

Gas Detector

Second Stage Vaporizer, E-304A Air Trap Vent

Pre-alarm GAH-304A = 20%

Alarm GAHH-304A= 40%

Alarm in Main Control Room

GD-304A

Page 11

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Second Stage Vaporizer Area and Auxiliary Building

Area 6

Pigging Station

Area 6

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Activation of Hazard Control Equipment

Gas Detector

Second Stage Vaporizer, E-304B Air Trap Vent

GD-304B

Pre-alarm GAH-304B = 20%

Alarm GAHH-304B= 40%

Alarm in Main Control Room

Gas Detector

Second Stage Vaporizer, E-304C Air Trap Vent

GD-304C

Pre-alarm GAH-304C = 20%

Alarm GAHH-304C= 40%

Alarm in Main Control Room

Gas Detector

Fired Heater. B-401A, Combustion Air Intake

GD-401A

Pre-alarm GAH-401A = 20%

Alarm GAHH-401A= 40%

Gas Detector

Fired Heater. B-401B, Combustion Air Intake

GD-401B

Pre-alarm GAH-401B = 20%

Alarm GAHH-401B= 40%

Gas Detector

Fired Heater. B-401C, Combustion Air Intake

GD-401C

Pre-alarm GAH-401C = 20%

Alarm GAHH-401C= 40%

Flame Detector

Piperack

NS-652

--

NI-652 (UVIR)

Alarm in Main Control Room

Flame Detector

Pieprack

NS-653

--

NI-653 (UVIR)

Alarm in Main Control Room

Flame Detector

Second Stage Vaporizer, E-304A

NS-654A

--

NI-654A (UVIR)

Flame Detector

Second Stage Vaporizer, E-304B

NS-654B

--

NI-654B (UVIR)

Flame Detector

Second Stage Vaporizer, E-304C

NS-654C

--

NI-654C (UVIR)

Flame Detector

Fuel Gas Area

NS-655

--

NI-655 (UVIR)

Heat Detector

Fired Heater, B-401A

XHS-659A

--

XHA-659A Alarm = 165 deg F

Heat Detector

Fired Heater, B-401B

XHS-659B

--

XHA-659B Alarm = 165 deg F

Heat Detector

Fired Heater, B-401C

XHS-659C

--

XHA-659C Alarm = 165 deg F

Gas Detector Gas Detector Flame Detector

Pigging Station Pigging Station Pigging Station

GD-661A GD-661B NS-661A

Flame Detector

Pigging Station

NS-661B

--

NI-661B (UVIR)

Heat Detector

Pigging Station

XHS-661A

--

Heat Detector

Pigging Station

XHS-661B

--

XHA-661A Alarm = 165 deg F XHA-661B Alarm = 165 deg F

Pre-alarm GAH-661A = 20% Pre-alarm GAH-661B = 20% --

Page 12

Alarm GAHH-661A = 40% Alarm GAHH-661B = 40% NI-661A (UVIR)

Alarm in Main Control Room and shutdown Fired Heater

ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Alarm in Main Control Room

Alarm in Main Control Room Alarm in Main Control Room ESD-2 Shutdown immediately if two or more adjacent alarms are active at the same time or if a single alarm is active for 30 min.

Alarm in Main Control Room Alarm in Main Control Room

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Sendout Metering Station

Area 6

Power Distribution Center

Area 7

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

Activation of Hazard Control Equipment

Gas Detector

Sendout Metering Station

GD-660A

Pre-alarm GAH-660A = 20%

Alarm GAHH-660A = 40%

Gas Detector

Sendout Metering Station

GD-660B

Pre-alarm GAH-660B = 20%

Alarm GAHH-660B = 40%

Heat Detector

Sendout Metering Station

XHS-660A

--

XHA-660A Alarm = 165 deg F

Heat Detector

Sendout Metering Station

XHS-660B

--

XHA-660B Alarm = 165 deg F

Flame Detector

Sendout Metering Station

NS-660A

--

NI-660A (UVIR)

Flame Detector

Sendout Metering Station

NS-660B

--

NI-660B (UVIR)

Gas Detector

Switchgear House HVAC Intake

GD-662A

Pre-alarm GAH-662A = 20%

Alarm GAHH-662A = 40%

Gas Detector

Power Distribution Center

GD-662B

Pre-alarm GAH-662B = 20%

Alarm GAHH-662B = 40%

Heat Detector

Power Distribution Center

XHS-662A

--

XHA-662A Alarm = 165 deg F

Heat Detector

Power Distribution Center

XHS-662B

--

XHA-662B Alarm = 165 deg F

--

XNA-660

Ammonia Storage Tank Area

Area 7

Smoke Detector

Ammonia Storage Tank and Forwarding Pumps

XNS-660

Emergency Diesel Building

Area 7

Gas Detector

Emergency Diesel Building, HVAC Air Intake

GD-663

Heat Detector

Emergency Diesel Building

XHS-664

--

XHA-664 Alarm = 165 deg F

Smoke Detector

Emergency Diesel Building

XNS-661A

--

XNA-661A

Smoke Detector

Emergency Diesel Building

XNS-661B

--

XNA-661B

Gas Detector

Fire Pump House HVAC Air Intake

GD-664

Heat Detector

Fire Pump House

XHS-665

--

XHA-665 Alarm = 165 deg F

Smoke Detector

Fire Pump House

XNS-662A

--

XNA-662A

Smoke Detector

Fire Pump House

XNS-662B

--

XNA-662B

Fire Pump House

Area 7

Pre-alarm GAH-663 = 20%

Pre-alarm GAH-664 = 20%

Page 13

Alarm GAHH-663 = 40%

Alarm GAHH-664 = 40%

Alarm in Main Control Room

ESD-2 Shutdown immediately if both alarms in Sendout Metering Station are active at the same time or if a single alarm is active for 30 min.

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Utility Building

Area 7

Main Control Room

Deluge Pump House

Administration Building

Security Building

Area 7

Area 7

Area 8

Area 8

Date: 01/11/2008 Revision: 0

Area or Equipment Monitored

Type

Activation Point

Tag Number

GD-669

Pre-alarm GAH-669 = 20%

Activation of Hazard Control Equipment

Gas Detector

Utility Buiding HVAC Air Intake

Smoke Detector

Utility Building

XNS-665A

--

XNA-665A

Smoke Detector

Utility Building

XNS-665B

--

XNA-665B

High Sensitivity Smoke Detector

Electrical Equipment Room

XNHS-664

--

XNHA-664

Gas Detector High Sensitivity Smoke Detector

Building HVAC Air Intake Data Storage Room/DCS Room

GD-671 XNHS-665A

High Sensitivity Smoke Detector High Sensitivity Smoke Detector High Sensitivity Smoke Detector Smoke Detector

Control Room

XNHS-665B

--

XNHA-665B

UPS Room

XNHS-665C

--

XNHA-665C

Mech./Elec. Room

XNHS-665D

--

XNHA-665D

Corridor

XNS-669A

--

XNA-669A

Smoke Detector

Break Room

XNS-669B

--

XNA-669B

Smoke Detector

Lab

XNS-669C

--

XNA-669C

Gas Detector

Building HVAC Air Intake

Smoke Detector

Deluge Pumps

XNS-667A

--

XNA-667A

Smoke Detector

Deluge Pumps

XNS-667B

--

XNA-667B

Heat Detector

Deluge Pumps

XHS-667

--

Gas Detector

Building HVAC Air Intake

GD-668

Smoke Detector

Mech./Elec. Room

XNS-664A

--

XNA-664A

Smoke Detector

Lobby

XNS-664B

--

XNA-664B

Smoke Detector

Break Room

XNS-664C

--

XNA-664C

Gas Detector

East Entrance

GD-667

Smoke Detector

West Entrance

XNS-663

GD-670

Pre-alarm GAH-671 = 20% --

Pre-alarm GAH-670 = 20%

Pre-alarm GAH-668 = 20%

Pre-alarm GAH-667 = 20%

--

Page 14

Alarm GAHH-669 = 40%

Alarm GAHH-671 = 40% XNHA-665A

Alarm GAHH-670 = 40%

XHA-667 Alarm = 165 deg F Alarm GAHH-668 = 40%

Alarm GAHH-667 = 40%

XNA-663

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown HVAC Intake on HH Alarm in Main Control Room. ESD-2 Shutdown immediately if 2 or more adjacent alarms are active or if a single alarm is active for 30 min.

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown HVAC Intake on HH

Alarm in Main Control Room

Alarm in Main Control Room and Shutdown HVAC Intake on HH

Alarm in Main Control Room

Critical Energy Infrastructure Information

HAZARD DETECTOR EQUIPMENT LIST Document No. 07902-LI-600-001 Job Number: 07902 Project Name: Oregon LNG

Location

Fire Area

Maintenance Building/ Warehouse

Area 8

Date: 01/11/2008 Revision: 0

Type

Area or Equipment Monitored

Activation Point

Tag Number

GD-665

Pre-alarm GAH-665 = 20%

Activation of Hazard Control Equipment

Gas Detector

Building HVAC Air Intake

Heat Detector

Warehouse

XHS-663A

--

XHA-663A Alarm = 165 deg F

Heat Detector

Workshop

XHS-663B

--

XHA-663B Alarm = 165 deg F

Smoke Detector

Workshop

XNS-668A

--

XNA-668A

Smoke Detector

Warehouse

XNS-668B

--

XNA-668B

High Sensitivity Smoke Detector

Mech./Elec. Room

XNHS-663

--

XNHA-663

Page 15

Alarm GAHH-665 = 40%

Alarm in Main Control Room and Shutdown Ventilation on HH

Alarm in Main Control Room

Critical Energy Infrastructure Information

EMERGENCY RESPONSE MANUAL

Appendix C Oregon LNG Terminal Fire Control Matrix

February 4, 2008 DRAFT

Oregon LNG Warrenton, OR Firewater Equipment List

Job No. 07902 Doc No. 07902-LI-600-002, Rev: A Page 1 of 1

FIREWATER EQUIPMENT LIST By H H C H H

REV NUMBER: ISSUE PURPOSE: DATE: BY: CHECKED: APPROVED:

CH·IV International

A Issued for Client Review 1/14/08 RRV OOA AAR

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG Location/ Area Covered

14-Jan-08 Revision: A Type of Equipment

Tag Number

Capacity Required

Administration Building (A-804)

Automatic Sprinkler System

N/A

845 gpm

Maintenance Building / Warehouse (A-805)

Automatic Sprinkler System

N/A

2550 gpm

Compressor Building (A-820)

Automatic Sprinkler System

N/A

2420 gpm

Fire Pump House (A-860)

Automatic Sprinkler System

N/A

703 gpm

Emergency Diesel Generator Building (A-850)

Automatic Sprinkler System

N/A

248 gpm

Security Building (A-803)

Automatic Sprinkler System

N/A

252 gpm

Deluge Pump House (A-861)

Automatic Sprinkler System

N/A

424 gpm

Deluge System

N/A

9,200 gpm

Deluge System

N/A

10,500 gpm

N/A

9200 gpm

07902-PI-600-404 Tank 201A 07902-PI-600-404 Tank 201B 07902-PI-600-404 Tank 201C

Deluge System

Discharge Conditions

Activation Capabilities

Activates automatically by fusible link type sprinklers on high temperatures. Activates automatically by 0.2 gpm/ft2 fusible link type sprinklers on high temperatures. Activates automatically by 0.3 gpm/ft2 fusible link type sprinklers on high temperatures. Activates automatically by 0.25 gpm/ft2 fusible link type sprinklers on high temperatures. Activates automatically by 0.25 gpm/ft2 fusible link type sprinklers on high temperatures. Activates automatically by 0.1 gpm/ft2 fusible link type sprinklers on high temperatures. Activates automatically by 0.25 gpm/ft2 fusible link type sprinklers on high temperatures. Manually activated by plant 2 0.1 gpm/ft personnel Manually activated by plant 2 0.1 gpm/ft personnel Manually activated by plant 2 0.1 gpm/ft personnel 0.1 gpm/ft2

1

07902-PI-600-402 Grid D-1

Fire Hydrant (2-way with 2- /2" hose connections).

FH-600

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-601

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid F-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-602

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid F-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-603

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid G-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-604

N/A

100 psig

Manually activated by plant personnel

Page 2

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG Location/ Area Covered

14-Jan-08 Revision: A Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

07902-PI-600-402 Grid H-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-605

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-2

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-606

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-3

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-607

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid G-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-608

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid G-2

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-609

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid F-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-610

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid F-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-611

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-612

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-3

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-613

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-2

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-614

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid D-3

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-615

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid D-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-616

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid D-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-617

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid D-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-618

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-619

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-620

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-621

N/A

100 psig

Manually activated by plant personnel

Page 3

Activation Capabilities

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG Location/ Area Covered

14-Jan-08 Revision: A Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

07902-PI-600-402 Grid E-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-622

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-623

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-624

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-625

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-626

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-627

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-628

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-629

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-630

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid E-7

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-631

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-7

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-632

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-7

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-633

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-634

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-635

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-636

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-637

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-638

N/A

100 psig

Manually activated by plant personnel

Page 4

Activation Capabilities

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG

14-Jan-08 Revision: A

Location/ Area Covered

Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

07902-PI-600-402 Grid G-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-639A

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid H-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-639B

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-7

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-641

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-642

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-6

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-643

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-644

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-645

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-646

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-5

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-647

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid C-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-648

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-4

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-649

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-2

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-650

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-2

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-651

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid B-1

Fire Hydrant (2-way with 2-1/2" hose connections)

FH-652

N/A

100 psig

Manually activated by plant personnel

07902-PI-600-402 Grid D-1

1

150 foot 2- /2" hose reel

FR-600

Page 5

N/A

N/A

Activation Capabilities

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG

14-Jan-08 Revision: A

Location/ Area Covered

07902-PI-600-402 Grid G-1

07902-PI-600-402 Grid H-3

07902-PI-600-402 Grid F-4

Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

Activation Capabilities

1

FR-604

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-607

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-610

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

07902-PI-600-402 Grid F-4

150 foot 2- /2" hose reel

FR-611

07902-PI-600-402 Grid E-3

150 foot 2-1/2" hose reel

FR-613

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid C-4

150 foot 2-1/2" hose reel

FR-616

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid E-4

150 foot 2-1/2" hose reel

FR-619

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid E-5

150 foot 2-1/2" hose reel

FR-620

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

Page 6

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG

14-Jan-08 Revision: A

Location/ Area Covered

07902-PI-600-402 Grid E-5

07902-PI-600-402 Grid E-6

07902-PI-600-402 Grid E-6

Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

Activation Capabilities

1

FR-623

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-626

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-629

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

07902-PI-600-402 Grid E-7

150 foot 2- /2" hose reel

FR-631

07902-PI-600-402 Grid H-7

150 foot 2-1/2" hose reel

FR-632

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid H-7

150 foot 2-1/2" hose reel

FR-633

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid H-6

150 foot 2-1/2" hose reel

FR-634

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid H-6

150 foot 2-1/2" hose reel

FR-635

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

Page 7

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG

14-Jan-08 Revision: A

Location/ Area Covered

07902-PI-600-402 Grid H-6

07902-PI-600-402 Grid H-6

07902-PI-600-402 Grid H-5

Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

Activation Capabilities

1

FR-636

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-637

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-638

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

07902-PI-600-402 Grid H-5

150 foot 2- /2" hose reel

FR-639B

07902-PI-600-402 Grid C-7

150 foot 2-1/2" hose reel

FR-641

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid C-6

150 foot 2-1/2" hose reel

FR-642

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid C-6

150 foot 2-1/2" hose reel

FR-643

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

07902-PI-600-402 Grid B-5

150 foot 2-1/2" hose reel

FR-645

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

Page 8

FIREWATER EQUIPMENT LIST Document No. 07902-LI-600-002 Job Number: 07902 Project Name: Oregon LNG

14-Jan-08 Revision: A

Location/ Area Covered

07902-PI-600-402 Grid D-5

07902-PI-600-402 Grid B-2

Type of Equipment

Tag Number

Capacity Required

Discharge Conditions

Activation Capabilities

1

FR-647

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-650

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

1

FR-651

N/A

N/A

Hose reel pre-connected to hydrant, with additional 2-1/2 inch collapsible hoses provided in the same location.

FM-602

N/A

100 psig

FM-611

N/A

100 psig

FM-639A

N/A

100 psig

FM-639B

N/A

100 psig

FM-647

N/A

100 psig

150 foot 2- /2" hose reel

150 foot 2- /2" hose reel

07902-PI-600-402 Grid B-2

150 foot 2- /2" hose reel

07902-PI-600-402 Grid F-1 07902-PI-600-402 Grid F-4 07902-PI-600-402 Grid H-5 07902-PI-600-402 Grid G-4 07902-PI-600-402 Grid C-5

500 gpm Fire Monitor, Remote Operated, Hydrant Mounted 500 gpm Fire Monitor, Remote Operated, Hydrant Mounted 1000 gpm Fire Monitor, Remote Operated and Elevated 1000 gpm Fire Monitor, Remote Operated and Elevated 500 gpm Fire Monitor, Remote Operated, Hydrant Mounted

Page 9

Manually activated and controlled by plant personnel Manually activated and controlled by plant personnel Manually activated and controlled by plant personnel Manually activated and controlled by plant personnel Manually activated and controlled by plant personnel

Oregon LNG Warrenton, OR Dry Chemical, CO2, and High Expansion Foam Equipment List

Job No. 07902 Doc No. 07902-LI-600-003, Rev: A Page 1 of 1

DRY CHEMICAL, CO2, AND HIGH EXPANSION FOAM EQUIPMENT LIST By H H C H H

REV NUMBER: ISSUE PURPOSE: DATE: BY: CHECKED: APPROVED:

CH·IV International

A Issued for Client Review 12/31/07 RRV OOA AAR

DRY CHEMICAL AND HIGH EXPANSION FOAM EQUIPMENT LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location/ Area Covered

Date: 12/31/2007 Revision: A

Type of System

Tag Number

Manufacturer

Model Number

System Size

Discharge Conditions

Unloading Platform (See 07902-PI-620-421)

Dry Chemical System

FL-610

Ansul or equivalent

S-3000 or equivalent

Minimum of 0.013 To Be Determined in lb/s/ft2 to control fire Final Design hazards

Remote Manual and Local Manual

Compressor Building (A-820) (See 07902-PI-620-422)

Dry Chemical System

FL-624

Ansul or equivalent

S-3000 or equivalent

Minimum of 0.013 To Be Determined in lb/s/ft2 to control fire Final Design hazards

Remote Manual and Local Manual

HP Pump Area (See 07902-PI-620-423)

Dry Chemical System

FL-631

Ansul or equivalent

S-3000 or equivalent

Minimum of 0.013 To Be Determined in lb/s/ft2 to control fire Final Design hazards

Remote Manual and Local Manual

LNG Tank T-201A PSV Outlet (See 07902-PI-200-107-01, Diagram 107-01-01)

Dry Chemical System

FL-620A

Ansul or equivalent

S-3000 or equivalent

Minimum of 1 To Be lb/s/mmscfd to control Determined in the natural gas hazard Remote Manual Final Design during tank pressure relief events

LNG Tank T-201B PSV Outlet (See 07902-PI-200-107-02, Diagram 107-02-01)

Dry Chemical System

FL-620B

Ansul or equivalent

S-3000 or equivalent

Minimum of 1 lb/s/mmscfd to control To Be Determined in the natural gas hazard Remote Manual Final Design during tank pressure relief events

LNG Tank T-201C PSV Outlet (See 07902-PI-200-107-03, Diagram 107-03-01)

Dry Chemical System

FL-620C

Ansul or equivalent

S-3000 or equivalent

Minimum of 1 lb/s/mmscfd to control To Be Determined in the natural gas hazard Remote Manual Final Design during tank pressure relief events

LNG Spill Containment (S-606) (See 07902-PI-640-441)

High Expansion Foam System

FL-641

Ansul or equivalent

Jet-X High Minimum of 5 ft of Expansion To Be foam over the sump Foam Determined in surface area in 1 Generator or Final Design minute equivalent

Page 2

Activation Capabilities

Remote Manual and Local Manual

DRY CHEMICAL EXTINGUISHER LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location / Area Covered

Unloading Platform Unloading Platform Unloading Platform Pier Pier Pier Pier Pier LNG Storage Tank T-201A Pipe Rack LNG Storage Tank T-201A Pump Platform LNG Storage Tank T-201B Pipe Rack LNG Storage Tank T-201B Pump Platform LNG Storage Tank T-201C Pipe Rack LNG Storage Tank T-201C Pump Platform Pier/Shore Interface Pipe Rack Between LNG Tanks and HP Pumps Spill Containment Sump Area Gas Make Up Vaporizer Area Vapor Return Blower Area BOG Compressors BOG Compressors HP Pumps Area HP Pumps Area HP Pumps Area

Date: 12/31/2007 Revision: A Drawing / Grid

Manufacturer

07902-DG-610-442 Grid E-1 07902-DG-610-442 Grid E-1 07902-DG-610-442 Grid F-1 07902-DG-610-442 Grid E-1 07902-DG-610-442 Grid E-3 07902-DG-610-442 Grid D-5 07902-DG-610-442 Grid D-4 07902-DG-610-442 Grid C-7 07902-DG-620-452 Grid D-1 07902-DG-620-452 Grid D-1 07902-DG-620-452 Grid D-2 07902-DG-620-452 Grid D-2 07902-DG-620-452 Grid D-3 07902-DG-620-452 Grid D-3 07902-DG-620-452 Grid D-1 07902-DG-620-452 Grid D-4 07902-DG-620-452 Grid D-4 07902-DG-620-452 Grid D-5 07902-DG-620-452 Grid D-5 07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid D-6

Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Page 3

Extinguisher Type

Extinguisher Size (Dry Chemical Capacity)

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Wheeled

300 lb

Hand Held

27 lb

Wheeled

300 lb

Hand Held

27 lb

Wheeled

300 lb

Hand Held

27 lb

Wheeled

300 lb

Wheeled

300 lb

Wheeled

300 lb

Wheeled

300 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Wheeled

300 lb

Hand Held

27 lb

Hand Held

27 lb

DRY CHEMICAL EXTINGUISHER LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location / Area Covered

HP Pumps Area HP Pumps Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area First Stage Vaporizers Area Auxiliary Building Fired Heater

Date: 12/31/2007 Revision: A Drawing / Grid

Manufacturer

07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid D-6 07902-DG-620-452 Grid E-6 07902-DG-620-452 Grid E-6 07902-DG-620-452 Grid F-6 07902-DG-620-452 Grid F-6 07902-DG-620-452 Grid E-6 07902-DG-620-452 Grid E-6 07902-DG-620-452 Grid E-6 07902-DG-620-452 Grid F-6 07902-DG-620-452 Grid F-6 07902-DG-620-452 Grid G-6 07902-DG-620-452 Grid G-6

Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent

Page 4

Extinguisher Type

Extinguisher Size (Dry Chemical Capacity)

Hand Held

27 lb

Hand Held

27 lb

Wheeled

300 lb

Wheeled

300 lb

Wheeled

300 lb

Wheeled

300 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Wheeled

300 lb

Hand Held

27 lb

DRY CHEMICAL EXTINGUISHER LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location / Area Covered

Fuel Gas Area Second Stage Vaporizers Area Ammonia Storage Tank Area Emergency Diesel Generator Firewater Tank Area Fire Pump House Deluge Pump House

Date: 12/31/2007 Revision: A Drawing / Grid

Manufacturer

07902-DG-620-452 Grid G-6 07902-DG-620-452 Grid G-6 07902-DG-620-452 Grid G-6 07902-DG-620-452 Grid D-7 07902-DG-620-452 Grid D-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid B-6

Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent

Page 5

Extinguisher Type

Extinguisher Size (Dry Chemical Capacity)

Wheeled

300 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

Hand Held

27 lb

CO2 EXTINGUISHER LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location / Area Covered

Platform Control Room Platform Control Room Power Distribution Center Power Distribution Center Power Distribution Center Power Distribution Center Power Distribution Center Power Distribution Center Main Control Room Main Control Room

Date: 12/31/2007 Revision: A Drawing / Grid

Manufacturer

07902-DG-610-442 Grid F-1 07902-DG-610-442 Grid F-1 07902-DG-620-452 Grid F-7 07902-DG-620-452 Grid F-7 07902-DG-620-422 Grid F-7 07902-DG-620-452 Grid F-7 07902-DG-620-452 Grid F-7 07902-DG-620-452 Grid F-7 07902-DG-620-452 Grid C-5 07902-DG-620-452 Grid C-6

Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent

Page 6

Extinguisher Type

Extinguisher Size (Capacity)

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

Hand Held

20 lb

PORTABLE FIRE EXTINGUISHER (ABC) LIST Document No. 07902-LI-600-003 Job Number: 07902 Project Name: Oregon LNG Location / Area Covered

Maintenance Building/Warehouse Maintenance Building/Warehouse Maintenance Building/Warehouse Security Building Administration Building Administration Building Administration Building Utility Building

Date: 12/31/2007 Revision: A Drawing / Grid

Manufacturer

07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid C-7 07902-DG-620-452 Grid B-7 07902-DG-620-452 Grid B-6

Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent Ansul or equivalent

Page 7

Extinguisher Type

Extinguisher Size (Capacity)

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

Hand Held

10 lb

EMERGENCY RESPONSE MANUAL

Appendix D Oregon LNG Terminal Fire Control Plot Plans

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix E Oregon LNG Terminal Regulatory Agency Emergency Notification Summary

TO BE INCLUDED IN FINAL VERSION OF EMERGENCY RESPONSE PLAN

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix F Oregon LNG Terminal Emergency Response Procedures

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Contents LNG Spills and Flammable Gas Leaks Emergency Response Procedure Fire Emergency Response Procedure Structural Failure of an LNG Storage Tank Emergency Response Procedure Collapse of Buildings, Systems or Equipment Emergency Response Procedure Loss of Electrical Power Emergency Response Procedure LNG Carrier Departure Emergency Response Procedure Vehicle Accidents Emergency Response Procedure Breaches of Site Security Emergency Response Procedure Bomb Threat or Discovery of an Explosive Device Emergency Response Procedure

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure LNG and Flammable Gas Leaks

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LNG AND FLAMMABLE GAS LEAKS

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

4

4

RESPONSIBILITY

4

5

SCOPE OF RESPONSE

4

5.1 Controllable Emergency

4

5.2 Uncontrollable Emergency

5

6

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LNG AND / OR FLAMMABLE VAPOR LEAK

5

6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

6

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LNG AND FLAMMABLE GAS LEAKS

1

INTRODUCTION

A release of LNG and / or flammable, natural gas vapor from process equipment and piping is an emergency condition. If the flammable gas is mixed with sufficient air and confined in a building or other enclosure, it can be explosive. However, if the gas is in the open air and is not confined, it will merely burn if ignited. The release of gas, whether indoors or outdoors is a dangerous event and must be treated as such. The Oregon LNG Terminal incorporates features that are designed to minimize leaks of flammable products. Features have been included in the design to contain LNG spills and also to minimize flammable vapor formation resulting from LNG spills. Spill containment is essential in preventing the spill material from escaping the facility or spreading over a large area. Keeping a spill contained can minimize the effort, time, and expense in spill remediation. Flammable gas detectors and low temperature detectors will alert Terminal Personnel to leaks within buildings or within process areas. In many cases, the detection of a LNG or flammable gas leak will also result in the automatic initiation of a sequence of events that will isolate equipment and systems to reduce the size of the leak. An LNG and / or flammable gas release at the Terminal will be categorized by the Emergency Director as: •

A controllable emergency condition in which the Terminal Operations personnel can prevent harm to personnel or equipment by taking reasonable and prudent actions to ensure the Terminal is in a safe condition.



An uncontrollable emergency condition in which the Terminal Operations personnel cannot prevent harm to personnel or equipment by taking reasonable and prudent actions to maintain the Terminal in a safe condition

The purpose of this procedure is to detail the sequence of actions to be taken by Terminal Personnel in the event of an LNG and / or flammable gas leak at the Terminal that has, or has the potential to result in a controllable or uncontrollable emergency.

2 APPLICABILITY This procedure must be followed in response to all LNG and / or flammable gas leak events and applies to all Terminal personnel, contractors, and visitors.

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LNG AND FLAMMABLE GAS LEAKS 3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for responding to LNG and / or flammable gas leaks situations. This Procedure is designed to comply with the following: •

National Fire Protection Association (NFPA)



NFPA 30, Flammable and Combustible Liquids Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG)

4 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this Procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Emergency Response Plan and implementing this Procedure in response to a LNG and / or flammable gas leak event.

5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Emergency Response Team Leader and determine the classification of a LNG and / or flammable vapor leak emergency situation. The following actions will be taken accordingly.

5.1

Controllable Emergency The Emergency Response Team will implement the actions detailed in Section 6 of this Procedure. The Terminal Emergency Director will instruct the Public Informational Contact to notify Local Fire Department to request their support, if required.

4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LNG AND FLAMMABLE GAS LEAKS 5.2

Uncontrollable Emergency The Emergency Response Team will implement the actions detailed in Section 6 of this Procedure. The Terminal Emergency Director will instruct the Public Information Contact to notify the following emergency organizations, if required: •

Local Fire Department;



Oregon State Police and County Sheriff’s Office; and



State Fire Marshall’s Office.

If the Terminal Emergency Director classifies the Uncontrollable Emergency as a General Emergency, the Terminal Emergency Director will instruct the Public Information Contact to notify the following organizations as required: •

Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LNG AND / OR FLAMMABLE VAPOR LEAK 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a fire situation. •

Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor ignites;

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LNG AND FLAMMABLE GAS LEAKS

6.2



Coordinate the off–site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of LNG and flammable vapor leaks; and



Consult with the Terminal Emergency Director

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment to cut off supply to the leak emergency;



Remove the ignition source of power to the process equipment from the remote source location if deemed safe;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Fire

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE FIRE

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

4

5

SCOPE OF RESPONSE

4

5.1 Controllable Emergency

4

5.2 Uncontrollable Emergency

4

6

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A FIRE SITUATION

5

6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

5

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE FIRE

1

INTRODUCTION

The Oregon LNG Terminal incorporates features that are designed to minimize the occurrence of fires and also features that will contain the spread of fires if they occur. The design also includes features that will alert Terminal Personnel to fires detected within buildings or within process areas. In many cases, the detection of fires will also result in the automatic initiation of a sequence of events that will isolate sources of the fire and also initiate fire fighting systems. A fire at the Terminal will be categorized by the Emergency Director as: •

A controllable emergency condition in which the Terminal Operations personnel can prevent harm to personnel or equipment by taking reasonable and prudent actions to ensure the Terminal is in a safe condition.



An uncontrollable emergency condition in which the Terminal Operations personnel cannot prevent harm to personnel or equipment by taking reasonable and prudent actions to maintain the Terminal is in a safe condition

The purpose of this procedure is to detail the sequence of actions to be taken by Terminal Personnel in the event of a fire at the Terminal that has, or has the potential to result in a controllable or uncontrollable emergency.

2 APPLICABILITY This procedure must be followed in response to all fire events regardless of size and applies to all Terminal personnel, contractors, and visitors.

3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for responding to fire situations. This Procedure is designed to comply with the following: •

National Fire Protection Association (NFPA)



NFPA 30, Flammable and Combustible Liquids Code



NFPA 472, Standard for Professional Competence of Responders to Hazardous Materials Incidents.



NFPA 600, Industrial Fire Brigades

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE FIRE 4 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this Procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Emergency Response Plan and implementing this Procedure in response to a fire event.

5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Emergency Response Team Leader and determine the classification of a fire emergency situation. The following actions will be taken accordingly.

5.1

Controllable Emergency The Emergency Response Team will implement the actions detailed in Section 6Error! Reference source not found. of this Procedure. Since the Terminal personnel are only trained to fight particular fires, the Terminal Emergency Director will instruct the Public Information Contact to notify the Local Fire Department to request their support, if required.

5.2

Uncontrollable Emergency The Emergency Response Team will implement the actions detailed in Section 6 of this Procedure. Since the Terminal personnel are only trained to fight particular fires, the Terminal Emergency Director will instruct the Public Information Contact to notify the following emergency organizations, if required: •

Local Fire Department;



Oregon State Police and County Sheriff’s Office; and



State Fire Marshall’s Office.

If the Terminal Emergency Director classifies the Uncontrollable Emergency as a General Emergency, the Terminal Emergency Director will instruct the Public Information Contact to notify the following organizations as required: •

Office of Homeland Security, Emergency Preparedness; 4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE FIRE •

United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A FIRE SITUATION 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a fire situation.

6.2



Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit additional property damage;



Coordinate the off–site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of flammable gas and liquid leaks; and



Consult with the Terminal Emergency Director

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment to cut off fuel supply;



Remove all electrical hazards by isolating power sources;



Remove all personnel to safe locations and assist in rescue activities as required.



Operate fixed fire suppression systems and equipment



Operate mobile and portable fire suppression equipment and systems

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE FIRE •

Provide other assistance as needed and as training permits.

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Structural Failure of an LNG Tank

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK

Table of Contents Section

Page

1

INTRODUCTION

3

2

CODES AND STANDARDS

3

3

GENERAL DESCRIPTION

3

4

HAZARD DETECTION AND MITIGATION

4

5

RESPONSIBILITY

5

6

SCOPE OF RESPONSE

5

6.1 Controllable Emergency

5

6.2 Uncontrollable Emergency

5

7

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LNG AND / OR FLAMMABLE VAPOR RELEASE CAUSED BY A STRUCTURAL FAILURE OF AN LNG STORAGE TANK.6 7.1 Emergency Response Team Leader

6

7.2 Emergency Response Team Members

6

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK

1

INTRODUCTION

The Oregon LNG Import Terminal is designed with 3x 160,000m³ (cubic meter) capacity full containment LNG storage tanks. These Full Containment Tanks will also be located within a diked area that will be capable of containing the contents of one full tank. The purpose of this procedure is to provide guidance for mitigating the environmental impact of an accidental release of LNG from a storage tank failure.

2 CODES AND STANDARDS THE CODES AND INDUSTRY STANDARDS REFERENCED HEREIN ARE AS FOLLOWS: API STD 620-96, “Design and Construction of Large, Welded, Low-Pressure Storage Tanks” API 620 Appendix L, API 650 Appendix E “ Earthquake loads of flat bottomed, and vertically oriented storage tanks” WOZNIAK, R.S. AND MITCHELL, V.W “Basis of Seismic Design Provisions for Welded Steel Storage Tanks” (Ref: API 1978 Proceedings - Refinery Department) AMERICAN SOCIETY OF CIVIL ENGINEERS (ASCE) “Guidelines for Seismic Evaluation and Design of Petrochemical Facilities” NATIONAL FIRE PROTECTION ASSOCIATION NFPA 59A 2001 Edition

3 GENERAL DESCRIPTION The primary purpose of the Oregon LNG Import Terminal is to receive, store, and send out revaporized LNG via the high pressure transmission pipeline. There are four hazards resulting from LNG product handling, or exposure; cryogenic temperatures, dispersion characteristics, stratification due to changes in product density, and flammability. Revaporized LNG, or the boil off from Liquefied Natural Gas (LNG) is colorless, and odorless, and creates an asphyxiation hazard because it can displace the air in a given area. LNG, depending on its origin, has a clear range of heating values and density, which make up its composition. The composition, and heating values of each delivery cargo are identified on the delivery documentation. 3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK LNG carriers transport the cold (-260°F) LNG to import base load facilities such as the Oregon LNG Import Terminal where the liquid is off loaded, and stored in Insulated Cryogenic Storage Tanks awaiting delivery to the downstream customers via an offsite high pressure pipeline system.

4 HAZARD DETECTION AND MITIGATION There are several ways structural failure of an LNG tank could occur; construction defects, quality control deficiencies, or other phenomenon normally associated with developing, and building a new import terminal, however the reason many tanks fail is due to a phenomenon known as roll over. During storage, care must be taken to insure the density of the liquids being stored does not begin to cause stratification within the tanks. Normally delivered cargos will not remain inside of the storage tanks long enough to begin to stratify, however in the event of an emergency condition, caused by equipment failure, or system component failure, where the facility is not able to unload the stored LNG in a timely manner, or long periods occur between cargo delivery stratification of the product inside the storage tank could possibly create conditions that could allow stratification to occur. The definition of “ roll- over” is the thermodynamic phenomenon occurring when a heavier layer of LNG is stratified beneath a lighter layer. The lower layer slowly decreases in density as heat is added, expanding it while the upper layer can conceivably increase in density as the methane boils-off. When the two layers begin to mix the resulting mixing can cause violent turbulence inside of the storage tank with large volumes of vapor and could lead to damage, or failure of equipment and components. Since the only known case of tank damage from roll-over in Europe, several improvements to operating procedures have become industry standard, and help to prevent roll over from occurring. One such improvement is the installation of temperature, and density monitoring equipment inside of the storage tanks that visually displays the temperature at different levels giving operations system personnel indications that stratification may be occurring. At the Oregon LNG Terminal site an RTD temperature reading system will be used to read the temperature range in the walls, floor, and suspended deck of each LNG storage tank. If stratification is detected, and layers are believed to have formed, the operations personnel will be trained to detect stratification if it begins to occur and how to control it if it is detected by recalculating the product within the tank to mix it by pumping the bottom layer into the top of the tank. An understanding of the basic characteristics of LNG; pressure, temperature, density and heat transfer are necessary in order that the

4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK delivery product can be stored safely, and eliminate the possibility of roll over and damage to facility components.

5 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this procedure is administered as written. The Emergency Response Team leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Emergency Response Plan and implementing this procedure in response to a LNG tank structural failure.

6 SCOPE OF RESPONSE The terminal Emergency Director will consult with the Emergency Response Team Leader and determine the classification of a LNG and / or flammable vapor release, and the possible steps necessary to mitigate damage to equipment, systems, environment, or other components.

6.1

Controllable Emergency Unless otherwise stipulated elsewhere, the Emergency Response Team Leader will implement the actions detailed in Section 7 of this Procedure. The Terminal Emergency Director will instruct the public informational contact person to call 911 and the 911 operator will notify the appropriate agencies regarding the emergency.

6.2

Uncontrollable Emergency Unless otherwise stipulated elsewhere the Emergency Response Team Leader will implement the actions detailed in Section 7 of this procedure. The Terminal Emergency Director will instruct the Public Information Contact person to notify the appropriate authorities. If the Terminal Emergency Director classifies the Uncontrollable Emergency as a General Emergency, the Terminal Emergency Director will instruct the Public Information Contact person to notify the following organizations as required: •

Call 911 5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK 7 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LNG AND / OR FLAMMABLE VAPOR RELEASE CAUSED BY A STRUCTURAL FAILURE OF AN LNG STORAGE TANK. 7.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a structural failure of an LNG storage Tank

7.2



Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor ignites;



Coordinate the off–site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of LNG and flammable vapor leaks; and



Consult with the Terminal Emergency Director



Insure that any requests for mutual aid are handled properly.

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment, or systems to cut off supply to the leak;



Remove the ignition source of power to the process equipment from the remote source location if deemed safe to do;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems, or other firefighting equipment to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL FAILURE OF AN LNG TANK •

Provide feed- back to the Emergency Response Team Leader to insure the proper current information is available;



Report and monitor the condition of the emergency until the escaping product is contained.

7

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Collapse of Buildings, Systems or Equipment

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE COLLAPSE OF BUILDINGS, SYSTEMS, OR EQUIPMENT

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

3

5

SCOPE OF RESPONSE

4

5.1 Controllable Emergency

4

5.2 Uncontrollable Emergency

5

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE COLLAPSE OF BUILDINGS, SYSTEMS, OR EQUIPMENT

1

INTRODUCTION

The Oregon LNG Import Terminal includes several buildings, structures, and equipment that are used for many purposes. Although all buildings, structures, and equipment have been designed, and built in accordance with appropriate standards, there may be situations in which the integrity of a building or other structure, or equipment becomes compromised or fails completely. The purpose of this procedure is to define the actions to be taken in the event a collapse of building(s), structures, or equipment occurs.

2 APPLICABILITY This procedure shall be implemented by the Terminal Emergency Director at any time there is a likelihood of a collapse or possibility of a collapse of a building, structure, or equipment at the Oregon LNG Facility.

3 REGULATORY BACKGROUND Federal, state, and local agencies and proven industrial standards regulate and provide guidance for construction of LNG Terminal Buildings, Systems, and Equipment; National Fire Protection Association (NFPA) •

NFPA 30, Flammable and Combustible Liquid’s Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG) 49 §CFR 193



33 §CFR 127

4 RESPONSIBILITY The Oregon LNG Terminal Emergency Director is responsible for ensuring that this procedure is implemented whenever there is (or is a likelihood of) a building, structure, or equipment collapse.

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE COLLAPSE OF BUILDINGS, SYSTEMS, OR EQUIPMENT 5 SCOPE OF RESPONSE The Terminal Emergency Director will determine the classification of any emergency situation. The following actions will be taken accordingly. The Emergency Response Team Leader will implement the actions detailed in this Procedure as required to safeguard the terminal personnel, and property.

5.1

Controllable Emergency EMERGENCY RESPONSE TEAM LEADER The following describes the key roles and responsibilities of the Emergency Response Team Leader during a building, or equipment collapse, or equipment failure. •

Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event That flammable vapor ignites;



Coordinate the off site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of LNG and flammable vapor leaks; and



Consult with the Terminal Emergency Director

EMERGENCY RESPONSE TEAM MEMBERS At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment to cut off supply of any leak emergency;



Remove ignition sources;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE COLLAPSE OF BUILDINGS, SYSTEMS, OR EQUIPMENT 5.2

Uncontrollable Emergency EMERGENCY RESPONSE TEAM LEADER The following describes the key roles and responsibilities of the Emergency Response Team Leader during a building, or equipment collapse, or system failure. •

Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor ignites;



Coordinate the off site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of LNG and flammable vapor leaks; and



Consult with the Terminal Emergency Director

EMERGENCY RESPONSE TEAM MEMBERS At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment to cut off supply to any leak emergency;



Remove ignition sources;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Loss of Electrical Power

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LOSS OF ELECTRICAL POWER

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

4

5

SCOPE OF RESPONSE

4

5.1 Controllable Emergency

4

5.2 Uncontrollable Emergency

4

6

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LOSS OF ELECTRICAL POWER;

5

6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

5

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LOSS OF ELECTRICAL POWER

1

INTRODUCTION

The Oregon LNG Import Terminal will be powered from two, 115kV lines fed from either the Warrenton Substation, owned by Pacific Power, or the Clatsop Substation, owned by the Bonneville Power Administration (BPA). The 115kV power lines will be carried on an overhead line from the respective substation to two 100% capacity dedicated onsite 115kV/13.8kV step-down transformers. The Import Terminal design includes a standby diesel powered generator (G-502), which will be connected to the 4160V bus and will be used when the normal power supply has failed. G-502 has been sized to power non-process loads, i.e., non-motor loads, plus one in-tank LP LNG pump. Essential and emergency loads will be powered from UPS systems.

2 APPLICABILITY This procedure must be followed in response to all loss of power occurrences at the Oregon LNG Terminal.

3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for electrical service and personnel safety around electrical components. The standards noted herein are the standards used industry wide for new construction of hazardous or flammable gas handling terminals: •

(NEC) National Electrical Code



33CFR Part 127



49CFR Part 193



National Fire Protection Association (NFPA)



NFPA 30, Flammable and Combustible Liquids Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG)



OSHA

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LOSS OF ELECTRICAL POWER 4 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Terminal Emergency Director is responsible for initiating the Emergency Response Plan and implementing this procedure in response to a loss of electrical power event.

5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Terminal Manager, or designated incident scene commander to determine the status of a loss of electrical power, and what if any response protocol should be initiated. The following actions will be taken accordingly.

5.1

Controllable Emergency The Emergency Response Team will implement the actions detailed in this procedure. The Terminal Emergency Director will instruct the Public Information Contact person to notify the local authorities by calling emergency 911 if required.

5.2

Uncontrollable Emergency The Emergency Response Team will implement the actions detailed in this procedure. The Terminal Emergency Director will instruct the Public Information Contact person to notify the following emergency organizations through calling emergency 911, if required: •

Local Fire Department;



Oregon State Police and County Sheriff’s Office;



State Fire Marshall’s Office; and



Local Ambulance Services, or local Hospital

If the Terminal Emergency Director classifies the Uncontrollable Emergency as a General Emergency, the Terminal Emergency Director will instruct the Public 4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LOSS OF ELECTRICAL POWER Information Contact person to notify the following organizations through calling emergency 911: •

Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A LOSS OF ELECTRICAL POWER; 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a loss of electrical power situation.

6.2



Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor is released, or ignites;



Coordinate any off–site emergency response organizations and provide advice as needed;



Control all possible ignition sources; and



Consult with the terminal emergency director.

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: •

Secure valves, pumps, or other process equipment to cut off supply to any leak emergency; 5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE LOSS OF ELECTRICAL POWER •

Insure that the emergency generator is on line and providing needed electrical power;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control any flammable vapor formation; and



Provide other assistance as needed and as training permits.

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure LNG Carrier Departure

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

4

5

SCOPE OF RESPONSE

4

5.1 Controllable Ship Departure Emergency

6

4

5.1.1 Ship Emergency

4

5.1.2 Terminal Emergency

5

5.2 Uncontrollable Emergency

6

5.2.1 Ship Emergency – Actions to be Taken By Ship Master

6

5.2.2 Terminal Emergency – Actions to be Taken By Emergency Team Leader

6

EMERGENCY RESPONSE TEAM ACTIONS

7

6.1 Emergency Response Team Leader

7

6.2 Emergency Response Team Members

7

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE

1

INTRODUCTION

Once an LNG carrier has been securely moored at the LNG unloading berth the ship’s cargo control officer, and the designated terminal person in charge (PIC) will go through an examination process known as the pre transfer conference. In this pre transfer conference issues that may affect the ships ability to obtain the required discharge rate are identified. The cargo control officer and the person in charge (PIC) shall insure that all of the terminal and ship delivery systems are working properly and ready to be put into operation. Because of the nature of the cargo transfer process required for handling LNG, an unexpected emergency situation could arise at any moment either shipboard, or on the terminal that in the opinion of the master would necessitate immediate departure of the carrier from the berth. The master of the carrier is ultimately responsible for the safety of his ship, and although he has an obligation to coordinate arrival, and departure activities with the terminal, the final decision regarding moving the carrier from the mooring berth rests solely with the master. (Note: In most circumstances a carrier will require a minimum of one hour before it is ready to move under its own power).

2 APPLICABILITY This procedure must be followed in response to any unexpected emergency where the master of the carrier, or the terminal representative (PIC) deems it necessary that the carrier must immediately depart the mooring berth.

3 REGULATORY BACKGROUND Federal agency, U.S. Coast Guard, and other industry standards provide guidance for emergency departure of an LNG carrier from its location once it enters or is moored in restricted waters. Listed herein are the standards that apply: •

U.S. Coast Guard Marine Safety Office (MSO).



Waterway Suitability Assessment for the Columbia River



Oil Companies International Maritime Forum (OCIMF)



Society of International Gas Tankers, and Terminals Operators (SIGTTO)



International Maritime Organization (IMO)



33 CFR Part 127 3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE 4 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this procedure is administered as written. The emergency response team Leader, or the designated incident commander is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the emergency response plan and implementing this procedure in response to any situation where the carrier must depart the mooring berth in an unexpected emergency where remaining at the berth may cause further damage to the terminal, or carrier.

5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Emergency Response Team Leader and determine what further action if any is required. The following actions will be taken accordingly.

5.1

Controllable Ship Departure Emergency If the master feels that in order to protect the integrity of his carrier or personnel, or to prevent further damage to the ship, its crew, or terminal resources he may decide it is necessary for the ship to immediately depart from the Import Terminal. This could be directly caused by either an emergency situation arising at the terminal, or on board the ship. Once this decision is made the master will immediately order his carrier to make emergency preparations to get underway. Listed below are the steps required for this part of the procedure:

5.1.1 Ship Emergency If the emergency is ship related the carrier shall perform the following: • Notify the terminal that an emergency situation (if not visible) has

occurred, and the carrier is preparing to depart the berth • Commence preparations for getting underway • The master will initiate his ships emergency procedures plan • Notify the U.S. Coast Guard COTP Representative and provide a notice of

departure, the reason why and the estimated time for the move. • Initiate ESD if required to stop all LNG flow. • Call or have the agent notify the pilot, and tugs for immediate departure.

4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE • Request that the terminal personnel immediately purge the unloading arms

if attached. • Once the arm purge is completed have the terminal personnel immediately

disconnect and stow the unloading arms. (note: the ship will take at least 1 hour before it can move under its own power). • If the unloading arms cannot be purged or disconnected the ship may have

to initiate a breakaway departure, and rely on the arms PERC Connection to release the arms (this shall only be done if the terminal personnel cannot disconnect the arms because the emergency is in the unloading arm area). • Insure tugs have arrived, and pilot is on board prior to removing the

gangway or mooring lines • Make preparations to release the mooring lines. • Depart the berth.

5.1.2 Terminal Emergency If the emergency is terminal related the terminal shall perform the following: • Notify the carrier that an emergency condition has occurred, and request

that the master make preparations to get underway if the emergency may possibly cause a dangerous condition for the ship. • If an emergency condition at the terminal may not affect the safety of the

carrier it may be prudent for the carrier to be ready to move if necessary, but remain for the time being moored at the berth. • Notify the Coast Guard of the emergency • Initiate Emergency Response Plan Actions • Initiate ESD if required • Contact tugs, and pilots • Commence arm purge • Disconnect, and stow arms after purge is completed • Stow gangway after assuring personnel are off the ship • Prepare to disconnect mooring lines when the master is ready to sail.

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE 5.2

Uncontrollable Emergency In an uncontrolled emergency situation it may be necessary for the ship to leave the mooring berth immediately with little if any notice to the terminal. The master again is responsible for making the final decision to move his carrier unless it is overridden by the local Coast Guard Captain of the Port representative. The carrier will require the assistance of tugs to be pulled off of the berth (dead ship) because it will not be ready to move under its own power unless the ship is kept in a state of immediate readiness at all times (not normally done). The procedures listed here are the minimum that must be performed in order to complete this task:

5.2.1 Ship Emergency – Actions to be Taken By Ship Master • Notify the terminal representative to be ready to release all mooring lines • Contact United States Coast Guard • Call Tugs/ Pilots • Initiate ESD • Initiate PERC Departure if there is not enough time to stow the unloading

arms • Leave the berth as soon as safely possible.

5.2.2 Terminal Emergency – Actions to be Taken By Emergency Team Leader • Notify the carrier master or designated officer in charge of the watch that

the ship must get under way immediately (The master may already be aware of the emergency). • Notify United States Coast Guard. • Verify Tugs, and Pilots have been called. • Provide personnel to release the unloading arms, and mooring lines if

possible. The Terminal Emergency Director will instruct the Public Information Contact person to notify the following emergency organizations: • Call emergency 911

If the Terminal Emergency Director classifies the uncontrollable emergency as a general emergency, the Terminal Emergency Director will instruct the Public Information Contact person to notify the following organizations as required:

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE •

Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

6 EMERGENCY RESPONSE TEAM ACTIONS 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during an emergency LNG carrier departure.

6.2



Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor ignites;



Coordinate the off–site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of LNG and flammable vapor leaks; and



Consult with the Terminal Emergency Director

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the emergency response team members will: •

Secure valves, pumps, or other process equipment to cut off supply to the leak emergency;



Remove ignition sources;

7

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE EMERGENCY LNG CARRIER DEPARTURE •

Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

8

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Vehicle Accidents

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE VEHICLE ACCIDENTS

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

3

5

SCOPE OF RESPONSE

4

5.1 Controllable Emergency

4

5.2 Uncontrollable Emergency

4

6

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A VEHICLE ACCIDENT.

5

6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

5

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE VEHICLE ACCIDENTS

1

INTRODUCTION

This procedure provides guidance for reporting, and obtaining assistance in the event there is a vehicle accident at the Oregon LNG Import Terminal. Depending on the circumstances of the accident it may be necessary to initiate an emergency response to control release of flammable vapors into the atmosphere, or chemicals into the environment.

2 APPLICABILITY This procedure must be followed in response to any vehicle accidents occurring at the Oregon LNG Import Terminal where such accident could possibly impact the environment, or terminal’s visitor’s, personnel, or contractors.

3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for responding to a vehicle accident at the terminal: •

National Fire Protection Association (NFPA)



Department of Transportation (DOT)



NFPA 30, Flammable and Combustible Liquids Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG)

4 RESPONSIBILITY The Terminal Manager is responsible for ensuring that this procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Emergency Response Plan and implementing this procedure in response to a vehicle accident at the Oregon LNG Import Terminal.

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE VEHICLE ACCIDENTS 5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Emergency Response Team Leader and determine the proper response to a vehicle accident at the Oregon LNG Import Terminal.

5.1

Controllable Emergency The Emergency Response Team will implement the actions detailed in Section 6 of this procedure. The Terminal Emergency Director will instruct the Public Information Contact person to notify the appropriate authorities by calling emergency 911 as required.

5.2

Uncontrollable Emergency The Emergency Response Team will implement the actions detailed in Section 6 of this procedure. The Terminal Emergency Director will instruct the Public Information Contact person to notify the local police department by calling emergency 911 as required: If the Terminal Emergency Director classifies the uncontrollable emergency as a general emergency, the Terminal Emergency Director will instruct the Public Information Contact person to notify the following organizations by calling emergency 911 as required: •

Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE VEHICLE ACCIDENTS 6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A VEHICLE ACCIDENT. 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a vehicle accident, or accidental release of product or chemicals that may possibly impact the environment.

6.2



Make carefully planned decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event that flammable vapor ignites;



Coordinate the off–site emergency response organizations and provide advice as needed;



Control all ignition sources in the proximity of the emergency; and



Consult with the Terminal Emergency Director

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team members will: •

Secure valves, pumps, or other process equipment to cut off supply to any leak emergency caused by a vehicle accident;



Remove any ignition sources;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits.

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Breach of Site Security

1

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE BREACH OF SITE SECURITY

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

3

5

SCOPE OF RESPONSE

4

6

5.1 Security Breach- Terminal

4

5.2 Security Breach- Unloading Platform and Marine Pier

4

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A BREACH OF SECURITY;

5

6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

6

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE BREACH OF SITE SECURITY

1

INTRODUCTION

In the event of a breach of security at the Oregon LNG Import Terminal the following procedures shall be followed:

2 APPLICABILITY This procedure must be followed in response to any breach of security protocol.

3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for responding to a breach of security This Procedure is designed to comply with the following: •

33 CFR Parts 101, 103, 105.



49 CFR 172.800, 1520.7



NFPA 30, Flammable and Combustible Liquids Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG)



33 CFR Part 127



49 CFR Part 193.

4 RESPONSIBILITY The Terminal Emergency Director is responsible for ensuring that this Procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Facility Security Plan under the direction of the Facility Security Officer, and implementing this Procedure in response to a breach of facility security.

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE BREACH OF SITE SECURITY 5 SCOPE OF RESPONSE The Terminal Emergency Director will consult with the Facility Security Officer, and Emergency Response Team Leader to determine the scope of the incident, and the measures necessary to control and secure the breach. The following actions will be taken accordingly.

5.1

Security Breach- Terminal The Facility Security Officer will coordinate the required activities as outlined in the Facility Security Plan with the Terminal Emergency Director, and the Emergency response Team Leader. The Terminal Emergency Director will, as required, instruct the Public Information Contact person to notify any additional outside resources as required to secure the terminal and control the incident. Under no circumstances will any terminal security or other personnel make any attempt to apprehend or detain an individual.

5.2

Security Breach- Unloading Platform and Marine Pier The Unloading Platform and Marine Pier shall have a designated security zone around it at all times. In the event a vessel enters this security zone without prior approval a breach of security will have occurred. The first attempt would be to hail the vessel on VHF Channel TBD and determine its intentions if communications can be established. The following procedure shall be required for any security zone breach: •

Document the type of vessel, and apparent direction of travel;



Document the vessel identification number;



Document the date, and time the breach occurred; and



Document color or any other identification characteristics

The facility Security Officer will coordinate the required activities as outlined in the Facility Security Plan with the Terminal Emergency Director, and the Emergency response Team Leader. The Terminal Emergency Director will instruct the Public Information Contact person to notify the following emergency organizations, if required: •

Department of Homeland Security



United States Coast Guard 4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE BREACH OF SITE SECURITY If the Facility Security Officer classifies the breach of security as an Uncontrollable Emergency, or a General Emergency, the Facility Security Officer will coordinate with the Terminal Emergency Director to have additional outside resources called in. The Terminal Emergency Director will have the Public Information Contact person call the appropriate authorities as required: •

Office of Homeland Security, Emergency Preparedness;



United States Coast Guard;



State Fire Marshall’s Office;



Columbia River Pilots;



Oregon State Police and County Sheriff’s Office;



Local Fire Department; and



Local Ambulance.

6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A BREACH OF SECURITY; 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during a fire situation. •

Make strategic decisions to control and resolve the emergency;



Assure life safety considerations are given the highest priority;



Minimize environmental impacts through appropriate control strategies;



Contain the emergency to limit property damage in the event of a breach of security protocol;



Coordinate with the off–site emergency response organizations and provide advice as needed;



Consult with the Facility Security Officer, and the Terminal Emergency Director

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February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE BREACH OF SITE SECURITY 6.2

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will:



Secure valves, pumps, or other process equipment to cut off supply to any leak emergency;



Remove any potential ignition sources;



Remove all personnel to safe locations and assist in rescue activities as required;



Operate foam systems to control flammable vapor formation; and



Provide other assistance as needed and as training permits

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE

Emergency Response Procedure Structural Bomb Threat or Discovery of an Explosive Device

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February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE

Table of Contents Section

Page

1

INTRODUCTION

3

2

APPLICABILITY

3

3

REGULATORY BACKGROUND

3

4

RESPONSIBILITY

3

5

SCOPE OF RESPONSE

4

5.1 In Coming Bomb Threat

4

5.2 Discovery of an Explosive Device

4

6

EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE. 5 6.1 Emergency Response Team Leader

5

6.2 Emergency Response Team Members

5

6.3 Bomb Threat Fact Sheet

6

2

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE

1

INTRODUCTION

In the event of discovery of an explosive device, or information received that the Oregon LNG Import Terminal may have a bomb adjacent to or on its property the procedures outlined within this procedure will be put into operation by the Emergency Response Team.

2 APPLICABILITY This procedure must be followed in response to a Structural Bomb Threat, or discovery of an Explosive Device on or adjacent to the Oregon LNG Import Terminal

3 REGULATORY BACKGROUND Federal, state, and local agencies and industrial standards regulate and provide guidance for responding to a Structural Bomb Threat, or Discovery of an Explosive Device. This Procedure is designed to comply with the following: •

National Fire Protection Association (NFPA)



33 CFR Part 101,103, and 105.



49 CFR part 172.800, 1520.7



NFPA 30, Flammable and Combustible Liquids Code



NFPA 59A, Standard for the Production, Storage, and Handling of Liquefied Natural Gas (LNG)



33 CFR 127,



49 CFR Part 193

4 RESPONSIBILITY The Terminal Emergency Director is responsible for ensuring that this Procedure is administered as written. The Emergency Response Team Leader is the on-duty operation’s shift supervisor. The Emergency Response Team Leader is responsible for initiating the Emergency Response Plan and implementing this Procedure in response to a Structural Bomb Threat, or Discovery of an Explosive Device.

3

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE 5 SCOPE OF RESPONSE The Facility Security Officer will consult with the Terminal Emergency Director and the Emergency Response Team Leader and determine the appropriate action for the Structural Bomb Threat, or Discovery of an Explosive Device. The following actions will be taken accordingly.

5.1

In-coming Bomb Threat In the event an incoming caller makes notification that a potential bomb has been placed adjacent to or on the Oregon LNG Terminal Property the questions listed in the bomb threat fact sheet (Section 6.3) should be asked. Attempts should be made to keep the caller on the phone as long as possible so a possible trace of the call can be made. The Terminal Emergency Director will instruct the Public Information Contact person to notify the local authorities by calling 911 to request additional support, if required.

5.2

Discovery of an Explosive Device Security personnel will be notified of a possible bomb threat on the property and will initiate a full search of the area. If an object resembling an explosive device is observed the personnel in that area will be immediately evacuated to a safe location. The Facility Security Officer will coordinate notification activities with the Public Information Contact person through the Terminal Emergency Director. The Public Information Contact person will contact the local authorities by calling 911 and inform them of the emergency. The Emergency Response Team Leader will consult with the Terminal Emergency Director and determine the course of action necessary to safeguard the personnel and property as required. Under no circumstances shall any Oregon LNG employee their contractors, or visitors make any attempt to remove the suspected device from the property. The Terminal Emergency Director will instruct the Public Information Contact person to notify the following emergency organizations, if required: • The U.S. Army Explosive Ordnance Disposal Unit • The Federal Bureau of Investigation • State Fire Marshall’s Office.

If the Terminal Emergency Director classifies the Discovery of an Explosive Device as a General Emergency, the Terminal Emergency Director will instruct the Public 4

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE Information Contact person to notify the following organizations in addition to the ones listed above as required: • Office of Homeland Security, Emergency Preparedness; • United States Coast Guard; • Columbia River Pilots; • Oregon State Police and County Sheriff’s Office; • Local Fire Department; and • Local Ambulance.

6 EMERGENCY RESPONSE TEAM – ACTIONS TO BE TAKEN IN RESPONSE TO A STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE. 6.1

Emergency Response Team Leader The following describes the key roles and responsibilities of the Emergency Response Team Leader during discovery of an explosive device. • Make strategic decisions to control and resolve the emergency;

Assure life safety considerations are given the highest priority; and • Consult with the Terminal Emergency Director

6.2

Emergency Response Team Members At the direction of the Emergency Response Team Leader, the Emergency Response Team Members will: • Secure valves, pumps, or other process equipment to cut off supply to any potential

leak emergency; • Remove sources of ignition; and • Provide other assistance as needed and as training permits.

5

February 4, 2008 DRAFT

EMERGENCY RESPONSE PROCEDURE STRUCTURAL BOMB THREAT, OR DISCOVERY OF AN EXPLOSIVE DEVICE 6.3

Bomb Threat Fact Sheet Bomb Threat fact Sheet Caller's Voice sound Calm Angry Excited Slow Rapid Soft Loud Laughter Crying Normal Distinct Slurred Whispered if Voice is Familiar who did it sound like?

Sound nasal Stutters Lisp Raspy Deep Ragged Clearing Throat Deep Breathing Crackling Voice Disguised Accent Familiar

background Sounds street Noises Crockery Voices/ Crowds PA System Music House Noises Motor Office Machinery

Factory Noises Animal Noises Clear Static Local Long Distance Booth Other

Threat language Irrational Foul Well Spoken

Incoherant Taped Message

Remarks:

Report Call Immediately to:

Phone Number: Name:

Date: Position:

6

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix G Oregon LNG Terminal Offsite Emergency Evacuation Procedures

TO BE INCLUDED IN FINAL VERSION OF EMERGENCY RESPONSE PLAN

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix H Oregon LNG Terminal Offsite Emergency Evacuation Zones, Routes and Maps

TO BE INCLUDED IN FINAL VERSION OF EMERGENCY RESPONSE PLAN

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix I Oregon LNG Terminal Emergency Response Plan Documentation of Required Consultation

TO BE INCLUDED IN FINAL VERSION OF EMERGENCY RESPONSE PLAN

February 4, 2008 DRAFT

EMERGENCY RESPONSE MANUAL

Appendix J Oregon LNG Terminal Emergency Response Cost Sharing Plan Letter of Commitment

TO BE INCLUDED IN FINAL VERSION OF EMERGENCY RESPONSE PLAN

February 4, 2008 DRAFT