Magellan Pipeline
Product Specifications
Version 102 December 1, 2015
QUALITY CONTROL CONTACTS Brian Topping, Manager, Quality Assurance and Analytics Office:
(918) 574-7381
Cell:
(918) 724-0342
Rod Lawrence, Manager, Product Control Office:
(918) 574-7286
Cell:
(816) 805-3334
Tyler Caughman, Supervisor, Crude Quality Control Cell:
(918) 557-0107
Hele Thompson, Supervisor, Refined Quality Control Cell:
(918) 344-8196
Jerry Higgins, Quality Control Program Coordinator Office:
(918) 574-7485
Cell:
(918) 760-4130
Marcia Eckhoff, Quality Control Program Coordinator Office:
(515) 276-0169
Cell:
(515) 710-5146
Dirk Dunbar, Quality Control Program Coordinator Cell:
(832) 270-3089
Revision Date: July 1, 2015
PRODUCT ACCEPTANCE TERMS The most current version of the methods referenced in these specifications will prevail at all times. Alternate test methods listed in ASTM, MPL product specification standards may be used. In instances of dispute, tests will be conducted using the referee methods identified in the applicable standard. Sampling
LPG products must be sampled in accordance with D1265. All other products must be sampled according to D4057, D4177, and/or D5842. Compliance with Magellan Pipeline Specifications will be determined by the shipper’s analysis of a composite sample produced in accordance with D5854. Top, middle, and bottom samples may not deviate more than 1.0° API from the gravity of the composite, nor contain product below the flash point minimum for oils, or above the seasonal RVP maximum for gasolines.
Reporting
It is the responsibility of the shipper to enter a certificate of analysis representative of each shipment into Magellan’s Prospector database for approval. Tests performed by the carrier are for carrier's information and do not relieve the shipper of the responsibility to comply with the specifications. The carrier reserves the right to sample the product and/or tank water below any product proffered for shipment.
Workmanship
Products must be clear and bright, and free of sediment. Any undissolved water received with incoming product may be deducted from the shipment volume ticketed. Additionally, Magellan may request for the shipper to remove the water received, and/or invoice the shipper for water disposal and other costs incurred.
Revision Date: June 29, 2009
PRODUCT ACCEPTANCE TERMS Delivery test results may deviate by the amount of the reproducibility of the test method. Shipments of proprietary grades must comply with corrosion inhibitor requirements for the applicable product grade.
Revision Date: June 29, 2009
MAGELLAN PIPELINE ADDITIVE SPECIFICATIONS Magellan will permit the types and concentrations of additives detailed below; all other types and concentrations or additives are prohibited. Gasoline Additive Specifications The following additive specifications apply to all grades except aviation products, LPG’s, and Natural Gasoline, for the grades noted in each section. (H, I, J8, L, Q, and W Grade) Gum Inhibitors and Metal Deactivators Gasoline shipments may, but are not required to, contain any of the following gum inhibitors and/or metal deactivators: N, N'di-secondary butyl ortho-phenylenediamine N, N'di-secondary butyl para-phenylenediamine N, N'disalicylidene-1,2 propanediamine N, N'di(1-ethyl-3-methylpentyl)-para-phnylenediamine N, N'di-isopropyl-para-phenylenediamine N, n'bis-(1, 4-demethylpentyl)-p-phenylenediamine n-Butyl para-aminophenol 2-6-di-tert-butylphenol 2,4,6-tri-tert-butylphenol Ortho-tert-butylphenol
UOP 12P UOP 3455 Innospec AO-36 Ethanox 4776 Tolad 3905 Nalco 88BU-118 Tolad 4695
UOP 12S UOP 5S Innospec AO-37 Ethanox 4720 Tolad 3910 Unichem 7529
UOP 17P Innospec AO-31 Ethyl 733 Ethanox 4740 Specaid 8Q202 Pitt-Consol M-56 Specaid 8Q206
Revision Date: October 22, 2014
Gasoline, Fuel Oil and Diesel Fuel Additive Corrosion Inhibitors
Products requiring compliance with NACE standard TM0172 may contain any of the following corrosion inhibitors: Nalco 5403 Nalco Visco 3554 Apollo PRI-19 UOP Unicor Innospec DCI-6A Tolad 245 HiTech 580 Nalco EC5407A
Nalco 5405 Lubrizol 541 Innospec DCI-4A UOP Unicor J Hitec E-534 Tolad 4410 Spec-Aid 8Q5127
Baypros 853 UOP Unicor PL Unichem 7504 Tolad 249 Unichem 7501 Tolad 9715 Tolad 9719 Spec-Aid 8Q123ULS Spec-Aid 8Q110ULS
Fuel Oil and Diesel Fuel Additives Stability
Fuel oil and/or diesel fuel shipments may contain one or more of the following stability additives as required to achieve compliance with the stability characteristics outlined in the applicable grade specification. Innospec FOA-3 UOP Polyflo-121 UOP Polyflo-122 UOP Polyflo-128 Tolad 9022
Chemtec 7220 Spec-Aid 8Q403ULS Tolad 9076 Unichem 7530 Spec-Aid 8Q401
Specaid 8Q72 Nalco 5303 Nalco 5301 UOP Polyflo-195
Revision Date: October 22, 2014
Cold Flow Additives
Fuel oil and/or diesel fuel shipments requiring additives to achieve compliance with low temperature properties may, but are not required to contain one or more of the following pour point depressant additives: Hitec 4541 Innospec 2152 Betz Q5201 Hitec 4518 Exxon ECA 7305 UOP Polyflo 6000
Dyes
Innospec PDD-7450 Spec-Aid 8Q5201 Paradyne 25 Unichem 8094 Nalco 5375 Spec-Aid 8Q72ULS
Tolad 3005 Tolad 3030 Betz 8Q12 Hitec 4566 Spec-Aid 8Q14ULS
X5 Grade High Sulfur Fuel Oil is the only product in Magellan Pipeline that requires dye at the origin. Applicable dyes and required treat rates are listed in the X5 grade product specifications. XR Grade Low Sulfur Fuel Oil is dyed at the Magellan rack.
Revision Date: October 22, 2014
Seasonal Gasoline Volatility Classes Shipments From Origin Reid Vapor Pressure, D5191 1/ March 1 - September 15 DVPE using EPA formula 2/ September 16 – February 28 DVPE using D5191 formula Distillation, ASTM D 86 3/ 10% Evaporated F, max 50% Evaporated F, min 50% Evaporated F, max 90% Evaporated F, max Final Boiling Point F, max 4/ Residue, vol % max Driveability Index, D4814, max 3/
Class AA Class A 158 158 170 170 250 250 374 374 430 430 2 2
Class B Class C 149 140 170 170 245 240 374 365 430 430 2 2
1250
1250
1240
Vapor to Liquid Ratio=20:1, F 3,5/ Class 1 D5188, min 140
Class 2 133
Class 3 124
Class D 131 170 235 365 430 2
Class E 122 170 230 365 430 2
1230
1220
1200
Class 4 116
Class 5 105
1/
All gasoline deliveries will not exceed applicable Federal and State requirements.
2/
The calculation required for the EPA compliance period is published in 40 CFR 80.46.
3/
Specifications must be met before blending with denatured fuel ethanol.
4/
The final boiling point of all gasoline deliveries at terminals will be at or below 437 °F as determined by ASTM D86
5/ D5188 is the referee test method. The alternative equations in D4814 may also be used.
Revision Date: October 22, 2014
Schedule of Origin Volatility Requirements A GRADE
Colorado
DVPE) (Class)
Kansas
(DVPE) (Class)
Illinois
(DVPE) (Class)
Minnesota
(DVPE) (Class)
N. Dakota
(DVPE) (Class)
Oklahoma
(DVPE) (Class)
Texas
(DVPE) (Class)
Wisconsin
(DVPE) (Class)
Wyoming
(DVPE) (Class)
Jan. 1-15
Jan. Feb. Feb. Mar. Apr. 16-31 1-15 16-29 1-31 1-30
May 1-31
June July 1-30 1-31
Aug. Sept. Sept. Oct. 1-31 1-15 16-30 1-31
Nov. 1-30
Dec. 1-31
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
11.5 C-3
9.0 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
13.5 D-5
13.5 D-5
10.0 B-5
10.0 B-5
8.5 A-4
8.5 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
13.5 D-5
13.5 D-5
10.0 B-5
10.0 B-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-3
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
10.0 B-5
10.0 B-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-3
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
10.0 B-5
10.0 B-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
10.0 B-4
10.0 B-4
8.5 A-4
8.5 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
13.5 D-4
13.5 C-4
10.0 B-4
10.0 B-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 A-2
11.5 C-3
13.5 D-4
13.5 D-4
13.5 D-5
13.5 D-5
10.0 B-5
10.0 B-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-3
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
11.50 9.0 C-3 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters.
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements A1 GRADE Jan. 1-15 (DVPE) (Class)
N/A
Jan. Feb. Feb. Mar. Apr. 16-31 1-15 16-29 1-31 1-30
May 1-31
June July 1-30 1-31
Aug. Sept. Sept. Oct. 1-31 1-15 16-30 1-31
Nov. 1-30
Dec. 1-31
N/A
6.8 A-3
6.8 A-2
6.8 A-2
N/A
N/A
N/A
N/A
N/A
6.8 A-3
6.8 A-2
6.8 A-2
N/A
N/A
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters.
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements South System El Paso Deliveries A1X GRADE
Jan. 1-31 11.50 C-3
Feb. 1-29 10.00 B-2
Mar. 1-31 9.0 B-2
Apr. 1-15 9.0 B-2
Apr. 16-30 9.0 B-2
May. 1-31 9.00 A-1
June. 1-30 9.00 A-1
July. 1-31 9.00 A-1
Aug. 1-31 9.00 A-1
Sept. 1-15 9.0 B-2
Sept. 16-30 10.00 B-2
Oct. Nov. Dec. 1-30 1-30 1-31 11.50 11.50 11.50 C-3 C-3 C-3
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements
A5 GRADE Jan. Feb. Mar. 1-31 1-28 1-30 15.00 13.50 11.50 E-5 D-5 C-3
Apr. 1-30 9.0 A-3
May 1-31 9.0 A-3
June 1-30 9.0 A-2
July 1-31 9.0 A-2
Aug. 1-31 9.0 A-2
Sept. 1-15 9.0 A-2
Sept 16-30 10.00 B-2
Oct. 1-30 11.50 C-3
Nov. 1-31 13.5 D-4
Dec. 1-31 15.00 E-5
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements
AMS Grade
Colorado (DVPE)
Jan. 1-31 N/A
Feb. 1-28 N/A
Mar. 1-15 N/A
Mar. Apr. May. 16-31 1-30 1-31 N/A 7.8 7.8 A3 A3
June. July. 1-30 1-31 7.8 7.8 A2 A2
N/A
N/A
N/A
7.8 A-3
7.8 A-3
7.8 A-3
7.8 A-2
N/A
N/A
N/A
7.8 A-3
7.8 A-3
7.8 A-3
7.8 A-2
N/A
N/A
N/A
N/A
7.8 A-3
7.8 A-2
(CLASS)
Aug. 1-31 7.8 A2
Sept. Sept. Oct. Nov. 1-15 16-30 1-31 1-30 7.8 N/A N/A N/A A-2
Dec. 1-31 N/A
Kansas (DVPE) (CLASS)
7.8 A-2
7.8 A-2
7.8 A-2
N/A
N/A
7.8 A-2
7.8 A-2
N/A
7.8 A-2
7.8 A-2
N/A
N/A
N/A
N/A
Texas (DVPE) (Class)
7.8 A-2
N/A
Wyoming (DVPE)
(Class)
7.8 A-3
7.8 A-2
N/A
N/A
N/A
N/A
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements
AR Grade
Texas
(DVPE) (CLASS)
Jan. Feb. 1-31 1-20 13.5 13.5 D-4 D-4
Feb. 21-28 11.5 D-4
Mar. Mar. Apr. May. June. July. 1-20 21-31 1-30 1-31 1-30 1-31 9.0 Report Report Report Report Report A-3 A-3 A-3 A-3 A-3 A-2
Aug. Sept. 1-31 1-15 Report Report A-2 A-2
Sept. 16-30 10.0 B-2
Oct. Nov. Dec. 1-31 1-30 1-31 11.5 13.5 13.5 C-3 D-4 D-4
NR Grade
Texas
(DVPE)
(CLASS)
Oklahoma (DVPE) (Class)
Jan. Feb. Feb. Mar. 1-31 1-20 21-29 1-20 13.5 13.5 13.5 13.5 D-4 D-4 D-4 D-4
Jan. 1-20 15.0 E-5
Jan. 21-31 13.5 D-4
Mar. Apr. 21-31 1-30 Report Report A-3 A-3
May. June. July. 1-31 1-30 1-31 Report Report Report A-3 A-3 A-2
Feb. Feb. Feb. Mar. Mar Apr. 1-10 11-29 20-28 1-10 11-30 1-30 13.5 11.5 9.0 9.0 Report Report D-4 C-3 A-3 A-3 A-3 A-3
May. 1-31 Report A-3
Aug. Sept. Sept. 1-31 1-15 16-30 Report Report 10.0 A-2 A-2 B-2
June. 1-30 Report A-2
Oct. 1-31 11.5 C-3
Nov. 1-30 13.5 D-4
Dec. 1-31 13.5 D-4
July. Aug. Sept. Sept. Oct. Nov. Nov. Dec. 1-31 1-31 1-15 16-30 1-31 1-20 21-31 1-31 Report Report Report 11.5 13.5 13.5 15.0 15.0 A-2 A-2 A-2 C-3 D-4 D-4 E-5 E-5
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements South System El Paso Deliveries NEP Grade
Jan. 1-24 11.50 C-3
Jan. 25-31 10.00 B-2
Feb. 1-29 10.00 B-2
Mar. 1-31 10.00 B-2
Apr. 1-15 10.00 B-2
Apr. 16-30 9.00 A-1
May 1-31 9.00 A-1
June 1-30 9.00 A-1
July 1-31 9.00 A-1
Aug. 1-31 10.00 B-2
Sept. 1-30 10.00 B-2
Oct. 1-31 11.50 C-3
Nov. 1-30 11.50 C-3
Dec. 1-31 11.50 C-3
Revision Date: September 17, 2013
Schedule of Origin Volatility Requirements
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters. V GRADE Jan. Jan. Feb. Feb. Mar. Apr. May June July Aug. Sept. Sept. Oct. Nov. Dec. 1-15 16-31 1-15 16-29 1-31 1-30 1-31 1-30 1-31 1-31 1-15 16-30 1-31 1-30 1-31 Kansas
(DVPE) (CLASS)
Illinois
(DVPE) (CLASS)
Minnesota, N. Dakota, Wis
(CLASS)
Oklahoma
(DVPE)
(DVPE)
(CLASS)
Texas
(DVPE) (CLASS)
15.0 13.5 E-5 D-5
13.5 D-5
13.5 D-5
8.5 A-4
8.5 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
15.0 13.5 E-5 D-5
13.5 D-5
13.5 D-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-3
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
8.5 A-5
8.5 A-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-3
9.0 A-3
11.5 C-3
13.5 D-4
15.0 E-5
15.0 E-5
15.0 13.5 E-5 D-5
13.5 D-4
13.5 D-4
8.5 A-4
8.5 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
15.0 E-5
13.5 13.5 D-5 D-5
13.5 D-4
11.5 C-4
9.0 A-4
9.0 A-3
9.0 A-3
9.0 A-2
9.0 A-2
9.0 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 D-4
13.5 D-5
Revision Date: February 10, 2015
Schedule of Origin Volatility Requirements NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters.
V1 GRADE Colorado
Jan. 1-31 (DVPE) 15.0 (Class) E-5
Feb. Feb. Mar. 1-15 16-28 1-15 15.0 13.5 11.5 E-5 D-5 C-3
Mar. 16-31 11.5 C-3
Apr. May. June. July. Aug. Sept. 1-30 1-31 1-30 1-31 1-31 1-15 9.0 9.0 9.0 9.0 9.0 9.0 A-3 A-3 A-2 A-2 A-2 A-2
Sept. 16-30 10.0 B-2
Oct. Nov. Dec. 1-31 1-30 1-31 11.5 13.5 15.0 C-3 D-4 E-5
15.0 E-5
13.5 D-5
13.5 D-5
11.5 C-3
N/A
N/A
N/A
10.0 B-2
11.5 13.5 C-3 D-4
15.0 E-5
15.0 E-5
13.5 D-5
13.5 D-5
11.5 C-3
N/A
N/A
N/A
10.0 B-2
11.5 C-3
15.0 E-5
15.0 E-5
15.0 E-5
13.5 D-5
11.5 C-3
11.5 C-3
9.0 A-3
Mar. 1-31 11.5 C-5
Apr. 1-30 9.0 A-4
Kansas (DVPE) (Class)
N/A
N/A
N/A
N/A
Texas (DVPE)
(Class)
N/A
N/A
N/A
N/A
13.5 D-4
Wyoming (DVPE) (Class)
9.0 A-3
9.0 A-2
9.0 9.0 A-2 A-2
9.0 A-2
10.0 B-2
11.5 C-3
13.5 15.0 D-4 E-5
V2 GRADE
(DVPE) (CLASS)
Jan. Feb 1-31 1-29 15.0 15.0 E-5 E-5
May 1-31 9.0 A-4
June 1-30 9.0 A-3
July 1-31 9.0 A-3
Aug. 1-31 9.0 A-3
Sept. Sept. Oct. 1-15 16-31 1-31 9.0 11.5 13.5 A-3 C-3 D-4
Nov. 1-30 15.0 E-5
Dec. 1-31 15.0 E-5
Revision Date: February 10, 2015
Schedule of Origin Volatility Requirements NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters. V8 GRADE
Oklahoma Kansas Minnesota & Wisconsin
Jan. 16-31 (DVPE) 15.0 (CLASS) E-5
Feb. 1-15 13.5 D-4
Feb. 16-29 13.5 D-4
Mar. 1-31 13.5 D-4
Apr. 1-15 11.5 C-3
Apr. May 16-30 1-31 N/A N/A
June July 1-30 1-31 N/A N/A
Aug. Sept. Sept. Oct. 1-31 1-15 16-30 1-31 N/A N/A N/A N/A
Nov. 1-30 N/A
Dec. 1-31 N/A
15.0 (CLASS) E-5
15.0 E-5
15.0 E-5
13.5 D-4
11.5 C-3
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
15.0 E-5
15.0 E-5
13.5 D-4
11.5 C-4
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Jan. Feb. Feb. Mar. Apr. 1-15 1-15 16-29 1-31 1-30 N/A N/A N/A N/A 6.6 A-3
May 1-31 6.6 A-3
June 1-30 6.6 A-2
July 1-31 6.6 A-2
Aug. 1-31 6.6 A-2
Sept. 1-15 6.6 A-2
Sept. Oct. 16-30 1-31 6.6 N/A A-2
Nov. 1-30 N/A
Dec. 1-31 N/A
Jan. Feb. Feb. Mar. Apr. 1-15 1-15 16-29 1-31 1-30 N/A N/A N/A N/A 6.8 A-3
May 1-31 6.8 A-2
June 1-30 6.8 A-2
July 1-31 6.8 A-2
Aug. 1-31 6.8 A-2
Sept. Sept. Oct. 1-15 16-30 1-31 6.8 N/A N/A A-2
Nov. 1-30 N/A
Dec. 1-31 N/A
(DVPE)
(DVPE) (CLASS)
V66 Grade
(DVPE) (CLASS)
V68 GRADE
(DVPE) (CLASS)
Revision Date: February 10, 2015
Schedule of Origin Volatility Requirements NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters. VMS GRADE Colorado (DVPE)
Jan. 1-31 N/A
(Class)
Feb. Mar. Mar. Apr. 1-15 1-15 16-31 1-30 N/A N/A N/A 7.8 A-3
May 1-31 7.8 A-3
June 1-30 7.8 A-2
July 1-31 7.8 A-2
Aug. 1-31 7.8 A-2
Sept. Sept. Oct. 1-15 16-30 1-31 7.8 N/A N/A A-2
Nov. 1-30 N/A
Dec. 1-31 N/A
Kansas
(DVPE) N/A (Class)
N/A
N/A
7.8 A-3
7.8 A-3
7.8 A-3
7.8 A-2
7.8 A-2
7.8 A-2
7.8 A-2
N/A
N/A
N/A
N/A
Texas
(DVPE)
N/A
N/A
N/A
7.8 A-3
7.8 A-3
7.8 A-3
7.8 A-2
7.8 A-2
7.8 A-2
7.8 A-2
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
7.8 A-3
7.8 A-3
7.8 A-2
7.8 A-2
7.8 A-2
7.8 A-2
N/A
N/A
N/A
N/A
Apr. 1-30 9.0 A-3
May 1-31 9.0 A-3
June 1-30 9.0 A-2
July 1-31 9.0 A-2
Aug. 1-31 9.0 A-2
Sept. Sept. Oct. 1-15 16-30 1-31 9.0 10.0 11.5 A-2 B-2 C-3
Nov. 1-30 13.5 D-4
Dec. 1-31 13.5 D-5
(Class)
Wyoming
(DVPE)
(Class) VTX Grade Jan. 1-31 (DVPE) 13.5 (CLASS) D-5
Feb. Feb. Mar. 1-15 16-29 1-31 13.5 11.5 9.0 D-4 C-4 A-4
Revision Date: February 10, 2015
A Grade Premium Unleaded Gasoline Specifications (Conventional Gasoline - This product does not meet the requirements for reformulated gasoline and may not be used in any reformulated gasoline covered area.)
Product Property Gravity, ° API Color Volatility 2/ Benzene, vol % Mercaptan Sulfur, wt % 3/ Copper Corrosion Silver Corrosion Gum, Existent, mg/100 ml Oxidation Stability, minutes Phosphorus, g/gal Lead, g/gal Octane RON MON (R+M)/2 Sulfur, ppm 4/ Oxygenates, vol% Haze Rating 5/ NACE Corrosion Odor 6/
Test Method D287
D3606 D3227 D130 D7667, 7671 D381 D525 D3231 D3237
Origin Test Results Minimum Maximum Report Undyed
Deliveries1/
4.9 0.003 1 1 4
5
240 0.003 0.010
D2699 D2700
0.005 0.05
Report Report 91.0
D2622 D4815, D5599 D4176 TM0172, D7548
80 0.05 2
3
B+ Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
A1 Grade Premium Unleaded Gasoline Specifications (Conventional Gasoline – This product does not meet the requirements for reformulated gasoline and may not be used in any reformulated gasoline covered area.) Origin Test Test Results Product Property Method Minimum Maximum Deliveries1/ Gravity, ° API D287 Report Color Undyed Volatility 2/ Benzene, vol % D3606 4.9 Mercaptan Sulfur, wt % 3/ D3227 0.003 Copper Corrosion D130 1 Silver Corrosion D4814 1 Gum, Existent, mg/100 ml D381 4 5 Oxidation Stability, minutes D525 240 Phosphorus, g/gal D3231 0.003 0.005 Lead, g/gal D3237 0.010 0.05 Octane RON D2699 Report MON D2700 Report (R+M)/2 91.0 Sulfur, ppm 4/ D2622 80 Oxygenates, vol % D4815, D5599 0.05 Haze Rating 5/ D4176 2 3 NACE Corrosion TM0172, D7548 B+ Odor 6/ Nonoffensive 1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
A1X Grade Premium Unleaded Gasoline Specifications This is for export only and not for retail use in the United States Origin Test Test Results Method Minimum Maximum Deliveries1/ D287 Report Undyed
Product Property Gravity, ° API Color Volatility 2/ Benzene, vol % Mercaptan Sulfur, wt % 3/ Copper Corrosion Silver Corrosion Gum, Existent, mg/100 ml Oxidation Stability, minutes Phosphorus, g/gal Lead, g/gal Octane RON MON (R+M)/2 Sulfur, ppm 4/ Oxygenates, vol % Haze Rating 5/ NACE Corrosion Odor 6/
D3606 D3227 D130 D7667 D381 D525 D3231 D3237
4.9 0.003 1 1 4
5
240
D2699 D2700
0.003 0.010
0.005 0.05
80 0.05 2
3
Report Report 91.0
D2622 D4815, D5599 D4176 TM0172, D7548
B+ Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
A3 Premium Unleaded Gasoline Specifications (Conventional Gasoline - This product does not meet the requirements for reformulated gasoline and may not be used in any reformulated gasoline covered area.)
Product Property Gravity, °API Color Volatility 2/ Benzene, vol % Mercaptan Sulfur, wt % 3/ Copper Corrosion Silver Corrosion Gum, Existent, mg/100 ml Oxidation Stability, minutes Phosphorus, g/gal Lead, g/gal Octane RON MON (R+M)/2 Sulfur, ppm 4/ Oxygenates, vol % Haze Rating 5/ NACE Corrosion Odor 6/
Test Method D287
D3606 D3227 D130 D7667, D7671 D381 D525 D3231 D3237 D2699 D2700 D2622 D4815, D5599 D4176 TM0172, D7548
Origin Test Results Minimum Maximum Report Undyed
Deliveries1/
4.9 0.003 1 1 4
5
240 0.003 0.010
0.005 0.05
94.0 87.0 93.0 80 0.05 2
3
B+ Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
A5 , AMS, MP Grade 88.5 Sub-Octane Premium Unleaded Gasoline Specifications (Conventional Gasoline - This product does not meet the requirements for reformulated gasoline and may not be used in any reformulated gasoline covered area.)
Product Property Gravity, ° API Color Volatility 2/ Benzene, vol % Mercaptan Sulfur, wt % 3/ Copper Corrosion Silver Corrosion Gum, Existent, mg/100 ml Oxidation Stability, minutes Phosphorus, g/gal Lead, g/gal Octane RON MON (R+M)/2 Sulfur, ppm 4/ Oxygenates, vol % Haze Rating 5/ NACE Corrosion Odor 6/
Test Method D287
D3606 D3227 D130 D7667,7671 D381 D525 D3231 D3237
Origin Test Results Minimum Maximum Report Undyed
Deliveries1/
4.9 0.002 1 1 4
5
0.003 0.010
0.005 0.05
80 0.05 2
3
240
D2699 D2700
Report Report 88.5
D2622 D4815 D4176 TM0172, D7548
B+ Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
AR Grade Premium Gasoline Blendstock (RBOB) For Blending With 10.0% Denatured Fuel Ethanol (92% Purity) As Defined In ASTM D4806 VOC-Controlled Region 1 Complex Model Phase II
Product Property Gravity, ° API8/ Color Volatility 2/9/ Distillation, ASTM D 86 10% Evaporated °F, max 50% Evaporated °F, min 50% Evaporated °F, max 90% Evaporated °F, max Final Boiling Point °F, max3/ Residue, vol% max Drivability Index, max ASTM D4814
Test Method D287
Origin Test Results Minimum Maximum Report Undyed
Deliveries1/
Class AA Class A Class B Class C Class D Class E 158 158 149 140 131 122 150 150 150 150 150 150 250 250 245 240 235 230 374 374 374 365 365 365 430 430 430 430 430 430 2 2 2 2 2 2 1250 1250 1240 1230 1220 1200
Vapor/Liquid Ratio = 20:1 Class 1 Class 2 Class 3 Class 4 Class 5 °F, min4/ 129 122 116 107 102 2/8/ Vapor Pressure, D5191 E200 (vol%) D86 30 70 E300 (vol%) D86 70 100 Emission Performance Reduction (%) -27.0 Mercaptan Sulfur, wt % 3/ D3227 0.003 Copper Corrosion D130 1 Silver Corrosion D7667,7671 1 Gum, Existent, mg/100 ml D381 4 Oxidation Stability, minutes D525 240 Octane RON D2699 Report MON D2700 Report (R+M)/2 93.0 Phosphorus, g/gal D3231 0.003 Benzene, vol % D3606 1.3 4/ Aromatics (vol %) 50 Olefins (vol %) D1319 25 Sulfur, ppm D2622 80 Oxygen Content wt %5/ D5599 1.5 4.0 Oxygenates, (vol %) 8/ D4815 0.05 6/, 8/ Haze Rating D4176 2 NACE Corrosion8/ TM0172, D7548 B+ Odor 7/, 8/ Nonoffensive
5
0.005
3
Revision Date: December 1, 2015
AR Grade Premium Gasoline Blendstock (RBOB) (continued) 1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Refer to test methods in 40 CFR Chapter 1, Part 80.46.
5/
Oxygen content must meet a minimum of 1.5 wt. % and a maximum of 4.0 wt. % after blending of denatured fuel ethanol.
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
7/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
8/
Specifications must be met before blending of denatured fuel ethanol except for vapor pressure during the VOC compliance period, March 20th through October 1st, will be reported on the blended fuel.
9/
For products blended to meet EPA or state imposed summer VOC requirements, test must be performed for RVP in accordance with procedure described in 40 CFR, PART 80, Appendix E, Method 3.
**NOTE: This RBOB may not be combined with any other RBOB except RBOB having the same requirement for oxygenate type and amount. “Base Gasoline” Not for sale to the ultimate consumer. **NOTE: Heavy metals are not allowed to be present. **NOTE: All parameters must be met after blending with denatured fuel ethanol unless noted.
Revision Date: December 1, 2015
AZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB)
Product Property Octane RON MON (R+M)/2 1/ Oxygen Content (wt%) RVP (psi) Benzene (vol%) Aromatics (vol%) Olefins (vol%) CARB Predictive Model Calculation Color Corrosion (Cu)3 hrs @ 122F(50C) Corrosion (Ag) 3 hrs @122F (50C) 2/ Doctor test or Mercaptan sulfur (wt.%) Existent Gum (mg/100 ml) Gravity API @ 60F Oxidation stability (minutes) Phosphorous (gms/gal) Lead (gms/gal) Sulfur (ppm) NACE 3/ Haze Odor Volatility: Distil1ation, (F) Vapor/Liquid Ratio (V/L °F@ 20) Drivability Index (DI) 50%Evap Max 237
Grade Z6
1/ 2/ 3/
ASTM Test Method D 2699 D 2700
Test Results Minimum Maximum Report Report 89.5 D 4815 0.05 D 5191 8.0 D 3606 1.30 D 5769 33.1 D 1319 11.1 Pass Undyed D 130 1 D 7667,7671 1 D 4952 Negative D 3227 0.003 D 381 4 D 287 Report D 525 240 D 3231 0.003 D 5059 0.010 D 5453 80 TM0172, D7548 B+ D 4176 2 Olfactory Non-Offensive
D 86 D 2533 D 4814 90%Evap Max 335
End pt Max 430
V/L DI Min Max 140 1250
Total oxygen levels shall not exceed de minimums levels. The use of non-hydrocarbon blending components such as MTBE is prohibited. Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative. Product must be tested at 55F or tank temperature whichever is lower.
Product must be certified using current Arizona AZRBOB regulations from a state of Arizona registered supplier. In addition to the above a LPP Product Transfer Document for AZRBOB must be filled out and provided to Longhorn Pipe Line Quality Control. All gasoline must meet latest revision of ASTM D 4814. Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Longhorn Pipeline No additives or corrosion inhibitors containing phosphorus may be used in this gasoline. Revision Date: December 1, 2015
AZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB) (continued)
The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is prohibited. This is a base gasoline, not for sale to the ultimate consumer Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene will not be accepted for shipment. AZRBOB does not comply with the standards for Arizona CBG without the addition of oxygenate. This AZRBOB is intended for blending with 10% volume ethanol and may not be combined with AZRBOB’s requiring oxygenate blending with any other type or amount of oxygenate.
Revision Date: December 1, 2015
D Grade Premium Diesel Fuel Specifications
Product Property Gravity, °API Color Distillation, IBP, °F 50% Recovered, °F 90% Recovered, °F Copper Corrosion Cetane (1) Cetane Number OR (2) Cetane Index, A or B Cetane Index 2/ Flash Point, F Stability Thermal, % reflectance Aging Period (Minutes) Carbon Residue on 10% Bottoms, % Cloud Point, F Pour Point, F Viscosity, cSt at 104 F Ash, wt % Haze Rating 5/ NACE Corrosion Sulfur, ppm
Test Method D287 D1500 D86
Origin Test Results Minimum Report
2.0 340 460 540
D130 D613 D4737 D976 D93
48.0 48.0 40 140
D6468 (W) D6468 (Y) D6468
75 82 90
D524 D2500 D97 D445 D482 D4176 TM0172, D7548 D2622
Maximum
Deliveries1/ 2.5
640 1
140
0.20 4/ 4/
1.9
4.1 0.01 2
3
B+ 11
Revision Date: December 1, 2015
D Grade Premium Diesel Fuel Specifications (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics compliance per the EPA.
3/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet Evaporation at 485 F) after a 16 hour induction period by ASTM method D525 modified. Contact Magellan QC to request a copy of this method.
4/
Month January February March April May June July August September October November December
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank temperature at the time of sampling, whichever is lower.
Pour Point F, max 0 0 0 +10 +10 +10 +10 0 0 0 0 0
Cloud Point F, max +14 +14 +14 +20 +20 +20 +20 +14 +14 +14 +14 +14
Additional Requirements: Biodiesel: The use of any biodiesel fuel as a blending component is prohibited. Dyes: D Grade shipments may not be dyed.
Revision Date: December 1, 2015
E Grade Denatured Fuel Ethanol Specifications Specification Points
Test Method
Shipments
Apparent Proof, 60°F Or Density, 60°F
Hydrometer ASTM D-4052
Report Report
Water, Volume %, Maximum
ASTM E-203 or E-1064
1.0
Ethanol, Volume % Minimum Methanol, Volume %, Maximum
ASTM D-5501 ASTM D-5501
93.5 0.5
Sulfur, ppm (wt/wt), Maximum
ASTM D5453
10
Solvent Washed Gum, mg/100mL Maximum
ASTM D-381 Air Jet Method
Potential Sulfate, mass ppm Maximum
ASTM D7319
Chloride, mg/L Maximum
ASTM D-7319
Copper, mg/L Maximum
ASTM D-1688 Method A, Modified per D-4806
Acidity (as acetic acid), Mass % Maximum
ASTM D-1613 or D-7795
pHe Minimum Maximum
ASTM D-6423
Appearance @ 60°F
Visual Examination
Denaturant Content and Type Volume %
Deliveries
1/
93.0
5.0 4
8 0.08
0.007 6.5 9.0
2/
Corrosion Inhibitor Additive, One of the following is required:
Visibly free of suspended or precipitated contaminants. Must be clear and bright. 2
Minimum treat rate 6 lbs./1000 bbls. 20 lbs/1000 bbls. 20 lbs./1000 bbls. 20 lbs./1000 bbls. 20 lbs./1000 bbls. 20 lbs./1000 bbls. 13 lbs./1000 bbls. 13 lbs./1000 bbls. 13 lbs/1000 bbls. 13 lbs/1000 bbls. 6 lbs/1000 bbls 3 lbs/1000 bbls. 5 lbs/1000 bbls. 6 lbs/1000 bbls.
Vendor Innospec G. E. Betz Petrolite Nalco Betz Midcontinental Midcontinental Petrolite US Water Services US Water Services Ashland G.E. Power & Water NALCO US Water Services
Additive DCI-11 Plus Endcor GCC9711 Tolad 3222 5403 ACN 13 MCC5011E MCC5011PHE Tolad 3224 Corrpro 654 Corrpro 656 Amergy ECI-6 8Q123ULS EC5624A Plus Corrpro Pro NT
Revision Date: October 22, 2014
E Grade Denatured Fuel Ethanol Specifications (continued) 1/ Delivered products meets all applicable requirements at time and place of delivery. 2/ Only approved denaturants listed in D4806. The denaturant range must be within the guidelines provided for in IRS Notice 2009.06, which is 1.96% to no more than 2.5%.
Revision Date: October 22, 2014
H Grade Normal Butane Specifications
Product Property Composition, POD or Chromatography analysis Liquid vol % Normal Butane Isobutane Pentanes Propane Specific Gravity Vapor Pressure at 100 F, psi Weathering, 95% Evaporated Temp, F (Corrected) Residues, Non-Volatile Residue at 100F, ml Oil, No oil stain observation, ml Sulfur, ppm Copper Corrosion Dryness, Inspection Free Water Content
Test Method D2163
Origin Test Results Minimum Maximum
Deliveries1/
95
D1657 D1267 D1837
0.580
3 3 3 0.588 43 36
D2158
D3246
0.05 0.3 30
D1838
1 0
Additives: H grade normal butane shipments must be unstenched and contain no additives.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
I Grade Iso-Butane Specifications
Product Property Composition, POD or Chromatography analysis Liquid vol % Isobutane Propane Normal Butane Pentanes Specific Gravity Vapor Pressure at 100 F, psi Weathering, 95% Evaporated Temp, F (Corrected) Residues, Non-Volatile Residue at 100 F, ml Oil, No oil stain observation, ml Sulfur, grains per hundred cubic feet Copper Corrosion Dryness, Inspection Free Water Content
Test Method D2163
Origin Test Results Minimum Maximum
Deliveries1/
95
D1657 D1267 D1837
0.560
3.0 5.0 0.5 0.570 62 31
D2158
0.05 0.3
D1266 D1838
15 1 0
Additives: I grade Isobutane shipments must be unstenched and contain no additives.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
L Grade Propane Specifications
Product Property Composition Chromatography analysis Liquid vol % Propane Propylene Butanes and C4+ Pentanes and C5+ Specific gravity Vapor pressure at 100 F, psi Weathering, 95% evaporated Temp, F (corrected) Residues, Nonvolatile residue at 100 F, ml Oil, no oil stain observation, ml Sulfur, grains per hundred cubic feet Copper Corrosion Dryness, Valve Freeze, seconds
Test Method
Origin Test Results Minimum Maximum
Deliveries1/
D2163 90 5.0 2.5 D1657 D1267 D1837
None 0.500 175
0.510 208 -37
D2158 0.05 0.3 D2784
10
D1838 D2713
1 60
Additives: L Grade shipments must be unstenched and contain no additives. Unless otherwise notified in writing by shipper, L Grade propane deliveries will be odorized at the rate of 1.5 pounds Ethyl Mercaptan/10,000 gallons.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
NEP Grade Regular Unleaded Gasoline Specifications This is for export only and not for retail use in the United States. Origin Test Test Results Product Property Method Minimum Maximum Gravity, ° API D287 Report Color Undyed Volatility 2/ Benzene, vol % D3606 3.0 Mercaptan Sulfur, wt % 3/ D3227 0.003 Copper Corrosion D130 1 Silver Corrosion D7667,7671 1 Gum, Existent, (washed) mg/100 ml D381 4 Oxidation Stability, minutes D525 300 Phosphorus, g/gal D3231 0.003 Lead, g/gal D3237 0.010 Octane RON D2699 Report MON D2700 82.0 (R+M)/2 87.0 Sulfur, ppm D2622 1000 Oxygenates, vol % D4815, D5599 0.05 4/ Haze Rating D4176 2 NACE Corrosion TM0172, D7548 B+ Odor 5/ Nonoffensive
Deliveries1/
0.05
3
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
5/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
Revision Date: December 1, 2015
NR Grade Regular Gasoline Blendstock (RBOB) For Blending With 10.0% Denatured Fuel Ethanol (92% Purity) As Defined In ASTM D4806 VOC-Controlled Region 1 Complex Model Phase II
Product Property Gravity, ° API8/ Color Volatility 2/9/ Distillation, ASTM D 86 10% Evaporated °F, max 50% Evaporated °F, min 50% Evaporated °F, max 90% Evaporated °F, max Final Boiling Point °F, max3/ Residue, vol% max Drivability Index, max ASTM D4814
Origin Test Test Results Method Minimum Maximum D287 Report Undyed Class AA 158 150 250 374 430 2 1250
Class A 158 150 250 374 430 2 1250
Class B 149 150 245 374 430 2 1240
Deliveries1/
Class C Class D Class E 140 131 122 150 150 150 240 235 230 365 365 365 430 430 430 2 2 2 1230 1220 1200
Vapor/Liquid Ratio = 20:1 Class 1 Class 2 Class 3 Class 4 Class 5 4/ °F, min 129 122 116 107 102 Vapor Pressure, D5191 2/8/ E200 (vol%) D86 30 70 E300 (vol%) D86 70 100 Emission Performance Reduction (%) -27.0 Mercaptan Sulfur, wt % 3/ D3227 0.003 Copper Corrosion D130 1 Silver Corrosion D7667,7671 1 Gum, Existent, mg/100 ml D381 4 5 Oxidation Stability, minutes D525 240 Octane RON D2699 Report MON D2700 82.0 (R+M)/2 87.0 Phosphorus, g/gal D3231 0.003 0.005 Benzene, wt. % D3606 1.3 Aromatics (vol %)4/ 50 Olefins (vol %) D1319 25 Sulfur, ppm D2622 80 Oxygen Content wt %5/ D5599 1.5 4.0 8/ Oxygenates, (vol %) D4815 0.05 Haze Rating 6/, 8/ D4176 2 3 8/ NACE Corrosion TM0172, D7548 B+ Odor 7/, 8/ Nonoffensive Revision Date: December 1, 2015
NR Grade Regular Gasoline Blendstock (RBOB) (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Refer to test methods in 40 CFR Chapter 1, Part 80.46. 5/
Oxygen content must meet a minimum of 1.5 wt. % and a maximum of 4.0 wt. % after blending of denatured fuel ethanol.
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures, adjusted seasonally: February 16 – September 30 55 F max October 1– February 15 45 F max
7/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will not be accepted for shipment.
8/
Specifications must be met before blending of denatured fuel except for vapor pressure during the VOC compliance period, March 20th through October 1st, will be reported on the blended fuel.
9/
For products blended to meet EPA or state imposed summer VOC requirements, test must be performed for RVP in accordance with procedure described in 40 CFR, PART 80, Appendix E, Method 3.
**NOTE: This RBOB may not be combined with any other RBOB except RBOB having the same requirement for oxygenate type and amount. “Base Gasoline” Not for sale to the ultimate consumer. **NOTE: Heavy metals are not allowed to be present. **NOTE: All parameters must be met after blending with denatured fuel ethanol unless noted
Revision Date: December 1, 2015
NZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB)
Product Property Octane RON MON (R+M)/2 1/ Oxygen Content (wt%) RVP (psi) Benzene (vol%) Aromatics (vol%) Olefins (vol%) CARB Predictive Model Calculation Color Corrosion (Cu)3 hrs @ 122F(50C) Corrosion (Ag) 3 hrs @122F (50C) 2/ Doctor test or Mercaptan sulfur (wt.%) Existent Gum (mg/100 ml) Gravity API @ 60F Oxidation stability (minutes) Phosphorous (gms/gal) Lead (gms/gal) Sulfur (ppm) NACE 3/ Haze Odor Volatility: Distil1ation, (F) Vapor/Liquid Ratio (V/L °F@ 20) Drivability Index (DI) 50%Evap Max 237
Grade NZ6 1/ 2/ 3/
ASTM Test Method D 2699 D 2700
Test Results Minimum Maximum Report Report 84.0 D 4815 0.05 D 5191 8.0 D 3606 1.30 D 5769 33.1 D 1319 11.1 Pass Undyed D 130 1 D 7667,7671 1 D 4952 Negative D 3227 0.003 D 381 4 D 287 Report D 525 240 D 3231 0.003 D 5059 0.010 D 5453 80 TM0172, D7548 B+ D 4176 2 Olfactory Non-Offensive
D 86 D 2533 D 4814 90%Evap Max 335
End pt Max 430
V/L DI Min Max 140 1250
Total oxygen levels shall not exceed de minimus levels. The use of non-hydrocarbon blending components such as MTBE is prohibited. Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative. Product must be tested at 55F or tank temperature whichever is lower.
Product must be certified using current Arizona AZRBOB regulations from a state of Arizona registered supplier. In addition to the above a MMP Product Transfer Document for AZRBOB must be filled out and provided to Magellan Pipe Line Quality Control. All gasoline must meet latest revision of ASTM D 4814. Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Magellan Pipeline No additives or corrosion inhibitors containing phosphorus may be used in this gasoline.
Revision Date: December 1, 2015
NZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB) (continued)
The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is prohibited. This is a base gasoline, not for sale to the ultimate consumer Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene will not be accepted for shipment. AZRBOB does not comply with the standards for Arizona CBG without the addition of oxygenate. This AZRBOB is intended for blending with 10% volume ethanol and may not be combined with AZRBOB’s requiring oxygenate blending with any other type or amount of oxygenate. This product does not meet the requirements for reformulated gasoline and may not be used in any reformulated gasoline covered area.
Revision Date: December 1, 2015
Q Grade Commercial Jet Fuel Specifications
Product Property Gravity, o API Total Acidity , mg KOH/g Freezing Point, oF Existent Gum, mg/100 ml Sulfur, ppm Mercaptan Sulfur, wt % 2/ Color, Saybolt Copper Corrosion Water Separation Index Aromatics, vol % Net Heat of Combustion, BTU/lb 3/ Flash Point, oF Viscosity at –4 oF, cSt Electrical Conductivity, pSm Thermal Stability: Filter pressure drop, mm Hg Heater tube deposit rating Distillation 10% Recovered, °F 50% Recovered, °F 90% Recovered, °F Final Boiling Point, °F Residue, vol % Loss, vol % OR Simulated Distillation 10% Recovered, °F 50% Recovered, °F 90% Recovered, °F Final Boiling Point, °F Combustion (1) Smoke Point, mm OR (2) Smoke Point, mm AND Naphthalenes, vol % Particulate Matter, mg/L
Test Method D287 D3242 D2386 D381 D2622 D3227 D156 D130 D3948 D1319 D4809 D56,D93 D445 D2624 D32414/
Origin Test Results Minimum Maximum 37.5 50.5 0.10 -40 5 3000 0.003 +16 1 85 25 18,400 108 8.0 Report
Deliveries1/ 37.0 - 51.0
7
+14 75
100 5/
25
