REFERENCES 1.
Abeling, U., and Seyfried, C. (1992). ‘‘Anaerobic-aerobic treatment of high strength ammonium wastewater-nitrogen removal via nitrite.’’ Water Sci. Technol., 26(5-6), 1007–1015.
2.
A.C. Anthonisen, R.C. Loehr, T.B.S. Prakasam, E.G. Srinath, Inhibition of nitrification by ammonia and nitrous acid, J. WPCF 48 (1976) 835–852.
3.
A. Pollice,V. Tandoi, C. Lestingi, Influence of aeration and sludge retention time on ammonium oxidation to nitrite and nitrate, Water Res. 36 (2002) 2541–2546.
4.
Alongi, D. M., K. G. Boto, and A. I. Robertson. 1992. Nitrogen and phosphorus cycles. Pages 251-292 in A. I. Robertson and D. M. Alongi (eds.), Tropical mangrove ecosystems. American Geophysical Union Press, Washington, DC.
5.
Anthonisen, A.C., Loehr, R.C., Prakasam, T.B.S., Srinath, E.G., 1976. Inhibition of nitrification of ammonia and nitrous acid. Journal Water Pollution Control Federation 48 (5), 835-852.
6.
ASTM, Standard Methods for the Examination of Water and Wastewater (ASTM) 7th edition, 1989
7.
Avnimelech, Y. 1999. Carbon/nitrogen ratio as a control element in aquaculture systems. Aquaculture 176:227-235.
8.
Barnabe, G., 1994. On growing fish in intensive system. Aquaculture: biology and ecology of cultured species. In: Barnabe, G. (Ed.), Ellis Horwood Series in Aquaculture and Fisheries Support, pp. 353- 356.
9.
Blancheton, J.P., 2000. Developments in recirculation systems for Mediterranean fish species. Aquacult. Eng. 22, 17-31.
10. Boto, K. G. 1992. Nutrients and mangroves. Pages 138-145 in D. W. Connell and D. W. Hawker (eds.), Pollution in tropical aquatic systems. CRC Press, Boca Raton, Florida. 11. Briggs, M. R. P. and S. J. Funge-Smith. 1994. A nutrient budget of some intensive marine shrimp ponds in Thailand. Aquaculture and Fisheries Management 25:789-811. 12. Brown, J. J., E. P. Glenn, K. M, Fitzsimmons, and S. Smith. 1999. Halophytes for the treatment of saline aquaculture effluent. Aquaculture 175:255-268.
61
13. Castens, D. J., and Rozich, A. F. (1986). ‘‘Analysis of batch nitrification using substrate inhibition kinetic.’’ Biotechnol. Bioeng., 28, 461–465. 14. C. Fux, M. Boehler, P. Huber, I. Brunner,H. Siegrist, Biological treatment of ammonium-rich wastewater by partial nitritation and subsequent anaerobic ammonium oxidation (anammox) in a pilot plant, J. Biotechnol. 99 (2002) 295–306. 15. C. Hellinga, A.A.J.C. Schellen, J.W. Mulder, M.C.M. Van Loosdrecht, J.J. Heijnen, The SHARON process: an innovative method for nitrogen removal from ammonium-rich wastewater, Water Sci. Technol. 37 (1998) 135–142. 16. Chen, J.C., Lee, Y., 1997. Effects of nitrite on mortality, ion regulation, and acid - base balance of Macrobrachium rosenbergii at different external chloride concentrations. Aquat. Toxicol. 39, 291-305. 17. Clifford D. and Liu X. (1993) Ion exchange for nitrate removal. J. Am. Water Works Assoc. 85(4), 135-143. 18. Dahl C., Sund C., Kristensen Gh., and Vredenbregt L., 1997, Combined biological nitrification and denitrification of high-salinity wastewater. Water Sci. Technol. 36 (2-3) 345-352. 19. Dalmacija, B.; Karlovic, E.; Tamas, Z. and Miskovic, D., Purification of High-Salinity Wastewater by Activated Sludge Process. Water Research, Vol. 30, No. 2, pp. 295-298 (1996). 20. Dan Np., Visvanathan C., and Basu B., 2003. Comparative evaluation of yeast and bacterial treatment of high salinity wastewater based on biokinetic coefficients. Bioresour. Technol. 87 51-56. 21. Denton L. (1996) Microbiological Diversity of Denitrifying bacteria in HighNitrate Brines of varying salinity. M.S. Thesis, University of Colorado at Boulder. 22. DeVries I. and Hopstaken C. (1984) Nutrient cycling and ecosystem behavior in a saltwater lake. Netherlands Journal of Sea Research 18(3/4), 221-245. 23. Dierberg, F. E., and W. Kiattisimkul. 1996. Issues, impacts, and implications of shrimp aquaculture in Thailand. Environmental Management 20:649-666. 24. Duncan B. (1995) Effect of Ionic Strength on Denitrification of a High Salt, High Nitrate Brine Simulating Rocky Flats Evaporation Pond Water using Activated Sludge. M.S. Thesis, University of Colorado, Boulder, CO. 25. Esteves, J.L., Mille, G., Blanc, F., Bertrand, J.C., 1986. Nitrate reduction activity in a continuous flow-through in marine sediments. Microbiol. Ecol. 12, 283-290. 62
26. FAO, 1999. Aquaculture production statistics 1988-1997. Fisheries Circular no. 815 Rev, 11, Rome, 203 pp. 27. FAO Land and Water Development Division: Bio-Physical, Socio-Economic and Environmental Impacts of Salt-affected Soils, 2000. 28. F. Cec¸en, I.E. G¨onenc¸, Criteria for nitrification and denitrification of highstrength wastes in 2 upflow submerged filters, Water Environ. Res. 67 (1995) 132–142. 29. Fitria, E., 2002, Penurunan Bahan Organik Pada Limbah Tambak Udang Dengan Aktivitas Mikroorganisme, Thesis Program Magister, Institut Teknologi Bandung, 2002. 30. Focht, D.D., Verstraete, W., 1977. Biochemical ecology of nitrification and denitrification. In: Alexander, M. (Ed.), Advances in Microbial Ecology. Plenum, New York, pp. 135-214. 31. Fontenot, Q., Bonvillain, C., Kilgen, M., and Boopathy, R, Effects of temperature, salinity, and carbon: nitrogen ratio on sequencing batch reactor treating shrimp aquaculture wastewater, Bioresource Technology xxx (2006) xxx-xxx 32. Frakes and Hoff, 1982; T. Frakes and F.H. Hoff Jr., Effects of high nitrate-N on the growth and survival of juvenile and larval anemonefish, Amphiprion ocellaris, Aquaculture 29 (1982), pp. 155-158. 33. Frances, J., Allan, G.L., Nowak, B.F., 1998. The effects of nitrite on the shortterm growth of silver perch (Bidyanus bidyanus). Aquaculture 163, 6372. 34. Glass C. and Silverstein J., 1999. Denitrification of high-nitrate, high-salinity wastewater. Water Res. 33 (1) 223-229 35. Gee, C. S., Suidan, M. T., and Pfeffer, J. T. (1990). ‘‘Modelling of nitrification under substrate inhibition condition.’’ J. Environ. Eng., 116 (1831), 31–32. 36. Gibbs, M., Schiff, J.A., 1960. Chemosynthesis: The energy relations of chemoautotrophic organisms. In: Steward, F.C. (Ed.), Plant Physiology: A Treatise, Vol. IB: photosynthesis and chemosynthesis. Academic Press, New York, pp. 279-319. 37. Glenn, E. P., J. W. O'Leary, M. C. Watson, T. L., Thomas, and R. O., Kuehl. 1991. Salicornia bigelovii Torr: An oilseed halophyte for seawater irrigation. Science 251:1065-1067.
63
38. Handy, R.D., Poxton, M.G., 1993. Nitrogen pollution in marine culture: toxicity and excretion of nitrogenous compounds by marine fish. Rev. Fish Biol. Fish. 3, 205-241. 39. Hargreaves, J.A., 1998. Nitrogen biogeochemistry of aquaculture ponds. Aquaculture 166, 181- 212. 40. Hopkins, J. S., R. D. Hamilton, P. A. Sandifer, C. L. Browdy, and A. D. Stokes. 1993. Effect of water exchange rate on production water quality, effluent characteristics and nitrogen budgets of intensive shrimp ponds. Journal of the World Aquaculture Soc.24, 304-320. 41. H. Yoo, K.-H. Ahn, H.-J. Lee, K.-H. Lee, Y.-J. Kwak, K.-G. Song, Nitrogen removal from synthetic wastewater by simultaneous nitrification and denitrification (SND) via nitrite in an intermittently-aerated reactor,Water Res. 33 (1999) 145–154. 42. Indian Aquaculture Authority: Shrimp Aquaculture and the Environment - An Environment Impact Assessment Report, ch. 2; IAA report, April 2001. 43. Irwine and Ketchum, 1989. R.L. Irwine and L.H. Ketchum, Sequencing batch reactors for biological wastewater treatment, CRC Critical Reviews in Environmental Control 18 (1989), pp. 255–294. 44. J.M. Garrido,W.A.J. Van Benthum, M.C.M. Van Loosdrecht, J.J. Heijnen, Influence of dissolved oxygen concentration on nitrite accumulation in a biofilm airlift suspension reactor, Biotechnol. Bioeng. 53 (1997) 168–178. 45. J. Surmacz-Gorska, A. Cichon, K. Miksch, Nitrogen removal from wastewater with high ammonia nitrogen concentration via shorter nitrification and denitrification, Water Sci. Technol. 36 (1997) 73–78. 46. Kristensen H. and Jepsen S. (1991) Biological denitrification of wastewater from wet lime-gypsum flue gas desulphurization plants. Water Sci. Tech. 23(4-6), 691-700. 47. Lawson C. (1981) Development of a biological denitrification process for a high strength industrial waste, pp. 882-888. Proceedings of the 35th Purdue Ind. Waste Conf Purdue University. Lafayette, IN. 48. Lawton, G.W. and Eggert, C.V., Effects of High Sodium Chloride Concentrations on Trickling Filter Slimes. Sewage and Industrial Wastes, 29, 11, 1228 (Nov. 1957). 49. Lewis and Morris, 1986 W.M. Lewis Jr. and D.P. Morris, Toxicity of nitrite to fish: a review, Trans. Am. Fish. Soc. 115 (1986), pp. 183-195.
64
50. Lin, C. K., P. Ruamthaveesub, and P. Wanuchsoontorn. 1993. Integrated culture of green mussel (Perna viridis) in wastewater from an intensive shrimp pond: concept and practice. World Aquaculture 44:187-200. 51. M.S.M. Jetten, M. Wagner, J. Fuerst, M.C.M. Van Loosdrecht, G. Kuenen, M. Strous, Microbiology and application of the anaerobic ammonium oxidation (‘anammox’) process, Curr. Opin. Microbiol. 12 (2001) 283–288. 52. Marti´nez-Cordova, L. R., M. A. Porchas-Cornejo, H. Villareal-Colmenares, J. A. Caldero´n-Perez, and J. E. Naranjo-Paramo. 1998. Evaluation of three feeding strategies on the culture of white shrimp Penaeus vannamei Boone 1931 in low water exchange pond. 53. Mazik, P.M., Hinman, M.L., Winkelmann, D.A., Klaine, S.J., Simco, B.A., Parker, N.C., 1991. Influence of nitrite and chloride concentrations on survival and hematological profiles of striped bass. Trans. Am. Fish.Soc. 120, 247- 254. 54. Meincke, M., Krieg, E., Bock, E., 1989. Nitrosovibrio sp., the dominant ammonia-oxidizing bacteria in building sandstone. Appl. Env. Microbiol. 55 (8), 2108-2110. 55. Ministry Marine Affairs and Fisheries-Directorate General of Aquaculture in USDA foreign Agricultural service, Global Agriculture Information Network (GAIN) Report number: ID7024, Indonesia Fishery Products Shrimp Report 2007, 2007. 56. Pa´ez-Osuna, F., M. Hendrickx-Reners, and R. Cortes-Altamirano. 1994. Efecto de la calidad del agua y composicion biologica sobre la produccion en granjas camaronicolas. Informe final CONACYT proyecto 0625-N9110. 445 pp. (in Spanish). 57. Pa´ez-Osuna, F., S. R. Guerrero-Galva´n, A. C. Ruiz-Ferna´ndez, and R. Espinoza-Angulo. 1997. Fluxes and mass balances of nutrients in a semiintensive shrimp farm in north-western Mexico. Marine Pollution Bulletin 34:290 -297. 58. Pa´ez-Osuna, F., S. R. Guerrero-Galva´n, and A. C. Ruiz-Ferna´ndez. 1998. The environmental impact of shrimp aquaculture and the coastal pollution in Mexico. Marine Pollution Bulletin 36:65-75. 59. Pa´ez-Osuna, F., S. R. Guerrero-Galva´n, and A. C. Ruiz-Ferna´ndez. 1999. Discharge of nutrients from shrimp farming to coastal waters of the Gulf of California. Marine Pollution Bulletin 38:585-592. 60. Pambrun, V., Paul, E., Sperandio, M. Control and modeling of partial nitrification of effluents with high ammonia concentrations in sequencing bath reactor, Chem. Eng. Process. (2007) 65
61. Panswad T. and Anan C., (1999b). Specific oxygen, ammonia, and nitrate uptake rates of a biological nutrient removal process treating elevated salinity wastewater. Bioresour. Technol. 70 237-243. 62. Payne, W.J., 1973. Reduction of nitrogenous compounds by microorganisms. Bacteriol. Rev. 37 (4), 409-452. 63. Phillips, M. J. 1994. Aquaculture and the environment-striking a balance. Pages 29-31 in Proceedings of Infofish Aquatech 94, 29-31 August 1994, Colombo, Sri Lanka. 64. Pierce et al., 1993 R.H. Pierce, J.M. Weeks and J.M. Prappas, Nitrate toxicity to five species of marine fish, J. World Aquacult. Soc. 24 (1993), pp. 105-107 65. Rivera-Monroy, V. H., L. A. Torres, N. Bahamon, F. Newmark, and R. R. Twilley. 1999. The potential use of mangrove forests as nitrogen sinks of shrimp aquaculture pond effluents: The role of denitrification. Journal of the World Aquaculture Society 30:1 66. Robertson, A. I., and M. J. Phillips. 1995. Mangroves as filters of shrimp pond effluent: Predictions and biochemical research needs. Hydrobiologia 295:649-666. 67. Rodriguez-Valera F., Ruiz-Berraquero F. and Ramos-Cormenzana A. (1981) Characteristics of the heterotrophic bacterial populations in hypersaline environments of different salt concentrations. Micro. Ecol. 7, 235-243. 68. Rosa, M. F., Albuquerque, R. T., Ferna´ndez, J. M., Leite, S. G., and Medronho, R. A. (1997). ‘‘Nitrification of saline effluents.’’ Braz. J. Chem. Eng., 14(2), 151–158. 69. Rosenberry, B. About Shrimp Farming, ShrimpNews, August 2004 70. Rosenberry, B. 1998. World shrimp farming. Shrimp News International, San Diego, California, 328 pp. 71. Rosenthal and Otte, 1979 H. Rosenthal and G. Otte, Adaptation of a fish recirculating fish culture system to salinity change, Wissenschaftlichen Konnission fuer Meeresforschung 27 (1979), pp. 203–206. 72. Ruffier, P.J., Boyle, W.C., Wleinschmidt, J., 1981. Short-term acute bioassays to evaluate ammonia toxicity and effluent standards. J. Water Pollut. Control Fed. 53, 367- 377 73. Sandifer, P. A. and J. S. Hopkins. 1996. Conceptual design of a sustainable pond-based shrimp culture system. Aquacultural Engineering 15:41-52. 66
74. Schwedler and Tucker, 1983 T.E. Schwedler and C.S. Tucker, Empirical relationship between percent methemoglobin in channel catfish and dissolved nitrite and chloride in ponds, Trans. Am. Fish. Soc. 112 (1983), pp. 117-119. 75. Shishehchian, F., F. M. Yusoff, H, Omar, and M. S. Kamarudin 1999. Nitrogenous excretion of Penaeus monodon postlarvae fed with different diets. Marine Pollution Bulletin 39:224-227. 76. Simkins, S., Alexander, M., 1984. Models for mineralization kinetics with the variables of substrate concentration and population. Appl. Environ. Microbiol. 47, 1299–1306. 77. Supangat, A., 2000, Sistem Biofilter Untuk Meningkatkan kualitas Air Tambak Udang, JTM, vol VII, no. 3/2000. 78. Suzuki, L., Dular, U., Kwok, S.C., 1974. Ammonia or ammonium ion as substrate for oxidation by Nitrosomonas europaea cells and extracts. J. Bacteriol. 120, 556-558. 79. S.Y. Wang, D.W. Gao, Y.Z. Peng, P. Wang, Q. Yang, Nitrification– denitrification via nitrite for nitrogen removal from high nitrogen soybean wastewater with on-line fuzzy control,Water Sci. Technol. 49 (2004) 121– 127. 80. Tacon, A. G. J., Thematic Review of Feeds and Feed Management Practices in Shrimp Aquaculture, World Bank/NACA/WWF/FAO Consortium Program on Shrimp Farming and the Environment, 2002. 81. Talaro, K.P. Foundations in Microbiology sixth edition, Mc Graw Hill, Boston, 801 pp, 2006. 82. Timmons, M.B., Ebeling, J.M., Wheaton, F.W., Summerfelt, S.T., Vinci, B.J., 2002. Recirculating Aquaculture Systems, 2nd Edition. Cayuga Aqua Ventures, New York. 769 pgs. 83. Tomasso, 1994 J.R. Tomasso, Toxicity of nitrogenous wastes to aquaculture animals, Rev. Fish. Sci. 2 (1994), pp. 291-314. 84. Tunvilai, D., P. Songsanginda, and K. Chaiyakaj. 1993. Pollution loading of effluent from intensive tiger shrimp culture ponds. Technical paper 4/1993. National Institute of Coastal Aquaculture. Department of Fisheries. Kao Saen, Muang District, Songkhl 85. USDA foreign Agricultural service, Global Agriculture Information Network (GAIN) Report number: ID7024, Indonesia Fishery Products Shrimp Report 2007, 2007.
67
86. Van der Hoek P., Latour J. and Klapwijk A. (1987) Denitrification with methanol in the presence of high nitrate waste solutions. Appl. Micro. Biotech. 27, 199-205. 87. van Wyk, P., Davis-Hodgkins, M., Laramore, R., Main, K.L., Mountain, J., Scarpa, J., Farming Marine Shrimp in Recirculating Freshwater Systems, Harbor Branch Oceanographic Institution (HBOI) Manual, 1999. 88. Villaverde, S., Garcı´a, P., and Fdz-Polanco, F. (1997). ‘‘Influence of pH over nitrifying biofilm activity in submerged biofilter.’’ Water Res., 31 (5), 1180–1186. 89. Walsh et al., 2002 L.S. Walsh, P.E. Turk and P.G. Lee, Mariculture of the loliginid squid Sepioteuthis lessoniana through seven successive generations, Aquaculture 212 (2002), pp. 245-262. 90. Watson, S.W., 1971. Taxonomic considerations of the Nitrobacteraceae Buchanan. Int. J. Syst. Bacteriol. 21 (3), 254-270.
family
91. Watson, S.W., Bock, E., Valois, F.W., Waterbury, J.B., Schlosser, U., 1986. Nitrospira marina gen. nov. sp. nov.: A chemolithotrophic nitrite-oxidizing bacterium. Arch. Microbiol. 144, 1-7. 92. Woolard C. R. and Irvine R. L. (1995) Treatment of hypersaline wastewater in the sequencing batch reactor. Water Res. 29(4), 1159-1168. 93. X.H. Xia, Z.F. Yang , G.H. Huang, X.Q. Zhang, H. Yu, X. Rong, Nitrification in natural waters with high suspended-solid content––A study for the Yellow River, Chemosphere 57 (2004) 1017–1029 94. Z.J. Zhang, et al., Wastewater Treatment Engineering, 4th ed., China Architecture & Building Press, Beijing, China, 2000, p. 312 (in Chinese).
68
APPENDIX A ANALYTICAL METHODS
A.1. COD (Chemical Oxygen Demand) Titrimetric Method Most types of organic matter are oxidized by a boiling mixture of chromic and sulfuric acids. A sample is refluxed in strongly acidic solution with a known excess of potassium dichromate (K2Cr2O7). After digestion, the remaining unreduced K2Cr2O7 is titrated with ferrous ammonium sulfate to determine the amount of consumed and the oxidizable organic matter is calculated in terms of oxygen equivalent. The ratios of reagent weights, volume, and strengths are kept constant when sample volume was other from 50 ml. The standard 2-h reflux time may be reduced if it has been shown that a shorter period yields the same results. The following apparatus were used for COD analysis: borosilicate digestion tubes, heating block, oven, ampule sealer, and buret. The reagents used for COD analysis include: Potassium dichromate 0.05 N, FAS standard 0.05 N, digestion solution, and sulfuric acid reagent. The samples were digested in a heating block at 150oC for 2 hours. The samples were cooled and titrate with FAS until the color change from green into red. The COD was calculated using the following formula:
COD as mg O2 /L =
(A-B)* M * 8000 mL sample
where : A = ml FAS used for blank, B = ml FAS used for sample, and M = molarity of FAS. A.2. NO2- Colorimetric Method Nitrite (NO2-) was analyzed by colorimetric method (ASTM, 1989). Nitrite in the sample forms a reddish purple azo dye produced at pH 2.0 to 2.5 by coupling diazotized sulfanilamide with N-(1-naphthyl)-ethylenediamine dihydrochloride (NED dihydrochloride). The range of the method for spectrophotometric measurements was 10 to 1000 µg NO2-N/L. The color developed was read in spectrophotometer at 543 nm wavelength. The sample containing high nitrite concentration was measured by diluting sample with deionized water.
69
The reagents used for the analysis include nitrite free water, color reagent, sodium oxalate 0.025M, FAS 0.05 N, and stock nitrite solution. The color was developed by adding diazotized sulfanilamide with N-(1-naphthyl)ethylenediamine dihydrochloride (NED dihydrochloride) to 50 ml of sample. The color was read using specthrophotometer set at wavelength 543 nm. Standard curve was prepared using known NO2--N concentration solutions. A.3. NO3- Ultraviolet specthrophotometric Screening Method Nitrate (NO3-) was analyzed by colorimetric method (ASTM, 1989). The NO3calibration curve follows Beer's law up to 11 mg N/L. Measurement of UV absorption at 220 nm enables rapid determination of NO3-. Because dissolved organic matter also may absorb at 220 nm and NO3- does not absorb at 275 nm, a second measurement made at 275 nm may be used to correct the NO3- value. The sample containing high nitrite concentration was measured by diluting sample with deionized water. The reagents used for the analysis include nitrate free water, HCl 1N, and stock nitrite solution. Standard curve was prepared using known NO2--N concentration solutions. For samples and standards, subtract two times the absorbance reading at 275 nm from the reading at 220 nm to obtain absorbance due to NO3. A.4. NH3 Phenate Method An intensely blue compound, indophenol, is formed by the reaction of ammonia, hypochlorite, and phenol catalyzed by a manganese salt. The reagents used for the analysis include, ammonia free water, Hypochlorous acid reagent, manganese sulfate solution, 0.003M, phenate reagent, and stock ammonium solution. The color was developed by adding phenate reagent and hypochlorous acid to 50 ml of sample. The color was read using spectrophotometer set at wavelength 630 nm. Standard curve was prepared using known NH3-N concentration solutions. A.5. Total Solids Analysis A well-mixed sample is evaporated in a weighed dish and dried to constant weight in an oven at 103 to 105°C. The increase in weight over that of the empty dish represents the total solids. The following apparatus were used for used for total solids analysis, evaporating dishes, desiccators, oven, and analytical balance. Evaporating dish was ignited at 103 to 105°C for 1 h, cooled in dessicator, and then weighed immediately. 2,5 ml of sample was transferred to preweighed
70
dish and evaporated to dryness on a drying oven at least 1 h in an oven at 103 to 105°C, cooled in dessicator, then weighed. The total solid was calculated using the following formula:
mg total solids/L =
(A-B)X 1000 sample volume, mL
where: A = weight of dried residue + dish, mg, and B = weight of dish, mg A.6. Total Suspended Solids Analysis A well mixed sample is filtered through a weighed standard glass-fiber filter and the residue retained on the filter is dried to a constant weight at 103 to 105°C. The increase in weight of the filter represents the total suspended solids. If the suspended material clogs the filter and prolongs filtration, the difference between the total solids and the total dissolved solids may provide an estimate of the total suspended solids. The following apparatus were used for total solids analysis, evaporating dishes, desiccators, oven, glass-fiber filter disks, filter paper whatman 40, and analytical balance. Evaporating dish and filter paper were ignited at 103 to 105°C for 1 h, cooled in dessicator, then weighed immediately. 2.5 ml of sample was filtered, then the filter paper was transferred to preweighed dish and evaporated to dryness on a drying oven at least 1 h in an oven at 103 to 105°C, cooled in dessicator, then weighed. The total suspended solid was calculated using the following formula:
mg total suspended solids/L =
(A-B)X 1000 sample volume, mL
where: A = weight of filter + dried residue, mg, and B = weight of filter, mg
71
APPENDIX B ANALYSIS FLOW CHART
B.1 Chemical Oxygen Demand
Preparation of Digestion Solution
Preparation of Sulfuric Acid Reagent
5.108 g K2Cr2O7
2.75 g Ag2SO4
Heat to 103oC For 2 h
Add 0.5 kg (283 mL) cone H2SO4
Add 83.5 mL cone H2SO4 Let 1 to 2 days Add 16.65 g HgSO4
Sulfuric acid Reagent
Dissolve, cool to room temperature, dilute to 500 mL
Digestion solution
72
Preparation of Primary standard K2Cr2O7 0.05 N
Preparation of FAS Solution 0.05 N
9.8035 g FAS
0.6129 g K2Cr2O7
Add 10 ml H2SO4
Dilute to 250 mL
Dilute to 500 mL
K2Cr2O7 Standard
FAS standard 0.05 N Preparation of Ferroin Indicator 0.7425 g 1,1-0fenantrolin monohydrate
Add 0.3475 g FeSO4.7H2O
Dilute to 50 mL
Ferroin indicator
73
Sample Analysis
Sample, blank @ 2.5 mL Put each into the tube which was washed with 20 % H2 SO4
Add 1.5 mL digestion solution
Add 3.5 mL Sulfuric Acid Solution
Close culture tube and shake well Place in oven preheated to 1500C and reflux for 2h Cool to room temperature Add 2 drops of ferroin indicator
Titrate with FAS
COD concentration
74
B.2 NO2- Colorimetric Method Preparation of FAS Solution 0.05 N
Preparation of Color Reagent
25 mL 85 % phosphoric acid
9.8035 g FAS
Add 2.5 g sulfanilamide
Add 10 ml H2SO4
Add N-(1-naphtyl)ethlenediamine dihydrochloride
Dilute to 500 mL
Dilute to 250 mL FAS standard 0.05 N
Color reagent
Preparation of Stock Nitrite Preparation of Potassium Permanganate Solution
Solution
0.616 g NaNO2
4 g KMnO4
Dilute to 500 mL Dilute to 500 mL Add 1 mL CHCl3 KMnO4 standard 0.05 N
Stock Nitrite 1 mL=250 µg N
75
Preparation of Intermediate Nitrite Solution
Standardization of Stock Nitrite Solution
NO2stock
50 mL KMnO4 standard 0.05 N
Calculate 12.5/ NO2- stock concentration
Add 5 mL cone H2SO4
Add 50 mL NO2Stock solution
Dilute to 250 mL
Shake gently
NO2Intermediate solution 1 mL= 50 µg
Add 10 mL FAS 0.05 N
Preparation of Standard Nitrite Solution
Titrate with KMnO4
Make a blank
10 mL NO2intermesiate solution
NO2- stock Concentration
Dilute to 1000 mL
NO2- standard solution 1 mL= 0.5µg
76
Preparation of Standard Curve
Sample Analysis
NO2- standard solution With volume variation
Adjust pH 5-9
Dilute to 50 mL
Add 2 mL color reagent
Read Absorbance at 543 nm Plot A versus NO2concetration
Standard curve
77
B.3 NO3_ Analysis Preparation of Stock Nitrate Solution
Sample Analysis
2 mL Wastewater
KNO3
Remove suspended solid
Dry at 105 0C 24 h
Dilute to 50 mL, add 1 mL HCl 1 N, mix
Dissolve 0.18045 g dilute to 250 mL
Read A at 220 and 275 nm Dilute to 250 mL Add 2 mL CHCl3
Calculate NO3concentration =2 A275-A220
Nitrate stock solution
Plot A versus NO2concetration
Preparation of Standard Curve
NO3- concetration
Several volume of stock nitrate
Dilute to 50 mL, add 1 mL HCl 1 N, mix Read A at 220 and 275 nm Calculate NO3concentration =2 A275-A220 Plot A versus NO2concetration Standard curve
78
B.4 NH3 Phenate Method Preparation of Phenate Reagent
Preparation of Hypochlorous Acid Reagent
2.5 g NaOH
10 mL 5 % NaOCl
Add 40 ml water
Add 10 g Phenol
Dissolve in 100 mL water
Adjust pH to 6.5 to 7 with HCl
Phenate reagent
Hypochlorous acid reagent
Preparation of Stock Ammonium solution
Preparation of Manganous Sulfate Solution
381.9 mg anhydrous NH4CL
50 mg MnSO4.H2O
Dried at 1000C
Dissolve in 100 mL water
Dissolve in 1000 mL
MnSO4 0.003 M
Stock Ammonium Solution 1 ml = 122 µg
79
Preparation of Standard curve
Sample Analysis
Sample
Stock Ammonium Solution
Add 1 drop (0.05 mL) MnSO4 solution
Prepare 5 different concentrations 0.1 to 5µg
Add 0.5 mL hypochlorous acid reagent
Read the Absorbance at 630 nm
Immediately add 0.6 mL phenate reagent
Calibration curve
Read absorbance at 630 nm
Ammonia concentration
80
B.5 Total Solid Analysis Sample Analysis
Prepararation of Evaporating Dish
Sample
Cleaned dish
Transfer to preweighed dish
Heat to 103105oC For 1 h
Evaporate
Cool in desiccator
Heat to 103105oC For 1 h
Weigh
Cool in desiccator
Weight of dish
Weigh
Repeat the cycle of drying, cooling, desiccating, and weighing until i h i Weight of (dish + residu) - Weight of dish
Weight of total solids
81
B.6 Suspended Solids Analysis
Filtering apparatus with suction
Filter the sample
Wash 3 times with 10 ml distilled water
Transfer filter to dish
Dry at 103-105oC For 1h
Cool in the desiccator
Weigh
Repeat the cycle of drying, cooling, desiccating, and weighing until weight is constant Suspended solids concentration
82