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Section 15. REFINERY WASTES NITRIFICATION IN REFINERY WASTEWATER TREATMENT James A. Mueller, Director Kuen-Bing VVu, Graduate Student Environmental Engineering & Science Graduate Program Manhattan College Bronx, New York 10471 Stan Kaczmarek, Senior Engineer Exxon Research and Engineering Company Florham Park, New Jersey 07932 INTRODUCTION Many petroleum refineries biologically treat their wastewater to remove soluble contaminants. Given the variety of food sources available in refinery wastewaters, the biological reactors sustain mixed populations of microorganisms. Two groups of microorganisms, Nitrosomonas and Nitro- bacter, convert ammonia to nitrite and nitrate in a specific wastewater treatment process called nitrification. At many petroleum refineries, nitrification is essential to obtain low effluent ammonia concentrations. This is because ammonia is a regulated wastewater parameter that is also sometimes implicated in cases of aquatic toxicity. In an activated sludge biological oxidation system with a long sludge age, the consistent presence of nitrification gives an indication of a healthy system. However, nitrification is a sensitive process and a rise in effluent ammonia may signal problems for process performance . . . from a long-term inability to oxidize ammonia to the beginning of problems with other wastewater quality parameters, such as Biochemical Oxygen Demand and Total Suspended Solids. Previous research within and outside of Exxon has identified and validated the importance of several factors in maintaining the nitrification process. Dissolved oxygen concentrations above 2 mg/ 1, pH between 6 and 8, and sludge ages (or sludge retention times) greater than 10 days are now accepted as essential operating criteria for nitrification [1]. In this research, 5 laboratory activated sludge reactors were operated with these essentials, but under various hydraulic retention times, SRT's, and feed organic nitrogen conditions. The reactors were then "shocked" with simulated 4 hour spills of chemicals that are sometimes associated with nitrification upset in petroleum refineries. The purposes were to compare the nitrification performance of different activated sludge systems, to identify the dynamic responses of nitrification under feed quality upsets, and to examine the resiliency of the process. BACKGROUND In completely mixed refinery wastewater treatment systems designed for nitrification, organic carbon oxidation and nitrification occur simultaneously. Figure 1 shows a schematic of these processes. In organic carbon oxidation, chemical energy and carbon from the organic compounds are used by heterotrophic organisms for respiration and growth. The quantity of energy available to the het- erotrophs depends on the oxidation state of the organic carbon. Energy released by the reaction typically varies from 90 to 170 kcal per mole of organic carbon oxidized [2]. Nitrification is a two stage process carried out by autotrophic organisms. Nitrifiers do not require organic compounds for growth. Rather, they typically use carbon dioxide as their sole carbon source and energy from ammonia and nitrite for respiration and growth. Nitrosomonas convert ammonia to nitrite releasing 66.5 kcal of energy per mole of ammonia oxidized. Nitrobacters oxidize the nitrite to nitrate releasing 17.5 kcal of energy per mole of nitrite oxidized [3]. 507
Object Description
Purdue Identification Number | ETRIWC198551 |
Title | Nitrification in refinery wastewater treatment |
Author |
Mueller, James A. Wu, Kuen-Bing Kaczmarek, Stan |
Date of Original | 1985 |
Conference Title | Proceedings of the 40th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,36131 |
Extent of Original | p. 507-522 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-07-15 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 507 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Section 15. REFINERY WASTES NITRIFICATION IN REFINERY WASTEWATER TREATMENT James A. Mueller, Director Kuen-Bing VVu, Graduate Student Environmental Engineering & Science Graduate Program Manhattan College Bronx, New York 10471 Stan Kaczmarek, Senior Engineer Exxon Research and Engineering Company Florham Park, New Jersey 07932 INTRODUCTION Many petroleum refineries biologically treat their wastewater to remove soluble contaminants. Given the variety of food sources available in refinery wastewaters, the biological reactors sustain mixed populations of microorganisms. Two groups of microorganisms, Nitrosomonas and Nitro- bacter, convert ammonia to nitrite and nitrate in a specific wastewater treatment process called nitrification. At many petroleum refineries, nitrification is essential to obtain low effluent ammonia concentrations. This is because ammonia is a regulated wastewater parameter that is also sometimes implicated in cases of aquatic toxicity. In an activated sludge biological oxidation system with a long sludge age, the consistent presence of nitrification gives an indication of a healthy system. However, nitrification is a sensitive process and a rise in effluent ammonia may signal problems for process performance . . . from a long-term inability to oxidize ammonia to the beginning of problems with other wastewater quality parameters, such as Biochemical Oxygen Demand and Total Suspended Solids. Previous research within and outside of Exxon has identified and validated the importance of several factors in maintaining the nitrification process. Dissolved oxygen concentrations above 2 mg/ 1, pH between 6 and 8, and sludge ages (or sludge retention times) greater than 10 days are now accepted as essential operating criteria for nitrification [1]. In this research, 5 laboratory activated sludge reactors were operated with these essentials, but under various hydraulic retention times, SRT's, and feed organic nitrogen conditions. The reactors were then "shocked" with simulated 4 hour spills of chemicals that are sometimes associated with nitrification upset in petroleum refineries. The purposes were to compare the nitrification performance of different activated sludge systems, to identify the dynamic responses of nitrification under feed quality upsets, and to examine the resiliency of the process. BACKGROUND In completely mixed refinery wastewater treatment systems designed for nitrification, organic carbon oxidation and nitrification occur simultaneously. Figure 1 shows a schematic of these processes. In organic carbon oxidation, chemical energy and carbon from the organic compounds are used by heterotrophic organisms for respiration and growth. The quantity of energy available to the het- erotrophs depends on the oxidation state of the organic carbon. Energy released by the reaction typically varies from 90 to 170 kcal per mole of organic carbon oxidized [2]. Nitrification is a two stage process carried out by autotrophic organisms. Nitrifiers do not require organic compounds for growth. Rather, they typically use carbon dioxide as their sole carbon source and energy from ammonia and nitrite for respiration and growth. Nitrosomonas convert ammonia to nitrite releasing 66.5 kcal of energy per mole of ammonia oxidized. Nitrobacters oxidize the nitrite to nitrate releasing 17.5 kcal of energy per mole of nitrite oxidized [3]. 507 |
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