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Section Seven BIOLOGICAL: PHENOLIC WASTE TREATMENT 25 FATE OF AMMONIA, THIOCYANATE, PHENOLICS, AND CYCLIC AROMATICS WITHIN ACTIVATED SLUDGE COKING PLANT WASTE TREATMENT Clifford R. Lange, Assistant Professor David E. Chambers, Graduate Student Department of Civil Engineering, Auburn University Auburn, Alabama 36849-5337 INTRODUCTION Coal distillation processes, such as coal gasification and coal coking produce complex wastewaters. The coking process involves the destructive distillation of coal in an anoxic environment. The volatile compounds released during the coking process are either condensed or scrubbed out in the gas main or primary coolers. Tar is decanted from the condensate and the remaining aqueous waste, known as the flushing liquor or weak ammonia liquor (WAL), is the major source of coking plant wastewater. Coke plant wastewaters include a complex mixture of organic and inorganic compounds, including: ammonia, cyanide, thiocyanate, monohydric phenols (70% phenol, 25% m-cresol, and 5% o-cresol), heterocyclic nitrogenous compounds (HNCs), and polyaromatic hydrocarbons (PAHs). The concentrations of these wastewater constituents are a function of: coal type; coking temperature; and process technology. The ammonia and cyanide concentrations of the WAL are typically diminished by air stripping processes to make the wastewater more amenable to biological treatment. Dilution water may be added to the waste to reduce the concentrations of other inhibitory compounds prior to biological treatment. The goal of biological treatment of coking process wastewater is to mineralize organic contaminants and to oxidize the ammonia and thiocyanate to nitrate. One of the most commonly employed biological treatment processes for coking plant wastwaters is activated sludge. These processes are typically operated with long mean cell residence times (Ocs) and can achieve high degrees of ammonia nitrification, thiocyanate conversion, and organic removals. However, the presence of inhibitory compounds in the wastewater may cause process upsets. Nitrification is the biological oxidation of ammonia (NH4+) to nitrite (N02"), and ultimately to nitrate (NO,-). The specialized population of bacteria which mediate this oxidation are known as nitrifiers. Although there are seven known genera of nitrifiers, the species Nitrosomonas and Ni- trobacter perform most of the nitrification that occurs in wastewater treatment. Nitrosomonas eu- ropea has been identified as the only organism capable of oxidizing ammonia to nitrite in coking plant biological processes, while several species of Nitrobacter are known to oxidize nitrite to nitrate. Nitrifiers have low growth rates and cell yields and are easily out-competed by het- erotrophs under high growth rate conditions. Consequently, nitrification occurs only in low growth rate processes and is slow to recover from process upsets. Nitrifiers are inhibited by a number of compounds present in coking plant wastewater. Excessive levels of free ammonia were reported by Wong-Chong and Loehr1 to be inhibitory to Nitrosomonas (10 mg/L) and Nitrobacter (0.1 mg/L). Similarly, free nitrous acid (HN02) concentrations in excess of 0.22 mg/L are toxic to nitrifying populations. Thiocyanate concentrations of 52nd Purdue Industrial Waste Conference Proceedings, 1997. Ann Arbor Press, Chelsea, Michigan 48118. Printed in U.S.A. 247
Object Description
Purdue Identification Number | ETRIWC199725 |
Title | Fate of ammonia, thiocyanate, phenolics and cyclic aromatics within activated sludge coking plant waste treatment |
Author |
Lange, Clifford R. Chambers, David E. |
Date of Original | 1997 |
Conference Title | Proceedings of the 52nd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,20307 |
Extent of Original | p. 247-252 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
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Date Digitized | 2009-11-03 |
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Description
Title | page 247 |
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 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Section Seven BIOLOGICAL: PHENOLIC WASTE TREATMENT 25 FATE OF AMMONIA, THIOCYANATE, PHENOLICS, AND CYCLIC AROMATICS WITHIN ACTIVATED SLUDGE COKING PLANT WASTE TREATMENT Clifford R. Lange, Assistant Professor David E. Chambers, Graduate Student Department of Civil Engineering, Auburn University Auburn, Alabama 36849-5337 INTRODUCTION Coal distillation processes, such as coal gasification and coal coking produce complex wastewaters. The coking process involves the destructive distillation of coal in an anoxic environment. The volatile compounds released during the coking process are either condensed or scrubbed out in the gas main or primary coolers. Tar is decanted from the condensate and the remaining aqueous waste, known as the flushing liquor or weak ammonia liquor (WAL), is the major source of coking plant wastewater. Coke plant wastewaters include a complex mixture of organic and inorganic compounds, including: ammonia, cyanide, thiocyanate, monohydric phenols (70% phenol, 25% m-cresol, and 5% o-cresol), heterocyclic nitrogenous compounds (HNCs), and polyaromatic hydrocarbons (PAHs). The concentrations of these wastewater constituents are a function of: coal type; coking temperature; and process technology. The ammonia and cyanide concentrations of the WAL are typically diminished by air stripping processes to make the wastewater more amenable to biological treatment. Dilution water may be added to the waste to reduce the concentrations of other inhibitory compounds prior to biological treatment. The goal of biological treatment of coking process wastewater is to mineralize organic contaminants and to oxidize the ammonia and thiocyanate to nitrate. One of the most commonly employed biological treatment processes for coking plant wastwaters is activated sludge. These processes are typically operated with long mean cell residence times (Ocs) and can achieve high degrees of ammonia nitrification, thiocyanate conversion, and organic removals. However, the presence of inhibitory compounds in the wastewater may cause process upsets. Nitrification is the biological oxidation of ammonia (NH4+) to nitrite (N02"), and ultimately to nitrate (NO,-). The specialized population of bacteria which mediate this oxidation are known as nitrifiers. Although there are seven known genera of nitrifiers, the species Nitrosomonas and Ni- trobacter perform most of the nitrification that occurs in wastewater treatment. Nitrosomonas eu- ropea has been identified as the only organism capable of oxidizing ammonia to nitrite in coking plant biological processes, while several species of Nitrobacter are known to oxidize nitrite to nitrate. Nitrifiers have low growth rates and cell yields and are easily out-competed by het- erotrophs under high growth rate conditions. Consequently, nitrification occurs only in low growth rate processes and is slow to recover from process upsets. Nitrifiers are inhibited by a number of compounds present in coking plant wastewater. Excessive levels of free ammonia were reported by Wong-Chong and Loehr1 to be inhibitory to Nitrosomonas (10 mg/L) and Nitrobacter (0.1 mg/L). Similarly, free nitrous acid (HN02) concentrations in excess of 0.22 mg/L are toxic to nitrifying populations. Thiocyanate concentrations of 52nd Purdue Industrial Waste Conference Proceedings, 1997. Ann Arbor Press, Chelsea, Michigan 48118. Printed in U.S.A. 247 |
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