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BIODEGRADATION OF CYANIDE: NITRITE INTERFERENCE IN THE STANDARD TEST FOR TOTAL CYANIDE J. C. Rapean, Senior Staff Research Chemist R. A. Johnson, Senior Research Chemist T. P. Hanson, Senior Research Engineer WesthoUow Research Center Shell Development Company Houston, Texas 77001 INTRODUCTION Shell Chemical operates a plant at Axis, Alabama for the manufacture of BLADEX® Herbicide and atrazine. The BLADEX process produces a highly nitrogenous wastewater which is treated in a dedicated plant involving the steps shown in Figure 1. In this scheme, cyanide is removed by a reaction with formaldehyde. After hydrolysis, the wastewater is stripped to remove ammonia, neutralized and dduted for biotreatment. The biotreater is a conventional single-stage activated sludge system with a nominal residence time of 48 hours. Air is supplied by four surface aerators. Secondary clarification involves flocculation and settling. Phosphate is the only nutrient required since the organic nitrogen compounds in the wastewater supply the required nitrogen. Since start-up in August 1978 this treatment scheme has produced an effluent meeting all NPDES requirements. As a consequence of the cyanide in the raw process waste, the Alabama Water Improvement Commission imposed a limit on the discharge of cyanide of 0.87 pounds per day for the monthly average. At design flow rates, this corresponds to a concentration of 0.12 mg/l. Until August 1979 routine monitoring of the effluent showed cyanide concentrations well below this limit. Toward the end of August, cyanide appeared in the effluent unexpectedly. Analytical methods were checked between Shell laboratories and satisfactory repeatabUity and recovery of "spiked" samples confirmed that the observation of cyanide was real. Figure 2 shows typical cyanide and ammonia data for October. The only other observed change in plant performance during this period was a decrease in the level of nitrification. RAW WASTE v- CYANIDE ION Ha SO 2300 ~~] FORMALDEHYDE CYANIDE REMOVAL HYDROLYSIS AMMONIA STB 1 PCJR REQUIRED ■MM 0»T MjSO, NEUTRALIZER BIOTREATER TREATED W ) ASTEWATEfl Figure t. BLADEX herbicide wastewater treatment-cyanide removal. 430
Object Description
Purdue Identification Number | ETRIWC198042 |
Title | Biodegradation of cyanide : nitrite interference in the standard test for total cyanide |
Author |
Rapean, J. C. Johnson, R. A. Hanson, T. P. |
Date of Original | 1980 |
Conference Title | Proceedings of the 35th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,31542 |
Extent of Original | p. 430-436 |
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 | 2009-10-22 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 430 |
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 | BIODEGRADATION OF CYANIDE: NITRITE INTERFERENCE IN THE STANDARD TEST FOR TOTAL CYANIDE J. C. Rapean, Senior Staff Research Chemist R. A. Johnson, Senior Research Chemist T. P. Hanson, Senior Research Engineer WesthoUow Research Center Shell Development Company Houston, Texas 77001 INTRODUCTION Shell Chemical operates a plant at Axis, Alabama for the manufacture of BLADEX® Herbicide and atrazine. The BLADEX process produces a highly nitrogenous wastewater which is treated in a dedicated plant involving the steps shown in Figure 1. In this scheme, cyanide is removed by a reaction with formaldehyde. After hydrolysis, the wastewater is stripped to remove ammonia, neutralized and dduted for biotreatment. The biotreater is a conventional single-stage activated sludge system with a nominal residence time of 48 hours. Air is supplied by four surface aerators. Secondary clarification involves flocculation and settling. Phosphate is the only nutrient required since the organic nitrogen compounds in the wastewater supply the required nitrogen. Since start-up in August 1978 this treatment scheme has produced an effluent meeting all NPDES requirements. As a consequence of the cyanide in the raw process waste, the Alabama Water Improvement Commission imposed a limit on the discharge of cyanide of 0.87 pounds per day for the monthly average. At design flow rates, this corresponds to a concentration of 0.12 mg/l. Until August 1979 routine monitoring of the effluent showed cyanide concentrations well below this limit. Toward the end of August, cyanide appeared in the effluent unexpectedly. Analytical methods were checked between Shell laboratories and satisfactory repeatabUity and recovery of "spiked" samples confirmed that the observation of cyanide was real. Figure 2 shows typical cyanide and ammonia data for October. The only other observed change in plant performance during this period was a decrease in the level of nitrification. RAW WASTE v- CYANIDE ION Ha SO 2300 ~~] FORMALDEHYDE CYANIDE REMOVAL HYDROLYSIS AMMONIA STB 1 PCJR REQUIRED ■MM 0»T MjSO, NEUTRALIZER BIOTREATER TREATED W ) ASTEWATEfl Figure t. BLADEX herbicide wastewater treatment-cyanide removal. 430 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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