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SULFUR REMOVAL OF POLYSULFIDE RUBBER MANUFACTURING WASTEWATERS BY ANAEROBIC TREATMENT Bernard J. Obarsky, Graduate Student John Cirello, Assistant Professor Department of Environmental Science Cook College, Rutgers University New Brunswick, New Jersey 08903 Albert R. Roy, Manager Engineering and Environmental Services Van Note-Harvey Associates Consulting Engineers Princeton, New Jersey 08540 INTRODUCTION A bench scale treatability study was performed on the wastewater from a major manufacturer of polysulfide rubber. The study was undertaken to investigate the feasibility of removing sulfur through anaerobic biological treatment. Although, aerobic treatment of wastewaters by activated sludge can effect the oxidation of reduced forms of sulfur it fails to remove sulfur, converting reduced forms to oxidized forms (the mineral acid H2S04). Furthermore the use of a neutralizing agent such as lime becomes necessary to maintain the system pH within tolerable levels. The result is a voluminous quantity of sludge as calcium sulfate (gypsum) precipitate, which must be collected, de- watered and disposed of. Wastewater from polysulfide rubber manufacturing contain sodium sulfate, sodium thiosulfate (Na2S203), sodium tetrathionate (Na2H2S406), sodium polysulfide, chlorinated hydrocarbons and low-molecular-weight polymer. The use of anaerobic digestion to reduce the above sulfur species to hydrogen sulfide was veiwed as a possible first step of sulfur removal. There are reports that sulfate and sulfide may act as inhibitors to the anaerobic process [1,2,3,4,5,6,7]. Rudolfs and Zeller [1] reported decreased gas production as one of the effects of sulfate salts on the digestion of fresh solids. Rudolf and Amberg [2] found that sulfide levels in excess of 200 mg/1 could decrease gas production and subsequent activity by 70%. Lawrence et al. [3] confirmed that sulfide levels above 200 mg/1 produce severe toxic effects. More recently, United States Environmental Protection Agency Guidelines [4] suggest that sulfate levels as low as 500 mg/1 will inhibit anaerobic digestion-as reported by Gosh [5], Pohland and Kang [6]. Further the early findings of Rudolfs and Amberg [7] reported an upper limit of 2,400 mg/1 of SO4. In view of this, and because the polysulfide rubber manufacturing plant might produce wastewaters with sulfur levels similar to those mentioned above, a treatability study was considered appropriate. 402
Object Description
Purdue Identification Number | ETRIWC1978044 |
Title | Sulfur removal of polysulfide rubber manufacturing wastewaters by anaerobic treatment |
Author |
Obarsky, Bernard J. Cirello, John Roy, Albert R. |
Date of Original | 1978 |
Conference Title | Proceedings of the 33rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,27312 |
Extent of Original | p. 402-408 |
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 | 2009-06-22 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page0402 |
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 | SULFUR REMOVAL OF POLYSULFIDE RUBBER MANUFACTURING WASTEWATERS BY ANAEROBIC TREATMENT Bernard J. Obarsky, Graduate Student John Cirello, Assistant Professor Department of Environmental Science Cook College, Rutgers University New Brunswick, New Jersey 08903 Albert R. Roy, Manager Engineering and Environmental Services Van Note-Harvey Associates Consulting Engineers Princeton, New Jersey 08540 INTRODUCTION A bench scale treatability study was performed on the wastewater from a major manufacturer of polysulfide rubber. The study was undertaken to investigate the feasibility of removing sulfur through anaerobic biological treatment. Although, aerobic treatment of wastewaters by activated sludge can effect the oxidation of reduced forms of sulfur it fails to remove sulfur, converting reduced forms to oxidized forms (the mineral acid H2S04). Furthermore the use of a neutralizing agent such as lime becomes necessary to maintain the system pH within tolerable levels. The result is a voluminous quantity of sludge as calcium sulfate (gypsum) precipitate, which must be collected, de- watered and disposed of. Wastewater from polysulfide rubber manufacturing contain sodium sulfate, sodium thiosulfate (Na2S203), sodium tetrathionate (Na2H2S406), sodium polysulfide, chlorinated hydrocarbons and low-molecular-weight polymer. The use of anaerobic digestion to reduce the above sulfur species to hydrogen sulfide was veiwed as a possible first step of sulfur removal. There are reports that sulfate and sulfide may act as inhibitors to the anaerobic process [1,2,3,4,5,6,7]. Rudolfs and Zeller [1] reported decreased gas production as one of the effects of sulfate salts on the digestion of fresh solids. Rudolf and Amberg [2] found that sulfide levels in excess of 200 mg/1 could decrease gas production and subsequent activity by 70%. Lawrence et al. [3] confirmed that sulfide levels above 200 mg/1 produce severe toxic effects. More recently, United States Environmental Protection Agency Guidelines [4] suggest that sulfate levels as low as 500 mg/1 will inhibit anaerobic digestion-as reported by Gosh [5], Pohland and Kang [6]. Further the early findings of Rudolfs and Amberg [7] reported an upper limit of 2,400 mg/1 of SO4. In view of this, and because the polysulfide rubber manufacturing plant might produce wastewaters with sulfur levels similar to those mentioned above, a treatability study was considered appropriate. 402 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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