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20 COMPARISON OF THE ANAEROBIC CONTACT AND PACKED BED PROCESSES FOR THE TREATMENT OF EDIBLE OIL WASTEWATERS C. B. Saw, Senior Research Associate G. K. Anderson, Senior Lecturer J. A. Sanderson, Research Associate Department of Civil Engineering University of Newcastle upon Tyne Newcastle upon Tyne United Kingdom NE1 7RU INTRODUCTION The process of neutralization, which is carried out during the refining of certain edible oils, produces a soapstock from which fatty acids are recovered by means of acid splitting. Acid splitting is often carried out by the addition of sulfuric acid to the soapstock which causes the free fatty acids to separate from the acidic water phase. Once this separation has occurred, the water phase is drained to a fat separator where residual free fats are recovered. The final acid water represents the effluent from the process and contains predominantly glycerol, fat, and sodium sulfate. Conventional treatment of acid water involves a combination of chemical, physical, and biological processes with substantial mechanical input required for the dewatering of byproduct sludges. Chemical treatment with lime, followed by sedimentation, has been carried out in order to reduce the concentration of fatty matter to a level which can be tolerated by conventional aerobic biological treatment processes, e.g., activated sludge. Since chemical treatment alone removes only 50% of the COD, there is still a need for a sizable aerobic process to fully treat the effluent. This combination of treatment is known to be effective but involves high capital and operating costs. Possible Role of Anaerobic Process in the Treatment of Acid Water Experience from sewage sludge digestion has shown that anaerobic systems have the ability to degrade fatty matter. As such, it was thought that anaerobic biological treatment would be preferred to chemical treatment as a preliminary treatment process for acid water. The benefits sought by adopting the above process were: - degradation of fats, - low chemical requirements, - low sludge production, - low power requirements, and - moderate COD removal efficiency (>70%). For anaerobic treatment to be economically attractive in terms of minimizing the capital costs, it is also important that such treatment should be possible in one of the new generation of anaerobic reactors, such as, a contact digester, packed-bed digester, upflow sludge blanket digester or the expanded/fluidized bed digester. However, there are no such processes operating in the U.K. on edible oil refining wastewaters, and therefore it was decided, following preliminary laboratory tests, that pilot plant studies should be carried out in order to clearly identify the feasibility of treating acid water by means of an anaerobic process. 178
Object Description
Purdue Identification Number | ETRIWC198620 |
Title | Comparisons of the anaerobic contact and packed bed processes for the treatment of edible oil wastewaters |
Author |
Saw, C. B. Anderson, G. K. Sanderson, J. A. |
Date of Original | 1986 |
Conference Title | Proceedings of the 41st Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,37786 |
Extent of Original | p. 178-187 |
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 | 2009-07-13 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 178 |
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 | 20 COMPARISON OF THE ANAEROBIC CONTACT AND PACKED BED PROCESSES FOR THE TREATMENT OF EDIBLE OIL WASTEWATERS C. B. Saw, Senior Research Associate G. K. Anderson, Senior Lecturer J. A. Sanderson, Research Associate Department of Civil Engineering University of Newcastle upon Tyne Newcastle upon Tyne United Kingdom NE1 7RU INTRODUCTION The process of neutralization, which is carried out during the refining of certain edible oils, produces a soapstock from which fatty acids are recovered by means of acid splitting. Acid splitting is often carried out by the addition of sulfuric acid to the soapstock which causes the free fatty acids to separate from the acidic water phase. Once this separation has occurred, the water phase is drained to a fat separator where residual free fats are recovered. The final acid water represents the effluent from the process and contains predominantly glycerol, fat, and sodium sulfate. Conventional treatment of acid water involves a combination of chemical, physical, and biological processes with substantial mechanical input required for the dewatering of byproduct sludges. Chemical treatment with lime, followed by sedimentation, has been carried out in order to reduce the concentration of fatty matter to a level which can be tolerated by conventional aerobic biological treatment processes, e.g., activated sludge. Since chemical treatment alone removes only 50% of the COD, there is still a need for a sizable aerobic process to fully treat the effluent. This combination of treatment is known to be effective but involves high capital and operating costs. Possible Role of Anaerobic Process in the Treatment of Acid Water Experience from sewage sludge digestion has shown that anaerobic systems have the ability to degrade fatty matter. As such, it was thought that anaerobic biological treatment would be preferred to chemical treatment as a preliminary treatment process for acid water. The benefits sought by adopting the above process were: - degradation of fats, - low chemical requirements, - low sludge production, - low power requirements, and - moderate COD removal efficiency (>70%). For anaerobic treatment to be economically attractive in terms of minimizing the capital costs, it is also important that such treatment should be possible in one of the new generation of anaerobic reactors, such as, a contact digester, packed-bed digester, upflow sludge blanket digester or the expanded/fluidized bed digester. However, there are no such processes operating in the U.K. on edible oil refining wastewaters, and therefore it was decided, following preliminary laboratory tests, that pilot plant studies should be carried out in order to clearly identify the feasibility of treating acid water by means of an anaerobic process. 178 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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