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Electrochemical Process for Sewage Treatment CALVIN P.C. POON, Associate Professor Department of Civil and Environmental Engineering University of Rhode Island Kingston, R. I. 02881 INTRODUCTION Research on the control of undesirable aquatic growths has been influenced greatly be Liebig's Law of the Minimum which can be described as "the variation in productivity of land areas is most often determined by limitations imposed by the lack of some nutritional element." Consequently, removing nutrients has been proposed by many to eliminate the adverse effects of these contaminants. The need also arises from the fact that multiple reuse of water in the United States will soon equal the recoverable stream flow and groundwater supply. As the reuse of water becomes more prevalent, the problems of nutrient overfertilization will continue to increase. Since carbon is readily available in most waters as bicarbonates, nitrogen and phosphorus have been chosen by most researchers as the nutrients to control. The electrochemical process in the present study was used because of its high potential in phosphorus and nitrogen removal. However findings in experiments have demonstrated its equal effectiveness in BOD and suspended solids removal as well as its complete disinfection of the treated wastewater. The electrochemical process in this study is similar to that used by F6yn (I) to provide an effective and inexpensive method for nitrogen and phosphorus removal from domestic wastewater using sea water as the electrolyte. The purpose of the study is to investigate the mechanism of nitrogen and phosphorus removal for developing a better understanding and control of the process. Also the process is investigated as a means of total treatment of wastewater including primary, secondary and tertiary treatment in one single step. PROCESS DESCRIPTION Early development of electrolyte sewage treatment has a primary interest in generating chlorine for deodorizing and disinfecting wastewater. Eugene Hermite (2), as early as 1887, has described a method of treating sewage by mixing it with a proportion of seawater and electrolysing. He found, in addition to deodorizing and disinfecting effects, that Mg(OH)2 was produced as a powerful flocculent in the process which helped to bring down sewage solids effectively. Not too long later, in 1890, a sewage treatment plant was installed in London using what was known at that time as the Webster process (2). Iron went into sewage from insulated iron plates comprising the electrodes to form ferric hydroxide which caused rapid precipitation of sewage sludge and deodorization of wastewater. This same principal was employed by General Electric in their electro-coagulation process as a part of their shipboard waste treatment system (3). Foyn intended to use a similar process to electrolyse a seawater-sewage mixture to remove phosphates from sewage entering Oslo, Norway. His pilot plant study (1) showed 80 percent phosphates removal and 76-83 percent ammonia nitrogen removal. Significant removal of BOD and decreases in turbidity were also reported. Mendia in Italy (2) modified Foyn's process to treat a strong sewage. Clarifiers were used in conjunction with the electrolytic cells for better sewage solid removal. An average of 58 percent BOD removal was observed in the pilot study. Because the raw sewage contained very high BOD, much of it remained in the effluent being discharged. The ability of the process in BOD removal 281
Object Description
Purdue Identification Number | ETRIWC197327 |
Title | Electrochemical process for sewage treatment |
Author | Poon, Calvin P. C. |
Date of Original | 1973 |
Conference Title | Proceedings of the 28th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,23197 |
Extent of Original | p. 281-292 |
Series | Engineering extension series no. 142 |
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 | 2009-06-02 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 281 |
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 | Electrochemical Process for Sewage Treatment CALVIN P.C. POON, Associate Professor Department of Civil and Environmental Engineering University of Rhode Island Kingston, R. I. 02881 INTRODUCTION Research on the control of undesirable aquatic growths has been influenced greatly be Liebig's Law of the Minimum which can be described as "the variation in productivity of land areas is most often determined by limitations imposed by the lack of some nutritional element." Consequently, removing nutrients has been proposed by many to eliminate the adverse effects of these contaminants. The need also arises from the fact that multiple reuse of water in the United States will soon equal the recoverable stream flow and groundwater supply. As the reuse of water becomes more prevalent, the problems of nutrient overfertilization will continue to increase. Since carbon is readily available in most waters as bicarbonates, nitrogen and phosphorus have been chosen by most researchers as the nutrients to control. The electrochemical process in the present study was used because of its high potential in phosphorus and nitrogen removal. However findings in experiments have demonstrated its equal effectiveness in BOD and suspended solids removal as well as its complete disinfection of the treated wastewater. The electrochemical process in this study is similar to that used by F6yn (I) to provide an effective and inexpensive method for nitrogen and phosphorus removal from domestic wastewater using sea water as the electrolyte. The purpose of the study is to investigate the mechanism of nitrogen and phosphorus removal for developing a better understanding and control of the process. Also the process is investigated as a means of total treatment of wastewater including primary, secondary and tertiary treatment in one single step. PROCESS DESCRIPTION Early development of electrolyte sewage treatment has a primary interest in generating chlorine for deodorizing and disinfecting wastewater. Eugene Hermite (2), as early as 1887, has described a method of treating sewage by mixing it with a proportion of seawater and electrolysing. He found, in addition to deodorizing and disinfecting effects, that Mg(OH)2 was produced as a powerful flocculent in the process which helped to bring down sewage solids effectively. Not too long later, in 1890, a sewage treatment plant was installed in London using what was known at that time as the Webster process (2). Iron went into sewage from insulated iron plates comprising the electrodes to form ferric hydroxide which caused rapid precipitation of sewage sludge and deodorization of wastewater. This same principal was employed by General Electric in their electro-coagulation process as a part of their shipboard waste treatment system (3). Foyn intended to use a similar process to electrolyse a seawater-sewage mixture to remove phosphates from sewage entering Oslo, Norway. His pilot plant study (1) showed 80 percent phosphates removal and 76-83 percent ammonia nitrogen removal. Significant removal of BOD and decreases in turbidity were also reported. Mendia in Italy (2) modified Foyn's process to treat a strong sewage. Clarifiers were used in conjunction with the electrolytic cells for better sewage solid removal. An average of 58 percent BOD removal was observed in the pilot study. Because the raw sewage contained very high BOD, much of it remained in the effluent being discharged. The ability of the process in BOD removal 281 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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