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Electrolytic Control of Anaerobic Waste Treatment Processes FREDERIC C. BLANC, Assistant Professor Department of Civil Engineering Northeastern University Boston, Massachusetts 02115 INTRODUCTION Anaerobic treatment processes have provided an effective and economical means of stabilizing the concentrated wastewaters of certain industries and various types of organic sludges. The major portion of the municipal sewage sludge in North America is anaerobically treated. However, the full potential and capacity of anaerobic treatment is not being utilized due to a lack of understanding of the process and inadequate process monitoring and control. Automated process monitoring is possible by continuously measuring electrode potentials in the anaerobic solution. It has been demonstrated (1.2,3) that electrode potential measurement is a monitoring parameter for the methane fermentation stage of anaerobic sludge digestion. The possibility of controlling anaerobic treatment processes by correcting pH depression using direct current electrolysis was demonstrated in a previous investigation (3). In order to apply electrolytic pH control on a plant scale, the proper sizes, types and configurations of electrodes, types of solution connections and other design parameters must be determined. This investigation was conducted in order to establish some of the requirements and design parameters needed. BACKGROUND In wastewater treatment practice electrodialysis is the only process normally- considered when electrochemical treatment is mentioned. However, various electrolytic processes have been used and proposed for wastewater treatment since the year 1889. Miller and Knipe(4) have summarized the various electrochemical processes which have been used for wastewater treatment. Most of the electrochemical wastewater treatment processes used electrolysis to generate chlorine and metal ions in municipal sewage or municipal sewage mixed with sea water. The chlorine generated at the anode surface would chemically oxidize materials in the wastewater and kill bacteria. By selecting a suitable anode material such as iron or aluminum it is possible to generate coagulant ions which would improve suspended solids removal, form chemical precipitates and provide an intermediate degree of wastewater treatment. The concept of using direct current electrolysis to increase the pH of a solution is not new, but until recently (5) is was never proposed for the anaerobic digestion process. No mention of pH control by electrolysis could be found in the wastewater treatment literature. An examination of patent literature did indicate that this type of pH control had been used or proposed for use in other fields. In 1914, the Berna Milk Company of Thun Switzerland (6) received a British patent relating to a process for the deacidification of milk by subjecting it to an electric current. The application for this patent does not indicate the electrochemical reactions involved. In 1939, Brigs (7) obtained a process patent for varying the pH of sugar refining juices. Hydrogen evolution at the cathode and chlorine evolution at the anode were mentioned in the disclosure for this patent. Sandstrom (8) patented a device for changing the pH of a fermentable liquids. Thompson, et al (9) received a patent for an electrolytic pH regulator. This apparatus was designed to be used in laboratory experiments involving microbial cell and tissue culture media. It consisted of an outer platinum electrode which surrounded an inner electrode of silver. Hydrogen would be generated at the platinum e- electrode with silver chloride forming at the silver electrode. 349
Object Description
Purdue Identification Number | ETRIWC197333 |
Title | Electrolytic control of anaerobic waste treatment processes |
Author | Blanc, Frederic 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. 349-357 |
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 349 |
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 | Electrolytic Control of Anaerobic Waste Treatment Processes FREDERIC C. BLANC, Assistant Professor Department of Civil Engineering Northeastern University Boston, Massachusetts 02115 INTRODUCTION Anaerobic treatment processes have provided an effective and economical means of stabilizing the concentrated wastewaters of certain industries and various types of organic sludges. The major portion of the municipal sewage sludge in North America is anaerobically treated. However, the full potential and capacity of anaerobic treatment is not being utilized due to a lack of understanding of the process and inadequate process monitoring and control. Automated process monitoring is possible by continuously measuring electrode potentials in the anaerobic solution. It has been demonstrated (1.2,3) that electrode potential measurement is a monitoring parameter for the methane fermentation stage of anaerobic sludge digestion. The possibility of controlling anaerobic treatment processes by correcting pH depression using direct current electrolysis was demonstrated in a previous investigation (3). In order to apply electrolytic pH control on a plant scale, the proper sizes, types and configurations of electrodes, types of solution connections and other design parameters must be determined. This investigation was conducted in order to establish some of the requirements and design parameters needed. BACKGROUND In wastewater treatment practice electrodialysis is the only process normally- considered when electrochemical treatment is mentioned. However, various electrolytic processes have been used and proposed for wastewater treatment since the year 1889. Miller and Knipe(4) have summarized the various electrochemical processes which have been used for wastewater treatment. Most of the electrochemical wastewater treatment processes used electrolysis to generate chlorine and metal ions in municipal sewage or municipal sewage mixed with sea water. The chlorine generated at the anode surface would chemically oxidize materials in the wastewater and kill bacteria. By selecting a suitable anode material such as iron or aluminum it is possible to generate coagulant ions which would improve suspended solids removal, form chemical precipitates and provide an intermediate degree of wastewater treatment. The concept of using direct current electrolysis to increase the pH of a solution is not new, but until recently (5) is was never proposed for the anaerobic digestion process. No mention of pH control by electrolysis could be found in the wastewater treatment literature. An examination of patent literature did indicate that this type of pH control had been used or proposed for use in other fields. In 1914, the Berna Milk Company of Thun Switzerland (6) received a British patent relating to a process for the deacidification of milk by subjecting it to an electric current. The application for this patent does not indicate the electrochemical reactions involved. In 1939, Brigs (7) obtained a process patent for varying the pH of sugar refining juices. Hydrogen evolution at the cathode and chlorine evolution at the anode were mentioned in the disclosure for this patent. Sandstrom (8) patented a device for changing the pH of a fermentable liquids. Thompson, et al (9) received a patent for an electrolytic pH regulator. This apparatus was designed to be used in laboratory experiments involving microbial cell and tissue culture media. It consisted of an outer platinum electrode which surrounded an inner electrode of silver. Hydrogen would be generated at the platinum e- electrode with silver chloride forming at the silver electrode. 349 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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