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Effect of Heavy Metals on Anaerobic Digestion and the Role of Regulatory Agency when Municipal Sewage Treatment Plant is Upset TERRY M. REGAN, Acting Director Department of Water Pollution Control City of Lexington Lexington, Kentucky MERCER M. PETERS, Chief Chemist Water Pollution Control Commission Frankfort, Kentucky INTRODUCTION The main Lexington Waste Water Treatment Plant is a 12 MGD Kraus Modified Activated Sludge Plant with dual aeration. The digestion facilities consist of two primary digesters with a capacity of 1 MG each and equipped with PFT floating covers, external heat exchangers and Perth gas recirculation equipment. In addition to the primary digesters, there are four secondary digesters with a capacity of approximately 300,000 gal each and equipped with PFT floating covers and stand by hot water heating coils. At the time of the failure, the average daily flow at this plant was some 12 MGD with a daily withdrawal of some 75,000 gal of raw sludge, having a total solids content of some six to eight per cent from the primary settling tanks to the primary digesters daily. PLANT OPERATION Sludge is pumped from the primary settling tanks every two hr to the primary digesters. The primary digesters are used alternately and, therefore, receive sludge on a four hr alternating schedule. At the time of the failure, there was a 20 to 25 day retention time in the primary digesters and a 10 to 15 day retention in the secondary digesters. The primary digesters produce over 200,000 cu ft of gas a day. This gas is the primary fuel for three blower engines, all heat exchanger units and the heating system for the three largest building complexes in the plant. This gas represents 85 per cent of the plant's fuel requirements or, in dollars, some $36,000 per year. As important as this gas production is, it is not as important as the production of usable supernatant or digester liquor. The gas represents cost savings but the supernatant is essential for the operation of a Kraus modified plant. Without supernatant the Kraus plant is converted to a conventional activated sludge plant with a resulting loss of some 30 to 40 per cent of capacity. The city of Lexington, with a population of some 80,000 (in 1967), is located atop a geological dome some 15 miles from the nearest large body of water (The -645-
Object Description
Purdue Identification Number | ETRIWC197067 |
Title | Effect of heavy metals on anaerobic digestion and the role of regulatory agency when municipal sewage treatment plant is upset |
Author |
Regan, Terry M. Peters, Mercer M. |
Date of Original | 1970 |
Conference Title | Proceedings of the 25th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,18196 |
Extent of Original | p. 645-651 |
Series | Engineering extension series no. 137 |
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 | 2009-06-09 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page645 |
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 | Effect of Heavy Metals on Anaerobic Digestion and the Role of Regulatory Agency when Municipal Sewage Treatment Plant is Upset TERRY M. REGAN, Acting Director Department of Water Pollution Control City of Lexington Lexington, Kentucky MERCER M. PETERS, Chief Chemist Water Pollution Control Commission Frankfort, Kentucky INTRODUCTION The main Lexington Waste Water Treatment Plant is a 12 MGD Kraus Modified Activated Sludge Plant with dual aeration. The digestion facilities consist of two primary digesters with a capacity of 1 MG each and equipped with PFT floating covers, external heat exchangers and Perth gas recirculation equipment. In addition to the primary digesters, there are four secondary digesters with a capacity of approximately 300,000 gal each and equipped with PFT floating covers and stand by hot water heating coils. At the time of the failure, the average daily flow at this plant was some 12 MGD with a daily withdrawal of some 75,000 gal of raw sludge, having a total solids content of some six to eight per cent from the primary settling tanks to the primary digesters daily. PLANT OPERATION Sludge is pumped from the primary settling tanks every two hr to the primary digesters. The primary digesters are used alternately and, therefore, receive sludge on a four hr alternating schedule. At the time of the failure, there was a 20 to 25 day retention time in the primary digesters and a 10 to 15 day retention in the secondary digesters. The primary digesters produce over 200,000 cu ft of gas a day. This gas is the primary fuel for three blower engines, all heat exchanger units and the heating system for the three largest building complexes in the plant. This gas represents 85 per cent of the plant's fuel requirements or, in dollars, some $36,000 per year. As important as this gas production is, it is not as important as the production of usable supernatant or digester liquor. The gas represents cost savings but the supernatant is essential for the operation of a Kraus modified plant. Without supernatant the Kraus plant is converted to a conventional activated sludge plant with a resulting loss of some 30 to 40 per cent of capacity. The city of Lexington, with a population of some 80,000 (in 1967), is located atop a geological dome some 15 miles from the nearest large body of water (The -645- |
Resolution | 300 ppi |
Color Depth | 8 bit |
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