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■ Digester Gaslifter Mixing at Aurora Walter A. Sperry, Superintendent Aurora Sanitary District Aurora, Illinois On October 4th, 1957, the Aurora Sanitary District placed in operation, and for test, the first unit of a device for applying effective mixing to digestors. The purpose of this paper is to describe the apparatus and report some of the test results obtained. The Aurora plant had just completed (June 1956) two new and identical primary digesters. They were 50 ft square with a side wall depth of 16 ft and a capacity of 40,000 cu ft or 300,000 gallons each. They had flat fixed covers (8 in total rise) supported with four internal columns. The gas domes were 4 ft square and 4 ft 6 in high. The floor had a slope of 1 to 6 from a center sludge pocket, the center depth to the floor being 20 ft. They were heated by Walker Process "Heatx" equipment with 250 gpm circulating pumps. Primary sludge enters the digester from a tipping bucket meter about 8 ft out from the west wall and 5 ft below the digester roof. Since both digesters are fed with equal amounts of primary sludge, tests of the apparatus against an unmixed control could easily be made. The new gas recirculation apparatus consisted of three gas lift pumps operated by a Roots-Connersville compressor formerly used to preaerate raw sewage. This compressor was slowed to the proper capacity, and was equipped with an excess pressure relief, low pressure by-pass regulator, and excess temperature controller. The three Gaslifter pump tubes were 16 in in diameter and 14 ft long. The upper ends of these tubes were welded into the bottom of a common discharge head 36 in in diameter and with a 12 in side wall. The pump tubes and discharge head were supported from an agle-iron cage welded to the underside of the heavy gas dome coverplate. Thus the whole assembly could be lowered into position in the digester with a crane, and the gasketed coverplate bolted home. It was unnecessary therefore, to disturb the digester. When in position, the pump assembly hung centrally suspended from the gas dome cover. The overflow edge of the upper discharge head was 2.5 ft below the roof of the digester. 653
Object Description
Purdue Identification Number | ETRIWC195857 |
Title | Digester gaslifter mixing at Aurora |
Author | Sperry, Walter A. |
Date of Original | 1958 |
Conference Title | Proceedings of the thirteenth Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/cdm4/document.php?CISOROOT=/engext&CISOPTR=5739&REC=6 |
Extent of Original | p. 653-661 |
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 | 2008-09-22 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 653 |
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 | ■ Digester Gaslifter Mixing at Aurora Walter A. Sperry, Superintendent Aurora Sanitary District Aurora, Illinois On October 4th, 1957, the Aurora Sanitary District placed in operation, and for test, the first unit of a device for applying effective mixing to digestors. The purpose of this paper is to describe the apparatus and report some of the test results obtained. The Aurora plant had just completed (June 1956) two new and identical primary digesters. They were 50 ft square with a side wall depth of 16 ft and a capacity of 40,000 cu ft or 300,000 gallons each. They had flat fixed covers (8 in total rise) supported with four internal columns. The gas domes were 4 ft square and 4 ft 6 in high. The floor had a slope of 1 to 6 from a center sludge pocket, the center depth to the floor being 20 ft. They were heated by Walker Process "Heatx" equipment with 250 gpm circulating pumps. Primary sludge enters the digester from a tipping bucket meter about 8 ft out from the west wall and 5 ft below the digester roof. Since both digesters are fed with equal amounts of primary sludge, tests of the apparatus against an unmixed control could easily be made. The new gas recirculation apparatus consisted of three gas lift pumps operated by a Roots-Connersville compressor formerly used to preaerate raw sewage. This compressor was slowed to the proper capacity, and was equipped with an excess pressure relief, low pressure by-pass regulator, and excess temperature controller. The three Gaslifter pump tubes were 16 in in diameter and 14 ft long. The upper ends of these tubes were welded into the bottom of a common discharge head 36 in in diameter and with a 12 in side wall. The pump tubes and discharge head were supported from an agle-iron cage welded to the underside of the heavy gas dome coverplate. Thus the whole assembly could be lowered into position in the digester with a crane, and the gasketed coverplate bolted home. It was unnecessary therefore, to disturb the digester. When in position, the pump assembly hung centrally suspended from the gas dome cover. The overflow edge of the upper discharge head was 2.5 ft below the roof of the digester. 653 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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