| Main Title |
Technology assessment of the deep shaft biological reactor / |
| CORP Author |
Roy F. Weston, inc. |
| Publisher |
Municipal Environmental Research Laboratory, |
| Year Published |
1982 |
| Report Number |
EPA-600/2-82-002; EPA-68-03-2775; PB82237793 |
| Stock Number |
PB82-237793 |
| OCLC Number |
15530662 |
| Subjects |
Sewage--Purification--Activated sludge process
|
| Additional Subjects |
Sewage treatment ;
Technology assessment ;
Activated sludge process ;
Cost analysis ;
Design criteria ;
Performance evaluation ;
Biochemical oxygen demand ;
Deep shaft biological treatment process
|
| Internet Access |
|
| Holdings |
| Library |
Call Number |
Additional Info |
Location |
Last
Modified |
Checkout
Status |
| EJBD |
EPA 600-2-82-002 |
|
Headquarters Library/Washington,DC |
04/27/2016 |
| ELBD ARCHIVE |
EPA 600-2-82-002 |
Received from HQ |
AWBERC Library/Cincinnati,OH |
10/04/2023 |
| ELBD |
EPA 600-2-82-002 |
|
AWBERC Library/Cincinnati,OH |
11/20/1998 |
| ESAD |
EPA 600-2-82-002 |
|
Region 10 Library/Seattle,WA |
06/03/2005 |
| NTIS |
PB82-237793 |
Some EPA libraries have a fiche copy filed under the call number shown. |
|
07/26/2022 |
|
| Collation |
xi, 74 p. : ill. ; 28 cm. |
| Abstract |
The Deep Shaft biological treatment process is essentially a high-rate activated sludge process capable of operating at BOD5 loading ratios (F/M) between 0.5 and 2.0 kg BOD5/kg MLVSS. The hardware consists of a vertical subsurface reactor between 90 and 250 m (300 to 800 ft) deep, with hydraulic mean residence times on the order of 60 minutes. Depending on the operating mixed liquor volatile suspended solids concentration, the effluent from the reactor can be treated utilizing either the flotation or sedimentation process. Based on a cost and energy analysis, no definitive conclusions could be drawn relative to cost or energy savings that can be realized by use of the Deep Shaft process. For the plant capacities used in the cost analysis (1,892 to 37,850 cu m/d; 0.5 to 10.0 mgd), the installed capital cost estimates for the Deep Shaft process were equivalent (+ or - 25%) to the conventional air activated sludge process. Unit energy requirements (kwh/1000 cu m) were highest for the Deep Shaft process when treating domestic wastewater. |
| Notes |
"February 1982." "EPA-600/2-82-002." "Contract No. 68-03-2775." Includes bibliographical references (p. 60-62). |
| Place Published |
Cincinnati, Ohio |
| Corporate Au Added Ent |
Roy F. Weston, inc.; Municipal Environmental Research Laboratory. |
| PUB Date Free Form |
1982 |
| NTIS Prices |
PC A05/MF A01 |
| BIB Level |
m |
| Cataloging Source |
OCLC/T |
| Merged OCLC records |
15463196 |
| OCLC Time Stamp |
20140521121919 |
| Language |
eng |
| SUDOCS Number |
EP 1.89/2:600/2-82-002 |
| Origin |
OCLC |
| Type |
MERGE |
| OCLC Rec Leader |
01283cam 2200349Ia 45020 |
