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Effects of Loading on a Biological Tertiary Treatment System H. KIRK WILLARD, Predoctoral Research Associate D. A. CARLSON, Professor of Civil Engineering Department of Civil Engineering University of Washington Seattle, Washington INTRODUCTION Effluents from conventional wastewater treatment facilities contain a variety of materials which can act as nutrients to the receiving waters. As the effluent discharges increase in quantity the effect of the nutrient input to the natural receiving waters becomes more evident (1). The wastage of fertilizing materials has been increasing in the recent past and predictions for the future indicate rapidly increasing amounts of such nutrients will be added to our streams in the decades ahead (2). Often secondary treatment is insufficient protection for receiving waters, especially for the discharge from relatively large plants or an accumulation of treatment plants. Such plants may emit waste streams with 25 mg/l of SS and have BOD values in the range of 15 to 25 mg/l. These treated waste streams are still able to exert a significant detrimental effect on the receiving stream. Both Downing (3) and Reynolds and Yang (4) emphasize the effects of this effluent load, which is largely waste biomass, as a critical parameter in assessing the performance of conventional waste treatment processes. The removal of sizeable quantities of non-settle able materials from secondary treatment facilities often requires advanced waste treatment processes to effect adequate removal (5). In an effort to understandhow treatment plants might be more effectively designed, a new treatment system has been studied at the University of Washington. A schematic drawing of how this system might appear is shown in Figure 1. The two phases of this system are a biosynthesis step and a biomass reduction or particulate scrubbing unit. Each stage of this system is carried out biologically. PARTICULATE SCRUBBING SYSTEM THEORY The particulate scrubbing phase of our system, composed of an aerated channel with a large surface to volume ratio, provides the proper environment for at- Aeration Unit -ionass deduction I'nit u.C.D. Renoval Figure 1 - New two-phase waste treatment system. - 740 -
Object Description
Purdue Identification Number | ETRIWC196860 |
Title | Effects of wading on a biological tertiary treatment system |
Author |
Willard, H. Kirk Carlson, Dale A. |
Date of Original | 1968 |
Conference Title | Proceedings of the 23rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,15314 |
Extent of Original | p. 740-753 |
Series |
Engineering extension series no. 132 Engineering bulletin v. 53, no. 2 |
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 | 2009-05-20 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 740 |
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 | Effects of Loading on a Biological Tertiary Treatment System H. KIRK WILLARD, Predoctoral Research Associate D. A. CARLSON, Professor of Civil Engineering Department of Civil Engineering University of Washington Seattle, Washington INTRODUCTION Effluents from conventional wastewater treatment facilities contain a variety of materials which can act as nutrients to the receiving waters. As the effluent discharges increase in quantity the effect of the nutrient input to the natural receiving waters becomes more evident (1). The wastage of fertilizing materials has been increasing in the recent past and predictions for the future indicate rapidly increasing amounts of such nutrients will be added to our streams in the decades ahead (2). Often secondary treatment is insufficient protection for receiving waters, especially for the discharge from relatively large plants or an accumulation of treatment plants. Such plants may emit waste streams with 25 mg/l of SS and have BOD values in the range of 15 to 25 mg/l. These treated waste streams are still able to exert a significant detrimental effect on the receiving stream. Both Downing (3) and Reynolds and Yang (4) emphasize the effects of this effluent load, which is largely waste biomass, as a critical parameter in assessing the performance of conventional waste treatment processes. The removal of sizeable quantities of non-settle able materials from secondary treatment facilities often requires advanced waste treatment processes to effect adequate removal (5). In an effort to understandhow treatment plants might be more effectively designed, a new treatment system has been studied at the University of Washington. A schematic drawing of how this system might appear is shown in Figure 1. The two phases of this system are a biosynthesis step and a biomass reduction or particulate scrubbing unit. Each stage of this system is carried out biologically. PARTICULATE SCRUBBING SYSTEM THEORY The particulate scrubbing phase of our system, composed of an aerated channel with a large surface to volume ratio, provides the proper environment for at- Aeration Unit -ionass deduction I'nit u.C.D. Renoval Figure 1 - New two-phase waste treatment system. - 740 - |
Resolution | 300 ppi |
Color Depth | 8 bit |
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