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Anaerobic Filter — Kinetics and Application JAMES A. MUELLER, Associate Professor Environmental Engineering and Science Manhattan College Bronx, New York 10471 JOHN L. MANCINI, President Hydroscience, Inc. West Wood, New Jersey 07675 INTRODUCTION The anaerobic filter is basically a column or tower filled with rock or synthetic media operated in the upflow mode. Recent research on this process indicates it is a viable system for pretreatment of high strength industrial wastes. This paper presents the results of a research effort conducted to obtain a useful kinetic model of the system and to push the system experimentally to the limits of its capability. LITERATURE REVIEW A summary of anaerobic filter investigations conducted to date with their significance is given in Table I. In 1968, Young and McCarty (1, 2) conducted the initial research on the filter and presented the following equation to predict soluble ultimate BOD removal efficiency (%E). %E= 100(1 - L8 ) (1) t where, t * hydraulic detention time based on initial void volume. They also developed a mathematical model incorporating biological growth, solids transport, diffusional resistance of the biofilm and non-steady state solids buildup. The model was useful in describing the various process mechanisms but too complex for analysis or design. Following Young and McCarty's work, a number of studies were conducted to determine the applicability of the process to various types of industrial waste. Successful operation was obtained for all the wastes studied except for the petrochemical wastes, the latter due either to the toxicity of the raw waste, high H2S concentrations, or low pH produced in the filter. Figure 1 presents a plot of the COD removals obtained by all investigators against hydraulic detention time. The design equation presented by Young and McCarty for soluble ultimate BOD is seen to represent the upper bound of the highly scattered data. The lower removals obtained for many of the studies is due either to the nature of the specific industrial wastes or to high solids carryover. From two studies, data on sludge age versus 423
Object Description
Purdue Identification Number | ETRIWC1975036 |
Title | Anaerobic filter : kinetics and application |
Author |
Mueller, James A. Mancini, John L. |
Date of Original | 1975 |
Conference Title | Proceedings of the 30th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,25691 |
Extent of Original | p. 423-447 |
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 | 2009-06-29 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page423 |
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 | Anaerobic Filter — Kinetics and Application JAMES A. MUELLER, Associate Professor Environmental Engineering and Science Manhattan College Bronx, New York 10471 JOHN L. MANCINI, President Hydroscience, Inc. West Wood, New Jersey 07675 INTRODUCTION The anaerobic filter is basically a column or tower filled with rock or synthetic media operated in the upflow mode. Recent research on this process indicates it is a viable system for pretreatment of high strength industrial wastes. This paper presents the results of a research effort conducted to obtain a useful kinetic model of the system and to push the system experimentally to the limits of its capability. LITERATURE REVIEW A summary of anaerobic filter investigations conducted to date with their significance is given in Table I. In 1968, Young and McCarty (1, 2) conducted the initial research on the filter and presented the following equation to predict soluble ultimate BOD removal efficiency (%E). %E= 100(1 - L8 ) (1) t where, t * hydraulic detention time based on initial void volume. They also developed a mathematical model incorporating biological growth, solids transport, diffusional resistance of the biofilm and non-steady state solids buildup. The model was useful in describing the various process mechanisms but too complex for analysis or design. Following Young and McCarty's work, a number of studies were conducted to determine the applicability of the process to various types of industrial waste. Successful operation was obtained for all the wastes studied except for the petrochemical wastes, the latter due either to the toxicity of the raw waste, high H2S concentrations, or low pH produced in the filter. Figure 1 presents a plot of the COD removals obtained by all investigators against hydraulic detention time. The design equation presented by Young and McCarty for soluble ultimate BOD is seen to represent the upper bound of the highly scattered data. The lower removals obtained for many of the studies is due either to the nature of the specific industrial wastes or to high solids carryover. From two studies, data on sludge age versus 423 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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