page230 |
Previous | 1 of 9 | Next |
|
|
Loading content ...
Organic Concentration and Hydraulic Loading Versus Organic Loading in Evaluation of Trickling Filter Performance ECHOL E. COOK, Assistant Professor DON F. KINCANNON, Associate Professor School of Civil Engineering Oklahoma State University Stillwater, Oklahoma INTRODUCTION During the past several years a great deal of research has been conducted on the trickling filter process of waste treatment. Lately, a great deal of the research has centered on the development of new design formulations. The major consideration is whether the efficiency of a trickling filter is dependent upon the organic concentration of a waste, or the hydraulic flow rate. Investigators in the field are in conflict over the relative importance of each of these two parameters. Velz (1), Germain (2) Galler and Gotaas(3) contend that the organic concentration of the waste is the controlling factor in the removal of BOD realized in a trickling filter. Schulze (4,5,6), Eckenfelder (7,8,9) and Etzel (10) indicate that the hydraulic loading or flow rate is the most important parameter to consider. Horton (11), Howland (12), Eckenfelder (9), and Sinkoff (13), believe that detention time or contact time between the waste and the filter biota determines the removal of BOD realized in a trickling filter. As contact time is related to flow rate, these may be considered to be the same parameter. Ingram (14) and the National Research Council (15), indicate that the important parameter to consider is the total lb of BOD applied to a filter, thus taking into account both the flow rate and the concentration of the waste. The purpose of this investigation was to observe the relationship of the organic concentration of a waste and its flow rate and their influence on the removal of organics in a trickling filter. EXPERIMENT, EQUIPMENT AND PROCEDURE A model fixed bed reactor has been designed and built in this laboratory to study selected design parameters of fixed bed reactors. The general arrangement of the experimental fixed bed reactor is shown in Figure 1. Tap water from the city main enters into a constant head tank from which the flow is controlled by a rotameter and flows into a wet well. The concentrated synthetic waste is pumped into the wet well where it is mixed with the tap water to provide the concentration of waste desired. If it is desired to study an industrial waste in order to gain design data, then the constant head tank could be utilized as the reservoir for the soluble waste. Also, in this case, the concentrated feed unit would be eliminated. The waste is pumped from the wet well to the distribution system. The waste is sprayed over -230-
Object Description
Purdue Identification Number | ETRIWC197022 |
Title | Organic concentration and hydraulic loading versus organic loading in evaluation of trickling filter performance |
Author |
Cook, Echol E. Kincannon, Don F. |
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. 230-238 |
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 | page230 |
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 | Organic Concentration and Hydraulic Loading Versus Organic Loading in Evaluation of Trickling Filter Performance ECHOL E. COOK, Assistant Professor DON F. KINCANNON, Associate Professor School of Civil Engineering Oklahoma State University Stillwater, Oklahoma INTRODUCTION During the past several years a great deal of research has been conducted on the trickling filter process of waste treatment. Lately, a great deal of the research has centered on the development of new design formulations. The major consideration is whether the efficiency of a trickling filter is dependent upon the organic concentration of a waste, or the hydraulic flow rate. Investigators in the field are in conflict over the relative importance of each of these two parameters. Velz (1), Germain (2) Galler and Gotaas(3) contend that the organic concentration of the waste is the controlling factor in the removal of BOD realized in a trickling filter. Schulze (4,5,6), Eckenfelder (7,8,9) and Etzel (10) indicate that the hydraulic loading or flow rate is the most important parameter to consider. Horton (11), Howland (12), Eckenfelder (9), and Sinkoff (13), believe that detention time or contact time between the waste and the filter biota determines the removal of BOD realized in a trickling filter. As contact time is related to flow rate, these may be considered to be the same parameter. Ingram (14) and the National Research Council (15), indicate that the important parameter to consider is the total lb of BOD applied to a filter, thus taking into account both the flow rate and the concentration of the waste. The purpose of this investigation was to observe the relationship of the organic concentration of a waste and its flow rate and their influence on the removal of organics in a trickling filter. EXPERIMENT, EQUIPMENT AND PROCEDURE A model fixed bed reactor has been designed and built in this laboratory to study selected design parameters of fixed bed reactors. The general arrangement of the experimental fixed bed reactor is shown in Figure 1. Tap water from the city main enters into a constant head tank from which the flow is controlled by a rotameter and flows into a wet well. The concentrated synthetic waste is pumped into the wet well where it is mixed with the tap water to provide the concentration of waste desired. If it is desired to study an industrial waste in order to gain design data, then the constant head tank could be utilized as the reservoir for the soluble waste. Also, in this case, the concentrated feed unit would be eliminated. The waste is pumped from the wet well to the distribution system. The waste is sprayed over -230- |
Resolution | 300 ppi |
Color Depth | 8 bit |
Tags
Comments
Post a Comment for page230