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Treatment of Pulp and Paper Mill Waste for High Rate Filtration Using Plastic Filter Media W. WESLEY ECKENFELDER, JR., Associate Professor of Sanitary Engineering and EDWIN L. BARNHART, Research Associate Department of Civil Engineering Manhattan College Riverdale, New York In recent years plastic filter media has been applied to the treatment of pulp and paper mill wastes. Hydraulic loadings as high as 4.0 gpm/ft2 and organic loadings as high as 800 lbs BOD/1000 ft3/day have been employed. BOD removals as high as 50 per cent have been reported under these conditions. The performance of these filters has been related to the filter depth, the contact time between waste flow and filter surface and the quantity of active slime on the filter media. This paper presents results obtained relating contact time to filter surface and on the BOD removal capacity of two types of filter media in the treatment of dilute black liquor and a board mill waste. RESIDENCE TIME RELATIONSHIPS It has long been recognized that the time of contact of a waste with a filter surface influences the BOD removal rate. Time of contact is in turn related to the hydraulic loading and to the presence of filter slime. Typical results obtained on various filter media relating mean contact time to hydraulic loading are shown in Figure 1. It is apparent from Figure 1 that increasing the hydraulic load will decrease the mean residence time. A general relationship developed by the authors showed that contact time per unit filter depth is related to the specific surface (ft2/ft3) ofthe filter media and to the hydraulic loading through the relationship: t/D . C^ CD in which t = mean residence time D = filter depth C = constant Ay = specific surface Q = hydraulic loading m & n = constants In Equation (1) m is a constant for any geometrically similar media and n decreases as Av decreases. The presence of filter slime influences the residence time-hydraulic loading relationship. Bloodgood, et al. (1), showed that for flow over an inclined plane, the increase in retention time in the presence of slime employ- - 105 -
Object Description
Purdue Identification Number | ETRIWC196211 |
Title | Treatment of pulp and paper mill waste for high rate filtration using plastic filter media |
Author |
Eckenfelder, W. Wesley (William Wesley), 1926- Barnhart, Edwin L. |
Date of Original | 1962 |
Conference Title | Proceedings of the seventeenth Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/cdm4/document.php?CISOROOT=/engext&CISOPTR=9369&REC=10 |
Extent of Original | p. 105-115 |
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 | 2009-05-18 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 105 |
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 | Treatment of Pulp and Paper Mill Waste for High Rate Filtration Using Plastic Filter Media W. WESLEY ECKENFELDER, JR., Associate Professor of Sanitary Engineering and EDWIN L. BARNHART, Research Associate Department of Civil Engineering Manhattan College Riverdale, New York In recent years plastic filter media has been applied to the treatment of pulp and paper mill wastes. Hydraulic loadings as high as 4.0 gpm/ft2 and organic loadings as high as 800 lbs BOD/1000 ft3/day have been employed. BOD removals as high as 50 per cent have been reported under these conditions. The performance of these filters has been related to the filter depth, the contact time between waste flow and filter surface and the quantity of active slime on the filter media. This paper presents results obtained relating contact time to filter surface and on the BOD removal capacity of two types of filter media in the treatment of dilute black liquor and a board mill waste. RESIDENCE TIME RELATIONSHIPS It has long been recognized that the time of contact of a waste with a filter surface influences the BOD removal rate. Time of contact is in turn related to the hydraulic loading and to the presence of filter slime. Typical results obtained on various filter media relating mean contact time to hydraulic loading are shown in Figure 1. It is apparent from Figure 1 that increasing the hydraulic load will decrease the mean residence time. A general relationship developed by the authors showed that contact time per unit filter depth is related to the specific surface (ft2/ft3) ofthe filter media and to the hydraulic loading through the relationship: t/D . C^ CD in which t = mean residence time D = filter depth C = constant Ay = specific surface Q = hydraulic loading m & n = constants In Equation (1) m is a constant for any geometrically similar media and n decreases as Av decreases. The presence of filter slime influences the residence time-hydraulic loading relationship. Bloodgood, et al. (1), showed that for flow over an inclined plane, the increase in retention time in the presence of slime employ- - 105 - |
Resolution | 300 ppi |
Color Depth | 8 bit |
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