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BENTHAL INTERACTIONS IN A KRAFT MILL WASTEWATER LAGOON M. R. Collins, Graduate Student Z. K. Chowdhury, Graduate Student C. W. Bryant, Assistant Professor Department of Civil Engineering and Engineering Mechanics University of Arizona Tucson, Arizona 85721 INTRODUCTION The performance of an aerated stabilization basin (ASB) is affected by the influent properties, the kinetics within the liquid layer, and the physical and biological processes in the benthal zone. This paper describes the impact of the later processes within an operational Kraft mill lagoon. The focus of this study was the first cell of a three-cell lagoon system treating a daily flow of about 100,000 m'/day from a Kraft mill. The treatment system is shown in Figure 1. Prior to input to the lagoon system, the alkaline waste stream was passed through a clarifier to remove cellulose fibers. The first cell to treat the entire waste stream was a partially suspended lagoon with a theoretical detention time of 7.7 days and an applied power level of 1.13 W/m'. The second partially suspended cell had a detention time of 6.5 days and an applied power level of 0.55 W/m'. The final cell provided a detention time of 12.6 days and no mechanical aeration. By florescent dye studies [1] the first aerated cell was found to have primary flow patterns as shown in Figure 2. The cell behaved as a series of three mixed reactor zones that interact with three corresponding dead zones, as shown in Figure 3. The total dead zone volume was 59% of the lagoon volume, and the effective detention time was only 3.3 days. After the hydraulics of the cell had been defined, il was of interest to define whether there was a discernible variation in benthal activity from zone to zone. Processes within the benthal zone result in the solubilization of organic solids and the subsequent stabilization or feedback of the soluble products. The total oxygen demand of the benthal solids may be: 1) exerted as a direct demand in the aerobic zone; 2) transported to the overlying water column Figure 1. Complete Kraft mill lagoon treatment system. Circles indicate the location of surface aerators. 325
Object Description
Purdue Identification Number | ETRIWC198533 |
Title | Benthal interactions in a kraft mill wastewater lagoon |
Author |
Collins, M. R. Chowdhury, Z. K. Bryant, C. W. (Curtis W.) |
Date of Original | 1985 |
Conference Title | Proceedings of the 40th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,36131 |
Extent of Original | p. 325-334 |
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 | 2009-07-15 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 325 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | BENTHAL INTERACTIONS IN A KRAFT MILL WASTEWATER LAGOON M. R. Collins, Graduate Student Z. K. Chowdhury, Graduate Student C. W. Bryant, Assistant Professor Department of Civil Engineering and Engineering Mechanics University of Arizona Tucson, Arizona 85721 INTRODUCTION The performance of an aerated stabilization basin (ASB) is affected by the influent properties, the kinetics within the liquid layer, and the physical and biological processes in the benthal zone. This paper describes the impact of the later processes within an operational Kraft mill lagoon. The focus of this study was the first cell of a three-cell lagoon system treating a daily flow of about 100,000 m'/day from a Kraft mill. The treatment system is shown in Figure 1. Prior to input to the lagoon system, the alkaline waste stream was passed through a clarifier to remove cellulose fibers. The first cell to treat the entire waste stream was a partially suspended lagoon with a theoretical detention time of 7.7 days and an applied power level of 1.13 W/m'. The second partially suspended cell had a detention time of 6.5 days and an applied power level of 0.55 W/m'. The final cell provided a detention time of 12.6 days and no mechanical aeration. By florescent dye studies [1] the first aerated cell was found to have primary flow patterns as shown in Figure 2. The cell behaved as a series of three mixed reactor zones that interact with three corresponding dead zones, as shown in Figure 3. The total dead zone volume was 59% of the lagoon volume, and the effective detention time was only 3.3 days. After the hydraulics of the cell had been defined, il was of interest to define whether there was a discernible variation in benthal activity from zone to zone. Processes within the benthal zone result in the solubilization of organic solids and the subsequent stabilization or feedback of the soluble products. The total oxygen demand of the benthal solids may be: 1) exerted as a direct demand in the aerobic zone; 2) transported to the overlying water column Figure 1. Complete Kraft mill lagoon treatment system. Circles indicate the location of surface aerators. 325 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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