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Algae Separation From Oxidation Pond Effluents A.A. FRIEDMAN, Assistant Professor Department of Civil Engineering Tennessee Technological University Cookeville, Tennessee 38501 DAVID A. PEAKS, Project Engineer AWARE, Inc. Nashville, Tennessee 37202 R.L. NICHOLS, President Nichols Engineering Services, Inc. Union City, Tennessee 38261 INTRODUCTION During the preceding two decades, thousands of oxidation ponds or stabilization lagoons have been built by municipalities and industries to meet secondary wastewater treatment objectives (1). Low capital cost accompanied by minimal operation and maintenance costs relative to conventional biological wastewater treatment systems led to the rapid adoption by designers concerned with treating small flows or seasonal wastewaters wherever land was relatively inexpensive. Design criteria based on organic surface loading rates and hydraulic detention times have been developed and adopted by most states. In general, well designed and operated stabilization lagoons have proven effective in removing soluble organic material from wastewaters. However, in recent years analyses of maturation and facultative lagoon effluents have indicated that effluent algae carryover can impose a significant oxygen demand on receiving waters (2, 3). Theoretical calculation of the oxygen demand created by algae destruction suggests that 1.58 mg of 02 are required to oxidize one mg of algae (dry weight) to C02 and water. Bare, et al. (4) found that 1.11 mg O, was required per mg of algae obtained from laboratory studies and 0.81 mg 02 per mg algae obtained from field studies. Varma and Digiano (5) reported that 0.67 mg 02 was required for each mg of algae destroyed. Data resulting from algae obtained in both laboratory and field experiments during this study indicate an oxygen demand of 1.19 mg 02 per mg algae as shown in Figure 1. Despite the cited differences in oxygen demand per unit weight of algae, one can conclude that a significant oxygen demand is imposed on receiving waters by algae discharged from lagoon effluents. Only the removal or destruction of algae prior to discharge can sufficiently improve effluent quality to an acceptable level so that lagoons can again be considered suitable for the design of low cost wastewater treatment systems. In 493
Object Description
Purdue Identification Number | ETRIWC1975041 |
Title | Algae separation from oxidation pond effluents |
Author |
Friedman, A. A. (Alexander A.) Peaks, David A. Nichols, R. 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. 493-505 |
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 | page493 |
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 | Algae Separation From Oxidation Pond Effluents A.A. FRIEDMAN, Assistant Professor Department of Civil Engineering Tennessee Technological University Cookeville, Tennessee 38501 DAVID A. PEAKS, Project Engineer AWARE, Inc. Nashville, Tennessee 37202 R.L. NICHOLS, President Nichols Engineering Services, Inc. Union City, Tennessee 38261 INTRODUCTION During the preceding two decades, thousands of oxidation ponds or stabilization lagoons have been built by municipalities and industries to meet secondary wastewater treatment objectives (1). Low capital cost accompanied by minimal operation and maintenance costs relative to conventional biological wastewater treatment systems led to the rapid adoption by designers concerned with treating small flows or seasonal wastewaters wherever land was relatively inexpensive. Design criteria based on organic surface loading rates and hydraulic detention times have been developed and adopted by most states. In general, well designed and operated stabilization lagoons have proven effective in removing soluble organic material from wastewaters. However, in recent years analyses of maturation and facultative lagoon effluents have indicated that effluent algae carryover can impose a significant oxygen demand on receiving waters (2, 3). Theoretical calculation of the oxygen demand created by algae destruction suggests that 1.58 mg of 02 are required to oxidize one mg of algae (dry weight) to C02 and water. Bare, et al. (4) found that 1.11 mg O, was required per mg of algae obtained from laboratory studies and 0.81 mg 02 per mg algae obtained from field studies. Varma and Digiano (5) reported that 0.67 mg 02 was required for each mg of algae destroyed. Data resulting from algae obtained in both laboratory and field experiments during this study indicate an oxygen demand of 1.19 mg 02 per mg algae as shown in Figure 1. Despite the cited differences in oxygen demand per unit weight of algae, one can conclude that a significant oxygen demand is imposed on receiving waters by algae discharged from lagoon effluents. Only the removal or destruction of algae prior to discharge can sufficiently improve effluent quality to an acceptable level so that lagoons can again be considered suitable for the design of low cost wastewater treatment systems. In 493 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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