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The Treatment of Toxic Industrial Wastewaters By A Two Step Process ALLAN R. WILHELMI, Industrial Application Engineer ROBERT B. ELY, Manager of Industrial Sales Zimpro, Inc. (Division of Sterling Drug) Rothschild, Wisconsin 54474 INTRODUCTION The objective of this paper is to describe the applicability and flexibility of an environmental engineering unit process called "Wet Air Oxidation" to the treatment of a large class of industrial wastewaters which do not readily lend themselves to treatment by other means. For this "class," biological treatment is either impossible or extremely difficult because the wastes are biologically refractory or are toxic to treatment organisms. Incineration is likely to be uneconomical in light of present energy costs because the flow is high and/ or the waste is dilute. Further, incineration might be impractical if an air pollution problem is created. These factors together with the pressure to abandon deep well and ocean dumping as disposal means are causing more attention to be focused on wet air oxidation as a viable treatment alternative. The process of wet air oxidation is well established; more than 120 Zimpro Inc. wet air oxidation units are either in operation or under construction throughout the world. A number are dedicated specifically to the treatment of problem industrial wastes. Included in this category are the wastes from the manufacture of acrylonitrile, monodosium glutamate, polysulfide based rubbers, metallurgical coke, petrochemicals, and pharmaceuticals. Although wet air oxidation alone may be used as the complete treatment process it is often uneconomical to achieve the typically required 99+% reductions in a single step. Instead, a two-step approach can be effectively used; the first, wet air oxidation accomplishing 50-95% COD reduction, the second, a biological or biophysical polishing step. The emphasis of this paper will be to demonstrate the compatibility between wet air oxidation and biological treatment and in particular biophysical treatment. WET AIR OXIDATION Almost any material that is subject to oxidation — biological, chemical, or thermal — can be oxidized at relatively low temperatures, under water, in the presence of air. Wet air oxidation should not be confused with submerged combustion in that temperatures in the wet air oxidation process rarely rise above 400 to 600 F and no flame is involved. Figure I shows the basic elements of a wet air oxidation flow scheme. Wastewater containing some oxidizable material is pumped through an exchanger. There the temperature is increased to a point at which the reaction between the oxidizable material 288
Object Description
Purdue Identification Number | ETRIWC1975024 |
Title | Treatment of toxic industrial wastewaters by a two step process |
Author |
Wilhelmi, Allan R. Ely, R. B. (Robert B.) |
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. 288-295 |
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 | 2009-06-25 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page288 |
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 | The Treatment of Toxic Industrial Wastewaters By A Two Step Process ALLAN R. WILHELMI, Industrial Application Engineer ROBERT B. ELY, Manager of Industrial Sales Zimpro, Inc. (Division of Sterling Drug) Rothschild, Wisconsin 54474 INTRODUCTION The objective of this paper is to describe the applicability and flexibility of an environmental engineering unit process called "Wet Air Oxidation" to the treatment of a large class of industrial wastewaters which do not readily lend themselves to treatment by other means. For this "class," biological treatment is either impossible or extremely difficult because the wastes are biologically refractory or are toxic to treatment organisms. Incineration is likely to be uneconomical in light of present energy costs because the flow is high and/ or the waste is dilute. Further, incineration might be impractical if an air pollution problem is created. These factors together with the pressure to abandon deep well and ocean dumping as disposal means are causing more attention to be focused on wet air oxidation as a viable treatment alternative. The process of wet air oxidation is well established; more than 120 Zimpro Inc. wet air oxidation units are either in operation or under construction throughout the world. A number are dedicated specifically to the treatment of problem industrial wastes. Included in this category are the wastes from the manufacture of acrylonitrile, monodosium glutamate, polysulfide based rubbers, metallurgical coke, petrochemicals, and pharmaceuticals. Although wet air oxidation alone may be used as the complete treatment process it is often uneconomical to achieve the typically required 99+% reductions in a single step. Instead, a two-step approach can be effectively used; the first, wet air oxidation accomplishing 50-95% COD reduction, the second, a biological or biophysical polishing step. The emphasis of this paper will be to demonstrate the compatibility between wet air oxidation and biological treatment and in particular biophysical treatment. WET AIR OXIDATION Almost any material that is subject to oxidation — biological, chemical, or thermal — can be oxidized at relatively low temperatures, under water, in the presence of air. Wet air oxidation should not be confused with submerged combustion in that temperatures in the wet air oxidation process rarely rise above 400 to 600 F and no flame is involved. Figure I shows the basic elements of a wet air oxidation flow scheme. Wastewater containing some oxidizable material is pumped through an exchanger. There the temperature is increased to a point at which the reaction between the oxidizable material 288 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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