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WET OXIDATION OF TOXIC ORGANIC SUBSTANCES C. Robert Baillod, Professor Richard A. Lamparter, Research Engineer David G. Leddy, Associate Professor Michigan Technological University Houghton, Michigan 49931 INTRODUCTION The treatment and safe disposal of hazardous organic waste material in an environmentally acceptable manner and at a reasonable cost is a topic of great national importance. Many toxic organics are long lived in the natural environment and resistant to biological breakdown. Destruction of these organic waste materials can be achieved by oxidation to carbon dioxide, water and inorganic forms of nitrogen sulfur and chlorine. There are several processes that may be employed to achieve oxidation of waste organic materials. These are: (a) Chemical Oxidation (using oxidizing agents such as ozone); (b) Biological Oxidation; (c) Wet Oxidation; and (d) Incineration. The choice of which process is best suited to a waste stream will depend upon the nature of the particular waste, and the concentration of the stream. Figure 1 shows a conceptual relationship between process cost and concentration of organic pollutant [ 1 ]. For low concentrations of labile organics, chemical oxidation may be suitable. For higher concentrations of biodegradable organic compounds, biological oxidation processes such as activated o > o o o K O. INCINERATION- Figure 1. Conceptual relationship between process costs and influent organic concentration. 0 10 INFLUENT ORGANIC CONCENTRATION ppm ,6 sludge may be most cost effective. As the concentration of organic material increases beyond 30%, high temperature incineration becomes practical. Wet oxidation is ideally suited to liquid wastes which are too dilute to incinerate by dry combustion and two refractory to handle by chemical and biological oxidation. Many of the toxic organic substances regulated by Section 307 of the 1977 Amendments to the Federal Water Pollution Control Act (PL95-217) are resistant to biological degradation and may be present in various industrial waste streams. The objective of this research was to investigate the utility of the wet oxidation process in the destruction of typical priority pollutants. 206
Object Description
Purdue Identification Number | ETRIWC197921 |
Title | Wet oxidation of toxic organic substances |
Author |
Baillod, C. Robert Lamparter, Richard A. Leddy, David G. |
Date of Original | 1979 |
Conference Title | Proceedings of the 34th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,30453 |
Extent of Original | p. 206-213 |
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 | 2009-06-24 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page0206 |
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 | WET OXIDATION OF TOXIC ORGANIC SUBSTANCES C. Robert Baillod, Professor Richard A. Lamparter, Research Engineer David G. Leddy, Associate Professor Michigan Technological University Houghton, Michigan 49931 INTRODUCTION The treatment and safe disposal of hazardous organic waste material in an environmentally acceptable manner and at a reasonable cost is a topic of great national importance. Many toxic organics are long lived in the natural environment and resistant to biological breakdown. Destruction of these organic waste materials can be achieved by oxidation to carbon dioxide, water and inorganic forms of nitrogen sulfur and chlorine. There are several processes that may be employed to achieve oxidation of waste organic materials. These are: (a) Chemical Oxidation (using oxidizing agents such as ozone); (b) Biological Oxidation; (c) Wet Oxidation; and (d) Incineration. The choice of which process is best suited to a waste stream will depend upon the nature of the particular waste, and the concentration of the stream. Figure 1 shows a conceptual relationship between process cost and concentration of organic pollutant [ 1 ]. For low concentrations of labile organics, chemical oxidation may be suitable. For higher concentrations of biodegradable organic compounds, biological oxidation processes such as activated o > o o o K O. INCINERATION- Figure 1. Conceptual relationship between process costs and influent organic concentration. 0 10 INFLUENT ORGANIC CONCENTRATION ppm ,6 sludge may be most cost effective. As the concentration of organic material increases beyond 30%, high temperature incineration becomes practical. Wet oxidation is ideally suited to liquid wastes which are too dilute to incinerate by dry combustion and two refractory to handle by chemical and biological oxidation. Many of the toxic organic substances regulated by Section 307 of the 1977 Amendments to the Federal Water Pollution Control Act (PL95-217) are resistant to biological degradation and may be present in various industrial waste streams. The objective of this research was to investigate the utility of the wet oxidation process in the destruction of typical priority pollutants. 206 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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