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ENHANCEMENT OF OIL REFINERY ACTIVATED SLUDGE BY ADDITION OF POWDERED ACTIVATED CARBON Michael K. Stenstrom, Research Engineer Colin G. Grieves, Research Engineer Research and Development Center Amoco Oil Company Naperville, Illinois 60540 INTRODUCTION The National Pollutant Discharge Elimination System (NPDES), as created by PL-92-500, requires all industries in the United States to reduce water pollution to essentially zero by 1985. The first phase of the reduction program is to be implemented by mid-1977 and required industries to operate best practicable control technology currently available (BPT) wastewater treatment plants. The second objective is to develop, construct, and operate best available technology, economically achievable (BAT) treatment plants by 1983. The development program, and experience in operating the BPT and BAT treatment plants, will result in further progress toward the final goal of the program, which is elimination of all pollutant discharges, if such elimination is technologically and economically achievable. Attainment of BPT treatment requires the implementation of best practicable technology. The U.S. EPA has suggested in their guideline document [1] the treatment sequence shown in Figure 1. Although other suitable treatment methods are available, many other refiners as well as Amoco have followed the general outline. Modifications in the suggested treatment have been made in many instances to utilize existing facilities or improve the process Refinery Waste- water Gravity Separator Stop Otl to Treatment Dissolved Air Flotation Equalization Aeration Tank Sludge Recycle Granular Media Filter Final -Effluent Sludge to Treatment Figure 1. Schematic of refinery BPT wastewater treatment system. due to peculiarities of each installation. Granular activated carbon columns have been proposed for BAT treatment. The add-on columns would utilize the existing treatment BPT facilities and would, in theory, provide an economical method of achieving 1983 standards. An alternate technique, and the subject of this paper, is powdered activated carbon enhancement of the activated sludge process shown in Figure 1. If the technique were successful, no additional equipment would be required other than the carbon handling and, in some cases, regeneration facilities, which would also be required of the granular 196
Object Description
Purdue Identification Number | ETRIWC1977022 |
Title | Enhancement of oil refinery activated sludge by addition of powdered activated carbon |
Author |
Stenstrom, Michael K. Grieves, Colin G. |
Date of Original | 1977 |
Conference Title | Proceedings of the 32nd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,26931 |
Extent of Original | p. 196-205 |
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 | 2009-06-30 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page196 |
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 | ENHANCEMENT OF OIL REFINERY ACTIVATED SLUDGE BY ADDITION OF POWDERED ACTIVATED CARBON Michael K. Stenstrom, Research Engineer Colin G. Grieves, Research Engineer Research and Development Center Amoco Oil Company Naperville, Illinois 60540 INTRODUCTION The National Pollutant Discharge Elimination System (NPDES), as created by PL-92-500, requires all industries in the United States to reduce water pollution to essentially zero by 1985. The first phase of the reduction program is to be implemented by mid-1977 and required industries to operate best practicable control technology currently available (BPT) wastewater treatment plants. The second objective is to develop, construct, and operate best available technology, economically achievable (BAT) treatment plants by 1983. The development program, and experience in operating the BPT and BAT treatment plants, will result in further progress toward the final goal of the program, which is elimination of all pollutant discharges, if such elimination is technologically and economically achievable. Attainment of BPT treatment requires the implementation of best practicable technology. The U.S. EPA has suggested in their guideline document [1] the treatment sequence shown in Figure 1. Although other suitable treatment methods are available, many other refiners as well as Amoco have followed the general outline. Modifications in the suggested treatment have been made in many instances to utilize existing facilities or improve the process Refinery Waste- water Gravity Separator Stop Otl to Treatment Dissolved Air Flotation Equalization Aeration Tank Sludge Recycle Granular Media Filter Final -Effluent Sludge to Treatment Figure 1. Schematic of refinery BPT wastewater treatment system. due to peculiarities of each installation. Granular activated carbon columns have been proposed for BAT treatment. The add-on columns would utilize the existing treatment BPT facilities and would, in theory, provide an economical method of achieving 1983 standards. An alternate technique, and the subject of this paper, is powdered activated carbon enhancement of the activated sludge process shown in Figure 1. If the technique were successful, no additional equipment would be required other than the carbon handling and, in some cases, regeneration facilities, which would also be required of the granular 196 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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