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Section Seven INDUSTRIAL WASTE CASE HISTORIES C. PETROCHEMICAL, DYE, AND POLYMERS 78 SIMULATION FOR OPTIMIZATION OF A BIOLOGICAL WASTEWATER TREATMENT PROCESS AT A PETROCHEMICAL PLANT Richard M. Jones, Senior Process Engineer Wastewater Technology Centre Ontario, Canada Peter L. Dold, Associate Professor Alison J. Baker, Graduate Assistant Troy A. Briggs, Graduate Student Department of Civil Engineering, McMaster University Ontario, Canada INTRODUCTION An Ontario petrochemical plant was concerned with the operation of the activated sludge system treating its wastewaters and wanted to evaluate different operating strategies to optimize system performance. A schematic illustration of this treatment facility is shown in Figure 1. The plant consists ot four aeration basins (ATI, AT2, AT3, and AT4) and three clarifiers (SC) and receives a number of different influent streams which feed into the system at different points. Streams 1 and 2 are combined in an aerated equalization tank (ET) before feeding into AT2. Streams 3, 4, and 5 are fed directly into ATI. The flowrates and loadings associated with each of the influent streams are also presented in Figure 1. Streams 1 and 2 account for a large portion of the total influent flow, but the concentrations of each stream are relatively low. On the other hand, Streams 3, 4, and 5, are highly concentrated streams with relatively low flows. The present operating configuration was developed to maximize the hydraulic residence time of the highly concentrated, low flow streams which tend to contain hard-to- degrade compounds. Another important operating issue is that the influent wastewaters contain low levels of nitrogen. In addition, under the present operating configuration, the nitrogen loading is not evenly distributed through the plant. Figure 1 shows that although approximately 50% of the COD load is associated \Q 4 0.01 3 \coo LOAD 31 8 12 %NH3 LOAD 41 1 49 2-*- ET -i 6 3- 0 4- 4 s-+\ AT1 AT2 -*- AT3 Figure 1. Schematic illustration of the petrochemical plant activated sludge process. 49th Purdue Industrial Waste Conference Proceedings, 1994 Lewis Publishers, Chelsea, Michigan 48118. Printed in U.S.A. 737
Object Description
Purdue Identification Number | ETRIWC199478 |
Title | Simulation for optimization of a biological wastewater treatment process at a petrochemical plant |
Author |
Jones, Richard M. Dold, Peter L. Baker, Alison J. Briggs, Troy A. |
Date of Original | 1994 |
Conference Title | Proceedings of the 49th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,44602 |
Extent of Original | p. 737-744 |
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 |
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Date Digitized | 2009-12-10 |
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Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 737 |
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 | Section Seven INDUSTRIAL WASTE CASE HISTORIES C. PETROCHEMICAL, DYE, AND POLYMERS 78 SIMULATION FOR OPTIMIZATION OF A BIOLOGICAL WASTEWATER TREATMENT PROCESS AT A PETROCHEMICAL PLANT Richard M. Jones, Senior Process Engineer Wastewater Technology Centre Ontario, Canada Peter L. Dold, Associate Professor Alison J. Baker, Graduate Assistant Troy A. Briggs, Graduate Student Department of Civil Engineering, McMaster University Ontario, Canada INTRODUCTION An Ontario petrochemical plant was concerned with the operation of the activated sludge system treating its wastewaters and wanted to evaluate different operating strategies to optimize system performance. A schematic illustration of this treatment facility is shown in Figure 1. The plant consists ot four aeration basins (ATI, AT2, AT3, and AT4) and three clarifiers (SC) and receives a number of different influent streams which feed into the system at different points. Streams 1 and 2 are combined in an aerated equalization tank (ET) before feeding into AT2. Streams 3, 4, and 5 are fed directly into ATI. The flowrates and loadings associated with each of the influent streams are also presented in Figure 1. Streams 1 and 2 account for a large portion of the total influent flow, but the concentrations of each stream are relatively low. On the other hand, Streams 3, 4, and 5, are highly concentrated streams with relatively low flows. The present operating configuration was developed to maximize the hydraulic residence time of the highly concentrated, low flow streams which tend to contain hard-to- degrade compounds. Another important operating issue is that the influent wastewaters contain low levels of nitrogen. In addition, under the present operating configuration, the nitrogen loading is not evenly distributed through the plant. Figure 1 shows that although approximately 50% of the COD load is associated \Q 4 0.01 3 \coo LOAD 31 8 12 %NH3 LOAD 41 1 49 2-*- ET -i 6 3- 0 4- 4 s-+\ AT1 AT2 -*- AT3 Figure 1. Schematic illustration of the petrochemical plant activated sludge process. 49th Purdue Industrial Waste Conference Proceedings, 1994 Lewis Publishers, Chelsea, Michigan 48118. Printed in U.S.A. 737 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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