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THE NEGATIVE IMPACT OF INDUSTRIAL WASTE ON PHYSICAL-CHEMICAL TREATMENT W. Guirguis, Research Manager J. P. Harris, Chief Engineer Cleveland Regional Sewer District Cleveland, Ohio 44114 P. B. Melnyk, Assistant Professor Case Institute of Technology Cleveland, Ohio 44106 INTRODUCTION Physical-Chemical Treatment (PCT) for wastewaters has been investigated extensively in the past decade as a tertiary step for existing treatment facilities. Recently, PCT has been accepted as an alternative process for complete treatment of wastewaters. In 1973, ten PCT plants were reported [ 1 ] to be either under design or construction, whereas three of these are now in operation. The lower space requirements, ability to absorb wide variations in both hydraulic and concentration loadings, and insensitivity to toxic shock loads are advantages which have increased the interest in employing PCT. The typical flow scheme for a physical-chemical process, as shown in Figure 1, includes: (a) chemical addition to precipitate soluble wastes and provide nuclei for particle growth; (b) flocculation to promote particle growth; (c) solids separation; (d) pH adjustment; (e) activated carbon adsorption to remove soluble organics; and (f) disinfection to destroy microorganisms. Chemical recovery and spent activated carbon regeneration may also be included. To date, limited experience is available on the application of PCT to combined industrial municipal wastes. The majority of data reported are from bench- and pilot-scale systems. This paper evaluates the performance of PCT on combined wastes, and demonstrates both its limitations and the need for process modification. FLOCCULAIOFI tK'f AC CANON 1 Cltp Figure 1. Flow scheme of typical physical-chemical treatment. EXPERIMENTAL PROCEDURES The data referenced hereafter were obtained from a PC pilot plant in operation since 1974 [2,3). The hydraulic capacity of this plant is a constant 30 gpm. The influent contains wastes from both industrial and municipal sources. The principal unit operations include single-stage lime treatment, solids separation, activated carbon adsorption and ozone disinfection. These operations are carried on 24 hr/day, 7 days/week. Samples are collected hourly, composited, and chemical analyses are carried in accordance with Standard Methods [4]. A listing of the values of pertinent operating parameters at each stage is given in Table I. 753
Object Description
Purdue Identification Number | ETRIWC197667 |
Title | Negative impact of industrial waste on physical-chemical treatment |
Author |
Guirguis, W. Harris, J. P. Melnyk, P. B. (Peter B.) |
Date of Original | 1976 |
Conference Title | Proceedings of the 31st Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,27048 |
Extent of Original | p. 753-763 |
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 | 2009-07-08 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 753 |
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 NEGATIVE IMPACT OF INDUSTRIAL WASTE ON PHYSICAL-CHEMICAL TREATMENT W. Guirguis, Research Manager J. P. Harris, Chief Engineer Cleveland Regional Sewer District Cleveland, Ohio 44114 P. B. Melnyk, Assistant Professor Case Institute of Technology Cleveland, Ohio 44106 INTRODUCTION Physical-Chemical Treatment (PCT) for wastewaters has been investigated extensively in the past decade as a tertiary step for existing treatment facilities. Recently, PCT has been accepted as an alternative process for complete treatment of wastewaters. In 1973, ten PCT plants were reported [ 1 ] to be either under design or construction, whereas three of these are now in operation. The lower space requirements, ability to absorb wide variations in both hydraulic and concentration loadings, and insensitivity to toxic shock loads are advantages which have increased the interest in employing PCT. The typical flow scheme for a physical-chemical process, as shown in Figure 1, includes: (a) chemical addition to precipitate soluble wastes and provide nuclei for particle growth; (b) flocculation to promote particle growth; (c) solids separation; (d) pH adjustment; (e) activated carbon adsorption to remove soluble organics; and (f) disinfection to destroy microorganisms. Chemical recovery and spent activated carbon regeneration may also be included. To date, limited experience is available on the application of PCT to combined industrial municipal wastes. The majority of data reported are from bench- and pilot-scale systems. This paper evaluates the performance of PCT on combined wastes, and demonstrates both its limitations and the need for process modification. FLOCCULAIOFI tK'f AC CANON 1 Cltp Figure 1. Flow scheme of typical physical-chemical treatment. EXPERIMENTAL PROCEDURES The data referenced hereafter were obtained from a PC pilot plant in operation since 1974 [2,3). The hydraulic capacity of this plant is a constant 30 gpm. The influent contains wastes from both industrial and municipal sources. The principal unit operations include single-stage lime treatment, solids separation, activated carbon adsorption and ozone disinfection. These operations are carried on 24 hr/day, 7 days/week. Samples are collected hourly, composited, and chemical analyses are carried in accordance with Standard Methods [4]. A listing of the values of pertinent operating parameters at each stage is given in Table I. 753 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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