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Dissolved-Air Ion Flotation of Industrial Wastes Hexavalent Chromium ROBERT B. GRIEVES, Professor and Chairman Department of Chemical Engineering University of Kentucky Lexington, Kentucky GREGORY A. ETTELT, Director of Laboratories Metropolitan Sanitary District of Greater Chicago Chicago, Illinois J. THOMAS SCHRODT, Assistant Professor Department of Chemical Engineering University of Kentucky Lexington, Kentucky DIBAKAR BHATTACHARYYA, Fellow and Research Associate Department of Chemical Engineering University of Kentucky Lexington, Kentucky INTRODUCTION Foam separation has been used successfully on a process scale for the removal of ABS and other soluble organics from secondary sewage effluents and on a pilot- plant scale for the concentration of radioactive cations from nuclear wastes. Ion flotation, a foam separation process, has been applied to hexavalent chromium (1,2,3,4,5) and to cyanide complexed by iron (6,7) in the laboratory and has been used for the first time (8) on a pilot plant scale. The ion flotation process involves the addition to the waste of a cationic surface-active agent, oppositely-changed to the HCrO.~(Cr2p72") lon which is to be separated. The resulting surface-active complex which is a colloidal suspension of particulates produced by reaction between the surfactant and the dichromate, is floated to the surface' of the suspension by gas bubbles at the interfaces of which it is absorbed, and a froth is formed. A polymer may be useful in promoting the aggregation of the collodial particulates, providing more efficient flotation. Dissolved-air flotation, based on the release of a pressurized flow in which air is dissolved, generally produces bubbles of diameter one to two orders of magnitude smaller than dispersed-air flotation, with a concommitant increase in interfacial area. The objective of this study is to evaluate the efficiency of a pilot plant scale, dissolved-air ion flotation unit for the removal and concentration of dichromate. The evaluation is based on the dependent variables: the fractional flotation (removal) of dichromate, the enrichment ratio for dichromate, and the fractional flotation (removal) of surfactant Each dependent variable is related analytically to five independent variables by a multiple regression analysis. Optimum values of the independent variables are determined and a chemical cost estimate is carried out, based on an experimentally varified process for surfactant recovery and reuse. 154
Object Description
Purdue Identification Number | ETRIWC196814 |
Title | Dissolved-air ion flotation of industrial wastes : hexavalent chromium |
Author |
Grieves, R. B., 1935- Ettelt, G. A. (Gregory A.) Schrodt, J. Thomas Bhattacharyya, Dibakar |
Date of Original | 1968 |
Conference Title | Proceedings of the 23rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,15314 |
Extent of Original | p. 154-164 |
Series |
Engineering extension series no. 132 Engineering bulletin v. 53, no. 2 |
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 | 2009-05-20 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 154 |
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 | Dissolved-Air Ion Flotation of Industrial Wastes Hexavalent Chromium ROBERT B. GRIEVES, Professor and Chairman Department of Chemical Engineering University of Kentucky Lexington, Kentucky GREGORY A. ETTELT, Director of Laboratories Metropolitan Sanitary District of Greater Chicago Chicago, Illinois J. THOMAS SCHRODT, Assistant Professor Department of Chemical Engineering University of Kentucky Lexington, Kentucky DIBAKAR BHATTACHARYYA, Fellow and Research Associate Department of Chemical Engineering University of Kentucky Lexington, Kentucky INTRODUCTION Foam separation has been used successfully on a process scale for the removal of ABS and other soluble organics from secondary sewage effluents and on a pilot- plant scale for the concentration of radioactive cations from nuclear wastes. Ion flotation, a foam separation process, has been applied to hexavalent chromium (1,2,3,4,5) and to cyanide complexed by iron (6,7) in the laboratory and has been used for the first time (8) on a pilot plant scale. The ion flotation process involves the addition to the waste of a cationic surface-active agent, oppositely-changed to the HCrO.~(Cr2p72") lon which is to be separated. The resulting surface-active complex which is a colloidal suspension of particulates produced by reaction between the surfactant and the dichromate, is floated to the surface' of the suspension by gas bubbles at the interfaces of which it is absorbed, and a froth is formed. A polymer may be useful in promoting the aggregation of the collodial particulates, providing more efficient flotation. Dissolved-air flotation, based on the release of a pressurized flow in which air is dissolved, generally produces bubbles of diameter one to two orders of magnitude smaller than dispersed-air flotation, with a concommitant increase in interfacial area. The objective of this study is to evaluate the efficiency of a pilot plant scale, dissolved-air ion flotation unit for the removal and concentration of dichromate. The evaluation is based on the dependent variables: the fractional flotation (removal) of dichromate, the enrichment ratio for dichromate, and the fractional flotation (removal) of surfactant Each dependent variable is related analytically to five independent variables by a multiple regression analysis. Optimum values of the independent variables are determined and a chemical cost estimate is carried out, based on an experimentally varified process for surfactant recovery and reuse. 154 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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