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33 ECONOMIC SENSITIVITY OF THE DISSOLVED AIR FLOTATION PROCESS WITH RESPECT TO OPERATIONAL VARIABLES Beth Pascual, Graduate Research Assistant Berrin Tansel, Assistant Professor Department of Civil and Environmental Engineering Florida International University University Park, Miami, Florida 33199 Robert Shalewitz, Project Engineer U.S. Army Belvoir Research, Development and Engineering Center Ft. Belvoir, Virginia 22060 INTRODUCTION Flotation is a physical treatment of solid/liquid separation that conforms with the goals of RCRA for removal and recovery of oily wastes. The use of Dissolved Air Flotation (DAF) has been applied to treating oil-bearing wastes in many industries for the past several decades. With the expanding use of DAF, more investigation into kinetics and the effects on operational variables is needed for optimal design. The DAF process follows mass transfer principles for removal of soluble substances. Air is introduced into a contaminated water stream under pressure. The liquid becomes supersaturated as pressure is reduced and excess air is released in the form of minute air bubbles within the water column. Dissolved material adheres to the bubbles and rises to the surface where it forms a layer of "float" that is easily removed. The effluent, drawn from the clarified zone near the bottom perimeter of the main tank, is discharged or recycled back into the system. The stipulations of this research include the ability to remove a major portion of emulsified oil and yet retain certain operational and size criteria. The need for operational analysis is essential in optimizing the PHC removal and cost efficiency. An extensive literature review phase and experimental phase preceded the economic analysis portion of this research in order to determine optimum operating conditions. A general description of experimental procedure and results is presented. For a more detailed description of experimental procedure, the reader is referred to previous work by the authors.9"'2 EXPERIMENTAL PHASE Experimental Design The effects of source water type, coagulant usage, contamination concentration, recycle ratio, flow rate, detention time, and mode of operation (batch or continuous, full-pressurization or effluent- recirculation) on organics removal were studied. A 60-liter bench scale DAF unit designed to operate at an ideal pressure of 50 psi was run in a series of 100% recycle tests and 50% recycle tests to determine the effect of each parameter on the PHC removal. At 100% recycle, the DAF system was filled with contaminated water and allowed to run in batch mode for 30 minutes. At 50% recycle, the system was modified to run in a continuous mode in order to replace the water exiting the system. Figure 1 presents a schematic of the experimental set-up. The contaminant mixture used in the experiments was a 1:1:1 mixture of regular unleaded gasoline, diesel, and jet fuel. Water samples were prepared with 150 ppm and 1500 ppm contaminant concentrations. The experiments were conducted using natural pond water and synthetic brackish (10,000 TDS) water. Coagulation with a low molecular-weight aluminum-sulfate based cationic polymer was used as a pretreatment prior to the DAF process. The coagulation process involved the addition of the polymer 49th Purdue Industrial Waste Conference Proceedings, 1994 Lewis Publishers, Chelsea, Michigan 48118. Printed in U.S.A. 305
Object Description
Purdue Identification Number | ETRIWC199433 |
Title | Economic sensitivity of the dissolved air flotation process with respect to operational variables |
Author |
Pascual, Beth Tansel, Berrin Shalewitz, Robert |
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. 305-310 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
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Color Depth | 8 bit |
Description
Title | page 305 |
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 | 33 ECONOMIC SENSITIVITY OF THE DISSOLVED AIR FLOTATION PROCESS WITH RESPECT TO OPERATIONAL VARIABLES Beth Pascual, Graduate Research Assistant Berrin Tansel, Assistant Professor Department of Civil and Environmental Engineering Florida International University University Park, Miami, Florida 33199 Robert Shalewitz, Project Engineer U.S. Army Belvoir Research, Development and Engineering Center Ft. Belvoir, Virginia 22060 INTRODUCTION Flotation is a physical treatment of solid/liquid separation that conforms with the goals of RCRA for removal and recovery of oily wastes. The use of Dissolved Air Flotation (DAF) has been applied to treating oil-bearing wastes in many industries for the past several decades. With the expanding use of DAF, more investigation into kinetics and the effects on operational variables is needed for optimal design. The DAF process follows mass transfer principles for removal of soluble substances. Air is introduced into a contaminated water stream under pressure. The liquid becomes supersaturated as pressure is reduced and excess air is released in the form of minute air bubbles within the water column. Dissolved material adheres to the bubbles and rises to the surface where it forms a layer of "float" that is easily removed. The effluent, drawn from the clarified zone near the bottom perimeter of the main tank, is discharged or recycled back into the system. The stipulations of this research include the ability to remove a major portion of emulsified oil and yet retain certain operational and size criteria. The need for operational analysis is essential in optimizing the PHC removal and cost efficiency. An extensive literature review phase and experimental phase preceded the economic analysis portion of this research in order to determine optimum operating conditions. A general description of experimental procedure and results is presented. For a more detailed description of experimental procedure, the reader is referred to previous work by the authors.9"'2 EXPERIMENTAL PHASE Experimental Design The effects of source water type, coagulant usage, contamination concentration, recycle ratio, flow rate, detention time, and mode of operation (batch or continuous, full-pressurization or effluent- recirculation) on organics removal were studied. A 60-liter bench scale DAF unit designed to operate at an ideal pressure of 50 psi was run in a series of 100% recycle tests and 50% recycle tests to determine the effect of each parameter on the PHC removal. At 100% recycle, the DAF system was filled with contaminated water and allowed to run in batch mode for 30 minutes. At 50% recycle, the system was modified to run in a continuous mode in order to replace the water exiting the system. Figure 1 presents a schematic of the experimental set-up. The contaminant mixture used in the experiments was a 1:1:1 mixture of regular unleaded gasoline, diesel, and jet fuel. Water samples were prepared with 150 ppm and 1500 ppm contaminant concentrations. The experiments were conducted using natural pond water and synthetic brackish (10,000 TDS) water. Coagulation with a low molecular-weight aluminum-sulfate based cationic polymer was used as a pretreatment prior to the DAF process. The coagulation process involved the addition of the polymer 49th Purdue Industrial Waste Conference Proceedings, 1994 Lewis Publishers, Chelsea, Michigan 48118. Printed in U.S.A. 305 |
Resolution | 300 ppi |
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