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DISSOLVED AIR FLOTATION PERFORMANCE K. Larry Roberts, Graduate Research Assistant Dennis W. Weeter, Associate Professor Roy O. Ball, Assistant Professor Department of Civil Engineering University of Tennessee Knoxville, Tennessee 37916 INTRODUCTION Dissolved Air Flotation (DAF) is a member of a class of processes which have been designated adsorptive bubble separation techniques [ 1 ]. Other members of the class have been used primarily for selective removal of a component of a particular process or pollutant stream. DAF has been generally applied to the nonselective removal of suspended solids and emulsified liquids from water and wastewater. The conventional design procedure for DAF systems has been based on a combination of parameters such as hydraulic loading, solids loading, and amount of air available for flotation. In order to determine if these parameters are a reliable means of predicting DAF performance for design purposes, a field evaluation of eight DAF systems was conducted. The remainder of this paper consists of a brief review of DAF technology (design process and theoretical concepts), a description of the field evaluation, and a presentation and discussion of the results of the field evaluation. DAF REVIEW Figure 1 is a generalized schematic which shows most of the components which might be found in a DAF system. The function of each of these components is to create or maintain some specific condition conducive to the attachment of bubbles to the impurities in the waste stream. Dissolved air flotation, like many pollution control operations, benefits from receiving an equalized feed stream both in terms of hydraulic and pollutant loading. For streams high in emulsified oil concentration, an API separator frequently preceeds DAF. In order to enhance particle agglomeration as well as bubble-particle adhesion, chemical conditioning is frequently utilized. Chemicals are commonly added in a rapid mix tank with 1-5 minutes detention time. For a recycle system, the recycle flow is returned to this tank. The principal operation following feed conditioning is air introduction and dissolution. Air may be directly injected into the appropriate stream through a separate pump or may be metered with a rotometer into the suction side of a centrifugal pump. The latter method provides an economical means of air introduction but is limited to approximately 4% air by volume to prevent cavitation and subsequent damage to the pump. Following air introduction, the stream is generally detained in a dissolution tank with from 1-5 minutes detention time. According to Henry's Law, the solubility of the air 194
Object Description
Purdue Identification Number | ETRIWC1978020 |
Title | Dissolved air flotation performance |
Author |
Roberts, K. Larry Weeter, Dennis W. Ball, Roy O. |
Date of Original | 1978 |
Conference Title | Proceedings of the 33rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,27312 |
Extent of Original | p. 194-199 |
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 | 2009-06-22 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page0194 |
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 | DISSOLVED AIR FLOTATION PERFORMANCE K. Larry Roberts, Graduate Research Assistant Dennis W. Weeter, Associate Professor Roy O. Ball, Assistant Professor Department of Civil Engineering University of Tennessee Knoxville, Tennessee 37916 INTRODUCTION Dissolved Air Flotation (DAF) is a member of a class of processes which have been designated adsorptive bubble separation techniques [ 1 ]. Other members of the class have been used primarily for selective removal of a component of a particular process or pollutant stream. DAF has been generally applied to the nonselective removal of suspended solids and emulsified liquids from water and wastewater. The conventional design procedure for DAF systems has been based on a combination of parameters such as hydraulic loading, solids loading, and amount of air available for flotation. In order to determine if these parameters are a reliable means of predicting DAF performance for design purposes, a field evaluation of eight DAF systems was conducted. The remainder of this paper consists of a brief review of DAF technology (design process and theoretical concepts), a description of the field evaluation, and a presentation and discussion of the results of the field evaluation. DAF REVIEW Figure 1 is a generalized schematic which shows most of the components which might be found in a DAF system. The function of each of these components is to create or maintain some specific condition conducive to the attachment of bubbles to the impurities in the waste stream. Dissolved air flotation, like many pollution control operations, benefits from receiving an equalized feed stream both in terms of hydraulic and pollutant loading. For streams high in emulsified oil concentration, an API separator frequently preceeds DAF. In order to enhance particle agglomeration as well as bubble-particle adhesion, chemical conditioning is frequently utilized. Chemicals are commonly added in a rapid mix tank with 1-5 minutes detention time. For a recycle system, the recycle flow is returned to this tank. The principal operation following feed conditioning is air introduction and dissolution. Air may be directly injected into the appropriate stream through a separate pump or may be metered with a rotometer into the suction side of a centrifugal pump. The latter method provides an economical means of air introduction but is limited to approximately 4% air by volume to prevent cavitation and subsequent damage to the pump. Following air introduction, the stream is generally detained in a dissolution tank with from 1-5 minutes detention time. According to Henry's Law, the solubility of the air 194 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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