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22 DEVELOPMENT OF LOW-COST FLOTATION TECHNOLOGY AND SYSTEMS FOR WASTEWATER TREATMENT Milos Krofta, President Daniel Guss, Vice President Krofta Engineering Corporation Lenox, Massachusetts 01240 Lawrence K. Wang, Director & Professor Lenox Institute for Research, Inc. Lenox, Massachusetts 01240 INTRODUCTION Activated sludge consists of biological floes which are matrices of microorganisms, non-living organics and inorganic substances. The microorganisms include bacteria, fungi, protozoa (Sarcodina, Mastigophora, Sporozoa, Ciliata, and Suctoria), rotifers, viruses and higher forms of animals such as insect larvae, worms and crustaceans. The activated sludge process is one of the most common biological wastewater treatment processes, and can be defined as a suspended-growth system in which biological floes are continuously circulated to come into contact and to oxidize the organic waste substances in the presence of oxygen and nutrients. The waste organic matter is aerobically converted to gaseous carbon dioxide, cell tissue of microorganisms (C5H7NO2), and other simple soluble end products. Part of microorganisms (i.e. activated sludge) are returned to the aeration basin in order to maintain a constant microbial population (i.e. constant mixed liquor suspended solids). The wastewater is considered to be adequately treated when the excess microorganisms (i.e. excess waste sludge) and residual suspended solids are separated from the aqueous phase by clarification, and the clarified effluent meets the Federal and State Effluent Standards. The most common clarification used today is sedimentation. The recent and accelerating emphasis on water pollution control has necessitated the rapid development of improved biological waste treatment systems to aid in cost and energy savings. The use of secondary flotation clarification in place of, or in assisting secondary sedimentation clarification in the activated sludge process system is one recent advancement in this basic process. The potential of this development, in terms of higher suspended solids and BOD removals from existing plants and expansion of hydraulic capacity at significantly reduced cost, is expected to result in extremely rapid acceptance by municipalities and industry. The primary distinguishing feature of the improved activated sludge treatment system is that high rate dissolved air flotation, known as Supracell, is the secondary clarifier for separation of suspended solids from the aeration basin effluent, as opposed to secondary sedimentation alone in conventional activated sludge systems. The concept of using flotation for water-solid separation is not new at all; many engineers have applied the flotation technology in sludge separation since the early 1920's. The major deterrent to flotation use in the municipal and industrial processes envisaged by these early practicing engineers was economics, with objections centering mainly around the cost of gas bubble generation and retention. There has been significant evolution of dissolved air flotation clarifiers during the last 50 years. The following progress has been made: 1) Specific clarification load increased from 1.5 gpm/sq ft (60 Lpm/sq m) to 3.5 gpm/sq ft (140 Lpm/sq m) and for triple stacked unit to 10 gpm/sq ft (420 Lpm/sq m); 2) The retention time of water in the flotation clarifier decreased from 30 min to 3 min; 3) The largest unit size increased from 260 gpm (1000 Lpm) to 7900 gpm (30,000 Lpm) and for triple stacked units to 23,700 gpm (90,000 Lpm); 4) The size of modern DAF units is much smaller. (It allows construction predominantly in stainless steel prefabricated for easy erection); 5) The smaller size and weight, 120 lb/sq ft (60 kg/m^), allows installation on posts leaving free passage under the unit, therefore, it is easier to find available space for indoor installation and to construct inexpensive housing; 6) Air dissolving is improved and now requires only 10 seconds retention time in the air dissolving tube instead of the previous 60 seconds, accordingly this reduction in retention time results in smaller air dissolving tubes which are predominantly built from stainless 185
Object Description
Purdue Identification Number | ETRIWC198722 |
Title | Development of low-cost flotation technology and systems for wastewater treatment |
Author |
Krofta, Milos Guss, Daniel Wang, Lawrence K. |
Date of Original | 1987 |
Conference Title | Proceedings of the 42nd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,38818 |
Extent of Original | p. 185-196 |
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 | 2009-08-03 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 185 |
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 | 22 DEVELOPMENT OF LOW-COST FLOTATION TECHNOLOGY AND SYSTEMS FOR WASTEWATER TREATMENT Milos Krofta, President Daniel Guss, Vice President Krofta Engineering Corporation Lenox, Massachusetts 01240 Lawrence K. Wang, Director & Professor Lenox Institute for Research, Inc. Lenox, Massachusetts 01240 INTRODUCTION Activated sludge consists of biological floes which are matrices of microorganisms, non-living organics and inorganic substances. The microorganisms include bacteria, fungi, protozoa (Sarcodina, Mastigophora, Sporozoa, Ciliata, and Suctoria), rotifers, viruses and higher forms of animals such as insect larvae, worms and crustaceans. The activated sludge process is one of the most common biological wastewater treatment processes, and can be defined as a suspended-growth system in which biological floes are continuously circulated to come into contact and to oxidize the organic waste substances in the presence of oxygen and nutrients. The waste organic matter is aerobically converted to gaseous carbon dioxide, cell tissue of microorganisms (C5H7NO2), and other simple soluble end products. Part of microorganisms (i.e. activated sludge) are returned to the aeration basin in order to maintain a constant microbial population (i.e. constant mixed liquor suspended solids). The wastewater is considered to be adequately treated when the excess microorganisms (i.e. excess waste sludge) and residual suspended solids are separated from the aqueous phase by clarification, and the clarified effluent meets the Federal and State Effluent Standards. The most common clarification used today is sedimentation. The recent and accelerating emphasis on water pollution control has necessitated the rapid development of improved biological waste treatment systems to aid in cost and energy savings. The use of secondary flotation clarification in place of, or in assisting secondary sedimentation clarification in the activated sludge process system is one recent advancement in this basic process. The potential of this development, in terms of higher suspended solids and BOD removals from existing plants and expansion of hydraulic capacity at significantly reduced cost, is expected to result in extremely rapid acceptance by municipalities and industry. The primary distinguishing feature of the improved activated sludge treatment system is that high rate dissolved air flotation, known as Supracell, is the secondary clarifier for separation of suspended solids from the aeration basin effluent, as opposed to secondary sedimentation alone in conventional activated sludge systems. The concept of using flotation for water-solid separation is not new at all; many engineers have applied the flotation technology in sludge separation since the early 1920's. The major deterrent to flotation use in the municipal and industrial processes envisaged by these early practicing engineers was economics, with objections centering mainly around the cost of gas bubble generation and retention. There has been significant evolution of dissolved air flotation clarifiers during the last 50 years. The following progress has been made: 1) Specific clarification load increased from 1.5 gpm/sq ft (60 Lpm/sq m) to 3.5 gpm/sq ft (140 Lpm/sq m) and for triple stacked unit to 10 gpm/sq ft (420 Lpm/sq m); 2) The retention time of water in the flotation clarifier decreased from 30 min to 3 min; 3) The largest unit size increased from 260 gpm (1000 Lpm) to 7900 gpm (30,000 Lpm) and for triple stacked units to 23,700 gpm (90,000 Lpm); 4) The size of modern DAF units is much smaller. (It allows construction predominantly in stainless steel prefabricated for easy erection); 5) The smaller size and weight, 120 lb/sq ft (60 kg/m^), allows installation on posts leaving free passage under the unit, therefore, it is easier to find available space for indoor installation and to construct inexpensive housing; 6) Air dissolving is improved and now requires only 10 seconds retention time in the air dissolving tube instead of the previous 60 seconds, accordingly this reduction in retention time results in smaller air dissolving tubes which are predominantly built from stainless 185 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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