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79 TREATMENT OF DAIRY WASTEWATER BY CHEMICAL COAGULATION Frederic C. Blanc, Professor Rita Navia, Graduate Student Department of Civil Engineering Northeastern University Boston, Massachusetts, 02115 INTRODUCTION Industrial dairy wastewaters are generally high strength wastes containing soluble, colloidal and suspended solids with a high concentration of BOD. The more than 5,000 industrial dairy plants in this country have a large waste load to treat and dispose of. If discharged into the municipal sewer system, such wastewaters often produce a high pollution load which is unacceptable to the Publically Owned Treatment Works [POTW]. This then results in a requirement for industrial pretreatment of such wastes before discharge to the collection system. Chemical coagulation-flocculation followed by sedimentation, which plays an important role in many solid liquid separation schemes and is widely used in water and wastewater treatment may be used in the pretreatment of dairy wastewaters in some instances. This method can remove BOD, COD and suspended solids from the waste stream and may be economically feasible for some of the industrial dairy product facilities which are located in urban areas. In this study a laboratory investigation of chemical coagulation treatment of dairy processing wastewater using alum, ferric chloride, or ferrous sulfide together with lime was performed. Extensive testing to determine chemical requirements and combinations for various removal efficiencies was conducted. Following the laboratory studies, a cost analysis was performed evaluating treatment benefits and pretreatment process economics based on costs of local sewer user surcharges. BACKGROUND Dairy wastes are generated by disposing of residues, wasting of by-product, process equipment cleaning and leakage or spills. The main organic constituents in dairy wastewaters consist of fats, proteins and carbohydrates in various proportions which are associated with milk. Other organics found in some dairy industry wastewaters may come from processing companion products such as orange juice, other fruit juices, or ice cream and sherbet additives such as fruits, nuts, coloring substances or sugar. The BOD strength of dairy wastewaters varies depending on the type of production process. This parameter has been reported to vary from as low as 40 mg/L to as high as 10,000 mg/L, with a mean of 2,300 mg/L.' Suspended solids, which are mostly organic, are typically present in concentrations up to 2,000 mg/L.' COD values range from 80 mg/L to 95,000 mg/L with a typical mean of 4,500 mg/L for various types of dairy plants.2 Phosphorus, which comes from milk and cleaning compounds is typically present in a mean concentration of 49 mg/L.2 The reported values of pH range from 4.5 to 9.2.3 The treatment objectives for dairy wastewaters are described by the Environmental Protection Agency in Effluent Guidelines and Standards for Dairy Products.4 Treatment or pretreatment processes for dairy wastewaters are usually the biological type with the most common being: activated sludge, trickling filters, rotating biological contactors, lagooning, land treatment, and anaerobic reactors. Anaerobic processes as described by Sobkowicz5 for the treatment of cheese production wastewaters or Backman6 for treating dairy wastewater have the capability of handling high organic loadings in a pretreatment application. Table I depicts the range of treatment efficiency for various biological treatment processes treating dairy wastewaters. Chemical treatment or pretreatment of dairy wastewaters is not practiced to a great extent. There are not many reports of chemical treatment in the wastewater treatment literature. A physical- chemical pretreatment system was described by Bough and Swientek with reported cost savings.8 45th Purdue Industrial Waste Conference Proceedings, © 1991 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 681
Object Description
Purdue Identification Number | ETRIWC199079 |
Title | Treatment of dairy wastewater by chemical coagulation |
Author |
Blanc, Frederic C. Navia, Rita |
Date of Original | 1990 |
Conference Title | Proceedings of the 45th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,41605 |
Extent of Original | p. 681-690 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
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Color Depth | 8 bit |
Description
Title | page 681 |
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 | 79 TREATMENT OF DAIRY WASTEWATER BY CHEMICAL COAGULATION Frederic C. Blanc, Professor Rita Navia, Graduate Student Department of Civil Engineering Northeastern University Boston, Massachusetts, 02115 INTRODUCTION Industrial dairy wastewaters are generally high strength wastes containing soluble, colloidal and suspended solids with a high concentration of BOD. The more than 5,000 industrial dairy plants in this country have a large waste load to treat and dispose of. If discharged into the municipal sewer system, such wastewaters often produce a high pollution load which is unacceptable to the Publically Owned Treatment Works [POTW]. This then results in a requirement for industrial pretreatment of such wastes before discharge to the collection system. Chemical coagulation-flocculation followed by sedimentation, which plays an important role in many solid liquid separation schemes and is widely used in water and wastewater treatment may be used in the pretreatment of dairy wastewaters in some instances. This method can remove BOD, COD and suspended solids from the waste stream and may be economically feasible for some of the industrial dairy product facilities which are located in urban areas. In this study a laboratory investigation of chemical coagulation treatment of dairy processing wastewater using alum, ferric chloride, or ferrous sulfide together with lime was performed. Extensive testing to determine chemical requirements and combinations for various removal efficiencies was conducted. Following the laboratory studies, a cost analysis was performed evaluating treatment benefits and pretreatment process economics based on costs of local sewer user surcharges. BACKGROUND Dairy wastes are generated by disposing of residues, wasting of by-product, process equipment cleaning and leakage or spills. The main organic constituents in dairy wastewaters consist of fats, proteins and carbohydrates in various proportions which are associated with milk. Other organics found in some dairy industry wastewaters may come from processing companion products such as orange juice, other fruit juices, or ice cream and sherbet additives such as fruits, nuts, coloring substances or sugar. The BOD strength of dairy wastewaters varies depending on the type of production process. This parameter has been reported to vary from as low as 40 mg/L to as high as 10,000 mg/L, with a mean of 2,300 mg/L.' Suspended solids, which are mostly organic, are typically present in concentrations up to 2,000 mg/L.' COD values range from 80 mg/L to 95,000 mg/L with a typical mean of 4,500 mg/L for various types of dairy plants.2 Phosphorus, which comes from milk and cleaning compounds is typically present in a mean concentration of 49 mg/L.2 The reported values of pH range from 4.5 to 9.2.3 The treatment objectives for dairy wastewaters are described by the Environmental Protection Agency in Effluent Guidelines and Standards for Dairy Products.4 Treatment or pretreatment processes for dairy wastewaters are usually the biological type with the most common being: activated sludge, trickling filters, rotating biological contactors, lagooning, land treatment, and anaerobic reactors. Anaerobic processes as described by Sobkowicz5 for the treatment of cheese production wastewaters or Backman6 for treating dairy wastewater have the capability of handling high organic loadings in a pretreatment application. Table I depicts the range of treatment efficiency for various biological treatment processes treating dairy wastewaters. Chemical treatment or pretreatment of dairy wastewaters is not practiced to a great extent. There are not many reports of chemical treatment in the wastewater treatment literature. A physical- chemical pretreatment system was described by Bough and Swientek with reported cost savings.8 45th Purdue Industrial Waste Conference Proceedings, © 1991 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 681 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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