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86 TREATMENT OF SOFT DRINK SYRUP AND BOTTLING WASTEWATER USING ANAEROBIC UPFLOW PACKED BED REACTORS Damian J. Capobianco, Graduate Student Frederic C. Blanc, Professor Department of Civil Engineering Northeastern University Boston, Massachusetts 02115 INTRODUCTION In recent years, investigations into the performance of hi-rate anaerobic stabilization, as applied to industrial wastewater, has led to the development of a number of process regimes and has increased the general understanding of the treatment mechanisms involved. Anaerobic treatment has displayed the ability to degrade many industrial wastes readily and at substantial loading rates. In particular, the process seems to be applicable to the soluble organic waste components originating in the food processing industry. The process through effective, does not produce an effluent of sufficient quality for surface discharge. However, as an industrial pretreatment device for direct discharge to sewer, the process may show itself to be very effective and economically attractive as compared to aerobic treatment. The first documented attempt at hi-rate treatment was the anaerobic filter which was developed by Young and McCarty1 in the 1960s. Since that time there have been many other reactor designs and modifications of the original packed bed reactor. The purpose of this study was to determine the performance of an anaerobic up-flow packed bed reactor treating wastewater originating from soft drink manufacturing. The results of the experiment show the process to be effective in the stabilization of this type of wastewater with treatment producing greater than 90% soluble COD removal at substantial organic loadings. SOFT DRINK WASTEWATER ORIGIN AND CHARACTERISTICS Wastewater from the soft drink industry originates from syrup manufacturing and packaging, bottling production runs, process water purification, and washdowns of equipment and conduits. In syrup production, a sucrose or fructose sugar base is normally mixed with a flavor formulation in a mixer. The resulting syrup is stored, packaged, or transported in plant for use in soft drink bottling production lines. Wastewater produced in the syrup room is comparatively low in flow and particularly high in organic content. The wastewater will result from sugar and syrup spillage associated with mixing. Packaging production line spillage, along with tank cleanouts and equipment washdowns will produce additional high strength wastewater. During a bottling production run, bottles will pass through some type of wash and rinse sequence before being filled, capped, labeled, and prepared for shipping. In this phase of production, wastewater will be generated from bottle washing and rinsing, labeling, production line spillage, equipment lubrication, and washdowns. Flows will be substantially larger than those associated with syrup production, and strengths are likely to vary. The wastewater will contain waste soft drink, syrup, detergents, lubricants, and perhaps caustics. Table I displays the results of various composite samplings performed over a three year period on the effluent of a Massachusetts syrup production and bottling facility as reported by O'Shaughnessy and Blanc.2 The results show COD to range from 1940 to 8880 by mg/L, BOD5 to range from 960 to 6200 mg/L and TSS remaining below 40 mg/L. The high soluble strengths along with the low TSS are well suited for anaerobic filters. Treatment reported in the literature include RO, facultative lagoons, and RBC. The main advantages associated with anaerobic treatment over aerobic treatment for this 44th Purdue Industrial Waste Conference Proceedings, © 1990 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 777
Object Description
Purdue Identification Number | ETRIWC198986 |
Title | Treatment of soft drink syrup and bottling wastewater using anaerobic upflow packed bed reactors |
Author |
Capobiano, Damian J. Blanc, Frederic C. |
Date of Original | 1989 |
Conference Title | Proceedings of the 44th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,40757 |
Extent of Original | p. 777-786 |
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 |
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Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 777 |
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 | 86 TREATMENT OF SOFT DRINK SYRUP AND BOTTLING WASTEWATER USING ANAEROBIC UPFLOW PACKED BED REACTORS Damian J. Capobianco, Graduate Student Frederic C. Blanc, Professor Department of Civil Engineering Northeastern University Boston, Massachusetts 02115 INTRODUCTION In recent years, investigations into the performance of hi-rate anaerobic stabilization, as applied to industrial wastewater, has led to the development of a number of process regimes and has increased the general understanding of the treatment mechanisms involved. Anaerobic treatment has displayed the ability to degrade many industrial wastes readily and at substantial loading rates. In particular, the process seems to be applicable to the soluble organic waste components originating in the food processing industry. The process through effective, does not produce an effluent of sufficient quality for surface discharge. However, as an industrial pretreatment device for direct discharge to sewer, the process may show itself to be very effective and economically attractive as compared to aerobic treatment. The first documented attempt at hi-rate treatment was the anaerobic filter which was developed by Young and McCarty1 in the 1960s. Since that time there have been many other reactor designs and modifications of the original packed bed reactor. The purpose of this study was to determine the performance of an anaerobic up-flow packed bed reactor treating wastewater originating from soft drink manufacturing. The results of the experiment show the process to be effective in the stabilization of this type of wastewater with treatment producing greater than 90% soluble COD removal at substantial organic loadings. SOFT DRINK WASTEWATER ORIGIN AND CHARACTERISTICS Wastewater from the soft drink industry originates from syrup manufacturing and packaging, bottling production runs, process water purification, and washdowns of equipment and conduits. In syrup production, a sucrose or fructose sugar base is normally mixed with a flavor formulation in a mixer. The resulting syrup is stored, packaged, or transported in plant for use in soft drink bottling production lines. Wastewater produced in the syrup room is comparatively low in flow and particularly high in organic content. The wastewater will result from sugar and syrup spillage associated with mixing. Packaging production line spillage, along with tank cleanouts and equipment washdowns will produce additional high strength wastewater. During a bottling production run, bottles will pass through some type of wash and rinse sequence before being filled, capped, labeled, and prepared for shipping. In this phase of production, wastewater will be generated from bottle washing and rinsing, labeling, production line spillage, equipment lubrication, and washdowns. Flows will be substantially larger than those associated with syrup production, and strengths are likely to vary. The wastewater will contain waste soft drink, syrup, detergents, lubricants, and perhaps caustics. Table I displays the results of various composite samplings performed over a three year period on the effluent of a Massachusetts syrup production and bottling facility as reported by O'Shaughnessy and Blanc.2 The results show COD to range from 1940 to 8880 by mg/L, BOD5 to range from 960 to 6200 mg/L and TSS remaining below 40 mg/L. The high soluble strengths along with the low TSS are well suited for anaerobic filters. Treatment reported in the literature include RO, facultative lagoons, and RBC. The main advantages associated with anaerobic treatment over aerobic treatment for this 44th Purdue Industrial Waste Conference Proceedings, © 1990 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 777 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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