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55 COUPLED BIOLOGICAL DOWNFLOW FLUID BED REACTOR TREATMENT OF SYNFUELS WASTEWATER Charles D. Turner, Associate Professor Department of Civil Engineering Chung Seng Ong, Graduate Research Assistant John R. Gallagher, Research Microbiologist Energy and Mineral Research Center University of North Dakota Grand Forks, North Dakota 58202 INTRODUCTION Despite the current glut of crude oil on the world market, the oil resource is very limited and by the turn of the century alternate sources of energy will be replacing oil. Another form of energy, nuclear energy, is not acceptable to the American public and the solar energy industry is stagnated. Coal, in all its forms, is the most readily extractable and technologically available source of energy in the United States. Because of this, the production of synfuels from coal will become a major source of nonelectric power in the United States near the turn of the century. Synfuels processes, such as the Lurgi dry ash gasification process, produce wastewater with high concentrations of both organic and inorganic contaminants. These contaminants are difficult to remove prior to discharge and create operational problems if recycled back into the process. Cost- efficient production of synfuels can only take place if the technologies for production and waste management are developed prior to prototype plant construction. This research involved the application of coupled fluid bed reactors that combine nitrification and denitrification with organics removal in hydraulically connected anoxic and oxic columns for the treatment of synfuels wastewater from the Great Plains Gasification Plant (GPGP) near Beulah, North Dakota. The wastewater contained BOD5 and ammonia concentrations of 1250 mg/L and 1100 mg/L, respectively. The wastewater was treated at the University of North Dakota Energy and Mineral Research Center where the coupled bed process reduced the BOD5 and ammonia concentrations by 80% or more each. This paper reviews the fundamentals of the treatment process, previous research, bench-scale equipment, operation and results of the research. BACKGROUND Synfuels wastewater that utilizes coal as the process feedstock can be expected to have characteristics related to the chemical makeup and structure of the coal. The specific synfuels process also regulates wastewater characteristics. Process variables that most affect wastewater composition are gasifier temperature and pressure. Coal variables include coal rank, such as lignite, subbituminous, and bituminous and the variability in sulfur, ash and trace metal contents. Each specific process whether it be Lurgi, Texaco, or KILNGAS, will produce wastewater with distinctly different chemical characteristics for various coal types and each synfuels process will generate different wastewater characteristics with the same coal. Table I shows the COD, BOD5, ammonia, phenol and thiocyanate content of wastewater from several gasification processes. These values represent characteristics after solvent extraction and ammonia stripping. Although the values vary widely, high ammonia concentrations are typical of each wastewater. By-product recovery reduces organic and inorganic concentrations in the wastewater to the point of optimizing economic recovery of those products. GPGP utilizes the Phenosolvan for phenol recovery, Phosam-W for ammonia recovery, and the sulfolin process for sulfur recovery. After passing through the Phenosolvan and Phosam-W units, the wastewater is termed stripped gas liquor (SGL). The by- 43rd Purdue Industrial Waste Conference Proceedings, © 1989 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 469
Object Description
Purdue Identification Number | ETRIWC198855 |
Title | Coupled biological downflow fluid bed reactor treatment of synfuels wastewater |
Author |
Turner, Charles D. Ong, Chong Seng Gallagher, John R. |
Date of Original | 1988 |
Conference Title | Proceedings of the 43rd Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,39828 |
Extent of Original | p. 469-478 |
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 | 2009-08-14 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 469 |
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 | 55 COUPLED BIOLOGICAL DOWNFLOW FLUID BED REACTOR TREATMENT OF SYNFUELS WASTEWATER Charles D. Turner, Associate Professor Department of Civil Engineering Chung Seng Ong, Graduate Research Assistant John R. Gallagher, Research Microbiologist Energy and Mineral Research Center University of North Dakota Grand Forks, North Dakota 58202 INTRODUCTION Despite the current glut of crude oil on the world market, the oil resource is very limited and by the turn of the century alternate sources of energy will be replacing oil. Another form of energy, nuclear energy, is not acceptable to the American public and the solar energy industry is stagnated. Coal, in all its forms, is the most readily extractable and technologically available source of energy in the United States. Because of this, the production of synfuels from coal will become a major source of nonelectric power in the United States near the turn of the century. Synfuels processes, such as the Lurgi dry ash gasification process, produce wastewater with high concentrations of both organic and inorganic contaminants. These contaminants are difficult to remove prior to discharge and create operational problems if recycled back into the process. Cost- efficient production of synfuels can only take place if the technologies for production and waste management are developed prior to prototype plant construction. This research involved the application of coupled fluid bed reactors that combine nitrification and denitrification with organics removal in hydraulically connected anoxic and oxic columns for the treatment of synfuels wastewater from the Great Plains Gasification Plant (GPGP) near Beulah, North Dakota. The wastewater contained BOD5 and ammonia concentrations of 1250 mg/L and 1100 mg/L, respectively. The wastewater was treated at the University of North Dakota Energy and Mineral Research Center where the coupled bed process reduced the BOD5 and ammonia concentrations by 80% or more each. This paper reviews the fundamentals of the treatment process, previous research, bench-scale equipment, operation and results of the research. BACKGROUND Synfuels wastewater that utilizes coal as the process feedstock can be expected to have characteristics related to the chemical makeup and structure of the coal. The specific synfuels process also regulates wastewater characteristics. Process variables that most affect wastewater composition are gasifier temperature and pressure. Coal variables include coal rank, such as lignite, subbituminous, and bituminous and the variability in sulfur, ash and trace metal contents. Each specific process whether it be Lurgi, Texaco, or KILNGAS, will produce wastewater with distinctly different chemical characteristics for various coal types and each synfuels process will generate different wastewater characteristics with the same coal. Table I shows the COD, BOD5, ammonia, phenol and thiocyanate content of wastewater from several gasification processes. These values represent characteristics after solvent extraction and ammonia stripping. Although the values vary widely, high ammonia concentrations are typical of each wastewater. By-product recovery reduces organic and inorganic concentrations in the wastewater to the point of optimizing economic recovery of those products. GPGP utilizes the Phenosolvan for phenol recovery, Phosam-W for ammonia recovery, and the sulfolin process for sulfur recovery. After passing through the Phenosolvan and Phosam-W units, the wastewater is termed stripped gas liquor (SGL). The by- 43rd Purdue Industrial Waste Conference Proceedings, © 1989 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 469 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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