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6 ADVANCED BIOLOGICAL TREATMENT OF HAZARDOUS CONSTITUENTS IN K051 PETROCHEMICAL SLUDGES Robert E. Marks, Graduate Research Assistant Stephen D. Field, Adjunct Associate Professor Department of Civil Engineering Andrew K. Wojtanowicz, Associate Professor Department of Petroleum Engineering Gary A. Breitenbeck, Associate Professor Department of Agronomy Louisiana State University Baton Rouge, Louisiana 70803 INTRODUCTION A trend is developing in insitu cleanup of hazardous waste sites of: using initial biologically-driven suspended growth processes for primary destruction of hazardous constituents, followed by land treatment for final polishing of the biological products.1 This application of biological processes for the treatment of organic sludges and contaminated soils offers a promising new technology and an alternative to incineration as a method for destroying or altering hazardous constituents. The application of the biological suspended growth process, however, is not well defined and this project will obtain data for developing engineering parameters which will make the process more efficient and thus reduce cost factors and cleanup times. A well engineered approach will permit faster reductions in constituent toxicity thus further restricting the opportunity for migration potential of the hazardous constituents into surface and ground waters. The development of an alternative technology for treatment of refining and petrochemical wastes is driven by impending restrictive disposal regulations2 due to provisions of the Resource Conservation and Recovery Act (RCRA). These provisions regulate the future use of land disposal for hazardous wastes and also mandate that the volume, toxicity and mobility of the wastes be reduced. The statutes stress that permanent, cost-effective solutions are employed that are acceptable to the public, to the maximum extent possible. An alternative technology based on biological processes will limit the toxicity and migration potential of many organic compounds found in petrochemical and other industrial wastes. 1. Current Research The current research is centered on biodegradation of recalcitrant petrochemical sludges in sealed continuous stirred tank reactors (CSTRs). The specific sludge to be used in the research contains eight polynuclear aromatics (PNAs) cited by the United States Environmental Protection Agency (USEPA) as hazardous wastes. Benzo(a)pyrene [B(a)P] was selected in this research as the primary target contaminant due to its strong carcinogenic nature and low allowable release concentrations in sludges. Chemical properties of eight key PNAs are shown on Table 1 (Chemical Properties of Key PNAs). The low solubility of B(a)P of 0.003 mg/1 is considered to be the rate limiting step in biodegradation reactions where B(a)P is a constituent.3 Equilibrium conditions in the vigorously stirred aerobic 1 liter reactors were confirmed by daily monitoring of key parameters which include: sludge oil & solids mass balances, B(a)P mass balances, pH, culture plating, carbon dioxide respiration, and total suspended solids (TSS). B(a)P loadings are increased from 286 mg/kg of dry feed solids to 34,896 mg/ kg. Test reactors processing solid wastes at B(a)P feed rates of 286-289 mg/kg, met the 1990 USEPA constituent concentration limit (CCL) for B(a)P of 12 mg/kg for allowable land disposal. An anionic surfactant, Triton N-101, was added to all petrochemical sludges augmented with B(a)P at loadings of 1,600 mg/kg and higher. All sampling and analytical protocols followed USEPA methodologies.4 Mass balance removals of B(a)P and other similar aromatic hydrocarbons were found to exceed 90%. 46th Purdue Industrial Waste Conference Proceedings, 1992 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 45
Object Description
Purdue Identification Number | ETRIWC199106 |
Title | Advanced biological treatment of hazardous constituents in K051 petrochemical sludges |
Author |
Marks, Robert E. Field, Stephen D. Wojtanowicz, Andrew K. Breitenbeck, Gary A. |
Date of Original | 1991 |
Conference Title | Proceedings of the 46th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://e-archives.lib.purdue.edu/u?/engext,42649 |
Extent of Original | p. 45-54 |
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 | 2009-11-24 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page 45 |
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 | 6 ADVANCED BIOLOGICAL TREATMENT OF HAZARDOUS CONSTITUENTS IN K051 PETROCHEMICAL SLUDGES Robert E. Marks, Graduate Research Assistant Stephen D. Field, Adjunct Associate Professor Department of Civil Engineering Andrew K. Wojtanowicz, Associate Professor Department of Petroleum Engineering Gary A. Breitenbeck, Associate Professor Department of Agronomy Louisiana State University Baton Rouge, Louisiana 70803 INTRODUCTION A trend is developing in insitu cleanup of hazardous waste sites of: using initial biologically-driven suspended growth processes for primary destruction of hazardous constituents, followed by land treatment for final polishing of the biological products.1 This application of biological processes for the treatment of organic sludges and contaminated soils offers a promising new technology and an alternative to incineration as a method for destroying or altering hazardous constituents. The application of the biological suspended growth process, however, is not well defined and this project will obtain data for developing engineering parameters which will make the process more efficient and thus reduce cost factors and cleanup times. A well engineered approach will permit faster reductions in constituent toxicity thus further restricting the opportunity for migration potential of the hazardous constituents into surface and ground waters. The development of an alternative technology for treatment of refining and petrochemical wastes is driven by impending restrictive disposal regulations2 due to provisions of the Resource Conservation and Recovery Act (RCRA). These provisions regulate the future use of land disposal for hazardous wastes and also mandate that the volume, toxicity and mobility of the wastes be reduced. The statutes stress that permanent, cost-effective solutions are employed that are acceptable to the public, to the maximum extent possible. An alternative technology based on biological processes will limit the toxicity and migration potential of many organic compounds found in petrochemical and other industrial wastes. 1. Current Research The current research is centered on biodegradation of recalcitrant petrochemical sludges in sealed continuous stirred tank reactors (CSTRs). The specific sludge to be used in the research contains eight polynuclear aromatics (PNAs) cited by the United States Environmental Protection Agency (USEPA) as hazardous wastes. Benzo(a)pyrene [B(a)P] was selected in this research as the primary target contaminant due to its strong carcinogenic nature and low allowable release concentrations in sludges. Chemical properties of eight key PNAs are shown on Table 1 (Chemical Properties of Key PNAs). The low solubility of B(a)P of 0.003 mg/1 is considered to be the rate limiting step in biodegradation reactions where B(a)P is a constituent.3 Equilibrium conditions in the vigorously stirred aerobic 1 liter reactors were confirmed by daily monitoring of key parameters which include: sludge oil & solids mass balances, B(a)P mass balances, pH, culture plating, carbon dioxide respiration, and total suspended solids (TSS). B(a)P loadings are increased from 286 mg/kg of dry feed solids to 34,896 mg/ kg. Test reactors processing solid wastes at B(a)P feed rates of 286-289 mg/kg, met the 1990 USEPA constituent concentration limit (CCL) for B(a)P of 12 mg/kg for allowable land disposal. An anionic surfactant, Triton N-101, was added to all petrochemical sludges augmented with B(a)P at loadings of 1,600 mg/kg and higher. All sampling and analytical protocols followed USEPA methodologies.4 Mass balance removals of B(a)P and other similar aromatic hydrocarbons were found to exceed 90%. 46th Purdue Industrial Waste Conference Proceedings, 1992 Lewis Publishers, Inc., Chelsea, Michigan 48118. Printed in U.S.A. 45 |
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Color Depth | 8 bit |
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