Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater

Energy recovery from the anaerobic treatment of crab processing wastewater was investigated. Biogas from two laboratory-scale, upflow anaerobic filters (Systems A and B) was collected and analyzed to determine percent by volume composition of methane (CH₄), carbon dioxide (CO₂), and hydrogen sulfide...

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Main Author: Rodenhizer, Jeffrey Smith
Other Authors: Environmental Engineering
Format: Others
Language:en
Published: Virginia Tech 2014
Subjects:
Online Access:http://hdl.handle.net/10919/41350
http://scholar.lib.vt.edu/theses/available/etd-03032009-040415/
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spelling ndltd-VTETD-oai-vtechworks.lib.vt.edu-10919-413502021-10-13T05:39:13Z Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater Rodenhizer, Jeffrey Smith Environmental Engineering LD5655.V855 1995.R634 Energy recovery from the anaerobic treatment of crab processing wastewater was investigated. Biogas from two laboratory-scale, upflow anaerobic filters (Systems A and B) was collected and analyzed to determine percent by volume composition of methane (CH₄), carbon dioxide (CO₂), and hydrogen sulfide (H₂S). Biogas produced by System A (upflow anaerobic bed filter) produced biogas averaging 68, 28, and 1.5 % CH₄, CO₂, and HS, respectively. System A average gas production ranged from 6.3 to 15.8 liters per day (L/d) (6.6 to 10.0 L gas/L feed) for COD reductions ranging from 11,000 to 27,000 milligrams per day (mg/d) and COD loadings ranging from 16,700 to 43,600 mg/d. System B (upflow anaerobic packed filter) produced biogas averaging 68, 28, and 1.4 % CH₄, CO₂, and H₂S, respectively. System B average gas production ranged from 7.5 to 19.5 L/d (7.1 to 11.9 L gas/L feed) for COD reductions ranging from 11,700 to 28,700 mg/d and COD loadings ranging from 16,100 to 48,500 mg/d. A pilot-scale biogas collection system was constructed to collect, treat (remove H₂S), store, and utilize the biogas produced by an anaerobic/aerobic crab processing wastewater treatment system treating between 15 and 30 gallons per day (gpd). Biogas was produced by a 190 gallon upflow anaerobic bed filter and a 190 gallon anaerobic clarifier operated in series. Preliminary results indicated biogas production rates comparable to maximum average gas production rates of the laboratory-scale systems at approximately 10 L gas/L feed. Biogas was stored in a 120 gallon tank at up to 12 pounds per square inch (psi) following removal of hydrogen sulfide. Biogas was then burned in a modified natural gas hot water heater to produce heated water for maintaining the anaerobic reactors at 35°C. Master of Science 2014-03-14T21:30:32Z 2014-03-14T21:30:32Z 1995 2009-03-03 2009-03-03 2009-03-03 Thesis Text etd-03032009-040415 http://hdl.handle.net/10919/41350 http://scholar.lib.vt.edu/theses/available/etd-03032009-040415/ en OCLC# 34071830 LD5655.V855_1995.R634.pdf In Copyright http://rightsstatements.org/vocab/InC/1.0/ x, 110 leaves BTD application/pdf application/pdf Virginia Tech
collection NDLTD
language en
format Others
sources NDLTD
topic LD5655.V855 1995.R634
spellingShingle LD5655.V855 1995.R634
Rodenhizer, Jeffrey Smith
Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
description Energy recovery from the anaerobic treatment of crab processing wastewater was investigated. Biogas from two laboratory-scale, upflow anaerobic filters (Systems A and B) was collected and analyzed to determine percent by volume composition of methane (CH₄), carbon dioxide (CO₂), and hydrogen sulfide (H₂S). Biogas produced by System A (upflow anaerobic bed filter) produced biogas averaging 68, 28, and 1.5 % CH₄, CO₂, and HS, respectively. System A average gas production ranged from 6.3 to 15.8 liters per day (L/d) (6.6 to 10.0 L gas/L feed) for COD reductions ranging from 11,000 to 27,000 milligrams per day (mg/d) and COD loadings ranging from 16,700 to 43,600 mg/d. System B (upflow anaerobic packed filter) produced biogas averaging 68, 28, and 1.4 % CH₄, CO₂, and H₂S, respectively. System B average gas production ranged from 7.5 to 19.5 L/d (7.1 to 11.9 L gas/L feed) for COD reductions ranging from 11,700 to 28,700 mg/d and COD loadings ranging from 16,100 to 48,500 mg/d. A pilot-scale biogas collection system was constructed to collect, treat (remove H₂S), store, and utilize the biogas produced by an anaerobic/aerobic crab processing wastewater treatment system treating between 15 and 30 gallons per day (gpd). Biogas was produced by a 190 gallon upflow anaerobic bed filter and a 190 gallon anaerobic clarifier operated in series. Preliminary results indicated biogas production rates comparable to maximum average gas production rates of the laboratory-scale systems at approximately 10 L gas/L feed. Biogas was stored in a 120 gallon tank at up to 12 pounds per square inch (psi) following removal of hydrogen sulfide. Biogas was then burned in a modified natural gas hot water heater to produce heated water for maintaining the anaerobic reactors at 35°C. === Master of Science
author2 Environmental Engineering
author_facet Environmental Engineering
Rodenhizer, Jeffrey Smith
author Rodenhizer, Jeffrey Smith
author_sort Rodenhizer, Jeffrey Smith
title Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
title_short Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
title_full Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
title_fullStr Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
title_full_unstemmed Collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
title_sort collection, analysis, and utilization of biogas generated by the anaerobic treatment of crab processing wastewater
publisher Virginia Tech
publishDate 2014
url http://hdl.handle.net/10919/41350
http://scholar.lib.vt.edu/theses/available/etd-03032009-040415/
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