INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES

<p align ="justify">The world's energy demand are increasing by the human population. Crisis of the energy prompted us to found alternative energy sources derived from easily obtainable materials and environmentally friendly. Ethanol is an alternative fuel that can be used as a...

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Main Author: GUMILAR (NIM: 25313309), ANDRI
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/25553
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:25553
spelling id-itb.:255532018-09-17T14:51:41ZINFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES GUMILAR (NIM: 25313309), ANDRI Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/25553 <p align ="justify">The world's energy demand are increasing by the human population. Crisis of the energy prompted us to found alternative energy sources derived from easily obtainable materials and environmentally friendly. Ethanol is an alternative fuel that can be used as a substitute for fossil fuels. The previous research has given results that ethanol can be produced from the wastewater with high concentration of organic by anaerobic processes. In this study, wastewater used are the synthetic waste by the variation of N2 flushing about 12; 24; 36 and 48 hours then flushing has continued by internal biogas. The concentration of soluble and total COD was obtained in a row was 6515 mg/L and 2816 mg/L. The maximum concentration of ethanol production in the reactor by flushing N2 12 hours, 24 hours, 36 hours and 48 hours respectively is 58.59; 78.83; 54.72 and 54.12 mgCOD/L with the rate of formation of 0.35 to 3.92 mgCOD/L/ hour. To acetate, the maximum concentration generated in each successive reactor 732.63; 726.52; 712.36 and 950.39 mgCOD/L with the formation rate of acetate ranged from 0.57 to 61.29 mgCOD/L/hour. maximum partial pressure of H2 gas produced from each of these reactors produce different results, namely a row 1.29; 8.65; 3.35 and 1.88 kPa. The results showed that flushing the reactor with N2 for 24 hours gives the greatest efficiency of ethanol formation is 78.83 mgCOD/L with the rate of formation of a maximum of 3.92 mgCOD/L/hour and a maximum yield of 0.028.<p align ="justify"> text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description <p align ="justify">The world's energy demand are increasing by the human population. Crisis of the energy prompted us to found alternative energy sources derived from easily obtainable materials and environmentally friendly. Ethanol is an alternative fuel that can be used as a substitute for fossil fuels. The previous research has given results that ethanol can be produced from the wastewater with high concentration of organic by anaerobic processes. In this study, wastewater used are the synthetic waste by the variation of N2 flushing about 12; 24; 36 and 48 hours then flushing has continued by internal biogas. The concentration of soluble and total COD was obtained in a row was 6515 mg/L and 2816 mg/L. The maximum concentration of ethanol production in the reactor by flushing N2 12 hours, 24 hours, 36 hours and 48 hours respectively is 58.59; 78.83; 54.72 and 54.12 mgCOD/L with the rate of formation of 0.35 to 3.92 mgCOD/L/ hour. To acetate, the maximum concentration generated in each successive reactor 732.63; 726.52; 712.36 and 950.39 mgCOD/L with the formation rate of acetate ranged from 0.57 to 61.29 mgCOD/L/hour. maximum partial pressure of H2 gas produced from each of these reactors produce different results, namely a row 1.29; 8.65; 3.35 and 1.88 kPa. The results showed that flushing the reactor with N2 for 24 hours gives the greatest efficiency of ethanol formation is 78.83 mgCOD/L with the rate of formation of a maximum of 3.92 mgCOD/L/hour and a maximum yield of 0.028.<p align ="justify">
format Theses
author GUMILAR (NIM: 25313309), ANDRI
spellingShingle GUMILAR (NIM: 25313309), ANDRI
INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
author_facet GUMILAR (NIM: 25313309), ANDRI
author_sort GUMILAR (NIM: 25313309), ANDRI
title INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
title_short INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
title_full INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
title_fullStr INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
title_full_unstemmed INFLUENCE OF N2 FLUSHING AND Fe2+, Zn2+ ADDITION FOR ETHANOL AND ACIDOGENIC PRODUCT FORMATION FROM THE CONVERSION OF HIGH ORGANIC CONCENTRATION WASTEWATER BY ANAEROBIC PROCESSES
title_sort influence of n2 flushing and fe2+, zn2+ addition for ethanol and acidogenic product formation from the conversion of high organic concentration wastewater by anaerobic processes
url https://digilib.itb.ac.id/gdl/view/25553
_version_ 1822921599603441664