Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation

A complete set-up of obtaining bio-hydrogen from palm oil mill effluent (POME) was successfully demonstrated in this study. The proposed set-up is a combination of upflow anaerobic sludge blanket (UASB) bioreactor (POME is digested to obtain methane) and subsequent a dry reforming tubular reactor (c...

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Main Authors: Mohamad Mokhtar, Ibrahim, Zulkifly, Jemaat, Nour, Abdurahman Hamid
Format: Article
Language:English
Published: Trans Tech Publications 2021
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/35339/
http://umpir.ump.edu.my/id/eprint/35339/1/Biohydrogen%20paper.pdf
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author Mohamad Mokhtar, Ibrahim
Zulkifly, Jemaat
Nour, Abdurahman Hamid
author_facet Mohamad Mokhtar, Ibrahim
Zulkifly, Jemaat
Nour, Abdurahman Hamid
author_sort Mohamad Mokhtar, Ibrahim
building UMP Institutional Repository
collection Online Access
description A complete set-up of obtaining bio-hydrogen from palm oil mill effluent (POME) was successfully demonstrated in this study. The proposed set-up is a combination of upflow anaerobic sludge blanket (UASB) bioreactor (POME is digested to obtain methane) and subsequent a dry reforming tubular reactor (conversion of methane into bio-hydrogen). The UASB reactor with 10 litres working volume was operated in continuous operation at mesophilic temperature (38 °C), pH was maintained between 6.5 and 7.2 by adding buffering solution containing of 5 gL-1 of calcium oxide (CaO) and hydraulic retention time (HRT) was set at 1 day. Prior to feeding of POME, the UASB reactor was inoculated with sludge taken from anaerobic pond at Lepar Hilir Palm Oil Mill. Then, the reactor was continuously fed with the raw POME with COD concentration of 7,773 mgL-1 and organic loading rate (OLR) of 7.61 g CODL-1d-1. Meanwhile the dry reforming fixed-bed tubular reactor was operated at 750 °C and 0.1 g catalyst type Ni/SBA-15. Biogas produced from the UASB reactor was fed into the tubular reactor and gas samples were collected at the inlet and outlet and analyzed using GC-TCD. On average, the UASB reactor produced about 32 Ld-1 biogas containing of 80 % methane and removing 67 % of COD. This biogas was fed into the dry reforming rector and the reaction took place in the reactor produced about 32 % of H2, 0.24 % of CH4, 28 % of CO2 and 39 % of CO. This result yielded a H2/CO ratio close to 1, demonstrated an efficient route for producing bio-hydrogen gas. Meanwhile, CH4 conversion was recorded at 99.7 %.
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spelling ump-353392022-09-30T08:35:18Z http://umpir.ump.edu.my/id/eprint/35339/ Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation Mohamad Mokhtar, Ibrahim Zulkifly, Jemaat Nour, Abdurahman Hamid TP Chemical technology A complete set-up of obtaining bio-hydrogen from palm oil mill effluent (POME) was successfully demonstrated in this study. The proposed set-up is a combination of upflow anaerobic sludge blanket (UASB) bioreactor (POME is digested to obtain methane) and subsequent a dry reforming tubular reactor (conversion of methane into bio-hydrogen). The UASB reactor with 10 litres working volume was operated in continuous operation at mesophilic temperature (38 °C), pH was maintained between 6.5 and 7.2 by adding buffering solution containing of 5 gL-1 of calcium oxide (CaO) and hydraulic retention time (HRT) was set at 1 day. Prior to feeding of POME, the UASB reactor was inoculated with sludge taken from anaerobic pond at Lepar Hilir Palm Oil Mill. Then, the reactor was continuously fed with the raw POME with COD concentration of 7,773 mgL-1 and organic loading rate (OLR) of 7.61 g CODL-1d-1. Meanwhile the dry reforming fixed-bed tubular reactor was operated at 750 °C and 0.1 g catalyst type Ni/SBA-15. Biogas produced from the UASB reactor was fed into the tubular reactor and gas samples were collected at the inlet and outlet and analyzed using GC-TCD. On average, the UASB reactor produced about 32 Ld-1 biogas containing of 80 % methane and removing 67 % of COD. This biogas was fed into the dry reforming rector and the reaction took place in the reactor produced about 32 % of H2, 0.24 % of CH4, 28 % of CO2 and 39 % of CO. This result yielded a H2/CO ratio close to 1, demonstrated an efficient route for producing bio-hydrogen gas. Meanwhile, CH4 conversion was recorded at 99.7 %. Trans Tech Publications 2021 Article PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/35339/1/Biohydrogen%20paper.pdf Mohamad Mokhtar, Ibrahim and Zulkifly, Jemaat and Nour, Abdurahman Hamid (2021) Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation. Materials Science Forum, 1025. pp. 177-182. ISSN 0255-5476. (Published) https://doi.org/10.4028/www.scientific.net/MSF.1025.177 https://doi.org/10.4028/www.scientific.net/MSF.1025.177
spellingShingle TP Chemical technology
Mohamad Mokhtar, Ibrahim
Zulkifly, Jemaat
Nour, Abdurahman Hamid
Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title_full Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title_fullStr Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title_full_unstemmed Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title_short Obtaining Bio-Hydrogen from Palm Oil Mill Effluent (POME) - A Preliminary Evaluation
title_sort obtaining bio-hydrogen from palm oil mill effluent (pome) - a preliminary evaluation
topic TP Chemical technology
url http://umpir.ump.edu.my/id/eprint/35339/
http://umpir.ump.edu.my/id/eprint/35339/
http://umpir.ump.edu.my/id/eprint/35339/
http://umpir.ump.edu.my/id/eprint/35339/1/Biohydrogen%20paper.pdf