Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach

Hydrogen is considered as an attractive clean fuel for the future. Hydrogen production via biomass steam gasification is receiving attention due to its sustainability and zero net carbon emission. Coupled with in-situ CO2 adsorption, this process has been proven to be environment friendly. The paper...

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Main Authors: Inayat, Abrar, Ahmad, Murni M, Abdul Mutalib, M I, Yusup, Suzana
Format: Citation Index Journal
Language:English
Published: Asian Network for Scientific Information 2010
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spelling oai:scholars.utp.edu.my:29172023-01-03T08:49:42Z http://scholars.utp.edu.my/id/eprint/2917/ Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach Inayat, Abrar Ahmad, Murni M Abdul Mutalib, M I Yusup, Suzana TP Chemical technology Hydrogen is considered as an attractive clean fuel for the future. Hydrogen production via biomass steam gasification is receiving attention due to its sustainability and zero net carbon emission. Coupled with in-situ CO2 adsorption, this process has been proven to be environment friendly. The paper reports on the impact of temperature, steam/biomass ratio and sorbent/biomass ratio on hydrogen production performance in a steam gasification process using a simulation model developed in MATLAB. In this work, biomass is assumed as char, and gasification and CO2 adsorption occur in one gasifier. The model is used to predict the product gas composition, hydrogen yield and thermodynamic efficiency of the process. The results show that with the increase in temperature and steam/biomass ratio, the hydrogen concentration and yield increase, however the thermodynamic efficiency decreases. Hydrogen yield increases from 78 to 97 g/kg of biomass with the increase in temperature and steam/biomass ratio within the range of 800 to 1300 K and 2.0 to 5.0 respectively. Maximum hydrogen efficiency of 87 % is observed at 800 K and steam/biomass ratio of 2.0. At the sorbent/biomass of 1.52, hydrogen purity is predicted to reach 0.98 mole fraction with CO2 present in system absorbed. At 950 K with steam/biomass ratio of 3.0 and sorbent/biomass ratio of 1.0, a maximum hydrogen concentration of 0.81 mole fraction is obtained in the product gas. The steam feed rate is found to have the most impact on the hydrogen production and thermodynamic efficiency among the process parameters. Asian Network for Scientific Information 2010-10-18 Citation Index Journal PeerReviewed application/pdf en http://scholars.utp.edu.my/id/eprint/2917/1/67486C6Dd01.pdf Inayat, Abrar and Ahmad, Murni M and Abdul Mutalib, M I and Yusup, Suzana (2010) Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach. [Citation Index Journal] http://scialert.net/archivedetails.php?issn=1812-5654&issueno=152 10.3923/jas.2010.3183.3190 10.3923/jas.2010.3183.3190 10.3923/jas.2010.3183.3190
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
language English
topic TP Chemical technology
spellingShingle TP Chemical technology
Inayat, Abrar
Ahmad, Murni M
Abdul Mutalib, M I
Yusup, Suzana
Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
description Hydrogen is considered as an attractive clean fuel for the future. Hydrogen production via biomass steam gasification is receiving attention due to its sustainability and zero net carbon emission. Coupled with in-situ CO2 adsorption, this process has been proven to be environment friendly. The paper reports on the impact of temperature, steam/biomass ratio and sorbent/biomass ratio on hydrogen production performance in a steam gasification process using a simulation model developed in MATLAB. In this work, biomass is assumed as char, and gasification and CO2 adsorption occur in one gasifier. The model is used to predict the product gas composition, hydrogen yield and thermodynamic efficiency of the process. The results show that with the increase in temperature and steam/biomass ratio, the hydrogen concentration and yield increase, however the thermodynamic efficiency decreases. Hydrogen yield increases from 78 to 97 g/kg of biomass with the increase in temperature and steam/biomass ratio within the range of 800 to 1300 K and 2.0 to 5.0 respectively. Maximum hydrogen efficiency of 87 % is observed at 800 K and steam/biomass ratio of 2.0. At the sorbent/biomass of 1.52, hydrogen purity is predicted to reach 0.98 mole fraction with CO2 present in system absorbed. At 950 K with steam/biomass ratio of 3.0 and sorbent/biomass ratio of 1.0, a maximum hydrogen concentration of 0.81 mole fraction is obtained in the product gas. The steam feed rate is found to have the most impact on the hydrogen production and thermodynamic efficiency among the process parameters.
format Citation Index Journal
author Inayat, Abrar
Ahmad, Murni M
Abdul Mutalib, M I
Yusup, Suzana
author_facet Inayat, Abrar
Ahmad, Murni M
Abdul Mutalib, M I
Yusup, Suzana
author_sort Inayat, Abrar
title Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
title_short Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
title_full Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
title_fullStr Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
title_full_unstemmed Effect of Process Parameters on Hydrogen Production and Efficiency in Biomass Gasification Using Modelling Approach
title_sort effect of process parameters on hydrogen production and efficiency in biomass gasification using modelling approach
publisher Asian Network for Scientific Information
publishDate 2010
url http://scholars.utp.edu.my/id/eprint/2917/1/67486C6Dd01.pdf
http://scholars.utp.edu.my/id/eprint/2917/
http://scialert.net/archivedetails.php?issn=1812-5654&issueno=152
_version_ 1754532108401901568
score 13.214268