Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification

Due to the availability of agricultural land and significant production of palm oil in Malaysia, there is abundance of biomass in the form of agricultural wastes. This work reports a mathematical model for the flowsheet developed for hydrogen production from empty fruit bu...

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Main Authors: Inayat, Abrar, Ahmad, Murni M, Abdul Mutalib, M I, Yusup, Suzana
Format: Conference or Workshop Item
Language:English
Published: 2010
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Online Access:http://scholars.utp.edu.my/id/eprint/3048/1/Flowsheet_development_and_modelling_of_hydrogen_production_from_empty_fruit_bunch_%28EFB%29_via_steam_gasification_%28PRES_2010%29.pdf
http://scholars.utp.edu.my/id/eprint/3048/
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spelling oai:scholars.utp.edu.my:30482023-01-03T08:49:51Z http://scholars.utp.edu.my/id/eprint/3048/ Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification Inayat, Abrar Ahmad, Murni M Abdul Mutalib, M I Yusup, Suzana TP Chemical technology Due to the availability of agricultural land and significant production of palm oil in Malaysia, there is abundance of biomass in the form of agricultural wastes. This work reports a mathematical model for the flowsheet developed for hydrogen production from empty fruit bunch from oil palm via steam gasification with in-situ carbon dioxide capture by CaO as sorbent. The flowsheet model incorporates the chemical reaction kinetics, mass and energy balances calculations. Parameter analysis on the influence of the temperature, steam/biomass and sorbent/biomass ratios are performed. It is predicted that more than 70 mole% hydrogen can be produced at 1150 K. In addition, CO2 are predicted to be fully absorbed from the system at sorbent/biomass ratio of 2.0. It is observed that the thermodynamic efficiency of the gasifier increases with temperature reaching a maximum efficiency of 84% at steam/biomass ratio of 2.0. It is shown that by using CaO as the sorbent in the gasifier, the efficiency can be increased by 10% compared to the conventional gasification method. 2010-08-28 Conference or Workshop Item PeerReviewed application/pdf en http://scholars.utp.edu.my/id/eprint/3048/1/Flowsheet_development_and_modelling_of_hydrogen_production_from_empty_fruit_bunch_%28EFB%29_via_steam_gasification_%28PRES_2010%29.pdf Inayat, Abrar and Ahmad, Murni M and Abdul Mutalib, M I and Yusup, Suzana (2010) Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification. In: 13th Conference on Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction (PRES 2010), 28 Aug-1 Sep 2010, Prague, Czech Republic.
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
Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
description Due to the availability of agricultural land and significant production of palm oil in Malaysia, there is abundance of biomass in the form of agricultural wastes. This work reports a mathematical model for the flowsheet developed for hydrogen production from empty fruit bunch from oil palm via steam gasification with in-situ carbon dioxide capture by CaO as sorbent. The flowsheet model incorporates the chemical reaction kinetics, mass and energy balances calculations. Parameter analysis on the influence of the temperature, steam/biomass and sorbent/biomass ratios are performed. It is predicted that more than 70 mole% hydrogen can be produced at 1150 K. In addition, CO2 are predicted to be fully absorbed from the system at sorbent/biomass ratio of 2.0. It is observed that the thermodynamic efficiency of the gasifier increases with temperature reaching a maximum efficiency of 84% at steam/biomass ratio of 2.0. It is shown that by using CaO as the sorbent in the gasifier, the efficiency can be increased by 10% compared to the conventional gasification method.
format Conference or Workshop Item
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 Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
title_short Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
title_full Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
title_fullStr Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
title_full_unstemmed Flowsheet Development and Modelling of Hydrogen Production from Empty Fruit Bunch (EFB) via Steam Gasification
title_sort flowsheet development and modelling of hydrogen production from empty fruit bunch (efb) via steam gasification
publishDate 2010
url http://scholars.utp.edu.my/id/eprint/3048/1/Flowsheet_development_and_modelling_of_hydrogen_production_from_empty_fruit_bunch_%28EFB%29_via_steam_gasification_%28PRES_2010%29.pdf
http://scholars.utp.edu.my/id/eprint/3048/
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score 13.214268