Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production

This study addresses the energy flows and energy efficiency of integrated catalytic adsorption biomass steam gasification for hydrogen production in a pilot scale bubbling fluidized bed system utilizing palm kernel shell as feedstock. The integrated catalytic adsorption utilizes catalyst and CO2 ads...

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Main Authors: Khan, Z., Yusup, S., Kamble, P., Naqvi, M., Watson, I.
Format: Article
Published: Elsevier Ltd 2018
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-85047071819&doi=10.1016%2fj.apenergy.2018.05.020&partnerID=40&md5=02d5f5cd17ba3c6fee9ff06922df515a
http://eprints.utp.edu.my/21425/
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spelling my.utp.eprints.214252018-09-25T06:34:50Z Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production Khan, Z. Yusup, S. Kamble, P. Naqvi, M. Watson, I. This study addresses the energy flows and energy efficiency of integrated catalytic adsorption biomass steam gasification for hydrogen production in a pilot scale bubbling fluidized bed system utilizing palm kernel shell as feedstock. The integrated catalytic adsorption utilizes catalyst and CO2 adsorbent together in the single fluidized bed gasifier. Various variables such as effect of temperature (600�750 °C), steam to biomass ratio (1.5�2.5 w/w), adsorbent to biomass ratio (0.5�1.5 w/w), fluidization velocity (0.15�0.26 m/s) and biomass particle size (0.355�0.500 to 1.0�2.0 mm) are investigated. The results imply that the overall requirement of gasification energy increases with increasing gasification temperature, steam to biomass ratio, fluidization velocity, and decreases with adsorbent to biomass ratio whilst no significant increase is observed by varying the biomass particle size. However, a slight reduction in required energy is observed from 600 °C to 675 °C which might be due to strong CO2 adsorption, an exothermic reaction, and contributes to the energy requirements of the process. Besides, hydrogen-based energy efficiencies increase with increasing temperature while first increases to a medium value of steam to biomass ratio (2.0), adsorbent to biomass ratio (1.0) and fluidization velocity (0.21 m/s) followed by a slight decrease (or remains unchanged). The integrated catalytic adsorption steam gasification is found to be a high energy consuming process and thus, waste heat integration needs to be implemented for feasible hydrogen production. © 2018 Elsevier Ltd Elsevier Ltd 2018 Article NonPeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-85047071819&doi=10.1016%2fj.apenergy.2018.05.020&partnerID=40&md5=02d5f5cd17ba3c6fee9ff06922df515a Khan, Z. and Yusup, S. and Kamble, P. and Naqvi, M. and Watson, I. (2018) Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production. Applied Energy, 225 . pp. 346-355. http://eprints.utp.edu.my/21425/
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/
description This study addresses the energy flows and energy efficiency of integrated catalytic adsorption biomass steam gasification for hydrogen production in a pilot scale bubbling fluidized bed system utilizing palm kernel shell as feedstock. The integrated catalytic adsorption utilizes catalyst and CO2 adsorbent together in the single fluidized bed gasifier. Various variables such as effect of temperature (600�750 °C), steam to biomass ratio (1.5�2.5 w/w), adsorbent to biomass ratio (0.5�1.5 w/w), fluidization velocity (0.15�0.26 m/s) and biomass particle size (0.355�0.500 to 1.0�2.0 mm) are investigated. The results imply that the overall requirement of gasification energy increases with increasing gasification temperature, steam to biomass ratio, fluidization velocity, and decreases with adsorbent to biomass ratio whilst no significant increase is observed by varying the biomass particle size. However, a slight reduction in required energy is observed from 600 °C to 675 °C which might be due to strong CO2 adsorption, an exothermic reaction, and contributes to the energy requirements of the process. Besides, hydrogen-based energy efficiencies increase with increasing temperature while first increases to a medium value of steam to biomass ratio (2.0), adsorbent to biomass ratio (1.0) and fluidization velocity (0.21 m/s) followed by a slight decrease (or remains unchanged). The integrated catalytic adsorption steam gasification is found to be a high energy consuming process and thus, waste heat integration needs to be implemented for feasible hydrogen production. © 2018 Elsevier Ltd
format Article
author Khan, Z.
Yusup, S.
Kamble, P.
Naqvi, M.
Watson, I.
spellingShingle Khan, Z.
Yusup, S.
Kamble, P.
Naqvi, M.
Watson, I.
Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
author_facet Khan, Z.
Yusup, S.
Kamble, P.
Naqvi, M.
Watson, I.
author_sort Khan, Z.
title Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
title_short Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
title_full Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
title_fullStr Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
title_full_unstemmed Assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
title_sort assessment of energy flows and energy efficiencies in integrated catalytic adsorption steam gasification for hydrogen production
publisher Elsevier Ltd
publishDate 2018
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-85047071819&doi=10.1016%2fj.apenergy.2018.05.020&partnerID=40&md5=02d5f5cd17ba3c6fee9ff06922df515a
http://eprints.utp.edu.my/21425/
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