Hydrogen production from glycerol reforming over Ni based catalysts

Su Hyun Cho; Seung Hoon Kim; Seung Hwan Lee; Bang Hee Kim; Sang Woo Kim; Arunabha Datta; Kwan Young Lee; Dong Ju Moon

Hydrogen production from glycerol reforming over Ni based catalysts

Su Hyun Cho, Seung Hoon Kim, Seung Hwan Lee, Bang Hee Kim, Sang Woo Kim, Arunabha Datta, Kwan Young Lee, Dong Ju Moon

Department of Chemical and Biological Engineering

Research output: Chapter in Book/Report/Conference proceeding › Conference contribution

Abstract

Aqueous phase reforming of glycerol over Ni-based catalysts was carried out at 225°C, 23 bar and LHSV=4 h^-1. The Ni-based catalysts were prepared by an incipient wetness impregnation method. The catalysts were characterized by N₂ physisorption and XRD. It was found that Ni (20 wt%)-Co(3 wt%)/γ-Al₂O₃ catalyst showed higher glycerol conversion with H₂/CO = 4 than the other catalysts.The results suggest that the Ni-Co/γ-Al₂O₃ catalyst can be applied to the synthesis gas production system using APR of glycerol for application in synfuel production.

Original language	English
Title of host publication	AIChE 2012 - 2012 AIChE Annual Meeting, Conference Proceedings
Publication status	Published - 2012
Event	2012 AIChE Annual Meeting, AIChE 2012 - Pittsburgh, PA, United States Duration: 2012 Oct 28 → 2012 Nov 2

Publication series

Name	AIChE Annual Meeting, Conference Proceedings

Other

Other	2012 AIChE Annual Meeting, AIChE 2012
Country/Territory	United States
City	Pittsburgh, PA
Period	12/10/28 → 12/11/2

Keywords

Aqueous phase reforming
Glycerol
Ni-Co/ γ-AlO
Synthesis gas

ASJC Scopus subject areas

Chemical Engineering(all)
Chemistry(all)

UN SDGs

This output contributes to the following UN Sustainable Development Goals (SDGs)

Cite this

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title = "Hydrogen production from glycerol reforming over Ni based catalysts",

abstract = "Aqueous phase reforming of glycerol over Ni-based catalysts was carried out at 225°C, 23 bar and LHSV=4 h-1. The Ni-based catalysts were prepared by an incipient wetness impregnation method. The catalysts were characterized by N2 physisorption and XRD. It was found that Ni (20 wt%)-Co(3 wt%)/γ-Al2O3 catalyst showed higher glycerol conversion with H2/CO = 4 than the other catalysts.The results suggest that the Ni-Co/γ-Al2O3 catalyst can be applied to the synthesis gas production system using APR of glycerol for application in synfuel production.",

keywords = "Aqueous phase reforming, Glycerol, Ni-Co/ γ-AlO, Synthesis gas",

author = "Cho, {Su Hyun} and Kim, {Seung Hoon} and Lee, {Seung Hwan} and Kim, {Bang Hee} and Kim, {Sang Woo} and Arunabha Datta and Lee, {Kwan Young} and Moon, {Dong Ju}",

year = "2012",

language = "English",

isbn = "9780816910731",

series = "AIChE Annual Meeting, Conference Proceedings",

booktitle = "AIChE 2012 - 2012 AIChE Annual Meeting, Conference Proceedings",

}

TY - GEN

T1 - Hydrogen production from glycerol reforming over Ni based catalysts

AU - Cho, Su Hyun

AU - Kim, Seung Hoon

AU - Lee, Seung Hwan

AU - Kim, Bang Hee

AU - Kim, Sang Woo

AU - Datta, Arunabha

AU - Lee, Kwan Young

AU - Moon, Dong Ju

PY - 2012

Y1 - 2012

N2 - Aqueous phase reforming of glycerol over Ni-based catalysts was carried out at 225°C, 23 bar and LHSV=4 h-1. The Ni-based catalysts were prepared by an incipient wetness impregnation method. The catalysts were characterized by N2 physisorption and XRD. It was found that Ni (20 wt%)-Co(3 wt%)/γ-Al2O3 catalyst showed higher glycerol conversion with H2/CO = 4 than the other catalysts.The results suggest that the Ni-Co/γ-Al2O3 catalyst can be applied to the synthesis gas production system using APR of glycerol for application in synfuel production.

AB - Aqueous phase reforming of glycerol over Ni-based catalysts was carried out at 225°C, 23 bar and LHSV=4 h-1. The Ni-based catalysts were prepared by an incipient wetness impregnation method. The catalysts were characterized by N2 physisorption and XRD. It was found that Ni (20 wt%)-Co(3 wt%)/γ-Al2O3 catalyst showed higher glycerol conversion with H2/CO = 4 than the other catalysts.The results suggest that the Ni-Co/γ-Al2O3 catalyst can be applied to the synthesis gas production system using APR of glycerol for application in synfuel production.

KW - Aqueous phase reforming

KW - Glycerol

KW - Ni-Co/ γ-AlO

KW - Synthesis gas

UR - http://www.scopus.com/inward/record.url?scp=84871817123&partnerID=8YFLogxK

M3 - Conference contribution

AN - SCOPUS:84871817123

SN - 9780816910731

T3 - AIChE Annual Meeting, Conference Proceedings

BT - AIChE 2012 - 2012 AIChE Annual Meeting, Conference Proceedings

T2 - 2012 AIChE Annual Meeting, AIChE 2012

Y2 - 28 October 2012 through 2 November 2012

ER -

Hydrogen production from glycerol reforming over Ni based catalysts

Abstract

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Keywords

ASJC Scopus subject areas

UN SDGs

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