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^*

^*Corresponding author for this work

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

General Chemical Engineering
General Chemistry

UN SDGs

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

Cite this

@inproceedings{aebb9bc0e2124692aba497c9a4a29a56,

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 - https://www.scopus.com/pages/publications/84871817123

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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