Hydrogen production from water-gas shift reaction over Ni-Cu-CeO2 oxide catalyst: The effect of preparation methods

Ajay Jha; Dae Woon Jeong; Won Jun Jang; Yeol Lim Lee; Hyun Seog Roh

doi:10.1016/j.ijhydene.2015.05.173

Hydrogen production from water-gas shift reaction over Ni-Cu-CeO₂ oxide catalyst: The effect of preparation methods

Ajay Jha, Dae Woon Jeong, Won Jun Jang, Yeol Lim Lee, Hyun Seog Roh

Division of Environmental Engineering

Research output: Contribution to journal › Article › peer-review

34 Citations (Scopus)

Abstract

The effect of the preparation method on the activity and stability of Ni-Cu-CeO₂ oxide catalysts have been investigated in the high temperature water-gas shift (HT-WGS) reaction. The highest CO conversion (85%) and selectivity was achieved by the catalyst prepared by evaporation induced self-assembly method (Ni-Cu-CeO₂-SG) at a very high GHSV of 84,000 h^-1. The improved performance of the catalyst was attributed to the mesoporous nature of the Ni-Cu-CeO₂-SG which can provide higher surface area and facilitate the easier diffusion of gas through its mesoporous channels.

Original language	English
Pages (from-to)	9209-9216
Number of pages	8
Journal	International Journal of Hydrogen Energy
Volume	40
Issue number	30
DOIs	https://doi.org/10.1016/j.ijhydene.2015.05.173
Publication status	Published - 2015 Aug 10

Bibliographical note

Funding Information:
This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT and Future Planning (2013R1A1A1A05007370). This work is financially supported by Korea Ministry of Environment (MOE) as “Knowledge-based environmental service (waste to energy recycling) human resource development project”.

Publisher Copyright:
© 2015 Hydrogen Energy Publications, LLC.

All Science Journal Classification (ASJC) codes

Renewable Energy, Sustainability and the Environment
Fuel Technology
Condensed Matter Physics
Energy Engineering and Power Technology

UN SDGs

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

Access to Document

10.1016/j.ijhydene.2015.05.173

Cite this

@article{004e94368bdd4c299844b95e99d628a0,

title = "Hydrogen production from water-gas shift reaction over Ni-Cu-CeO2 oxide catalyst: The effect of preparation methods",

abstract = "The effect of the preparation method on the activity and stability of Ni-Cu-CeO2 oxide catalysts have been investigated in the high temperature water-gas shift (HT-WGS) reaction. The highest CO conversion (85%) and selectivity was achieved by the catalyst prepared by evaporation induced self-assembly method (Ni-Cu-CeO2-SG) at a very high GHSV of 84,000 h-1. The improved performance of the catalyst was attributed to the mesoporous nature of the Ni-Cu-CeO2-SG which can provide higher surface area and facilitate the easier diffusion of gas through its mesoporous channels.",

author = "Ajay Jha and Jeong, {Dae Woon} and Jang, {Won Jun} and Lee, {Yeol Lim} and Roh, {Hyun Seog}",

note = "Funding Information: This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT and Future Planning (2013R1A1A1A05007370). This work is financially supported by Korea Ministry of Environment (MOE) as “Knowledge-based environmental service (waste to energy recycling) human resource development project”. Publisher Copyright: {\textcopyright} 2015 Hydrogen Energy Publications, LLC.",

year = "2015",

month = aug,

day = "10",

doi = "10.1016/j.ijhydene.2015.05.173",

language = "English",

volume = "40",

pages = "9209--9216",

journal = "International Journal of Hydrogen Energy",

issn = "0360-3199",

publisher = "Elsevier Limited",

number = "30",

}

TY - JOUR

T1 - Hydrogen production from water-gas shift reaction over Ni-Cu-CeO2 oxide catalyst

T2 - The effect of preparation methods

AU - Jha, Ajay

AU - Jeong, Dae Woon

AU - Jang, Won Jun

AU - Lee, Yeol Lim

AU - Roh, Hyun Seog

N1 - Funding Information: This research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT and Future Planning (2013R1A1A1A05007370). This work is financially supported by Korea Ministry of Environment (MOE) as “Knowledge-based environmental service (waste to energy recycling) human resource development project”. Publisher Copyright: © 2015 Hydrogen Energy Publications, LLC.

PY - 2015/8/10

Y1 - 2015/8/10

N2 - The effect of the preparation method on the activity and stability of Ni-Cu-CeO2 oxide catalysts have been investigated in the high temperature water-gas shift (HT-WGS) reaction. The highest CO conversion (85%) and selectivity was achieved by the catalyst prepared by evaporation induced self-assembly method (Ni-Cu-CeO2-SG) at a very high GHSV of 84,000 h-1. The improved performance of the catalyst was attributed to the mesoporous nature of the Ni-Cu-CeO2-SG which can provide higher surface area and facilitate the easier diffusion of gas through its mesoporous channels.

AB - The effect of the preparation method on the activity and stability of Ni-Cu-CeO2 oxide catalysts have been investigated in the high temperature water-gas shift (HT-WGS) reaction. The highest CO conversion (85%) and selectivity was achieved by the catalyst prepared by evaporation induced self-assembly method (Ni-Cu-CeO2-SG) at a very high GHSV of 84,000 h-1. The improved performance of the catalyst was attributed to the mesoporous nature of the Ni-Cu-CeO2-SG which can provide higher surface area and facilitate the easier diffusion of gas through its mesoporous channels.

UR - http://www.scopus.com/inward/record.url?scp=84937517478&partnerID=8YFLogxK

UR - http://www.scopus.com/inward/citedby.url?scp=84937517478&partnerID=8YFLogxK

U2 - 10.1016/j.ijhydene.2015.05.173

DO - 10.1016/j.ijhydene.2015.05.173

M3 - Article

AN - SCOPUS:84937517478

VL - 40

SP - 9209

EP - 9216

JO - International Journal of Hydrogen Energy

JF - International Journal of Hydrogen Energy

SN - 0360-3199

IS - 30

ER -