Thermally integrated micro-channel fuel processor

Chang Hwan Kim; Andrew R. Tadd; Gap Yong Kim; Amit Dhingra; Hong Im; Jun Ni; Johannes Schwank; Levi T. Thompson

Thermally integrated micro-channel fuel processor

Chang Hwan Kim^*, Andrew R. Tadd, Gap Yong Kim, Amit Dhingra, Hong Im, Jun Ni, Johannes Schwank, Levi T. Thompson

^*Corresponding author for this work

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

Abstract

Integration of highly active and selective autothermal reforming (ATR), water gas shift, and preferential oxidation catalysts into a thermally integrated, micro-channel reactor system capable of producing 1 kw of H₂-rich gas for a proton exchange membrane fuel cell was studied. The catalysts were coated onto microporous Fe-Cr metal alloy foams and placed into microchannels within the thermally integrated reactor system. The ATR performance was stable over the 100 hr long-term stability test and the hydrogen efficiency for the system exceeded 70%. The catalysts and reactors for CO cleanup (water gas shift and preferential oxidation) were described. This is an abstract of a paper presented at the AIChE Annual Meeting (San Francisco, CA 11/12-17/2006).

Original language	English (US)
Title of host publication	2006 AIChE Annual Meeting
State	Published - 2006
Externally published	Yes
Event	2006 AIChE Annual Meeting - San Francisco, CA, United States Duration: Nov 12 2006 → Nov 17 2006

Other

Other	2006 AIChE Annual Meeting
Country/Territory	United States
City	San Francisco, CA
Period	11/12/06 → 11/17/06

ASJC Scopus subject areas

Biotechnology
Chemical Engineering(all)
Bioengineering
Safety, Risk, Reliability and Quality

Cite this

@inproceedings{be05bbb558124092b35bd3c912e1a84b,

title = "Thermally integrated micro-channel fuel processor",

abstract = "Integration of highly active and selective autothermal reforming (ATR), water gas shift, and preferential oxidation catalysts into a thermally integrated, micro-channel reactor system capable of producing 1 kw of H2-rich gas for a proton exchange membrane fuel cell was studied. The catalysts were coated onto microporous Fe-Cr metal alloy foams and placed into microchannels within the thermally integrated reactor system. The ATR performance was stable over the 100 hr long-term stability test and the hydrogen efficiency for the system exceeded 70%. The catalysts and reactors for CO cleanup (water gas shift and preferential oxidation) were described. This is an abstract of a paper presented at the AIChE Annual Meeting (San Francisco, CA 11/12-17/2006).",

author = "Kim, {Chang Hwan} and Tadd, {Andrew R.} and Kim, {Gap Yong} and Amit Dhingra and Hong Im and Jun Ni and Johannes Schwank and Thompson, {Levi T.}",

year = "2006",

language = "English (US)",

isbn = "081691012X",

booktitle = "2006 AIChE Annual Meeting",

note = "2006 AIChE Annual Meeting ; Conference date: 12-11-2006 Through 17-11-2006",

}

TY - GEN

T1 - Thermally integrated micro-channel fuel processor

AU - Kim, Chang Hwan

AU - Tadd, Andrew R.

AU - Kim, Gap Yong

AU - Dhingra, Amit

AU - Im, Hong

AU - Ni, Jun

AU - Schwank, Johannes

AU - Thompson, Levi T.

PY - 2006

Y1 - 2006

N2 - Integration of highly active and selective autothermal reforming (ATR), water gas shift, and preferential oxidation catalysts into a thermally integrated, micro-channel reactor system capable of producing 1 kw of H2-rich gas for a proton exchange membrane fuel cell was studied. The catalysts were coated onto microporous Fe-Cr metal alloy foams and placed into microchannels within the thermally integrated reactor system. The ATR performance was stable over the 100 hr long-term stability test and the hydrogen efficiency for the system exceeded 70%. The catalysts and reactors for CO cleanup (water gas shift and preferential oxidation) were described. This is an abstract of a paper presented at the AIChE Annual Meeting (San Francisco, CA 11/12-17/2006).

AB - Integration of highly active and selective autothermal reforming (ATR), water gas shift, and preferential oxidation catalysts into a thermally integrated, micro-channel reactor system capable of producing 1 kw of H2-rich gas for a proton exchange membrane fuel cell was studied. The catalysts were coated onto microporous Fe-Cr metal alloy foams and placed into microchannels within the thermally integrated reactor system. The ATR performance was stable over the 100 hr long-term stability test and the hydrogen efficiency for the system exceeded 70%. The catalysts and reactors for CO cleanup (water gas shift and preferential oxidation) were described. This is an abstract of a paper presented at the AIChE Annual Meeting (San Francisco, CA 11/12-17/2006).

UR - http://www.scopus.com/inward/record.url?scp=58049105155&partnerID=8YFLogxK

M3 - Conference contribution

AN - SCOPUS:58049105155

SN - 081691012X

SN - 9780816910120

BT - 2006 AIChE Annual Meeting

T2 - 2006 AIChE Annual Meeting

Y2 - 12 November 2006 through 17 November 2006

ER -

Thermally integrated micro-channel fuel processor

Abstract

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ASJC Scopus subject areas

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