Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation

M. Sheintuch; D. S.A. Simakov

Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation

M. Sheintuch^*, D. S.A. Simakov

^*Corresponding author for this work

Research output: Contribution to conference › Paper › peer-review

Abstract

A novel concept for hydrogen generation by methane steam reforming (SR) in a thermally coupled catalytic fixed bed membrane reformer was demonstrated. The reformer indirectly couples the endothermic methane SR and the exothermic methane oxidation by heat exchange between the compartments, while hydrogen is separated by a permselective Pd membrane. Good SR conversion was realized when the dimensionless ratio of methane feed to membrane hydrogen maximal flux was 0.3 or smaller and when steam to carbon ratio was below 3. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

Original language	English
Pages	517a
State	Published - 2009
Externally published	Yes
Event	8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering - Montreal, QC, Canada Duration: 23 Aug 2009 → 27 Aug 2009

Conference

Conference	8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering
Country/Territory	Canada
City	Montreal, QC
Period	23/08/09 → 27/08/09

UN SDGs

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

Cite this

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title = "Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation",

abstract = "A novel concept for hydrogen generation by methane steam reforming (SR) in a thermally coupled catalytic fixed bed membrane reformer was demonstrated. The reformer indirectly couples the endothermic methane SR and the exothermic methane oxidation by heat exchange between the compartments, while hydrogen is separated by a permselective Pd membrane. Good SR conversion was realized when the dimensionless ratio of methane feed to membrane hydrogen maximal flux was 0.3 or smaller and when steam to carbon ratio was below 3. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).",

author = "M. Sheintuch and Simakov, {D. S.A.}",

note = "Funding Information: Work supported by the Israel Ministry of Science, Program for Developing Scientific & Technological Infrastructure and Eshkol Scholarship, and by the United States–Israel Binational Science Foundation.; 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering ; Conference date: 23-08-2009 Through 27-08-2009",

year = "2009",

language = "英语",

pages = "517a",

}

Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation. / Sheintuch, M.; Simakov, D. S.A.
2009. 517a Paper presented at 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering, Montreal, QC, Canada.

Research output: Contribution to conference › Paper › peer-review

TY - CONF

T1 - Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation

AU - Sheintuch, M.

AU - Simakov, D. S.A.

N1 - Funding Information: Work supported by the Israel Ministry of Science, Program for Developing Scientific & Technological Infrastructure and Eshkol Scholarship, and by the United States–Israel Binational Science Foundation.

PY - 2009

Y1 - 2009

N2 - A novel concept for hydrogen generation by methane steam reforming (SR) in a thermally coupled catalytic fixed bed membrane reformer was demonstrated. The reformer indirectly couples the endothermic methane SR and the exothermic methane oxidation by heat exchange between the compartments, while hydrogen is separated by a permselective Pd membrane. Good SR conversion was realized when the dimensionless ratio of methane feed to membrane hydrogen maximal flux was 0.3 or smaller and when steam to carbon ratio was below 3. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

AB - A novel concept for hydrogen generation by methane steam reforming (SR) in a thermally coupled catalytic fixed bed membrane reformer was demonstrated. The reformer indirectly couples the endothermic methane SR and the exothermic methane oxidation by heat exchange between the compartments, while hydrogen is separated by a permselective Pd membrane. Good SR conversion was realized when the dimensionless ratio of methane feed to membrane hydrogen maximal flux was 0.3 or smaller and when steam to carbon ratio was below 3. This is an abstract of a paper presented at the 8th World Congress of Chemical Engineering (Montreal, Quebec, Canada 8/23-27/2009).

UR - http://www.scopus.com/inward/record.url?scp=77951560952&partnerID=8YFLogxK

M3 - 论文

AN - SCOPUS:77951560952

SP - 517a

T2 - 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering

Y2 - 23 August 2009 through 27 August 2009

ER -

Demonstration of a scaled-down autothermal membrane methane reformer for hydrogen generation

Abstract

Conference

UN SDGs

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