ctrlnum article-86
fullrecord <?xml version="1.0"?> <dc schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><title lang="en-US">Synthesis and Activity Test of Cu/ZnO/Al2O3 for the Methanol Steam Reforming as a Fuel Cell&#x2019;s Hydrogen Supplier</title><creator>Makertihartha, IGBN; Program Studi Teknik Kimia &#x2013; FTI &#x2013; ITB Jalan Ganesha 10 Bandung 40132, Indonesia</creator><creator>Subagjo, Subagjo; Program Studi Teknik Kimia &#x2013; FTI &#x2013; ITB Jalan Ganesha 10 Bandung 40132, Indonesia</creator><creator>Gunawan, Melia Laniwati; Program Studi Teknik Kimia &#x2013; FTI &#x2013; ITB Jalan Ganesha 10 Bandung 40132, Indonesia</creator><subject lang="en-US">Cu/ZnO/Al2O3; fuel cell; hydrogen production; methanol steam reforming</subject><description lang="en-US">The&#xA0; synthesis&#xA0; of&#xA0; hydrogen&#xA0; from&#xA0; hydrocarbons&#xA0; through&#xA0; the&#xA0; steam reforming&#xA0; of&#xA0; methanol&#xA0; on&#xA0; Cu/ZnO/Al2O3&#xA0; catalyst&#xA0; has&#xA0; been&#xA0; investigated.&#xA0; This process is assigned to be one of the promising alternatives for&#xA0; fuel cell hydrogen process source. Hydrogen synthesis from methanol can be carried out by means of&#xA0; methanol&#xA0; steam&#xA0; reforming&#xA0; which&#xA0; is&#xA0; a&#xA0; gas&#xA0; phase&#xA0; catalytic&#xA0; reaction&#xA0; between methanol and water. In this research, the&#xA0; Cu/ZnO/Al2O3&#xA0; catalyst&#xA0; prepared by the dry&#xA0; impregnation&#xA0; was&#xA0; used.&#xA0; The&#xA0; specific&#xA0; surface&#xA0; area&#xA0; of&#xA0; catalyst&#xA0; was&#xA0; 194.69 m2/gram.The&#xA0; methanol&#xA0; steam&#xA0; reforming&#xA0; (SRM)&#xA0; reaction&#xA0; was&#xA0; carried&#xA0; out&#xA0; by means of the injection of gas mixture containing methanol and water with 1:1.2 mol ratio and 20-90 mL/minute feed&#xA0; flow rate to a fixed bed reactor loaded by 1 g of catalyst. The reaction temperature was 200-300 &#xB0;C, and the reactor pressure was 1 atm. Preceding&#xA0; the reaction, catalyst was reduced in the H2/N2&#xA0; mixture at 160&#xA0; &#xB0;C.&#xA0; This&#xA0; study&#xA0; shows&#xA0; that&#xA0; at&#xA0; 300&#xA0; &#xB0;C&#xA0; reaction&#xA0; temperature,&#xA0; methanol conversion&#xA0; reached&#xA0; 100%&#xA0; at&#xA0; 28&#xA0; mL/minute&#xA0; gas&#xA0; flow&#xA0; rate.&#xA0; This&#xA0; conversion decreased&#xA0; significantly&#xA0; with&#xA0; the&#xA0; increase&#xA0; of&#xA0; gas&#xA0; flow&#xA0; rate.&#xA0; Meanwhile,&#xA0; the catalyst prepared for SRM&#xA0; was stable in 36 hours of operation at 260&#xA0; &#xB0;C. The catalyst exhibited a good stability although the reaction condition was shifted to a higher gas flow rate.</description><publisher lang="en-US">ITB Journal Publisher, LPPM ITB</publisher><contributor lang="en-US"/><date>2013-09-13</date><type>Journal:Article</type><type>Other:info:eu-repo/semantics/publishedVersion</type><type>Other:</type><type>File:application/pdf</type><identifier>http://journals.itb.ac.id/index.php/jets/article/view/86</identifier><identifier>10.5614/itbj.eng.sci.2009.41.1.3</identifier><source lang="en-US">Journal of Engineering and Technological Sciences; Vol 41, No 1 (2009); 37-49</source><source>2338-5502</source><source>2337-5779</source><language>eng</language><relation>http://journals.itb.ac.id/index.php/jets/article/view/86/82</relation><recordID>article-86</recordID></dc>
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author Makertihartha, IGBN; Program Studi Teknik Kimia – FTI – ITB Jalan Ganesha 10 Bandung 40132, Indonesia
Subagjo, Subagjo; Program Studi Teknik Kimia – FTI – ITB Jalan Ganesha 10 Bandung 40132, Indonesia
Gunawan, Melia Laniwati; Program Studi Teknik Kimia – FTI – ITB Jalan Ganesha 10 Bandung 40132, Indonesia
title Synthesis and Activity Test of Cu/ZnO/Al2O3 for the Methanol Steam Reforming as a Fuel Cell’s Hydrogen Supplier
publisher ITB Journal Publisher, LPPM ITB
publishDate 2013
topic Cu/ZnO/Al2O3
fuel cell
hydrogen production
methanol steam reforming
url http://journals.itb.ac.id/index.php/jets/article/view/86
http://journals.itb.ac.id/index.php/jets/article/view/86/82
contents The synthesis of hydrogen from hydrocarbons through the steam reforming of methanol on Cu/ZnO/Al2O3 catalyst has been investigated. This process is assigned to be one of the promising alternatives for fuel cell hydrogen process source. Hydrogen synthesis from methanol can be carried out by means of methanol steam reforming which is a gas phase catalytic reaction between methanol and water. In this research, the Cu/ZnO/Al2O3 catalyst prepared by the dry impregnation was used. The specific surface area of catalyst was 194.69 m2/gram.The methanol steam reforming (SRM) reaction was carried out by means of the injection of gas mixture containing methanol and water with 1:1.2 mol ratio and 20-90 mL/minute feed flow rate to a fixed bed reactor loaded by 1 g of catalyst. The reaction temperature was 200-300 °C, and the reactor pressure was 1 atm. Preceding the reaction, catalyst was reduced in the H2/N2 mixture at 160 °C. This study shows that at 300 °C reaction temperature, methanol conversion reached 100% at 28 mL/minute gas flow rate. This conversion decreased significantly with the increase of gas flow rate. Meanwhile, the catalyst prepared for SRM was stable in 36 hours of operation at 260 °C. The catalyst exhibited a good stability although the reaction condition was shifted to a higher gas flow rate.
id IOS361.article-86
institution Institut Teknologi Bandung
affiliation onesearch.perpusnas.go.id
institution_id 79
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library
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library_id 100
collection Journal of Engineering and Technological Sciences
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subject_area Technology, Applied Sciences/Teknologi, Ilmu Terapan
Engineering/Ilmu Teknik
city KOTA BANDUNG
province JAWA BARAT
repoId IOS361
first_indexed 2016-09-16T14:27:50Z
last_indexed 2018-11-16T02:35:31Z
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