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Mathematical Modelling of Catalytic Fixed-Bed Reactor for Carbon Dioxide Reforming of Methane over Rh/Al2O3 Catalyst

Bulletin of Chemical Reaction Engineering & Catalysis · Vol. ume (2008) · hlm. 21–29

DOI
10.9767/bcrec.3.1-3.7120.21-29
ISSN
1978-2993
Terbit
2008-12-15
Penerbit
Masyarakat Katalis Indonesia - Indonesian Catalyst Society (MKICS)
Bahasa
eng
Lisensi
creativecommons.org/licenses/by-sa/4.0

Abstrak

A one-dimensional mathematical model was developed to simulate the performance of catalytic fixed bed reactor for carbon dioxide reforming of methane over Rh/Al2O3 catalyst at atmospheric pressure. The reactions involved in the system are carbon dioxide reforming of methane (CORM) and reverse water gas shift reaction (RWGS). The profiles of CH4 and CO2 conversions, CO and H2 yields, molar flow rate and mole raction of all species as well as reactor temperature along the axial bed of catalyst were simulated. In addition, the effects of different reactor temperature on the reactor performance were also studied. The models can also be applied to analyze the performances of lab-scale micro reactor as well as pilot-plant scale reactor with certain modifications and model verification with experimental data. © 2008 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0)

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  • Cenderawasih University
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Luqman BuchoriAfiliasi tidak diketahui8
Didi D. AnggoroAfiliasi tidak diketahui4
Didi Dwi AnggoroAfiliasi tidak diketahui3
Purwanto PurwantoCenderawasih University3
Teguh RiyantoAfiliasi tidak diketahui3
Dorothy Hoo Wei LingAfiliasi tidak diketahui2
Udin MabruroAfiliasi tidak diketahui1
Bintang Ayu KalimantiniAfiliasi tidak diketahui1
Suherman SuhermanAfiliasi tidak diketahui1
N. A. S. AminAfiliasi tidak diketahui1
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Amalia Rizqi RamadhaniAfiliasi tidak diketahui1
Rahmat GernowoDiponegoro University1
Heri MulyantiAfiliasi tidak diketahui1
Wais AlqurniAfiliasi tidak diketahui1
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Teuku Irfan MaulanaAfiliasi tidak diketahui1
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Sumber metadata: OAI-PMH (metadata jurnal) https://journal.bcrec.id/index.php/bcrec/oai, pertama di-harvest 8 Nov 2026, terakhir terlihat 8 Nov 2026.
Metadata asli (oai_dc) 
<oai_dc:dc xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/  http://www.openarchives.org/OAI/2.0/oai_dc.xsd">
	<dc:title xml:lang="en-US">Mathematical Modelling of Catalytic Fixed-Bed Reactor for Carbon Dioxide Reforming of Methane over Rh/Al2O3 Catalyst</dc:title>
	<dc:creator>Saidina Amin, Nor Aishah</dc:creator>
	<dc:creator>Istadi, Istadi</dc:creator>
	<dc:creator>Yee, New Pei</dc:creator>
	<dc:subject xml:lang="en-US">fixed-bed; mass and energy balances; CORM; RWGS; simulation; Rh/Al2O3</dc:subject>
	<dc:description xml:lang="en-US">A one-dimensional mathematical model was developed to simulate the performance of catalytic fixed bed reactor for carbon dioxide reforming of methane over Rh/Al2O3 catalyst at atmospheric pressure. The reactions involved in the system are carbon dioxide reforming of methane (CORM) and reverse water gas shift reaction (RWGS). The profiles of CH4 and CO2 conversions, CO and H2 yields, molar flow rate and mole raction of all species as well as reactor temperature along the axial bed of catalyst were simulated. In addition, the effects of different reactor temperature on the reactor performance were also studied. The models can also be applied to analyze the performances of lab-scale micro reactor as well as pilot-plant scale reactor with certain modifications and model verification with experimental data. © 2008 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0)</dc:description>
	<dc:publisher xml:lang="en-US">Masyarakat Katalis Indonesia - Indonesian Catalyst Society (MKICS)</dc:publisher>
	<dc:contributor xml:lang="en-US"></dc:contributor>
	<dc:date>2008-12-15</dc:date>
	<dc:type>info:eu-repo/semantics/article</dc:type>
	<dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
	<dc:type xml:lang="en-US"></dc:type>
	<dc:format>application/pdf</dc:format>
	<dc:identifier>https://journal.bcrec.id/index.php/bcrec/article/view/19706</dc:identifier>
	<dc:identifier>10.9767/bcrec.3.1-3.7120.21-29</dc:identifier>
	<dc:source xml:lang="en-US">Bulletin of Chemical Reaction Engineering &amp; Catalysis; 2008: BCREC Volume 3 Issue 1-3 Year 2008 (December 2008); 21-29</dc:source>
	<dc:source>1978-2993</dc:source>
	<dc:language>eng</dc:language>
	<dc:relation>https://journal.bcrec.id/index.php/bcrec/article/view/19706/9542</dc:relation>
	<dc:rights xml:lang="en-US">Copyright (c) 2008 by Authors, Published by BCREC Group</dc:rights>
	<dc:rights xml:lang="en-US">https://creativecommons.org/licenses/by-sa/4.0</dc:rights>
</oai_dc:dc>