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Dynamic Behavior of Reverse Flow Reactor for Lean Methane Combustion

Journal of Engineering and Technological Sciences · Vol. 46 No. 3 (2014) · hlm. 299–317

DOI
10.5614/j.eng.technol.sci.2014.46.3.5
ISSN
2338-5502, 2337-5779
Terbit
2014-09-01
Penerbit
Directorate for Research and Community Services, Institut Teknologi Bandung
Bahasa
eng

Abstrak

The stability of reactor operation for catalytic oxidation of lean CH4 has been investigated through modeling and simulation, particularly the influence of switching time and heat extraction on reverse flow reactor (RFR) performance. A mathematical model of the RFR was developed, based on one-dimensional pseudo-homogeneous model for mass and heat balances, incorporating heat loss through the reactor wall. The configuration of the RFR consisted of inert-catalyst-inert, with or without heat extraction that makes it possible to store the energy released by the exothermic reaction of CH4 oxidation. The objective of this study was to investigate the dynamic behavior of the RFR for lean methane oxidation and to find the optimum condition by exploring a stability analysis of the simple reactor. The optimum criteria were defined in terms of CH4 conversion, CH4 slip, and heat accumulation in the RFR. At a switching time of 100 s, the CH4 conversion reached the maximum value, while the CH4 slip attained its minimum value. The RFR could operate autothermally with positive heat accumulation, i.e. 0.02 J/s. The stability of the RFR in terms of heat accumulation was achieved at a switching time of 100 s.

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  • Bandung Institute of Technology
  • Sultan Ageng Tirtayasa University
  • IPB University
  • Universitas Negeri Padang
  • Diponegoro University
  • Sumatera Institute of Technology
  • Universiti Brunei Darussalam
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Rekan penulisOrganisasiArtikel bersama
Melia Laniwati GunawanBandung Institute of Technology4
Anton IrawanSultan Ageng Tirtayasa University4
Tjokorde Walmiki SamadhiBandung Institute of Technology4
Hafid AlwanSultan Ageng Tirtayasa University2
Teguh KurniawanSultan Ageng Tirtayasa University2
I. G. B. N. MakertiharthaBandung Institute of Technology2
Elvi RestiawatyBandung Institute of Technology2
Herri SusantoBandung Institute of Technology2
IGBN MakertiharthaAfiliasi tidak diketahui2
Elfa Susanti ThamrinSumatera Institute of Technology1
Endang WarsikiIPB University1
Ono SuparnoIPB University1
Asep Bayu Dani NandiyantoIndonesia University of Education1
Darisman DarismanSultan Ageng Tirtayasa University1
Dina PujiantiSultan Ageng Tirtayasa University1
Muhammad Saifullah Abu BakarUniversiti Brunei Darussalam1
Heri PrabowoUniversitas Negeri Padang1
Arif AlgifariUniversitas Negeri Padang1
Tri Partono AdhiBandung Institute of Technology1
I Gusti Bagus Ngurah MakertiharthaBandung Institute of Technology1
Azizah NabilahBandung Institute of Technology1
Hanief AuliaBandung Institute of Technology1
Kindi Pyta GaniBandung Institute of Technology1
Arinta DewiBandung Institute of Technology1
Linea Alfa ArinaBandung Institute of Technology1
Katarina Ika KurniawatiBandung Institute of Technology1
Akhmaloka AkhmalokaBandung Institute of Technology1
David BahrinBandung Institute of Technology1
Aprilina PurbasariDiponegoro University1
Luqman BuchoriDiponegoro University1
Muhammad Dani SupardanUniversitas Syiah Kuala1
N. A. SutrisniningrumBandung Institute of Technology1
D. SantianiBandung Institute of Technology1
Kevin R. LismanaBandung Institute of Technology1
Khasin FuadiBandung Institute of Technology1
Semuel Pati SendaInstitut Teknologi Sepuluh Nopember1

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Sumber metadata: OAI-PMH (metadata jurnal) https://journals.itb.ac.id/index.php/jets/oai, pertama di-harvest 9 Nov 2026, terakhir terlihat 9 Nov 2026.
Metadata asli (oai_dc)
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	<dc:title xml:lang="en-US">Dynamic Behavior of Reverse Flow Reactor for Lean Methane Combustion</dc:title>
	<dc:creator>Budhi, Yogi W.</dc:creator>
	<dc:creator>Effendy, M.</dc:creator>
	<dc:creator>Bindar, Yazid</dc:creator>
	<dc:creator>Subagjo, S.</dc:creator>
	<dc:description xml:lang="en-US">The stability of reactor operation for catalytic oxidation of lean CH4 has been investigated through modeling and simulation, particularly the influence of switching time and heat extraction on reverse flow reactor (RFR) performance. A mathematical model of the RFR was developed, based on one-dimensional pseudo-homogeneous model for mass and heat balances, incorporating heat loss through the reactor wall. The configuration of the RFR consisted of inert-catalyst-inert, with or without heat extraction that makes it possible to store the energy released by the exothermic reaction of CH4 oxidation. The objective of this study was to investigate the dynamic behavior of the RFR for lean methane oxidation and to find the optimum condition by exploring a stability analysis of the simple reactor. The optimum criteria were defined in terms of CH4 conversion, CH4 slip, and heat accumulation in the RFR. At a switching time of 100 s, the CH4 conversion reached the maximum value, while the CH4 slip attained its minimum value. The RFR could operate autothermally with positive heat accumulation, i.e. 0.02 J/s. The stability of the RFR in terms of heat accumulation was achieved at a switching time of 100 s.</dc:description>
	<dc:publisher xml:lang="en-US">Directorate for Research and Community Services, Institut Teknologi Bandung</dc:publisher>
	<dc:date>2014-09-01</dc:date>
	<dc:type>info:eu-repo/semantics/article</dc:type>
	<dc:type>info:eu-repo/semantics/publishedVersion</dc:type>
	<dc:format>application/pdf</dc:format>
	<dc:identifier>https://journals.itb.ac.id/index.php/jets/article/view/880</dc:identifier>
	<dc:identifier>10.5614/j.eng.technol.sci.2014.46.3.5</dc:identifier>
	<dc:source xml:lang="en-US">Journal of Engineering and Technological Sciences; Vol. 46 No. 3 (2014); 299-317</dc:source>
	<dc:source>2338-5502</dc:source>
	<dc:source>2337-5779</dc:source>
	<dc:language>eng</dc:language>
	<dc:relation>https://journals.itb.ac.id/index.php/jets/article/view/880/533</dc:relation>
</oai_dc:dc>