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Experimental investigation of reverse flow porous medium reactor with premixed and non-premixed flames

•Design, made, and operation of a reverse flow porous medium reactor.•Premixed and non-premixed methane-air flames were experimentally investigated.•Thermal profiles, wave velocities and synthesis gas production were analyzed.•Non-premixed flames had a higher H2/CO ratio than premixed flames. Revers...

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Published in:Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2021-12, Vol.425, p.130178, Article 130178
Main Authors: Fierro, Matías, Requena, Pablo, Salgansky, Eugene, Toledo, Mario
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Language:English
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cited_by cdi_FETCH-LOGICAL-c227t-47b8ca9306097f82651fa0daad3ccc32d785d2e3b239bf7a9efae8e666dfe50c3
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container_title Chemical engineering journal (Lausanne, Switzerland : 1996)
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description •Design, made, and operation of a reverse flow porous medium reactor.•Premixed and non-premixed methane-air flames were experimentally investigated.•Thermal profiles, wave velocities and synthesis gas production were analyzed.•Non-premixed flames had a higher H2/CO ratio than premixed flames. Reverse flow porous medium reactor with premixed and non-premixed flames of methane and oxidant was experimentally investigated to evaluate its suitability for hydrogen (H2) and syngas production. Methane-air premixed, non-premixed, and non-premixed with steam were the tested cases for different inlet configurations. Thermal profiles, wave velocities, and H2 and carbon monoxide (CO) production for equivalence ratios (ϕ) of 2, 3 and 4 were analyzed. Methane-air premixed flames at ϕ = 2 obtained good performance with 1574 K average and 31% and 68% of H2 and CO yield, respectively. The H2/CO ratios in syngas registered were 1.1, 1.7 and 1.5 at equivalence ratios of ϕ = 2, 3, and 4, respectively. Methane-air non-premixed flames obtained higher temperature in the zone of methane injection but no higher syngas production when compared to the premixed case. The H2/CO ratios in syngas registered were 2 and 2.4 at equivalence ratios of ϕ = 2 and 3, respectively. Methane-air non-premixed with steam shows a similarity between the temperature of without steam cases, which implies the lower influence of the steam on the reaction mechanism. Results show that separate supply of reagents allows obtaining synthesis gas with a higher H2/CO ratio than premixed case.
doi_str_mv 10.1016/j.cej.2021.130178
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Reverse flow porous medium reactor with premixed and non-premixed flames of methane and oxidant was experimentally investigated to evaluate its suitability for hydrogen (H2) and syngas production. Methane-air premixed, non-premixed, and non-premixed with steam were the tested cases for different inlet configurations. Thermal profiles, wave velocities, and H2 and carbon monoxide (CO) production for equivalence ratios (ϕ) of 2, 3 and 4 were analyzed. Methane-air premixed flames at ϕ = 2 obtained good performance with 1574 K average and 31% and 68% of H2 and CO yield, respectively. The H2/CO ratios in syngas registered were 1.1, 1.7 and 1.5 at equivalence ratios of ϕ = 2, 3, and 4, respectively. Methane-air non-premixed flames obtained higher temperature in the zone of methane injection but no higher syngas production when compared to the premixed case. The H2/CO ratios in syngas registered were 2 and 2.4 at equivalence ratios of ϕ = 2 and 3, respectively. 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Reverse flow porous medium reactor with premixed and non-premixed flames of methane and oxidant was experimentally investigated to evaluate its suitability for hydrogen (H2) and syngas production. Methane-air premixed, non-premixed, and non-premixed with steam were the tested cases for different inlet configurations. Thermal profiles, wave velocities, and H2 and carbon monoxide (CO) production for equivalence ratios (ϕ) of 2, 3 and 4 were analyzed. Methane-air premixed flames at ϕ = 2 obtained good performance with 1574 K average and 31% and 68% of H2 and CO yield, respectively. The H2/CO ratios in syngas registered were 1.1, 1.7 and 1.5 at equivalence ratios of ϕ = 2, 3, and 4, respectively. Methane-air non-premixed flames obtained higher temperature in the zone of methane injection but no higher syngas production when compared to the premixed case. The H2/CO ratios in syngas registered were 2 and 2.4 at equivalence ratios of ϕ = 2 and 3, respectively. Methane-air non-premixed with steam shows a similarity between the temperature of without steam cases, which implies the lower influence of the steam on the reaction mechanism. 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Methane-air non-premixed with steam shows a similarity between the temperature of without steam cases, which implies the lower influence of the steam on the reaction mechanism. Results show that separate supply of reagents allows obtaining synthesis gas with a higher H2/CO ratio than premixed case.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.cej.2021.130178</doi></addata></record>
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subjects Non-premixed flames
Porous media combustion
Premixed flames
Reverse flow reactor
Syngas production
title Experimental investigation of reverse flow porous medium reactor with premixed and non-premixed flames
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