2013
DOI: 10.1016/j.cep.2013.03.021
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Characteristics of integrated micro packed bed reactor-heat exchanger configurations in the direct synthesis of dimethyl ether

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Cited by 41 publications
(38 citation statements)
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“…Considering that the CO conversion level in the present study is lower compared to the ones in Ref. 24 and 21, similar or somehow larger diffusivities ensure that the diffusion rates surpass reaction kinetics. The same is valid for the CO 2 diffusivity.…”
Section: Mass Transfer Limitationsmentioning
confidence: 75%
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“…Considering that the CO conversion level in the present study is lower compared to the ones in Ref. 24 and 21, similar or somehow larger diffusivities ensure that the diffusion rates surpass reaction kinetics. The same is valid for the CO 2 diffusivity.…”
Section: Mass Transfer Limitationsmentioning
confidence: 75%
“…The reactor consists of a 6 cm long reaction slit with rectangular cross section of 8.8 × 1.5 mm 2 , sandwiched between cross flow channels for circulation of a heat transfer oil. Such reactors have been studied earlier under similar operating conditions for the methanol [21][22][23] and the direct DME [24][25][26] syntheses, and established as practically isothermal, isobaric, free from mass transfer limitations, and with a narrow residence time distribution. Premixed synthesis gas with H 2 to CO molar ratio of either 1 (Syngas-1) or 2 (Syngas-2) was used as feed.…”
Section: Methodsmentioning
confidence: 99%
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