2009
DOI: 10.1016/j.cattod.2008.08.040
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Catalytic walls and micro-devices for generating hydrogen by low temperature steam reforming of ethanol

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Cited by 54 publications
(35 citation statements)
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“…For the activity curve of the Pd microreactor (MR-Pd), the result seems to indicate that there is a tendency for the CO conversion to slightly decrease at high temperatures (above 170ºC), which could be due, as previously observed for similar active phases [7] to the water-gas shift reactor becoming more relevant at high temperatures, as previously stated in the literature [27]. The enhanced performance of the microreactor with respect to the powder catalyst has been previously stated in the literature for several catalytic systems in microreactor configurations [11], [28], [29], [30]. In general, this enhanced microreactor behaviour is ascribed to mass and heat transfer processes favoured in the microchannels [4], [31], [27].…”
Section: Resultssupporting
confidence: 70%
“…For the activity curve of the Pd microreactor (MR-Pd), the result seems to indicate that there is a tendency for the CO conversion to slightly decrease at high temperatures (above 170ºC), which could be due, as previously observed for similar active phases [7] to the water-gas shift reactor becoming more relevant at high temperatures, as previously stated in the literature [27]. The enhanced performance of the microreactor with respect to the powder catalyst has been previously stated in the literature for several catalytic systems in microreactor configurations [11], [28], [29], [30]. In general, this enhanced microreactor behaviour is ascribed to mass and heat transfer processes favoured in the microchannels [4], [31], [27].…”
Section: Resultssupporting
confidence: 70%
“…Partial ethanol is combusted in the other side of the channel to supply heat required for reforming. Such design provides many technical advantages including rapid mass and heat transport due to large surface area to volume ratios, lower pressure drop, good structural and thermal stability, and precise control of reaction conditions leading to higher hydrogen yield [159,160]. The main challenges faced by this technique before it becomes final commercialization are system integration, reactor fabrication process, and catalyst regeneration or replacement.…”
Section: Future Development Directionsmentioning
confidence: 99%
“…With the resultant geometry, the specific contact area increased with respect to conventional microreactors up to fabulous values of 10 5 -10 6 m 2 /m 3 . A ∼0.01 cm 3 unit comprising >10 6 channels was successfully tested for ESR under residence times <1 s, rendering specific production rates exceeding 50 NL of H 2 per mL of liquid fed and cm 3 of reactor [5,6]. The low-temperature reforming of ethanol offers a nice solution for supplying hydrogen to portable fuel cells due to its high volumetric energy density, low cost, safety, and easy transportation [7].…”
Section: Introductionmentioning
confidence: 99%