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- W791037890 abstract "Abstract To experimentally study the effect of supercritical fluid on product desorption, methanol synthesis from CO/CO 2 /H 2 over the Cu/ZnO/Al 2 O 3 catalyst was conducted in the solvents of liquid paraffin, supercritical n -hexane, and their mixture. For the catalyst size of 0.15 mm at which the internal mass transfer resistance was negligible, methanol yields of 10% in n -paraffin and 18% in supercritical n -hexane were obtained respectively. From the conversion rates of CO 2 at different n -hexane pressures, the resistance ratio of CO 2 hydrogenation to methanol desorption was obtained to vary from 1:2.85 to 1:0.75 when n -hexane partial pressure was increased from 0 to 4.0 MPa. Furthermore, the resistance ratio of the consecutive steps of water–gas shift reaction (WGSR), CO 2 hydrogenation and methanol desorption were then evaluated with respect to CO as the reactant. It shows the resistance ratio of the three steps varies from 0.77:1:2.82 to 0.75:1:0.75 when n -hexane partial pressure was increased from 0 to 4.0 MPa." @default.
- W791037890 created "2016-06-24" @default.
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- W791037890 date "2015-09-01" @default.
- W791037890 modified "2023-09-25" @default.
- W791037890 title "Discrimination of methanol desorption resistance relative to the reaction steps in presence of supercritical n-hexane" @default.
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- W791037890 doi "https://doi.org/10.1016/j.cep.2015.06.020" @default.
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