کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
688500 | 889464 | 2007 | 5 صفحه PDF | دانلود رایگان |
A laboratory scale mini-pilot plant is successfully designed and built to carry out research in the liquid-phase methanol synthesis process in a impinging stream reactor, the reactor has good heat transfer and mass transfer performance because the catalyst slurry is atomized into fine drop when it goes through the pressure-flow nozzles, the mass transfer between gas phase and liquid-phase is promoted. Sustained operating conditions of temperatures approximately at 230 °C, space velocity at 10,000 h−1, high slurry recirculation flow rate and two or four opposed nozzles represent a major extension of the operating range for this type of reactor. A high slurry recirculation flow rate is benefit to the inter-phase mass transfer because the inter-phase disturbance is enhanced, and the catalyst slurry after atomized impacts each other when the opposed nozzles are used, this promotes the inter-phase interfusion and distribution so as to increase the gas–liquid mass transfer.
Journal: Chemical Engineering and Processing: Process Intensification - Volume 46, Issue 10, October 2007, Pages 905–909