Please use this identifier to cite or link to this item: http://ir.mu.ac.ke:8080/jspui/handle/123456789/5439
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dc.contributor.authorZhao, Zemeng-
dc.contributor.authorZhang, Xiu-
dc.contributor.authorLi, Guangjun-
dc.contributor.authorChu, Guangwen-
dc.contributor.authorArowo, Moses NyoTonglo-
dc.date.accessioned2021-11-23T12:00:10Z-
dc.date.available2021-11-23T12:00:10Z-
dc.date.issued2017-
dc.identifier.urihttps://doi.org/10.1002/ceat.201600396-
dc.identifier.urihttp://ir.mu.ac.ke:8080/jspui/handle/123456789/5439-
dc.description.abstractMass transfer characteristics in a rotor-stator reactor in terms of the overall volumetric mass-transfer coefficient (Kxa) using the N2-H2O-O2 system were investigated. The effects of various operating parameters including rotation speed, liquid volumetric flow rate, and gas volumetric flow rate on Kxa were systematically examined, and a gas-liquid mass transfer model was established to predict Kxa. Results reveal that Kxa increased with higher rotation speed, liquid volumetric flow rate, and gas volumetric flow rate. The results also confirm that the predicted values of Kxa were in agreement with the experimental values with deviation within 15 %. The results contribute to a better understanding of mass transfer characteristics in rotor-stator reactors.en_US
dc.language.isoenen_US
dc.publisherWiley online libraryen_US
dc.subjectMass Transferen_US
dc.subjectRotor-stator reactoren_US
dc.subjectProcess intensificationen_US
dc.subjectVolumetric flow rateen_US
dc.titleMass transfer characteristics in a rotor‐stator reactoren_US
dc.typeArticleen_US
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