Heat and mass transfer of binary distillation in a vertical wetted-wall column

• Published in: Chemical engineering research & design Vol. 128; pp. 49 - 58
• Main Authors: Park, Hong-ran, Kim, Yeongmin, Kwak, Sung Jo, Choi, Jiyeon, Yang, SeungCheol, Han, Moon Hee, Kim, Dong Kook
• Format: Journal Article
• Language: English
• Published: Rugby Elsevier B.V 01.12.2017; Elsevier Science Ltd
• Subjects: Binary distillation; Boundary layer; Boundary layers; Condensation; Distillation; Distilled water; Ethanol; Exponential functions; Fluid flow; Fluxes; Heat and mass transfer; Heat transfer; Laminar boundary layer; Mass transfer; Numerical analysis; Partial condensation; Reynolds number; Studies; Thermal boundary layer; Vapor phases; Wetted wall columns; Partial condensation; Heat and mass transfer; Binary distillation; Boundary layer
• ISSN: 0263-8762; 1744-3563
• DOI: 10.1016/j.cherd.2017.09.032

[Display omitted] •Total reflux distillation experiments on binary system of ethanol and water were carried out.•A flat perforated plate was applied for suction or injection of fluid.•The effects of partial condensation on a wetted-wall column was investigated.•The modified laminar boundary layer theory showed better agreement for ethanol–water binary distillation. In this study, we investigated the effects of partial condensation on the heat and mass transfer rates during ethanol–water binary distillation based on a laminar boundary layer theory applied to a wetted-wall column, as well as the characteristics of the boundary layer behavior on the vapor phase. The thickness of the thermal and concentration boundary layers were shown to decrease with an increase in partial condensation, whereas the heat and mass transfer rates were demonstrated to increase. The results of this study show that the dimensionless rates considered for the convective fluxes Sh/(1+αM) and Nu/(1+αH) can be determined through a combined application of the laminar boundary layer theory and function g(β) of a partial condensation ratio β (mole basis), where β is linearly proportional to υs/u∞ (dimensionless velocity), which is a term for the boundary condition at a vapor–liquid interface. A numerical analysis of the experiment data show that both Sh/(1+αM) and Nu/(1+αH) are approximately proportional to the Reynolds number (Re), and not to Re1/2, as is generally the case, under the condition υs=0. Therefore, we established the functional relationship g(β′)=0.4288–0.2844eβ″, i.e., the exponential function of β′, which was converted into a mass basis. The modified boundary layer theory was found to be completely self-consistent.