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Mass transfer coefficient

About: Mass transfer coefficient is a research topic. Over the lifetime, 7827 publications have been published within this topic receiving 168354 citations.


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Journal ArticleDOI
TL;DR: In this paper, mass transfer of CO2 is studied in a polypropylene hollow fiber membrane contactor when the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate is used as the absorption liquid.
Abstract: Carbon dioxide (CO2) and sulfur dioxide (SO2) are typical gases produced during coal combustion and their emissions have to be controlled and minimized in order to reduce environmental risks. Organic solvents are commonly used as absorption liquids for the chemical absorption of CO2 and SO2, and their use in combination with a membrane device is being studied recently. The volatile character of common solvents produces solvent losses due to their evaporation into the gas stream. Thus, the use of solvents with lower vapor pressure such as ionic liquids as absorption liquids may contribute to the performance of a zero solvent emission process. In the present study, mass transfer of CO2 is studied in a polypropylene hollow fiber membrane contactor when the ionic liquid 1-ethyl-3-methylimidazolium ethylsulfate is used as the absorption liquid. Mass transfer coefficients are compared with those obtained with a ceramic hollow fiber contactor for SO2 absorption. The overall mass transfer coefficient takes a valu...

53 citations

Journal ArticleDOI
TL;DR: In this article, the authors considered the problem of mass transfer between a one or two component bubble and the continuous phase with a chemical reaction occuring either in the continuous or in the dispersed phase.

53 citations

Journal ArticleDOI
TL;DR: In this paper, a microfluid flow-through cell with a very narrow inter-electrode gap and flowthrough electrodes was used to maximize mass transport towards the electrodes.

53 citations

Journal ArticleDOI
Mahdi Ramezani1, Bo Kong1, Xi Gao1, Michael G. Olsen1, R. Dennis Vigil1 
TL;DR: In this article, experimental measurements of the volumetric liquid mass transfer and bubble size distribution in a vertically oriented semi-batch gas-liquid Taylor-Couette vortex reactor with radius ratio η = ǫ/r/rǫ −075 and aspect ratio Γ −= h/(ro −− �) −40 were performed, and the results were presented for axial and azimuthal Reynolds number ranges of Rea −119 −143 and ReΘ −= 0 −35 −×104, respectively.

53 citations

Journal ArticleDOI
TL;DR: In this article, the effect of gas flow rate, liquid flow rate and diffusivity of the solute in the gas phase on the gas-side mass transfer coefficient was investigated in laboratory packed columns containing 38 in. (0.95 cm) ceramic Raschig rings.

53 citations


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Performance
Metrics
No. of papers in the topic in previous years
YearPapers
2023110
2022240
2021245
2020205
2019207
2018252