Zobrazeno 1 - 10
of 22
pro vyhledávání: '"Kuo-Tsong Yu"'
Publikováno v:
Chemical Engineering Research and Design. 163:182-191
Rayleigh convection is an interfacial transport phenomenon in the CO2 capture and storage processes. In the present paper, we proposed a mesoscale model to capture the convection structure caused by Rayleigh convection in a 20 mm × 10 mm CO2 absorpt
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3b659a6febc0fa8e26dfa081b5edbf63
https://doi.org/10.1016/j.cherd.2020.07.033
https://doi.org/10.1016/j.cherd.2020.07.033
Publikováno v:
Chemical Engineering Science. 195:494-506
An approach to enhancing the chemical reaction process based on flow pattern construction was proposed. We demonstrated that the entropy generation due to mass transfer, chemical reaction and the viscous dissipation tend to their extremums when the p
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::c12dbeec3c81aa9313714a2ea6dd73eb
https://doi.org/10.1016/j.ces.2018.09.048
https://doi.org/10.1016/j.ces.2018.09.048
Publikováno v:
Chemical Engineering Science. 248:117148
The performance of column-style equipment, including distillation columns or tower reactors, significantly depends on how uniformly distributed the gas flow is at the inlet section of the column. To improve the gas distribution uniformity, the so-cal
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ee21b01ab2b668ccec577152cac88acd
https://doi.org/10.1016/j.ces.2021.117148
https://doi.org/10.1016/j.ces.2021.117148
Publikováno v:
Chemical Engineering Science. 249:117306
Turbulent mass transport is an essential phenomenon in chemical reactors. A two-equation model of turbulent mass transport has been proposed for less numerical simulation error in previous work. However, there are still some model constants that have
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::1d8583e7998a0262a12720364be156fd
https://doi.org/10.1016/j.ces.2021.117306
https://doi.org/10.1016/j.ces.2021.117306
Publikováno v:
Chemical Engineering Science. 182:44-55
Heat or mass transfer becomes usually complicated if coupled with fluid flow. To model the process, the mass, heat, and momentum conservation equations have been well established, which are shown in our work not the only governing laws. We analyzed h
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::5f34b0b1e6674f246b0cba2cac2c0511
https://doi.org/10.1016/j.ces.2018.02.017
https://doi.org/10.1016/j.ces.2018.02.017
Publikováno v:
Chemical Engineering Science. 231:116265
A multi-objective topology optimization method is proposed to generate local solid structure that can enhance the solar thermal decomposition of the methane (TDM) reactor. Two dominant factors can govern the performance of solar reactor, with heat tr
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::9fb5857a021ed0cf02d5b164134dfc8a
https://doi.org/10.1016/j.ces.2020.116265
https://doi.org/10.1016/j.ces.2020.116265
Publikováno v:
Chemical Engineering Science. 146:26-34
An optimization method to find the thermodynamic limits of convective mass transfer for fixed viscous dissipation is developed. The method applies the principle of extremum entropy generation to the mass transfer problem. The mass transfer-induced en
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::32ebf5a3fcd3155864a9300f163917ce
https://doi.org/10.1016/j.ces.2016.01.059
https://doi.org/10.1016/j.ces.2016.01.059
Publikováno v:
Computers & Chemical Engineering. 134:106707
The optimum designs of combustor are traditionally based on trial and error method. In this paper, we propose a systematic optimization method for the optimum design of this kind of reactor. The optimization procedure is introduced by taking a premix
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::160e7facbd4fb0bd28ce79bacd9fe896
https://doi.org/10.1016/j.compchemeng.2019.106707
https://doi.org/10.1016/j.compchemeng.2019.106707
Publikováno v:
Chemical Engineering Research and Design. 99:176-184
In this paper, a novel process for C3 stream selective hydrogenation in ethylene plant is proposed. The proposed process combines the propylene catalytic reactive distillation for the hydrogenation with the column of depropanization to achieve a ther
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8ab2e03b9c5214797e13cf5609f7b34f
https://doi.org/10.1016/j.cherd.2015.03.029
https://doi.org/10.1016/j.cherd.2015.03.029
The importance of developing micro-combustor with high efficient is apparent, due to the demand for miniature power source with high energy density. A two-dimension model of micro-combustor for a premixed methane/air mixtures combustion process, unde
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::51521c06b6f2d841f4350989deeeb256
https://doi.org/10.1016/b978-0-444-64241-7.50319-0
https://doi.org/10.1016/b978-0-444-64241-7.50319-0
