Modeling of a novel multi-stage bubble column scrubber for flue gas desulfurization☆
暂无分享,去创建一个
[1] Odd Andreas Asbjornsen. Chemical Reactor Modelling , 1992, Concise Encyclopedia of Modelling & Simulation.
[2] R. Higbie,et al. The Rate of Absorption of a Pure Gas into a Still Liquid during Short Periods of Exposure , 1935 .
[3] W. Pasiuk-Bronikowska,et al. ABSORPTION OF SO2 INTO AQUEOUS SYSTEMS , 1991 .
[4] A. Schumpe,et al. Gas holdups, specific interfacial areas, and mass transfer coefficients of aerated carboxymethyl cellulose solutions in a bubble column , 1982 .
[5] Koichi Terasaka,et al. Bubble formation under constant-flow conditions , 1993 .
[6] W. Deckwer,et al. Mixing and mass transfer in tall bubble columns , 1974 .
[7] P. Calderbank,et al. Mass transfer coefficients, velocities and shapes of carbon dioxide bubbles in free rise through distilled water , 1964 .
[8] J. Stichlmair,et al. Two-phase flow and mass transfer in scrubbers† , 1991 .
[9] A. Lübbert. Gas Hold-up , 2002 .
[10] Y. Hishinuma,et al. SO2 absorption by water droplets. , 1985 .
[11] Kiyomi Akita,et al. Gas Holdup and Volumetric Mass Transfer Coefficient in Bubble Columns. Effects of Liquid Properties , 1973 .
[12] R. Shinnar. Chemical Reactor Modeling—The Desirable and the Achievable , 1978 .
[13] J. L. Huckaby,et al. Absorption of sulfur dioxide by growing and evaporating water droplets , 1989 .