Die berechnung der schütthöhe bei absorptionsvorgängen in füllkörperkolonnen
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[1] K. Onda,et al. Liquid‐side mass transfer coefficients in packed towers , 1959 .
[2] F. Yoshida,et al. Liquid Phase Mass Transfer Rates and Effective Interfacial Area in Packed Absorption Columns , 1958 .
[3] H. Shulman,et al. Performance of packed columns. IV. Effect of gas properties, temperature, and pressure on gasphase mass transfer coefficients , 1957 .
[4] H. Shulman,et al. Performance of packed columns. II. Wetted and effective‐interfacial areas, gas ‐ and liquid‐phase mass transfer rates , 1955 .
[5] G. Kling. Eine allgemeine Gesetzmäßigkeit über den Flüssigkeits‐Filmkoeffizienten beim Stoffaustausch in Türmen mit berieselten Ringfüllungen , 1953 .
[6] C. Bonilla,et al. Liquid-Gas Interfacial Area in Packed Columns , 1950 .
[7] A. P. Colburn,et al. Distillation and Absorption in Packed Columns A Convenient Design and Correlation Method , 1935 .
[8] E. R. Gilliland,et al. Diffusion of Vapors into Air Streams , 1934 .
[9] Jr. W. A. Peters,et al. The Efficiency and Capacity of Fractionating Columns , 1922 .
[10] G. Thodos,et al. Transfer processes in the flow of gases through packed and distended beds of spheres , 1963 .