期刊
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW
卷 88, 期 -, 页码 251-269出版社
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijmultiphaseflow.2016.09.002
关键词
Bubble length; Contactor; Gas-liquid; Hydrodynamics; Multiphase flow; Taylor flow
类别
资金
- Deutsche Forschungsgemeinschaft [LA/1416/9-1]
Current research proofs the potential of apparatuses containing minichannel flow structures to intensify gas-liquid-solid contacting processes. The excellent heat and mass transfer in these devices as well as a sharp RTD mainly result from the Taylor flow regime. A proper design of corresponding contactors requires precise information on the provided interfacial areas. However, the characterisation of gas-liquid Taylor flow with industrially relevant fluids at elevated pressure and created by capillary injection devices gained little attention so far. This work analyses adiabatic gas-liquid Taylor flow in a square minichannel of 1.0 mm hydraulic diameter using water, water-glycerol, or water-ethanol mixtures as liquid phase and hydrogen or nitrogen as gas phase to cover a broad range of material parameters. In the mixing zone located within the flow channel, gas was injected into the co-flowing liquid by so-called capillary injectors with variable inner diameter (0.184, 0.317, 0.490 mm). Two different bubble forming mechanisms were identified leading to a complex interaction between physical properties of the fluids, geometrical parameters and the observed gas bubble and liquid slug lengths. According to the Pi-theorem, these lengths were affected by 6 dimensionless groups, namely (u(G,s) / u(L,s)), Re-L, We(L), (d(ln,Cl) / d(h)), (d(Ou,Cl) / d(h)), and Theta*. Based on more than 370 experimental data, novel correlations to predict gas bubble and liquid slug lengths were developed. (C) 2016 Elsevier Ltd. All rights reserved.
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