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微通道气液两相流型及界面面积测定 被引量:1

Flow pattern and gas-liquid interfacial area in a microchannel contactor
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摘要 以氢氧化钠水溶液及纯二氧化碳气体为工质,研究了石英玻璃微通道中的气液两相流流型及两相界面面积。实验中可清晰分辨的流型为弹状流(Slug),弹状一环状流(Slug—annular)及搅拌流(Churn),由实验观测的结果建立了相应的流型图并与Triplett实验结果进行了比较,结果表明高液相表观流速对流型转换影响较大。在微通道中可以实现比较高的气液两相界面面积,实验范围内气液两相界面面积高达5070m^2/m^3。两相界面面积随气相表观流速的增加而增加,而液相表观流速对两相界面面积的影响则不显著。相对于弹状流区域,在弹状一环状流及搅拌流区域可以实现比较高的传质界面面积。搅拌流区域气液两相界面面积可以采用气液表观雷诺数进行很好关联,其绝对平均偏差仅为3.76%。 With aqueous solutions of sodium hydroxide and carbon dioxide as the working fluids, the flow patterns and the gas-liquid interface in a quartz microchaanel contactor are investigated. The discernable flow patterns are slng, slug-annular and churn. Based on the experimental data, the flow pattern map is developed and compared with the Triplett's correlations. It shows that the flow pattern transition is affected by the mass transfer especially when the supeficial liquid velocities are high. As high as 5 070 m2/m3, the microchannel contactor can provide a high gas-liquid interface area. The gas-liquid interface area increases with the increase of superficial gas velocities while the influence of superficial liquid velocities is not marked. Compared with the slug flow, a higher gas-liquid interface area can be achieved with a slug-annular and churn flow. The interface area can be well correlated with the superficial reyndds number for churn flow and the absolute mean deviation is only 3.76%.
出处 《现代化工》 CAS CSCD 北大核心 2009年第5期60-64,共5页 Modern Chemical Industry
关键词 微通道 两相流 流型 流型图 界面面积 microchanne two-phase flow flow pattern flow pattern regime interfacial area
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  • 1Ehrfeld W, Hessel V, I.owe H. Microreactors: New Technology for Modern Chemistry[ M]. Weinheim: Wiley-VCH, 2000.
  • 2Ehrfeld W,Hartmann H J,Hessel V, et al. Microreaction technology for process intensification and high throughput screening[ C ]//Micro Total Analysis Systems 2000, Proceedings, Enschede Netherlands: Springer,2000,33 - 40.
  • 3陈光文,袁权.微化工技术[J].化工学报,2003,54(4):427-439. 被引量:146
  • 4陈光文.微化工技术研究进展[J].现代化工,2007,27(10):8-13. 被引量:48
  • 5JENSEN K F. Microreaction engineering: Is small better? [J]. Chemical Engineering Science,2001,56(2) :293 - 303.
  • 6MAE K. Advanced chemical processing using microspace[ J]. Chemical Engineering Science, 2007,62 ( 18/19/20 ) : 4842 - 4851.
  • 7Ehrfeld W, Ehrfeld U. Micro fabrication for process intensification [ C]//Proceedings of the 5th International Conference on Microreaction Technology ( IMRET 5), Strasbourg: Springer-Verlag Berlin, 2001 : 27 - 30.
  • 8Wongwises S, Pipathattakul M. Flow pattern, pressure drop and void fraction of two-phase gas-liquid flow in an inclined narrow annular channel[J]. Experimental Thermal and Fluid Science, 2006, 30(4) : 345 - 354.
  • 9Bi Q C,Zhao T S, Cheng P. An experimental study of co-current two- phase flow patterns in small triangular channels[ C]//Proceedings of the 4th International Symposium on Muhiphase Flow and Heat Transfer, Xian:Xian Jiaotung Univ Press, 1999.
  • 10Coleman J W, Garimella S. Characterization of two-phase flow patterns in small diameter round and rectangular tubes[ J]. Internationa/Junrnal of Heat and Mass Transfer, 1999,42(15) :2869 - 2881.

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  • 1许立信,朱明乔,何潮洪.环己烷分子氧选择性氧化固体催化剂研究进展[J].合成纤维工业,2006,29(1):45-48. 被引量:4
  • 2Hendry D G, Gould C W, Schuetzle D, et al. Auto oxidations of cyclohexane and its autoxidation products [ J ]. J Org Chem, 1976,41(1) :1 -10.
  • 3Walling C. Limiting rates of hydrocarbon autoxidations [ J ]. J Amer Chem Soc,1969, 91 (27) : 7590 -7594.
  • 4Kestenbaum H, De Oliveira A L, Schmidt W, et al. Silver- catalyzed oxidation of ethylene to ethylene oxide in a microreac- tion system[J]. Ind Eng Chem Res, 2002, 41 (4):710- 719.
  • 5Ge Hao, Chen Guangwen, Yuan Quan, et al. Gas phase par- tial oxidation of toluene over modified V2O5// TiO2 catalysts in a microreactor[ J ]. Chem Eng J, 2007,127 ( 1/2/3 ) : 39 - 46.
  • 6Suresh A K, Sharma M M, Sridhar T. Engineering aspects of industrial liquid-phase air oxidation of hydrocarbons [ J ]. Ind Eng Chem Res, 2000, 39 ( 11 ) : 3958 - 3997.
  • 7Jevtic R, Ramachandran P A, Dudukovic M P. Effect of oxygen on cyclohexane oxidation : A stirred tank study [ J ]. Ind Eng Chem Res, 2009, 48 (17) : 7986 - 7993.
  • 8Barkelew C H. Stability of chemical reactors [ J ]. Chem Eng Prog Symp Ser,1959, 55:37 -49.
  • 9Leclerc A, Alame M, Schweich D, et al. Gas-liquid selective oxidations with oxygen under explosive conditions in a micro- structured reactor[J]. Lab Chip, 2008, 8(5) : 814 -817.
  • 10Jevtic R, Ramachandran P A, Dudukovie M P. Capillary reac- tor for cyclohexane oxidation with oxygen [ J ]. Chem Eng Res Des. , 2010, 88(3A) : 255-262.

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