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过氧化氢生产用三相固定床中泡沫流持液量的实验研究

Experimental Investigation on Liquid Holdup of Foaming Flow in Three-phase Packed-bed for Hydrogen Peroxide Production
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摘要  研究采用空气-蒽醌工作液体系模拟过氧化氢生产中蒽醌氢化用三相反应器内流体的流动情况。首先建立了实验测定部分发泡固定床内泡沫流持液量的方法。然后应用建立的方法测定了不同气液表观流速下动态持液量,并考察了气液表观流速对动态和总持液量的影响。最后,比较了10种用于估算发泡体系泡沫流区持液量经验式的计算精度。结果表明,分别采用Specchia和Larachi经验式估算动态和总持液量的计算误差均在5%以内。 In order to obtain the accurate relationship for the total and dynamic liquid holdup of foaming flow in the three-phase packed-bed used for hydrogen peroxide production by anthraquinone process. Air and anthraquinone working solution system was selected to simulate the fluid flow in the real reactor. At first, a method to measure liquid holdup for the foaming flow was initially established, and then the effect of gas and liquid superficial mass rate on the dynamic and total liquid holdup were discussed in detail. Finally, by comparison of 10 empirical relations for liquid holdup, it's indicated that Specchia and Larachi's correlations can be used to predict the dynamic and total liquid holdup of the foaming flow in the Three-phase packed-bed for hydrogenation of anthraquinone with an accuracy of 5%, respectively.
出处 《化学反应工程与工艺》 CAS CSCD 北大核心 2003年第4期330-336,共7页 Chemical Reaction Engineering and Technology
基金 国家重点基础研究发展规划"973"计划(编号:G2000048005)。
关键词 过氧化氢 生产设备 三相固定床 泡沫流 持液量 实验研究 气体-蒽醌工作液体系 Liquid holdup Foaming flow Three-phase packed-bed reactor Foaming system hydrogen peroxide production
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参考文献14

  • 1[1]Santacesaria E, DiSerio M, Russo A. Kinetic and Catalytic Aspects in the Hydrogen Peroxide Production via Anthraquinone[J]. Chem Eng Sci,1999, 54: 2799~2806. 被引量:1
  • 2[2]Solvay (BE). Making Hhydrogen Peroxide by the Anthraquinone Process [P]. GB 2334028A, 1999,8~11. 被引量:1
  • 3[3]Charpentier J C, Favier M. Some Liquid Holdup Experimental Data In Trickle-bed Reactors for Foaming and Non-foaming Hydrocarbon[J]. AIChE Journal, 1975, 21:1213~1218. 被引量:1
  • 4[4]Specchia V, Baldi G. Pressure Drop and Liquid Holdup for Two Phase Concurrent Flow in Packed Beds[J]. Chem Eng Sci, 1977,32:515~523. 被引量:1
  • 5[5]Sai P S T, Varma Y B R. Flow Pattern of the Phases and Liquid Saturation in Gas-Liquid Concurrent Downflow through Packed Beds[J]. The Canadian Journal of Chem Eng, 1988,66(6):353~360. 被引量:1
  • 6[6]Benkird K, Rode S, Midoux N. Prediction of Pressure Drop and Liquid Saturation in Trickle-bed Operated in High Interaction Regimes[J]. Chem Eng Sci, 1997, 52(21~22):4021~4032. 被引量:1
  • 7[7]Larachi F, Laurent A, Midoux N, et al. Experimental study of Trickle-Bed Reactor Operating at High Pressure: Two-phase Pressure Drop and Liquid Saturation[J]. Chem Eng Sci, 1991, 46:1233~1246. 被引量:1
  • 8[8]Yang X L, Wild G, Euzen J P. Study of Liquid Retention in Fixed-bed Reactor with Upword Flow of Gas and Liquid[J]. Int Chem Eng, 1993, 33: 72~84. 被引量:1
  • 9[9]Holub R A, Dudukovic M P, Ramachandran P A. Pressure Drop, Liquid Holdup, and Flow Regime Transition in Trickle Flow[J]. AIChE Journal, 1993,39: 302~321. 被引量:1
  • 10[10]Ellman M J, Midoux N, Wild G et al, A New Improved Liquid Holdup CorrelAtion for Trickle-bed Reactors[J]. Chem Eng Sci, 1990, 45: 1677~1684. 被引量:1

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