Non-isothermal micromixing in turbulent liquids: Theory and experiment

被引:55
作者
Baldyga, J [1 ]
Bourne, JR [1 ]
Walker, B [1 ]
机构
[1] ETH Zentrum, Tech Chem Lab, CH-8092 Zurich, Switzerland
关键词
competitive reactions; micromixing; selectivity; semibatch reactor; temperature segregation; turbulent mixing;
D O I
10.1002/cjce.5450760336
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Partial segregation of reagents occurs when reaction rates exceed mixing rates and frequently causes product distributions to be mixing-dependent. A simultaneous temperature segregation, whereby the temperature in a reaction zone differs from that in its surroundings, has rarely been considered when mixing reagents in the liquid phase. The Prandtl number is usually sufficiently small that engulfment, not thermal conduction, determines the local temperature. The engulfment model of micromixing can then be extended by a heat balance to specify this temperature. To evaluate this model, a new pair of fast competitive reactions (neutralisation and acetal hydrolysis) has been characterised thermochemically and kinetically. A Mettler RC1 calorimeter was operated under isothermal and adiabatic conditions with various stirrer speeds and HC1 was slowly added to a mixture of NaOH and 2,2-dimethoxypropane. Measured hydrolysis yields compared quite well with the extended engulfment model, although temperature segregation was of minor importance. It was also unimportant in other reaction systems (simultaneous neutralisation and ester hydrolysis; diazo coupling) employed earlier to study micromixing. Suggestions for further work are made.
引用
收藏
页码:641 / 649
页数:9
相关论文
共 13 条
  • [1] ORTHO-ESTER HYDROLYSIS - DIRECT EVIDENCE FOR A 3-STAGE REACTION-MECHANISM
    AHMAD, M
    BERGSTROM, RG
    CASHEN, MJ
    CHIANG, Y
    KRESGE, AJ
    MCCLELLAND, RA
    POWELL, MF
    [J]. JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1979, 101 (10) : 2669 - 2677
  • [2] A FLUID MECHANICAL APPROACH TO TURBULENT MIXING AND CHEMICAL REACTION PART I INADEQUACIES OF AVAILABLE METHODS
    Baldyga, J.
    Bourne, J. R.
    [J]. CHEMICAL ENGINEERING COMMUNICATIONS, 1984, 28 (4-6) : 231 - 241
  • [3] SIMPLIFICATION OF MICROMIXING CALCULATIONS .1. DERIVATION AND APPLICATION OF NEW MODEL
    BALDYGA, J
    BOURNE, JR
    [J]. CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1989, 42 (02): : 83 - 92
  • [4] COMPARISON OF THE ENGULFMENT AND THE INTERACTION-BY-EXCHANGE-WITH-THE-MEAN MICROMIXING MODELS
    BALDYGA, J
    BOURNE, JR
    [J]. CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1990, 45 (01): : 25 - 31
  • [5] Baldyga J., 1995, CHEM ENG J, V58, P183, DOI DOI 10.1016/0923-0467(95)02982-6
  • [6] BERGSTROM RG, 1980, CHEM FUNCTIONAL 2 S
  • [7] INVESTIGATION OF MICROMIXING IN STIRRED-TANK REACTORS USING PARALLEL REACTIONS
    BOURNE, JR
    YU, SY
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1994, 33 (01) : 41 - 55
  • [8] KINETICS OF THE DIAZO COUPLING BETWEEN 1-NAPHTHOL AND DIAZOTIZED SULFANILIC ACID
    BOURNE, JR
    KUT, OM
    LENZNER, J
    MAIRE, H
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (09) : 1761 - 1765
  • [9] HEAT-TRANSFER AND POWER MEASUREMENTS IN STIRRED TANKS USING HEAT-FLOW CALORIMETRY
    BOURNE, JR
    BUERLI, M
    REGENASS, W
    [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (02) : 347 - 354
  • [10] KINETICS OF HYDROLYSIS OF ACETALDEHYDE ETHYL HEMIACETAL IN AQUEOUS-SOLUTION
    CHIANG, Y
    KRESGE, AJ
    [J]. JOURNAL OF ORGANIC CHEMISTRY, 1985, 50 (25) : 5038 - 5040