Direct fluorination of toluene using elemental fluorine in gas/liquid microreactors

被引:282
作者
Jähnisch, K
Baerns, M
Hessel, V
Ehrfeld, W
Haverkamp, V
Löwe, H
Wille, C
Guber, A
机构
[1] Inst Angew Chem Berlin Adlershof EV, D-12489 Berlin, Germany
[2] Inst Mikrotech Mainz GMBH, D-55129 Mainz, Germany
[3] Forschungszentrum Karlsruhe, Inst Mikrostrukturtech, D-76021 Karlsruhe, Germany
关键词
fluorination; toluene; elemental fluorine; falling film microreactor; micro bubble column;
D O I
10.1016/S0022-1139(00)00300-6
中图分类号
O61 [无机化学];
学科分类号
070301 ; 081704 ;
摘要
Direct fluorination of toluene, pure or dissolved in either acetonitrile or methanol, using elemental fluorine was investigated in gas/liquid microreactors, namely a falling film microreactor and a micro bubble column. The experiments included measurements at high substrate concentrations and at high fluorine contents diluted in a nitrogen carrier gas, e.g. up to 50 vol.% fluorine. Results obtained were compared to the performance of a laboratory bubble column which served as a technological benchmark. Due to the formation of liquid layers of only a few tens of micrometers thickness, the microreactors provide very large interfacial areas, e.g. up to 40,000 m(2)/m(3). These values exceed by far those of the laboratory bubble column as well as all other devices applied in practice. The potential for enhancing mass and heat transfer was verified by several experiments resulting in an increase in conversion and selectivity for the microreactors compared to the laboratory benchmark. For the falling film microreactor, yields of up to 28% of monofluorinated ortho and para products for a degree of toluene conversion of 76% were obtained. These values are of the same order as described for the industrially applied Schiemann process. Space-time yields of the microreactors, when referred to the reaction channel volume, were orders of magnitude higher than those of the laboratory bubble column. Taking into account the construction material needed, the corresponding figures of merit, for an idealized geometry as well as the existing total reactor geometry, still indicate technological and economic benefits. A variation of operating conditions for the direct fluorination revealed that conversion can be increased in the microreactors by using higher fluorine-to-toluene ratios and reaction temperatures. The choice of solvent is also essential, with acetonitrile yielding much better results than methanol. (C) 2000 Elsevier Science S.A. All rights reserved.
引用
收藏
页码:117 / 128
页数:12
相关论文
共 22 条
  • [1] On aromatic fluoric compounds, I A new method for its representation
    Balz, G
    Schiemann, G
    [J]. BERICHTE DER DEUTSCHEN CHEMISCHEN GESELLSCHAFT, 1927, 60 : 1186 - 1190
  • [2] SUBSTRATE SELECTIVITY AND ORIENTATION IN AROMATIC-SUBSTITUTION BY MOLECULAR FLUORINE
    CACACE, F
    GIACOMELLO, P
    WOLF, AP
    [J]. JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1980, 102 (10) : 3511 - 3515
  • [3] SUBSTRATE SELECTIVITY AND ORIENTATION IN AROMATIC-SUBSTITUTION BY MOLECULAR FLUORINE
    CACACE, F
    WOLF, AP
    [J]. JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1978, 100 (11) : 3639 - 3641
  • [4] Elemental fluorine .1. Synthesis of fluoroaromatic compounds
    Chambers, RD
    Skinner, CJ
    Hutchinson, J
    Thomson, J
    [J]. JOURNAL OF THE CHEMICAL SOCIETY-PERKIN TRANSACTIONS 1, 1996, (07): : 605 - 609
  • [5] Recent studies at Durham on direct fluorination
    Chambers, RD
    Hutchinson, J
    Sandford, G
    [J]. JOURNAL OF FLUORINE CHEMISTRY, 1999, 100 (1-2) : 63 - 73
  • [6] DECKWER WD, 1984, REAKTIONSTECHNIK BLA
  • [7] Ehrfeld W., 1999, MICROREACTORS ULLMAN
  • [8] DIRECT LIQUID-PHASE FLUORINATION OF AROMATIC COMPOUNDS
    GRAKAUSK.V
    [J]. JOURNAL OF ORGANIC CHEMISTRY, 1970, 35 (03) : 723 - &
  • [9] CHARACTERIZATION OF A 2-PHASE IMPINGING JET ABSORBER .2. ABSORPTION WITH CHEMICAL-REACTION OF CO2 IN NAOH SOLUTIONS
    HERSKOWITS, D
    HERSKOWITS, V
    STEPHAN, K
    TAMIR, A
    [J]. CHEMICAL ENGINEERING SCIENCE, 1990, 45 (05) : 1281 - 1287
  • [10] Hessel V, 2000, MICROREACTION TECHNOLOGY: INDUSTRIAL PROSPECTS, P526