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Gas-liquid microreactors

H., WiLLE, C., Guber, a.. Direct fluorina-tion of tduene using elemental fluorine in gas/liquid microreactors, J. Fluorine Chem. 105, 1 (2000) 117-128. [Pg.114]

Hessel, V., Ehreeld, W., Golbig, K., Haveekamp, V., Lowe, H., Storz, M., WiLLE, C., Gubee, a., Jahnisch, K., Baerns, M., Gas/liquid microreactors for direct Jluorination of aromatic compounds using elemental fluorine, in Ehreeld, W. (Ed.), Microreaction Technology ... [Pg.651]

Hessel, V, Ehreeld, W., Heeweck, T., Haveekamp, V, Lowe, H., Schiewe, J., WiLLE, G., Keen, T, Lutz, N., Gas/liquid microreactors hydrodynamics and mass transfer, in Proceedings of the 4th International Conference on Microreaction Technology, IMRET 4, 5-9 March 2000, pp. 174-186, AIGliE Topical Conf. Proc., Atlanta, GA (2000). [Pg.651]

Characterization of a gas/liquid microreactor, the micro bubble column Determination of specific interfacial area, in Matlosz, M., Ehreeld, W., Baselt,... [Pg.651]

Chambers RD, Fox MA, Sandford G (2005) Elemental fluorine - Part 18. Selective Direct Fluorination of 1,3-Ketoesters and 1,3-Diketones using Gas/ Liquid Microreactor Technology. Lab Chip 5 1132-1139 Cheng RP, Gellman SH, DeGrado WF (2001) Beta-Peptides From Structure to Function. Chem Rev 101 3219-3232... [Pg.16]

Jahnisch K, Baerns M, Hessel V, Ehrfeld W, Haverkamp V, Lowe H, Wille C, Guber A (2000) Direct Fluorination of Toluene Using Elemental Fluorine in Gas/Liquid Microreactors. J Fluor Chem 105 117-128 Jahnisch K, Hessel V, Lowe H, Baerns M (2004) Chemistry in Microstructured Reactors. Angew Chem Int Ed 43 406 -46 Jensen KF (2001) Microreaction Engineering - is Small Better Chem Eng Sci 56 293-303... [Pg.18]

De Mas N, Gunther A, Kraus T, Schmidt MA, Jensen KF (2005) Scaled-out multilayer gas-liquid microreactor with integrated velocimetry sensors. Ind Eng Chem Res 44 8997-9013... [Pg.73]

Haverkamp, V., Emig, G., Hessel, V., Liauw, M.A. and Lowe, H. (2001) Characterization of a gas/liquid microreactor, the micro bubble column determination of specific interfadal area, in Microreaction Technology- IMRET 5 Proceedings of the 5th International Conference on Microreaction Technology (eds M. Matlosz, W. Ehrfeld and J.P. Baselt), Springer-Verlag, Berlin, pp. 202-214. [Pg.181]

Gas-liquid microreactors hydrodynamics and mass transfer, in Proceedings of the 4th International Conference on Microreaction Technology, IMRET 4, Atlanta, USA, pp. 174-186. [Pg.182]

Falling-film gas/liquid microreactors, as shown in Figure 8.2, are also useful for direct fluorination of organic compounds, such as toluene with F2 (Scheme 8.2). In this reactor a liquid reactant falls down through the channels and the gas also falls down on to the surface of the liquid flow to attain a high gas/liquid surface-to-volume ratio to accelerate the gas/liquid reaction. [Pg.139]

V. Hessel, W. Ehrfeld, T. Herweck, V. Haverkamp, H. Lowe, J. Schiewe, C. Wille, T. Kern, N. Lutz, Gas/Liquid Microreactors Hydrodynamics and Mass Transfer, in W. Ehrfeld, U. Eul, R.S. Wegeng (Eds.), Proceedings of the 4th International Conference on Microreaction Technology (IMRET 4), AIChE, Atlanta, 2000, p. 174. [Pg.112]

First, the overall mass transfer coefRcient k a of the microreactor was estimated to be 3-8 s [43]. For intensified gas liquid contactors, kj a can reach 3 s while bubble columns and agitated tanks do not exceed 0.2 s Reducing the flow rate and, accordingly, the liquid film thickness is a means of further increasing kj a, which is limited, however, by liquid dry-out at very thin films. Despite such large mass transfer coefficients, gas-liquid microreactors such as the falling film device may still operate between mass transfer and kinetic control regimes, as fundamental simulation studies on the carbon dioxide absorption have demonstrated [44]. Distinct concentration profiles in the liquid, and even gas, phase are predicted. [Pg.117]

Jahnisch, K., et al.. Direct flnorination of tolnene using elemental fluorine in gas/liquid microreactors. Journal of Fluorine Chemistry, 2000, 105 117-128. [Pg.1202]

Jahnisch K, Baems M, Hessel V et al (2000) Direct fluorination of toluene using elemental fluorine in gas/liquid microreactors. J Fluor Chem 105 117-123... [Pg.40]

Waelchli, S. Rudolf von Rohr, P. 2006. Two-phase flow characteristics in gas—liquid microreactors. International journal of multiphase flow, 32, 791-806. [Pg.49]

Waelchli S and Rohr PRV (2006), Two-phase flow characteristics in gas-liquid microreactors , Int J Multiphas Flow, 32,791-806. [Pg.232]

R.D. Chambers, M.A. Fox, G. Sandford, Elemental fluorine — Part 18. Selective direct fluorination of 1,3-ketoesters and 1,3-diketones using gas/liquid microreactor technology. Lab on a Chip, 2005, 5, 1132-1139. [Pg.38]

S. Waelchli, P.R. von Rohr, Two-phase flow characteristics for gas-liquid microreactors, Int. J. Multiphase Flow, 2006, 32, 791-806. [Pg.243]

I, 3-diketones using gas/liquid microreactor technology, Lab Chip 2005, 5, 1132-1139. [Pg.654]


See other pages where Gas-liquid microreactors is mentioned: [Pg.114]    [Pg.62]    [Pg.139]    [Pg.147]    [Pg.178]    [Pg.246]    [Pg.404]    [Pg.62]    [Pg.38]    [Pg.654]   
See also in sourсe #XX -- [ Pg.283 ]




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