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Microreactor capillary slug-flow

Kashid, M. N., Gerlach, 1., Goetz, S., Franzke, J., Acker, J., Platte, F., et al. (2005). Internal circulation within the liquid slugs of a liquid-liquid slug-flow capillary microreactor. Industrial... [Pg.7]

Ghaini, A., Kashid, M., Agar, D. (2010). Effective interfacial area for mass transfer in the liquid-liquid slug flow capillary microreactors. Chemical Engineering and Processing Process Intensification, 49, 358—366. [Pg.45]

Kashid, M. N., Agar, D. W. (2007). Hydrodynamics of liquid-liquid slug flow capillary microreactor flow regimes, slug size and pressure drop. Chemical Engineering Journal, 131, 1-13. [Pg.46]

Kashid, M.N. (2007) Experimental and Modelling Studies on Liquid-Liquid Slug Flow Capillary Microreactors, University of Dortmund, Dortmund. [Pg.328]

Power input, a decisive parameter for benchmarking technical reactors, has been investigated using the experimental pressure drop and compared with conventional contactor as shown in Table 15.5. The comparison reveals that the liquid-liquid slug flow microreactor requires much less power than the alternatives to provide large interfacial area - as high as a = 5000 m m in a 0.5 mm capillary microreactor, which is way above the values in a mechanically agitated reactor (a 500 m m ). [Pg.421]

M. N. Kashid, Experimental and modelling studies on liquid-liquid slug flow capillary microreactors, PhD Thesis, Technical University of Dortmimd, 2007. [Pg.438]

Sulfonations are a further important type of electrophilic substitution reaction. However, only very few examples can be found in the literature describing the use of microstructured reactors for the strongly exothermic liquid-phase sulfonation of aromatics (sulfonation of toluene wdth gaseous SO3 was described by Jaehnisch et al. [34]). Burns and Ramshaw [25, 35] claimed that their concept of performing liquid/liquid nitration reactions in a slug-flow capillary-microreactor can be also... [Pg.584]

Figure 0.4 Observed flow regimes in the capillary microreactor (Y-junction ID = 1 mm, capillary ID = 1 mm), (a) Slug flow, (b) drop flow, and (c) deformed interface flow. (Adapted from Kashid, M.N. and Agar, D.W., Chem. Eng. J. 131, 1, 2007.)... Figure 0.4 Observed flow regimes in the capillary microreactor (Y-junction ID = 1 mm, capillary ID = 1 mm), (a) Slug flow, (b) drop flow, and (c) deformed interface flow. (Adapted from Kashid, M.N. and Agar, D.W., Chem. Eng. J. 131, 1, 2007.)...

See other pages where Microreactor capillary slug-flow is mentioned: [Pg.576]    [Pg.207]    [Pg.147]    [Pg.207]    [Pg.307]    [Pg.54]    [Pg.341]    [Pg.79]    [Pg.9]    [Pg.225]   
See also in sourсe #XX -- [ Pg.61 , Pg.75 , Pg.102 , Pg.123 , Pg.148 , Pg.153 ]




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