By Lixin Cheng; Dieter Mewes
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Additional resources for Advances in multiphase flow and heat transfer Vol. 2
Standard inlets such as T-  and Y- junctions [16,19] have been used. Ioannou et al.  and Ngan et al. [17,18] fitted their Y-inlets with plates to ensure that the fluids joined in a stratified manner and all the mixing occured downstream of the inlet due to flow turbulence. When the dispersion is not formed at the inlet then a certain development length is required. However, the work by Ioannou et al. , where conductivity probes were used at different locations along the pipe, demonstrated that the dispersion had similar characteristics in all locations studied and at the high flowrates needed to sustain dispersed flow the development length was very short .
Phase inversion mostly occurs when the dispersed phase holdup is increased in order to obtain higher interfacial areas. g. ). The experimental work in liquid-liquid dispersions revealed the existence of the ambivalent region over which either liquid phase can be the stable dispersed phase . The ambivalent region is usually presented as a plot of the holdup of either the organic or sometimes the dispersed phase at inversion against agitation speed. An example of the former representation is given in Fig.
78, pp. 1645-1654, 1956. S. S. Kutateladze, Fundamentals of heat transfer, New York: Academic Press, 1963. D. A. Labuntsov, “Heat transfer in film condensation of pure steam on vertical surfaces and horizontal tubes, Tefloenergetika, vol. 4, pp. 72-84, 1957. K. H. Leinhard, “Laminar film condensation on plane and axisymmetric bodies in non-uniform gravity, J. Heat Transfer, vol. 93, pp. 97103, 1971. J. Gerstmann and P. Griffith, “Laminar film condensation on underside of horizontal and inclined surfaces”, Int.
Advances in multiphase flow and heat transfer Vol. 2 by Lixin Cheng; Dieter Mewes