Taylor vortex reactor

Taylor (1923) first observed the instability of fluid when the inner cylinder exceeds a critical speed between two coaxial cylinders in his established work. The laminar flow confined within the annulus region between two coaxial cylinders with the inner one differentially rotating with respect to the outer suffers centrifugal instability depending on the geometry and rotation rates. Taylor (1923) showed that an inviscid rotating flow to be 

According to Taylor (1923), the flow instability is observed when the Taylor number exceeds a critical value where Taylor number is defined by geometrical parameters and the speed of rotation  

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Taylor Vortex Reactor (TVR) Suspended Karpel et al., 1997 Sczechowski et al., 1995a. 

FIGURE 2.2. Taylor vortex reactor in operation (Reprinted from Chem. Eng. Sci.., 50(20), J.G. Sczechowski, C.A. Koval and R.D. Noble, A taylor vortex reactor for heterogeneous photocatalysis, pp. 3163-3173, Copyright 1995, with permission from Elsevier)... 

Kong B, Shanks JV, Vigil RD Enhanced algal growth rate in a Taylor vortex reactor, Biotechnol Bioeng 110(8) 2140-2149, 2013. 

Preparation of Monodisperse, Spherical Oxide Particles by Hydrolysis of Metal Alkoxide Using a Couette-Taylor Vortex Flow Reactor... 

Figure 12 Experimental set-up of Taylor vortex photocatalytic reactor (Dutta and Ray, 2004) (1) motor, (2) speed controller, (3) gear coupling, (4) UV lamp, (5) sample collection point, (6) lamp holder, (7) outer cylinder, (8) catalyst-coated inner cylinder.

As an alternative to a cascade of CSTR trains, a novel continuous reactor with a Couette-Taylor vortex flow (CTVF) has been proposed, which can realize any flow pattern between plug and perfectly mixed flows [361-366]. A continuous Couette-Taylor vortex flow reactor (CCTVFR) consists of two concentric cylinders with the inner cylinder rotating and with the outer cylinder at rest. Figure 29 shows a typical flow pattern caused by the rotation of the inner cylinder. 

Nomura et al. [360,364] first utilized a Couette-Taylor vortex flow reactor (CTVFR) for the continuous emulsion polymerization of St to clarify its char-... 

Couette-Taylor Continuous emulsion pol)mierization of styrene in a Couette-Taylor vortex flow reactor comprehensive kinetic study in dependence on reactor operation parameters 179... 

Dr Coney (1971) researched Taylor vortex flow with particular interest in rotary heat exchangers, which he later used in a rotary vapour compression cycle heat pump. Taylor-Couette flows are used in commercial intensified reactors now (see Chapter 5). 

The Taylor-Couette reactor (TCR), sometimes referred to as a vortex flow reactor, consists of two concentric cylinders, one of which rotates. Figure 5.23. 

Dutta, PK. and Ray, A.K. (2004). Experimental investigation of Taylor vortex photocatalytic reactor for water purification. Ghemical Engineering Science, Vol. 59, pp. 5249-5259. 

Reactor configurations involved in continuous emulsion polymerization include stirred tank reactors, tubular reactors, pulsed packed reactors, Couett-Taylor vortex flow reactors, and a variety of combinations of these reactors. Some important operational techniques developed for continuous emulsion polymerization are the prereactor concept, start-up strategy, split feed method, and so on. The fundamental principles behind the continuous emulsion polymerizations carried out in the basic stirred tank reactor and tubular reactor, which serve as the building blocks for the reaction systems of commercial importance, are the major focus of this chapter. 

Reactors which generate vortex flows (VFs) are common in both planktonic cellular and biofilm reactor applications due to the mixing provided by the VF. The generation of Taylor vortices in Couette cells has been studied by MRM to characterize the dynamics of hydrodynamic instabilities [56], The presence of the coherent flow structures renders the mass transfer coefficient approaches of limited utility, as in the biofilm capillary reactor, due to the inability to incorporate microscale details of the advection field into the mass transfer coefficient model. 

Giordano, R.L.C., Giordano, R.C. and Cooney, C.L. (2000). Performance of a continuous Taylor-Couette-Poiseuille vortex flow enzymic reactor with suspended particles. Process Biochemistry, Vol. 35, No. 10, pp. 1093-1101. 

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