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Flow behaviour of thickeners.

Flow between infinite parallel y planes.

Flow between modules of thiee-up, one-down Helikon cascade.

Flow between parallel plates

Flow between parallel plates with a uniform injection velocities through the plates.

Flow between two parallel plates in Example 3.8-1.

Flow between vertical parallel plates in Example 3.8-2.

Flow birefringence An vs. shear rate q for solutions of a polystyrene fraction of high molecular weight . Concentrations in g 100 cm3 are given near the curves

Flow birefringence in the isotropic phase of MBBA. Crosses represent the birefringence

Flow birefringence pattern .

Flow birefringence patterns T s-l.

Flow birefringence vs. shear rate for the solution decribed in the caption

Flow boiling data of Agostini et al. for R-236fa in a silicon multi-micro-channel test section at a mass velocity of 810.7 kg m s, a nominal pressure of 2.73 bar and saturation temperature of 25 C. The silicon test section without its cover plate is shown in the inset photograph.

Flow boiling heat transfer in a 25.4 mm i.d. tube at different heat fluxes

Flow boiling in midochannels with rapid manifold

Flow boiling in parallel micro-channels. G 95 kg m s, q 160kW m. Reprinted from Hetsroni et al. with permission

Flow boundary layer around a cylindrical solid. S stagnation point, A detachment point of the boundary layer

Flow by-cell setup for anodic oxidation of pentachlorophenol.

Flow calorimeter designed by Picker, Jolicoeur and Desnoyers .

Flow calorimeter with a chemical reaction in the liquid.

Flow calorimeter with heat source outside the flow tube.

Flow calorimeter, with a chemical reaction occurring in the liquid A. B reactants, A B reaction product a Differential thennocouple

Flow calorimeter.

Flow calorimeter. A, inlet ports only two of four showril C, mixing chamber

Flow capacities of perforated-plate towers. G greatest reported, F flooded.



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