By H. Oh
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Extra resources for Advanced Fluid Dynamics
Rodi, W. “Direct numerical simulation, large eddy simulation and unsteady Reynolds-averaged Navier-Stokes simulations of periodic unsteady flow in a low-pressure turbine cascade: a comparison. Proc. IMechI, Part A: Journal of Power and Energy, 2003; 217(4), pp. 403-411. L. “Characteristic based schemes for the Euler equations”, Annual. Rev. Fluid. Mech. 1986. 18. 337-365. L. “Linear bicharacteristic schemes without dissipation”, SISC, 19, 1998, pp. 1405-1427. W. and Webb. Comput. W. ” Journal of Computational Physics, 89, pp.
The density and pressure field satisfy the usual isentropic relation and the steady tangential momentum equation: p const ; p v 2 r r (3) The vortex is specified in the centre of an open square Cartesian domain, three sides of which are open boundaries and the forth one corresponds to an incident acoustic wave that is monochromatic with frequency f. and normal to the boundary. The incident wave boundary condition is imposed at distance R=10L from the vortex centre which is offset from the centre of the square computational box domain of linear size 40L.
The riser reactors consist of a tubular column in which both solid and gas flow upwards. The first fluidized bed gas generator was developed in Germany by Fritz Winkler in the 1920s. Later in the 1930s, the american petroleum industry started developing the fluidized bed technology for oil feedstock catalytic cracking, becoming the primary technology for such applications (Tavoulareas 1991). Inside the riser reactor, solid particles have a wide range of residence time, which is a disadvantage that reduces the overall conversion and the selectivity of the chemical reactions.
Advanced Fluid Dynamics by H. Oh