Hi, I'm looking to design a convergent-divergent nozzle in an effort to acquire the bottom strain drop using the program Ansys Fluent in second mode. In just about every simulation I do I improve a geometry price as a way to examine how that detail can affect pressure drops; then I consider the difference between inlet and outlet complete pressure to compute my stress drops, but I observe that inlet absolute pressure variations in every single simulation, why does this occur?
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I to begin with went with static stress at inlet-static pressure at outlet. (assuming the the dynamic force will Just about be very same as my flow is through regular cross portion pipe)
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You have to be contemplating full tension. And dynamic tension will never stay constant as being the flow will move with the pipe. The velocity profile is switching the dynamic strain will alter. At outlet we specify static tension.
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In which rho Va^two/two will be the dynamic strain, and Va is the average velocity of fluid equivalent to 50 percent of the maximum velocity profile, r=0, for laminar move and horizontal pipe. L could be the size of pipe and D diameter, file would be the friction variable, and rho the fluid density.
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