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Old   May 13, 2007, 06:43
Default Real gas modelling
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Billey
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Defined steam using R-W eqn of state,using total energy model,but showing high temperature values to the curresponding pressure values,Properties not matching with the sat steam tables.Solving with Rotating domain around impeller connected by frozen rotor interface with stationary inlet and stationary diffuser. what could be the problem? Does anybody have any idea?
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