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I at first went with static tension at inlet-static tension at outlet. (assuming the the dynamic tension will Pretty much be exact same as my move is thru regular cross section pipe)

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About temperature fall by means of an orifice, we frequently presume the force fall is isenthalpic. To get fluid Homes for authentic fluids you should use a fluids Homes database. Notice that a temperature drop won't be predicted for a perfect gasoline or a superbly incompressible fluid.  

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In fluent there are many options for tension, static dynamic, overall. May possibly any one suggest which one to think about if I'm on the lookout for force drop for move in the pipe.

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