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You said you ended up capable to operate with 50 m/s from scratch. From your UDF or Transient Table the utmost velocity is 15 m/s. Please verify your statements in this article.

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By way of a uncomplicated UDF I managed to obtain the velocity to raise with time but This is certainly in turn making a issue in static tension (gauge) as shown in the 2nd and third figures attached. 

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I'm functioning this transient simulation inside of a stand alone fluent component to do away with all other coupling difficulties for now. I am making certain that the move ailments are converging with each and every time stage (also attempted five hundred iterations for each time stage exactly where residuals went frequent for some time) And that i m checking lift and drag as physical values and they're converging with each stage increase in velocity (five, 10, fifteen ... 50). 

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I at first went with static strain at inlet-static tension at outlet. (assuming the the dynamic pressure will Virtually be same as my move is through constant cross portion pipe)

You concentrate on total pressure plot first and also u can plot static pressure and merge equally information by means of tech plot or in fluent far too then u simply decide the difference and in this manner In addition, you evaluate how the dynamic tension adjustments throughout the move.

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two) Suppose that if h2o inlet and outlet resource is a typical open up vessel what should be the value of it?

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In which rho Va^2/2 will be the dynamic stress, and Va is the standard velocity of fluid equivalent to 50 percent of the utmost velocity profile, r=0, for laminar circulation and horizontal pipe. L would be the size of pipe and D diameter, file may be the friction element, and rho the fluid density.

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I agree the velocity profile is transforming , but then is just not the average velocity usually same at each cross section.

While in the boundary ailments I set velocity inlet with 0 gouge supersonic pressure, and outflow outlet, am I forgetting one thing?

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