![]() Use Pipesim TM or PVTSim or any other commercial simulator to check the results from your program, for SRK and PR equations of state.(Note: The critical volume for each component can be calculated based on the given information, and they are different for SRK and PR). ![]() Compare the fluid properties calculated based on the results between SRK and PR. Calculate the fluid properties (density, viscosity and surface tension) of both liquid and gas phases at 1000 psia, and 90 ˚F.Run your program at separator conditions and compare the results between SRK and PR. The separator pressure and temperature are 1000 psia and 90 ˚F, respectively. Write a computer program that performs VLE calculations based on SRK and PR equation of state to obtain the K values of the components, and the compositions of the gas and the liquid phases, simultaneously.A hydrocarbon mixture entering a separator has the following feed composition. Starting with Equation C3, show the derivation of Equation C4.ģ. Please prove that the expression of “a” and “b” for van der Waals EOS in Table C1 of the composition model lectures are correct.Ģ.
0 Comments
Leave a Reply. |
AuthorWrite something about yourself. No need to be fancy, just an overview. ArchivesCategories |