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Thread: Common mistakes in process design/simulation

  1. #13
    Thanks Dear uetian98 for fairly good resource
    Best regards
    Qalander

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  3. There is also common mistakes in oil characterisation. Check out which approach is the most suitable to choose when characterising the crude in simulation.

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  5. Thanks a lot! Do someone use ansys cfx actually to simulate separation process in a gunbarrel?

  6. #16
    A commun mistake in crude heater simulation is not to consider the small thermal -----ing of large molecules, producing gas and other species.

    Jotar

  7. very nice & useful data.. thank you!

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  9. #18
    wonderful
    Thanks----------

  10. Exclamation Problem-lng terminal

    In my Simulation model whenever i i run the case it run smoothly but when i try to generate report from Report manager
    i just stuck & Hang

    Please tell me the reason...why it is happening also is there any other method to generate report for the given streams & specified properties only

    1- Also what do u think about Lee-kesler Method for density calculation for LNG
    is it right?

  11. #20
    Dear all Im a new member here ang need to update myself with the simulation stuff.
    Really appreciate the inputs given here.

  12. #21
    Nice topic for sharing experience

  13. Welcome! Enjoy this forum and just shoot up your curious here to get the some promising answers.

  14. Dear friends,
    Thanks for sharing. These tips are very useful.

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  16. In case of smulating thermosyphon reboiler be carefeul as hysys inside column flowsheet indicates very high temperature at the last column tray even so that the reboiler return temperature is lower than the inlet .This inlet temperature to reboiler is misleading .Solution is to take the stream out o fthe flow sheet and install reboiler there, on coming out it will start showing right temperatures

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