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Thread: Request: T-P Relationship of LPG

  1. #1

    Request: T-P Relationship of LPG

    Can someone create me a T-P relationship for 30% Butane & 70% Propane Mixture using Hysys v7.1, the same with 35~50%Butane and 65~50% Propane. This is really urgent, please help me. Since i dont have client for this apps. Just send me the tabulated data, or a graph with this e-mail

    pakskyo@yahoo.com

    Thank you in advance to those who can help me.

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  3. Re: Request: T-P Relationship of LPG

    Here you go. Done with UniSim using Peng-Robinson EoS rather than HYSYS, but results should be the same.

    [link Point to another website Only the registered members can access]


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  5. #3

    Re: Request: T-P Relationship of LPG

    @Gtaa

    can i ask for a data if there is ? i want to know the pressure at certain temperature, like 30degC, the bar would be___.

    And hmm how should i say this, can you email me the steps in creating the graph using that software you just created. ((IM USING THIS IN OUR THESIS STUDY for undergraduate ME.)

    Thank you

  6. Re: Request: T-P Relationship of LPG

    It will have to wait until Tuesday when I get back to the office. Can't you just read it off the graph? Draw a line from 30degC and read off the pressure at either the bubble point or dew point lines?

    UniSim and HYSYS are essentially the same thing. You use the 'envelope' utility and it draws it for you. However, to create the bubble point curve manually you set the vapor fraction to 0 and change the temperature in increments. The software will calculate the corresponding pressure. Just plot these. You create the dew point line by setting the vapor fraction to 1 and doing the same thing.

  7. Re: Request: T-P Relationship of LPG

    It will have to wait until Tuesday when I get back to the office. Can't you just read it off the graph? Draw a line from 30degC and read off the pressure at either the bubble point or dew point lines?

    UniSim and HYSYS are essentially the same thing. You use the 'envelope' utility and it draws it for you. However, to create the bubble point curve manually you set the vapor fraction to 0 and change the temperature in increments. The software will calculate the corresponding pressure. Just plot these. You create the dew point line by setting the vapor fraction to 1 and doing the same thing.

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  9. #6

    Re: Request: T-P Relationship of LPG

    hmmmm. Ill just wait for your reply. To let you know, i dont have a clue with hysys and unisim so that is why im asking for help. Dont have a ******* link >_<

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