
Originally Posted by
juncruz
CPIG is for gas, so I don't know if that will relate to CPL which is liquid. What I do is regress data as follows:
1. Put in the component in the components Specifications box
2. Go to “Molecular Structure” and draw the molecule
3. Go to “Data” and “New”. Enter a name for the ID (example CPLM)
4. Select type: “Pure comp”
5. Property: CPL- (liquid heat mass capacity)
6. Component: point to the component
7. You can then enter a constant parameter, either pressure or temperature. Normally I put a constant pressure of 1 atm for CPL
8. Go to Data tab; Below “STD-DEV”, Choose “DATA” and enter the values for the temperature, and corresponding CP value (you can change the unit). Put many data (different temperatures). The more the better. I normally put 5 – 8 data.
9. Then I go back to “Components” “Molecular Structure”, choose the component then “Structure”, then “Calculate Bonds”
10. Then I click on “TDE NIST”. Choose the component, then click “Evaluate now”
11. The I go to “Regression”, “New”. On Data set, choose the ID that you made on the data, (example CPLM)
12. Go to “Parameters”, choose “Type” Parameter. Element “1”. On the “Name”, there are many options for CP. I normally use CPLIKC but it depends on the type of component. Then the component. You have to make 1 -7 elements.
13. Then run the estimation.
Sometimes you have to determine what regression set works. Aside from CPLIKC, there is CPLPO, CPLTDECS, CPLSTMLPO, CPLXP1, CPLXP2. Especially if you have many components and properties to regress, it can be very very tedious.
Good luck!
First of all I want to thank you very much for your interes. I did everything you said but I always got the same problems: Aspen continues ignoring my datas.
I post you some images of the input I put and the results I got, maybe they could be useful
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