Method for providing robustness to the solution of the cubic equation of state

• US 20050010629A1
• Filed: 07/08/2003
• Published: 01/13/2005
• Est. Priority Date: 07/08/2003
• Status: Active Grant

• Current Assignee: ABB Incorporated (ABB Limited)
• Original Assignee: ABB Incorporated (ABB Limited)
• Inventors: Hess, Todd M., Su, Yang, Shertukde, Prasad V.
• Granted Patent: US 7,349,819 B2
• Time in Patent Office: Days
• US Class Current: 708/446
• CPC Class Codes: G01N 25/02 by investigating changes of state or changes of phase; by investigating sintering investigating or analysing oils or hydrocarbon fluids by measuring cloud point or pour point G01N33/2811
• CPC Class Codes: G01N 7/00 Analysing materials by measuring the pressure or volume of a gas or vapour

Abstract

The cubic equations of state (CEOS) relate pressure, temperature and molar volume of a mixture. The deviation of the physical properties of a mixture from ideality is expressed by the compressibility factor. The compressibility factor is calculated from the CEOS. There is described a solution to the CEOS which provides a continuous solution for compressibility factors over the entire range of operating conditions. This solution avoids the non-unique roots, trivial roots and singularities that are present in the prior art solutions of the CEOS.

Claims

1. A method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region, said method comprising:

a) calculating a pure liquid compressibility factor when said compressibility factor is in said liquid region;

b) using the second virial coefficient of said CEOS to determine from said pure liquid compressibility factor a vapor compressibility factor extensible in said liquid region; and

c) accepting the higher of said pure liquid compressibility factor or said vapor compressibility factor extensible in said liquid region.

2. The method of claim 1 further comprising determining that said compressibility factor is in said liquid region.

3. The method of claim 1 wherein said mixture has a vapor region and said method further comprises determining that said compressibility factor is in said vapor region and accepting a pure vapor compressibility factor when said compressibility factor is in said vapor region.

11. The method of claim 1 wherein said method is executed in a computing device in an industrial plant, said industrial plant comprising an industrial process, an automation system connected to said process, said computing device associated either with said process or said automation system.

4. A method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a vapor-liquid equilibrium region, said method comprising:

a) determining that said compressibility factor is in said vapor-liquid equilibrium region;

b) calculating when said compressibility factor is in said vapor-liquid equilibrium region a pure liquid compressibility factor;

c) using the virial coefficients of said CEOS and said pure liquid compressibility factor calculated when said compressibility factor is in said vapor-liquid equilibrium region to determine a vapor compressibility factor in said vapor-liquid equilibrium region; and

d) accepting the higher of said pure liquid compressibility factor calculated when said compressibility factor is in said vapor-liquid equilibrium region or said vapor compressibility factor calculated in said vapor-liquid equilibrium region.

5. A method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a vapor-liquid equilibrium region, said method comprising:

a) calculating a pure liquid compressibility factor for said vapor-liquid equilibrium region;

b) using the virial coefficients of said CEOS and said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region to determine a vapor compressibility factor in said vapor-liquid equilibrium region; and

c) accepting the higher of said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region or said vapor compressibility factor calculated in said vapor-liquid equilibrium region.

12. The method of claim 5 wherein said method is executed in a computing device in an industrial plant, said industrial plant comprising an industrial process, an automation system connected to said process, said computing device associated either with said process or said automation system.

6. A method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region and a vapor-liquid equilibrium region, said method comprising:

determining that said compressibility factor is either in said liquid region or in said vapor-liquid equilibrium region;

said method when said compressibility factor is in said liquid region comprising;

calculating a pure liquid compressibility factor;

using the second virial coefficient of said CEOS to determine from said pure liquid compressibility factor a vapor compressibility factor extensible in said liquid region; and

accepting the higher of said pure liquid compressibility factor or said vapor compressibility factor extensible in said liquid region;

said method when said compressibility factor is in said liquid region comprising;

calculating a pure liquid compressibility factor;

using the virial coefficients of said CEOS and said pure liquid compressibility factor to determine a vapor compressibility factor in said vapor-liquid equilibrium region; and

accepting the higher of said pure liquid compressibility factor or said vapor compressibility factor calculated in said vapor-liquid equilibrium region.

7. A method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region and a vapor-liquid equilibrium region, said method comprising:

a) calculating a pure liquid compressibility factor when said compressibility factor is in said liquid region;

b) using the second virial coefficient of said CEOS to determine from said pure liquid compressibility factor a vapor compressibility factor extensible in said liquid region; and

c) accepting the higher of said pure liquid compressibility factor or said vapor compressibility factor extensible in said liquid region;

d) calculating a pure liquid compressibility factor for said vapor-liquid equilibrium region;

e) using the virial coefficients of said CEOS and said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region to determine a vapor compressibility factor in said vapor-liquid equilibrium region; and

f) accepting the higher of said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region or said vapor compressibility factor calculated in said vapor-liquid equilibrium region.

8. A method for calculating the liquid compressibility factor of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region, said method comprising:

a) calculating a pure liquid compressibility factor when said compressibility factor is in said liquid region;

b) determining that the rate of change of said pure liquid compressibility factor with temperature is or is not less than zero; and

c) accepting said pure liquid compressibility as said liquid compressibility factor when said pure liquid compressibility factor rate of change is not less than zero.

9. The method of claim 8 further comprising:

calculating said liquid compressibility factor as the ratio of the change with temperature of two of the virial coefficients of said CEOS when said pure liquid compressibility factor rate of change is less than zero.

10. The method of claim 8 further comprising:

determining that said compressibility factor is in said liquid region.

13. The method of claim 8 wherein said method is executed in a computing device in an industrial plant, said industrial plant comprising an industrial process, an automation system connected to said process, said computing device associated either with said process or said automation system.

14. A computer readable medium having instructions for causing a computer to execute a method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region, said instructions comprising:

a) calculating a pure liquid compressibility factor when said compressibility factor is in said liquid region;

b) using the second virial coefficient of said CEOS to determine from said pure liquid compressibility factor a vapor compressibility factor extensible in said liquid region; and

c) accepting the higher of said pure liquid compressibility factor or said vapor compressibility factor extensible in said liquid region.

15. A computer readable medium having instructions for causing a computer to execute a method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a vapor-liquid equilibrium region, said instructions comprising:

a) calculating a pure liquid compressibility factor for said vapor-liquid equilibrium region;

b) using the virial coefficients of said CEOS and said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region to determine a vapor compressibility factor in said vapor-liquid equilibrium region; and

c) accepting the higher of said pure liquid compressibility factor calculated for said vapor-liquid equilibrium region or said vapor compressibility factor calculated in said vapor-liquid equilibrium region.

16. A computer readable medium having instructions for causing a computer to execute a method for calculating the compressibility factors of a mixture using the cubic equation of state (CEOS), said mixture having a liquid region, said instructions comprising:

a) calculating a pure liquid compressibility factor when said compressibility factor is in said liquid region;

b) determining that the rate of change of said pure liquid compressibility factor with temperature is or is not less than zero; and

c) accepting said pure liquid compressibility as said liquid compressibility factor when said pure liquid compressibility factor rate of change is not less than zero.