Performance of five equations of state for the prediction of VLE and densities of natural gas mixtures in the dense phase region

Chemical Engineering Communications

Volumn 189, Issue 4, 2002, Pages 151-172

  Botros, Kamal K ^a  

^a NOVA CHEMICALS CORPORATION   (Canada)

Author keywords

Dense phase; Density; Equation of states; Natural gas; VLE

Indexed keywords

DENSITY OF GASES; NATURAL GAS; PHASE EQUILIBRIA; PRESSURE EFFECTS; THERMAL EFFECTS;

GAS MIXTURES;

CHEMICAL ENGINEERING;

EQUATION OF STATE;

EID: 0142057213     PISSN: 00986445     EISSN: None     Source Type: Journal    
DOI: 10.1080/00986440211837     Document Type: Article

References (15)

1. Crawford, J. R., "The Genesis of the Alliance Pipeline Project", J. of Canadian Petroleum Technology, 36(1), 22-23, January, 1997.
2. Mazurek, D. M. and Anderson, P. S., "Application of Ultra-High Pressure Dense Phase Pipelines to Large Diameter Transmission Systems", presented at NOVA Gas International Seminars, Kuala Lumpur, Malaysia, December 12 13, 1994.
3. King, G. (1991). "Ultra-high pressure Arctic natural gas pipelines", Proceedings of the Canadian Petroleum Association, Pipeline Conference, Calgary, Alberta, Canada, pp. 14-16.
4. Penick, D. P., Thrasher, W. B. and Gibbons, R. (1985). "Operating Gas Pipelines at High Pressures", Adv In Offshore Oil & Gas Pipeline Technology Publ. By Gulf Publ. Co., Houston, TX, USA, pp. 215-225.
5. Price, J. C. (1995). "Applying the Latest Technology to Optimize Production and Cost in the Construction of Pipelines using X80 and X100 Steels", Pipeline Technology, Elsevier Science B.V., II, 287 298.
6. Peng, D. Y. and Robinson, D. B. (1976). "A New Two-Constant Equation of State", Ind. Eng. Chem. Fundam., 15(1), 59-64.
7. Soave, G. (1979). "Equilibrium Constants from a Modified Redlich-Kwong Equation of State", Chemical Engineering Science, 27, 1197-1203.
8. ASPEN PLUS Release 9.2-1. PC Version. Aspen Technology, Inc., Ten Canal Park, Cambridge, MA. Copyright 1981 - 1996.
9. Starling, K. E. (1971). "Thermo Data Refined for LPG", Hydrocarbon Processing, 3, 101.
10. Ellington, R. T., Eakin, B. E., Parent, J. D., Gami, D. C. and Bloomer, O. T. (1959). Thermodynamic and Transport Properties of Gases, Liquids, and Solids, ASME Heat Transfer Division, McGraw Hill, New York, p. 159.
11. Starling, K. E. and Savidge, J. L. (1992). "Compressibility Factors for Natural Gas and Other Related Hydrocarbon Gases", American Gas Association, Transmission Measurement Committee Report No. 8.
12. Jaeschke, M. et al. (1988). "High Accuracy Compressibility Factor Calculation for Natural Gases and Similar Mixtures by Use of a Truncated Virial Equation", Groupe European de Recherches Gaziers (GERG), Technical Memorandum TM2.
13. Haynes, W. M., McCarty, R. D. and Eaton, B. E. (1985). "Isochoric (p, Vm, x, T) Measurements on (Methane + Ethane) from 100 to 320 K at pressures up to 35 MPA", J. Chem. Thermodynamics, 17, 209-232.
14. Magee, J. W., Haynes and Hiza, M. J. (1997). "Isochoric (p, ρ, T) Measurements for Five Natural Gas Mixtures from T = (225 to 350) K at Pressures to 35 MPA", J. Chem. Thermodynamics, 29, 1439-1454.
15. Hwang, C.-A., Simon, P. P., Hou, H., Hall, K. R., Holste, J. C. and Marsh, K. N. (1997). "Burnett and Pycnometric (p, Vm, T) Measurements for Natural Gas Mixtures", J. Chem. Thermodynamics, 29, 1455-1472.