Open Access
Issue
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 74, 2019
Article Number 53
Number of page(s) 9
DOI https://doi.org/10.2516/ogst/2019027
Published online 28 May 2019
  • Ahmed T. (2016) Equations of state and PVT analysis: Applications for improved reservoir modeling, 2nd ed., Gulf Professional Publishing – Elsevier Inc., Cambridge, USA. [Google Scholar]
  • Atilhan M., Ejaz S., Zhou J., Cristancho D., Mantilla I., Holste J., Hall K. (2010) Characterization of deepwater natural gas samples. Part 1: 78% methane mixture with heavy components, J. Chem. Eng. Data 55, 4907–4911. [Google Scholar]
  • Ávila S., Blanco S., Velasco I., Rauzy E., Otín S. (2002) Thermodynamic properties of synthetic natural gases. 1. Dew-point curves of synthetic natural gases and their mixtures with water and methanol. Measurement and correlation, Ind. Eng. Chem. Res. 41, 3714–3721. [Google Scholar]
  • Ávila S., Benito A., Berro C., Blanco S., Otín S., Velasco I. (2006) Dew-point curves of natural gas. Measurement and modeling, Ind. Eng. Chem. Res. 45, 5179–5184. [Google Scholar]
  • Bahadori A. (2014) Natural gas processing: Technology and engineering design, Gulf Professional Publishing – Elsevier Inc., Waltham, USA. [Google Scholar]
  • Bell I., Jäger A. (2017) Calculation of critical points from Helmholtz-energy-explicit mixture models, Fluid Phase Equilib. 433, 159–173. [Google Scholar]
  • Campos A., da Silva N., Pereira M., Vasconcelos M. (2017) A review of Brazilian natural gas industry: Challenges and strategies, Renew. Sust. Energ. Rev. 75, 1207–1216. [CrossRef] [Google Scholar]
  • Demirel N., Demirel T., Deveci M., Vardar G. (2017) Location selection for underground natural gas storage using Choquet integral, J. Nat. Gas Sci. Eng. 45, 368–379. [Google Scholar]
  • Faramawy S., Zaki T., Sakr A. (2016) Natural gas origin, composition, and processing: A review, J. Nat. Gas Sci. Eng. 34, 34–54. [Google Scholar]
  • Farzaneh-Gord M., Niazmand A., Deymi-Dashtebayaz M., Rahbari H. (2015) Effects of natural gas compositions on CNG (compressed natural gas) reciprocating compressors performance, Energy 90, 1, 1152–1162. [CrossRef] [Google Scholar]
  • Foo D., Chemmangattuvalappil N., Ng D., Elyas R., Chen C., Elms R., Lee H., Chien I., Chong S., Chong C. (2017) Chemical engineering process simulation, 1st ed., Elsevier, Amsterdam, Netherlands. [Google Scholar]
  • Gas Processors Suppliers Association (1998) Engineering data book, 11th ed., GPSA, Tulsa, Okla. [Google Scholar]
  • Guerrero-Zárate D., Estrada-Baltazar A., Iglesias-Silva A. (2017) Calculation of critical points for natural gas mixtures with the GERG-2008 equation of state, Fluid Phase Equilib. 437, 69–82. [Google Scholar]
  • Heidemann R., Khalil M. (1980) The calculation of critical points, AlChE J. 26, 2, 769–779. [CrossRef] [Google Scholar]
  • Huang Q., Guo T. (1995) Prediction of the critical points of natural gas mixtures by rigorous and semi-empirical methods, J. Pet. Sci. Eng. 13, 3–4, 233–245. [Google Scholar]
  • International Organization for Standardization (2000) Natural gas – Determination of composition with defined uncertainty by gas chromatography – Part 4: Determination of nitrogen, carbon dioxide and C1 to C5 and C6+ hydrocarbons for a laboratory and on-line measuring system using two columns (ISO 6974-4:2000). [Google Scholar]
  • Jaeschke M., Humpherys A. (1991) The GERG databank of high accuracy compressibility factor measurements, Fortschr.-Ber. VDI Reihe 6, 251, 58. [Google Scholar]
  • Jiang J., Prausnitz J. (2000) Critical temperatures and pressures for hydrocarbon mixtures from an equation of state with renormalization-group theory corrections, Fluid Phase Equilib. 169, 127–147. [Google Scholar]
  • Jin C., Lim Y. (2018) Economic evaluation of NGL recovery process schemes for lean feed compositions, Chem. Eng. Res. Des. 129, 297–305. [Google Scholar]
  • Justo-García D., García-Sánchez F., Águila-Hernández J., Eustaquio-Rincón R. (2008) Application of the simulated annealing technique to the calculation of critical points of multicomponent mixtures with cubic equations of state, Fluid Phase Equilib. 264, 164–173. [Google Scholar]
  • Kunz O., Wagner W. (2012) The GERG-2008 wide-range equation of state for natural gases and other mixtures: An expansion of GERG-2004, J. Chem. Eng. Data 57, 3032–3091. [Google Scholar]
  • Louli V., Pappa G., Boukouvalas C., Skouras S., Solbraa E., Christensen K., Voutsas E. (2012) Measurement and prediction of dew point curves of natural gas mixtures, Fluid Phase Equilib. 334, 2012, 1–9. [Google Scholar]
  • Marquardt D. (1963) An algorithm for least-squares estimation of nonlinear parameters, J. Soc. Ind. Appl. Math. 11, 2, 431–441. [CrossRef] [MathSciNet] [Google Scholar]
  • MathWorks (2018) Optimization toolbox™ user’s guide. Version 8.2 (R2018b), The MathWorks Inc, Natick, USA. [Google Scholar]
  • Mazyan W., Ahmadi A., Ahmed H., Hoorfar M. (2016) Market and technology assessment of natural gas processing: A review, J. Nat. Gas Sci. Eng. 30, 487–514. [Google Scholar]
  • Michelsen M. (1980) Calculation of phase envelopes and critical points for multicomponent mixtures, Fluid Phase Equilib. 4, 1–2, 1–10. [Google Scholar]
  • Nasir Q., Sabil K., Lau K. (2015) Measurement of isothermal (vapor + liquid) equilibria, (VLE) for binary (CH4 + CO2) from T = (240.35 to 293.15) K and CO2 rich synthetic natural gas systems from T = (248.15 to 279.15) K, J. Nat. Gas Sci. Eng. 27, 1, 158–167. [Google Scholar]
  • Nasrifar K., Bolland O., Moshfeghian M. (2005) Predicting natural gas dew points from 15 equations of state, Energy Fuels 19, 561–572. [Google Scholar]
  • Nasrifar K., Rahmanian N. (2018) Equations of state with group contribution binary interaction parameters for calculation of two-phase envelopes for synthetic and real natural gas mixtures with heavy fractions, Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles 73, 7. [CrossRef] [Google Scholar]
  • Peng D. (1986) An empirical method for calculating vapor–liquid critical points of multicomponent mixtures, Can. J. Chem. Eng. 64, 827–830. [Google Scholar]
  • Peng D., Robinson D. (1976) A new two-constant equation of state, Ind. Eng. Chem. Fundam. 15, 1, 59–64. [CrossRef] [Google Scholar]
  • Peng D., Robinson D. (1977) A rigorous method for predicting the critical properties of multicomponent systems from an equation of state, AlChE J. 23, 2, 137–144. [CrossRef] [Google Scholar]
  • Sayed M., Al-Muntasheri G. (2016) Mitigation of the effects of condensate banking: A critical review, SPE Prod. Oper. 31, 2, 85–102. [Google Scholar]
  • Sloan E., Koh C. (2008) Clathrate hydrates of natural gases, 3rd ed., CRC Press, Taylor & Francis, New York, NY. [Google Scholar]
  • Yang Y., Li J., Wang S., Wen C. (2018) Gas-liquid two-phase flow behavior in terrain-inclined pipelines for gathering transport system of wet natural gas, Int. J. Press. Vessels Piping 162, 52–58. [CrossRef] [Google Scholar]

Current usage metrics show cumulative count of Article Views (full-text article views including HTML views, PDF and ePub downloads, according to the available data) and Abstracts Views on Vision4Press platform.

Data correspond to usage on the plateform after 2015. The current usage metrics is available 48-96 hours after online publication and is updated daily on week days.

Initial download of the metrics may take a while.