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Phase equilibria for liquefi eld natural gas (LNG) as a multicomponent mixture

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Języki publikacji
EN
Abstrakty
EN
Liquefied natural gas (LNG) has an increasingly important role in the global natural gas market. Global demand for natural gas will grow over the coming years. LNG is transported by ships to unloading points on the storage terminals. During the LNG unloading and storage processes some part of LNG evaporates into gas phase and causes changes in the composition of stored LNG. The main component of LNG is methane, the remaining components are primarily ethane, propane, butane and nitrogen. Depending on the participation of these components the basic thermodynamic parameters of LNG can significantly change. LNG is also product sensitive to changes of temperature. In order to better prediction of changes of individual paramete rs of stored LNG caused by changes of temperature and LNG composition vapor-liquid equilibrium (VLE) calculations are performed for cryogenic conditions using equations of state.
Rocznik
Strony
539--550
Opis fizyczny
Bibliogr. 13 poz., tab., wykr.
Twórcy
autor
  • AGH University of Science and Technology, Faculty of Drillin g, Oil and Gas, Krakow, Poland
Bibliografia
  • 1] Łaciak M.: Liquefied natural gas storage of variable composition. Archives of Mining Sciences, vol. 60, issue 1, 2015, pp. 225–238.
  • [2] Łaciak M.: Zwiększenie efektywności energetycznej odparowania oraz bezpieczeństwa magazynowania skroplonego gazu ziemnego (LNG). Wydawnictwa AGH, Kraków 2013.
  • [3] Adom E., Zahidul Islam S., Ji X.: Modelling of Boil-OffGas in LNG Tanks: A Case Study. International Journal of Engineering and Technology, vol. 2, no. 4, 2010, pp. 292–296.
  • [4] Peng D.Y., Robinson D.B.: A New Two-Constant Equation of State. Industrial and Engineering Chemistry Fundamentals, vol. 15, no. 1, 1976, pp. 59–64.
  • [5] Walas S.M.: Phase Equilibria in Chemical Engineering. Elsevier, 1985.
  • [6] Changjun Li, Wenlong Jia, Xia Wu: Application of Lee-Kesler equation of state to calculating compressibility factors of high pressure condensate gas. Energy Procedia, vol. 14, 2012, pp. 115–120.
  • [7] Radebaugh R.: About Cryogenics[in:] The MacMillan Encyclopedia Of Chemistry. New York 2002.
  • [8] Guidelines for Sampling and Sample Processing: Storage of Environmental Samples under Cryogenic Conditions. FIMBAE, 2008
  • [9] Łaciak M.: Thermodynamic processes involving Liquefied Natural Gas at the LNG receiving terminals. Archives of Mining Sciences, vol. 58, issue 2, 2013, pp. 349–359.
  • [10] Włodek T., Łaciak M.: Selected thermodynamic aspects of Liquefied Natural Gas (LNG) Pipeline Flow during unloading process. AGH Drilling, Oil and Gas, vol. 32, no. 2, 2015.
  • [11] Nghiem L.X., Aziz K., Li Y.K.: A Robust Iterative Method for Flash Calculations Using the Soave–Redlich–Kwong or the Peng–Robinson Equation of State. SPE paper 8285.
  • [12] Chen Q.S., Wegrzyn J., Prasad V.: Analysis of temperature and pressure changes in liquefied natural gas (LNG) cryogenic tanks. Cryogenics, vol. 44, 2004, pp. 701–709.
  • [13] Chorowski M.: Kriogenika. Podstawy i zastosowania. IPPU MASTA, 2007.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-1e9afe82-d99e-411d-86f3-c25e1bdbfcf5
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