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Abstrakty
Stricter environmental legislations make necessary or even profitable the utilization of gases that are by-products from different production processes and which have been wasted so far. To design the most suitable utilization technology for these gases a detailed knowledge of their properties is required. The parameters of vapour-liquid phase change are crucial for fuel handling. The physical and chemical properties of most commonly used gases are well known but the broad variety of gases produced during different industrial processes has not been investigated yet. The simple, fast and precise method of determination of their condensation curve is very useful. The determination of condensation curve for a gas composed mainly of hydrogen and propane has been described. The measurement method and testing equipment is universal and can be used for various compositions of gases and is also very suitable for gases containing a significant amount of hydrogen.
Słowa kluczowe
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Rocznik
Tom
Strony
53--61
Opis fizyczny
Bibliogr. 9 poz., rys., tab.
Twórcy
autor
autor
autor
autor
autor
- Warsaw University of Technology
Bibliografia
- [1] Chorng H. Twu, John E. Coon, and David Bluck; A Comparison of the Peng-Robinson and Soave-Redlich-Kwong Equations of State Using a New Zero-Pressure-Based Mixing Rule for the Prediction of High Pressure and High Temperature Phase Equilibria; Industrial & engineering chemistry research 37 (1998) pp. 1580-1585
- [2] Smith J. M., Van Ness H. C., Abbott M. M.; Introduction to Chemical Engineering Thermodynamics; McGraw-Hill ISBN-10 / ASIN: 0072402962, ISBN-13 / EAN: 9780072402964
- [3] AspenHYSYS software internal database – Software provided by Aspen Technology, Inc.
- [4] Novenario C. R., Caruthers J. M., Chao K-C; A Mixing Rule To Incorporate Solution Model into Equation of State; Industrial & engineering chemistry research 35, (1996) pp. 269-277
- [5] Ledanois J, M., Muller E. A., Colina C. M., Gonzalez-Mendizabal D., Santos J. W., Olivera-Fuentes C.; Correlations for Direct Calculation of Vapor Pressures from Cubic Equations of State; Industrial & engineering chemistry research 37, (1998), pp. 1673-678
- [6] Voulgaris M. E., Peters C. J., de Swaan Arons J.; Prediction of the Condensation Behavior of Natural Gas: A Comparative Study of the Peng Robinson and the Simplified-Perturbed-Hard-Chain Theory Equations of State; Industrial & engineering chemistry research 37, (1998), pp. 1696 1706
- [7] Kandil Mohamed, E. Marsh Kenneth, N, Goodwin Anthony R.H; A re-entrant resonator for the measurement of phase boundaries: dew points for {0.4026CH4 +0.5974C3H8}; The Journal of Chemical Thermodynamics 37 (2005) pp. 684-691
- [8] Schwarz C.E. Nieuwoudt I, Knoetze J.H.; Phase equilibrium of propane and alkanes Part III:Beyond hexacontane; Journal of Supercritical Fluids 41 (2007) pp. 327–334
- [9] Ju Hyok Kim, Min Soo Kim; Vapor–liquid equilibria for the carbon dioxide + propane system over a temperature range from 253.15 to 323.15K; Fluid Phase Equilibria 238 (2005) pp.13–19
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BWM4-0030-0015