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Bibliografias temáticas / Gas-liquid equilibrium

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Artigos de revistas

Literatura científica selecionada sobre o tema "Gas-liquid equilibrium"

Autor: Grafiati

Publicado: 23 de novembro de 2024

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Artigos de revistas sobre o assunto "Gas-liquid equilibrium"

1

Stringari, S., M. Barranco, A. Polls, P. J. Nacher, and F. Laloë. "Spin-polarized 3He : liquid gas equilibrium." Journal de Physique 48, no. 8 (1987): 1337–50. http://dx.doi.org/10.1051/jphys:019870048080133700.

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2

YAMAMOTO, Takayuki, Norizumi MOTOOKA, Osamu MORI, and Yoshihiro KISHINO. "Gas-Liquid Equilibrium Thruster of IKAROS." TRANSACTIONS OF THE JAPAN SOCIETY FOR AERONAUTICAL AND SPACE SCIENCES, AEROSPACE TECHNOLOGY JAPAN 12, ists29 (2014): Tf_13—Tf_18. http://dx.doi.org/10.2322/tastj.12.tf_13.

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3

Librovich, Bronislav V., Andrzej F. Nowakowski, Issa Chaer, and Savvas Tassou. "Non-equilibrium gas-liquid transition model." PAMM 7, no. 1 (2007): 2100029–30. http://dx.doi.org/10.1002/pamm.200700233.

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4

Xu, Hui. "The Research on SO₂ Desorption Equilibrium Mechanism of Sodium Alkali Desulfurization Regeneration Solution." Advanced Materials Research 898 (February 2014): 461–64. http://dx.doi.org/10.4028/www.scientific.net/amr.898.461.

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Sodium alkali flue gas desulfurization (FGD) is one of the most promising renewable FGD technologies, and the SO2 gases desorption in desulfurization regeneration solution is very important to directly affect its application. Based on the gas-liquid equilibrium relationships, this paper researched the equilibrium mechanism of SO2 desorption in the sodium alkali desulfurization regeneration solution. The results showed that SO2 desorption process is a mass transfer process that SO2 transfer from liquid phase to gas phase essentially, and SO2 desorption limit capacity depend mainly on the gas-li

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5

Percus, Jerome K. "Classical liquid-gas interface in thermal equilibrium." Journal of Statistical Physics 78, no. 3-4 (1995): 1165–69. http://dx.doi.org/10.1007/bf02183709.

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6

Clarke, Colin W., and David N. Glew. "Aqueous nonelectrolyte solutions. Part XV. The deuterium sulfide - deuterium oxide system and the deuterium sulfide D-hydrate." Canadian Journal of Chemistry 76, no. 8 (1998): 1119–29. http://dx.doi.org/10.1139/v98-133.

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The univariant (l1l2g) saturation vapor pressure of liquid deuterium oxide (phase l1) with liquid deuterium sulfide (phase l2) in equilibrium with a gas phase (g) has been measured in a stirred titanium reaction vessel at 19 temperatures from 33.003 to 18.905°C and at total pressures from 2.4500 to 1.7428 MPa. The univariant (hl1g) saturation vapor pressure of deuterium sulfide D-hydrate (phase h) in equilibrium with liquid deuterium oxide and a gas phase has been measured at 58 temperatures from 30.666 to 2.798°C and at pressures from 2.2959 to 0.11629 MPa. The maximum temperature for deuteri

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7

Chen, Panpan, Guoen Li, Hongfei Guo, and Ji Lin Cao. "Phase Equilibrium Study on the Quaternary System H₂O-Na₂SO₄-MgSO₄-C₃H₈ at 0°C and Pressure." Advanced Materials Research 550-553 (July 2012): 2690–94. http://dx.doi.org/10.4028/www.scientific.net/amr.550-553.2690.

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In order to develop a new technology for separating the bloedite by the method of gas hydrate formation, the phase equilibrium of the H2O-Na2SO4-MgSO4-C3H8 system and its subsystems was studied at 0°C and pressure.The equilibrium pressure and the composition of solid and liquid above system were investigated.It was found that equilibrium pressure of gas hydrate formation was increasing with the increase of the Na2SO4( or MgSO4) concentration. The addition of anionic surfactant SDS helped to lower the equilibrium pressure of gas hydrate formation. The mother liquor amount entrained in the gas h

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8

Mathis, Hélène. "A thermodynamically consistent model of a liquid-vapor fluid with a gas." ESAIM: Mathematical Modelling and Numerical Analysis 53, no. 1 (2019): 63–84. http://dx.doi.org/10.1051/m2an/2018044.

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This work is devoted to the consistent modeling of a three-phase mixture of a gas, a liquid and its vapor. Since the gas and the vapor are miscible, the mixture is subjected to a non-symmetric constraint on the volume. Adopting the Gibbs formalism, the study of the extensive equilibrium entropy of the system allows to recover the Dalton’s law between the two gaseous phases. In addition, we distinguish whether phase transition occurs or not between the liquid and its vapor. The thermodynamical equilibria are described both in extensive and intensive variables. In the latter case, we focus on th

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9

CHUJO, Toshihiro, Norizumi MOTOOKA, Takayuki YAMAMOTO, and Osamu MORI. "Development of Bipropellant Gas-Liquid Equilibrium Propulsion System." TRANSACTIONS OF THE JAPAN SOCIETY FOR AERONAUTICAL AND SPACE SCIENCES, AEROSPACE TECHNOLOGY JAPAN 14 (2016): 9–14. http://dx.doi.org/10.2322/tastj.14.9.

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10

Mitrovic, J. "Upon equilibrium of gas bubble in infinite liquid." Chemical Engineering Science 55, no. 12 (2000): 2265–70. http://dx.doi.org/10.1016/s0009-2509(99)00475-3.

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