Liquid—Vapor Phase Behavior and Liquid Phase Density in the System Neon—Argon at High Pressures

1967 ◽  
Vol 46 (9) ◽  
pp. 3282-3286 ◽  
Author(s):  
W. B. Streett
1934 ◽  
Vol 11 (2) ◽  
pp. 180-189 ◽  
Author(s):  
A. L. Geddes ◽  
C. C. Coffin

The homogeneous first order gaseous decomposition of paraldehyde to acetaldehyde has been studied at temperatures from 230 to 254 °C. up to pressures at which the liquid phase makes its appearance, i.e., 12 atm. at 230° and 18 atm. at 254 °C. Over-all velocity constants for the homogeneous reaction in the heterogeneous liquid-vapor system have been determined from these pressures up to the critical point. The data confirm results already published. It is found that in the purely gaseous system increase of pressure tends to diminish the reaction velocity. That the specific reaction velocity in the liquid phase is greater than that in the vapor phase is shown by the fact that the velocity constants of the heterogeneous systems increase progressively with the liquid-vapor ratio. Extrapolation to 100% of liquid gives velocity constants about five times as great as those characteristic of the vapor phase. Peculiarities in the behavior of the system at the critical point and preliminary measurements of the velocity of the trimolecular reverse reaction are described.


2016 ◽  
Vol 18 (21) ◽  
pp. 14252-14256 ◽  
Author(s):  
Julian Schulze ◽  
Johannes Möller ◽  
Jonathan Weine ◽  
Karin Julius ◽  
Nico König ◽  
...  

Dense protein solutions exhibit a reentrant liquid–liquid phase separation region at high pressures.


AIChE Journal ◽  
1962 ◽  
Vol 8 (4) ◽  
pp. 537-539 ◽  
Author(s):  
J. A. Davis ◽  
Newell Rodewald ◽  
Fred Kurata

2016 ◽  
Vol 9 (1) ◽  
pp. 36-43 ◽  
Author(s):  
Michal Ilčin ◽  
Martin Michalík ◽  
Klára Kováčiková ◽  
Lenka Káziková ◽  
Vladimír Lukeš

Abstract The molecular dynamics simulations of the liquid-vapor equilibrium of water including both water phases — liquid and vapor — in one simulation are presented. Such approach is preferred if equilibrium curve data are to be collected instead of the two distinct simulations for each phase separately. Then the liquid phase is not restricted, e.g. by insufficient volume resulting in too high pressures, and can spread into its natural volume ruled by chosen force field and by the contact with vapor phase as vaporized molecules are colliding with phase interface. Averaged strongly fluctuating virial pressure values gave untrustworthy or even unreal results, so need for an alternative method arisen. The idea was inspired with the presence of vapor phase and by previous experiences in gaseous phase simulations with small fluctuations of pressure, almost matching the ideal gas value. In presented simulations, the first idea how to calculate pressure only from the vapor phase part of simulation box were applied. This resulted into very simple method based only on averaging molecules count in the vapor phase subspace of known volume. Such simple approach provided more reliable pressure estimation than statistical output of the simulation program. Contrary, also drawbacks are present in longer initial thermostatization time or more laborious estimation of the vaporization heat. What more, such heat of vaporization suffers with border effect inaccuracy slowly decreasing with the thickness of liquid phase. For more efficient and more accurate vaporization heat estimation the two distinct simulations for each phase separately should be preferred.


1998 ◽  
Vol 58 (2) ◽  
pp. 2201-2212 ◽  
Author(s):  
N. B. Wilding ◽  
F. Schmid ◽  
P. Nielaba

2017 ◽  
Vol 45 ◽  
pp. 738-746 ◽  
Author(s):  
Mesude Ozturk ◽  
Sai R. Panuganti ◽  
Kai Gong ◽  
Kenneth R. Cox ◽  
Francisco M. Vargas ◽  
...  

Soft Matter ◽  
2010 ◽  
Vol 6 (24) ◽  
pp. 6136 ◽  
Author(s):  
Francisco J. Martinez-Veracoechea ◽  
Behnaz Bozorgui ◽  
Daan Frenkel

2014 ◽  
Vol 53 (45) ◽  
pp. 17833-17842 ◽  
Author(s):  
Kaustubh S. Rane ◽  
Vaibhaw Kumar ◽  
Scott Wierzchowski ◽  
Majeed Shaik ◽  
Jeffrey R. Errington

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