The Vapor Pressures and Some Thermodynamic Properties of Aqueous Solutions of Nickel Chloride at 25°C

1937 ◽  
Vol 41 (4) ◽  
pp. 563-565 ◽  
Author(s):  
J. N. Pearce ◽  
H. C. Eckstrom
Keyword(s):  
Thermodynamic Properties ◽  
Aqueous Solutions ◽  
Nickel Chloride ◽  
Vapor Pressures

Vapor pressures of aqueous solutions of (silver, thallium, sodium) nitrate at 98.5.degree.C

1980 ◽  
Vol 25 (4) ◽  
pp. 331-332 ◽  
Author(s):  
Marie Christine Abraham ◽  
Maurice Abraham ◽  
James Sangster
Keyword(s):  
Aqueous Solutions ◽  
Sodium Nitrate ◽  
Vapor Pressures

Thermodynamic Properties of Energetic Plasticizers: Experimental Vapor Pressures of Methyl-, Ethyl-, and Butyl-Nitroxyethyl Nitramines

2021 ◽  
Vol 66 (4) ◽  
pp. 1709-1716
Author(s):  
Greta Bikelytė ◽  
Martin A. C. Härtel ◽  
Marcel Holler ◽  
Andreas Neuer ◽  
Thomas M. Klapötke
Keyword(s):  
Thermodynamic Properties ◽  
Methyl Ethyl ◽  
Vapor Pressures ◽  
Energetic Plasticizers

Thermodynamic Properties of Liquid Helium Three. Vapor Pressures below 1°K

1957 ◽  
Vol 106 (2) ◽  
pp. 175-182 ◽  
Author(s):  
Stephen G. Sydoriak ◽  
Thomas R. Roberts
Keyword(s):  
Thermodynamic Properties ◽  
Liquid Helium ◽  
Vapor Pressures ◽  
Helium Three

scholarly journals COMPARISON OF GAZKONDNAFTA AND HYSYS SOFTWARE SYSTEMS IN THE FIELD OF COMPUTER MODELING OF OIL AND GAS TECHNOLOGIES

2021 ◽  
pp. 4-22
Author(s):  
O.V. Kalashnikov ◽  
S.V. Budniak ◽  
Yu.V. Ivanov ◽  
Yu.M. Belyansky ◽  
N.O. Aptulina ◽  
...  
Keyword(s):  
Natural Gas ◽  
Thermodynamic Properties ◽  
Aqueous Solutions ◽  
Computer Modeling ◽  
Oil And Gas ◽  
Software Systems ◽  
Program System ◽  
Aspen Hysys ◽  
Treatment Processes ◽  
Liquid Phases

The experimental and calculated according to program systems GasCondOil, Aspen-HYSYS and PRO-II compositions of the gas — liquid phases (hydrocarbon and aqueous solutions) and their thermodynamic properties are compared, as well as the accuracy of technological calculations of field pipelines and natural gas and oil treatment processes. It is shown that some of the field technological processes, calculated by the program system GasCondOil, are not modeled on Aspen-HYSYS. Bibl. 16, Fig. 9, Tab. 15.

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