Search Results

Search criteria:

17 matching references were found.

Michels, A.; Degruyter, J.; Niesen, F., Isotherms of ethylene between 0c and 50c and at pressures from 20 to 270 atm, Physica (Amsterdam), 1936, 3, 346-51. [all data]

Michels, A.; Gruyter, J. de; Niesen, F., Isotherms of ethylene between 0 deg and 15 deg and at pressures from 20 to 270 atm., Physica (Amsterdam), 1936, 3, 346. [all data]

Michels, A.; Gruyter, J. de; Niesen, F., Physica (Amsterdam), 1936, 3, 406. [all data]

Niesen, V.; Palavra, A.; Kidnay, A.J.; Yesavage, V.F., An apparatus for vapor-liquid equilibrium at elevated temperatures and pressures and selected results for the water-ethanol and methanol-ethanol systems, Fluid Phase Equilib., 1986, 31, 283. [all data]

Van Poolen, L.J.; Niesen, V.G.; Holcomb, C.D.; Outcalt, S.L., Critical densities from coexisting density data: application to refrigerants R22, R134a, and R124, Fluid Phase Equilib., 1994, 97, 97-118. [all data]

Niesen, V.G.; Van Poolen, L.J.; Outcalt, S.L.; Holcomb, C.D., Coexisting densities and vapor pressures of refrigerants R-22, R-134a, and R-124 at 300-395 K, Fluid Phase Equilib., 1994, 97, 81-95. [all data]

Holcomb, C.D.; Niesen, V.G.; Van Poolen, L.J.; Outcalt, S.L., Coexisting densities , vapor pressures and critical densities of refrigerants R-32 and R-152a, at 300-385 K, Fluid Phase Equilib., 1993, 91, 145-57. [all data]

Van Poolen, L.J.; Niesen, V.G.; Rainwater, J.C., Experimental method for obtaining critical densities of binary mixtures: application to ethane + n-butane, Fluid Phase Equilib., 1991, 66, 161-85. [all data]

Niesen, V.G.; Rainwater, J.C., Critical Locus, (Vapor + Liquid) Equilibria, and Coexisting Densities of (Carbon Dioxide + Propane) at Temperatures from 311 K to 361 K, J. Chem. Thermodyn., 1990, 22, 777. [all data]

Niesen, V.G., (Vapor + liquid) equilibria and coexisting densities of (carbon dioxide + n-butane) at 311 to 395 K, J. Chem. Thermodyn., 1989, 21, 915. [all data]

Niesen, V.G.; Yesavage, V.F., Application of a maximum likelihood method using implicit constraints to determine equation of state parameters from binary phase behavior data, Fluid Phase Equilib., 1989, 50, 249. [all data]

Brown, T.S.; Niesen, V.G.; Sloan, E.D.; Kinday, A.J., Fluid Phase Equilib., 1989, 53, 7-14. [all data]

Yesavage, V.F.; Niesen, V.G.; Flanigan, D.A.; Flanigan, J.W.; Sandarusi, J.A.; Kidnay, A.J., Enthalpy of Ternary Mixtures of Quinoline/1-Methylnaphthalene/trans- Decalin and Quaternary Mixtures of m-Cresol/Quinoline/-Methylnaphthal- ene/trans-Decalin between 291 and 650 K at Pressures of 207, J. Chem. Eng. Data, 1988, 33, 407. [all data]

Niesen, V.G.; Yesavage, V.F., Vapor-Liquid Equilibria for m-Cresol/Quinoline at Temperatures between 523 and 598 K, J. Chem. Eng. Data, 1988, 33, 138. [all data]

Niesen, V.G.; Yesavage, V.F., Vapor-Liquid Equilibria for m-Cresol/Tetralin and Tetralin/Quinoline at Temperatures Between 523 and 598 K, J. Chem. Eng. Data, 1988, 33, 253. [all data]

Flanigan, D.A.; Yesavage, V.F.; Cerise, K.S.; Niesen, V.G.; Kidnay, A.J., Enthalpy of quinoline between 291 and 655 K at pressures to 10342 kP, J. Chem. Thermodyn., 1988, 20, 109. [all data]

Yesavage, V.F.; Niesen, V.G.; Flanigan, D.A.; Kidnay, A.J., Enthalpy of ternary mixtures of m-cresol/1-methylnaphthalene/trans-decalin between 291 and 650 K at pressures of 207, 690, and 10342 kPa, J. Chem. Eng. Data, 1987, 32, 323. [all data]