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Author: | Mullins, J. |
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17 matching references were found.
Mullins, J.A.; Rawlings, J.B.; Johnston, K.P., Partial derivative quantities from phase equilibria relationships for mixtures, AIChE J., 1993, 39, 1363-9. [all data]
Ziegler, W.T.; Mullins, J.C.; Berquist, A.R., Calculation of the Vapor Pressure and Heats of Vaporization and Sublimation of Liquids and Solids below One Atmosphere Pressure. VIII. Xenon, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-764, Tech. Rep. No. 3, 1966. [all data]
Beard, A.M.; Mullins, J.C.; Barron, C.H.; Daniels, G.A., Vapor-liquid phase equilibrium at high pressures for the ethane- trinormalbutylaluminum and ethane-trinormalhexylaluminum systems, Fluid Phase Equilib., 1996, 116, 429-36. [all data]
Briones, J.A.; Mullins, J.C.; Thies, M.C., Liquid-liquid equilibria for the oleic acid-β-sitosterol-water system at elevated temperatures and pressures, Ind. Eng. Chem. Res., 1994, 33, 151-6. [all data]
Beard, A.M.; Mullins, J.C.; Daniels, G.A., Phase equilibria at high pressures for the ethane-heptane and ethane- triethylaluminum systems, Fluid Phase Equilib., 1993, 82, 93-100. [all data]
Coast, R.A.; Mullins, J.C.; Thies, M.C., Fluid Phase Equilib., 1991, 65, 327-38. [all data]
Mullins, J.C.; Ziegler, W.T., Phase equilibria in the argon - helium and argon - hydrogen systems from 68 to 108 k and pressures to 120 atmospheres, Adv. Cryog. Eng., 1965, 10, 171-81. [all data]
Ziegler, W.T.; Kirk, B.S.; Mullins, J.C.; Berquist, A.R., Calculation of the vap. press. & heats of vaporization & sublimation of liqs. & solids below 1 atms. prss. VII ethane, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-764, Tech. Rep. No. 1, 1964. [all data]
Ziegler, W.T.; Yarbrough, D.W.; Mullins, J.C., Calculation of the Vapor Pressure and Heats of Vaporization and Sublimation of Liquids and Solids below One Atmosphere Pressure. VI. Krypton, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-764, Tech. Rep. No. 1, 1964. [all data]
Ziegler, W.T.; Mullins, J.C., Calculation of the vap. press. & heats of vaporization & sublimation of liqs. & solids, especially below 1 atms. press. 1V. Nitrogen & Fluorine, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-663, Tech. Rep. No. 1, 1963. [all data]
Mullins, J.C.; Kirk, B.S.; Ziegler, W.T., , U. S. A. E. C. NP-13862, 1963. [all data]
Ziegler, W.T.; Mullins, J.C.; Kirk, B.S., Calculation of the Vapor Pressure and Heats of Vaporization and Sublimation of Liquids and Solids, Especially Below One Atmosphere Pressure. II. Argon, Ga. Inst. Technol., Eng. Exp. Stn., Proj. A-460, Tech. Rep. No. 2, 1962. [all data]
Mullins, J.C.; Ziegler, W.T.; Kirk, B.S., Adv. Cryog. Eng., 1962, 8, 126. [all data]
Kirk, B.S.; Ziegler, W.T.; Mullins, J.C., A comparison of methods of predicting equilibrium gas phase compositions in pressureized binary systems containing an essentially pure condensed phase, Adv. Cryog. Eng., 1961, 6, 413-28. [all data]
Briones, J.A.; Beaton, T.A.; Mullins, J.C.; Thies, M.C., Liquid-liquid equilibria for oleic acid-water mixtures at elevated temperatures and pressures, Fluid Phase Equilib., 1989, 53, 475. [all data]
Briones, J.A.; Mullins, J.C.; Thies, M.C.; Kim, B.U., Fluid Phase Equilib., 1987, 36, 235. [all data]
Munday, E.B.; Mullins, J.C.; Edie, D.D., Vapor pressure data for toluene, 1-pentanol, 1-butanol, water, and 1-propanol and for the water and 1-propanol system from 273.15 to 323.15 K, J. Chem. Eng. Data, 1980, 25, 191-4. [all data]