메뉴 건너뛰기




Volumn 41, Issue 3, 1996, Pages 537-542

Vapor-liquid equilibrium for methanol + 1,1-dimethylpropyl methyl ether at (288.15, 308.15, and 328.15) K

Author keywords

[No Author keywords available]

Indexed keywords

AZEOTROPES; EQUATIONS OF STATE OF LIQUIDS; ETHERS; MATHEMATICAL MODELS; METHANOL; PHASE EQUILIBRIA; PRESSURE MEASUREMENT; VAPOR PRESSURE;

EID: 0030134305     PISSN: 00219568     EISSN: None     Source Type: Journal    
DOI: 10.1021/je950300+     Document Type: Article
Times cited : (19)

References (32)
  • 1
    • 0016437957 scopus 로고
    • Statistical Thermodynamics of Liquid Mixtures. a New Expression for the Excess Gibbs Energy of Partly and Completely Miscible Systems
    • Abrams, D. S.; Prausnitz, J. M. Statistical Thermodynamics of Liquid Mixtures. A New Expression for the Excess Gibbs Energy of Partly and Completely Miscible Systems. AIChE J. 1975, 21, 116-128.
    • (1975) AIChE J. , vol.21 , pp. 116-128
    • Abrams, D.S.1    Prausnitz, J.M.2
  • 2
    • 0017907025 scopus 로고
    • Evaluation of Parameters for Nonlinear Thermodynamic Models
    • Anderson, T. F.; Abrams, D. S.; Grens, E. A., II. Evaluation of Parameters for Nonlinear Thermodynamic Models. AIChE J. 1978, 24, 20-29.
    • (1978) AIChE J. , vol.24 , pp. 20-29
    • Anderson, T.F.1    Abrams, D.S.2    Grens II, E.A.3
  • 3
    • 0028465931 scopus 로고
    • Vapor-Liquid Equilibria of Hydrocarbons and tert-Amyl Methyl Ether
    • Antosik, M.; Sandler, S. I. Vapor-Liquid Equilibria of Hydrocarbons and tert-Amyl Methyl Ether. J. Chem. Eng. Data 1994, 39, 584-587.
    • (1994) J. Chem. Eng. Data , vol.39 , pp. 584-587
    • Antosik, M.1    Sandler, S.I.2
  • 4
    • 84970567283 scopus 로고
    • Determination of Activity Coefficinets from Total Pressure Measurements
    • Barker, J. A. Determination of Activity Coefficinets from Total Pressure Measurements. Aust. J. Chem. 1953, 6, 207-210.
    • (1953) Aust. J. Chem. , vol.6 , pp. 207-210
    • Barker, J.A.1
  • 5
    • 5844297425 scopus 로고
    • Personal communication
    • Cancho, S. Personal communication, 1995.
    • (1995)
    • Cancho, S.1
  • 6
    • 0021513179 scopus 로고
    • Vapor Pressures, Refractive Indexes, and Densities at 20.0 °C, and Vapor-Liquid Equilibrium at 101.325 kPa, in the tert-Amyl Methyl Ether-Methanol System
    • Cervenkova, I.; Boublik, T. Vapor Pressures, Refractive Indexes, and Densities at 20.0 °C, and Vapor-Liquid Equilibrium at 101.325 kPa, in the tert-Amyl Methyl Ether-Methanol System. J. Chem. Eng. Data 1984, 29, 425-427.
    • (1984) J. Chem. Eng. Data , vol.29 , pp. 425-427
    • Cervenkova, I.1    Boublik, T.2
  • 7
    • 0019547804 scopus 로고
    • Maximize Blend Ethers with MTBE and TAME
    • Chase, J.; Galvez, B. B. Maximize Blend Ethers with MTBE and TAME. Hydrocarbon Process, 1981, 60, 89-93.
    • (1981) Hydrocarbon Process , vol.60 , pp. 89-93
    • Chase, J.1    Galvez, B.B.2
  • 10
    • 0026205276 scopus 로고
    • The MHV2 Model: A UNIFAC-Based Equation of State Model for Prediction of Gas Solubility and Vapor-Liquid Equilibria at Low and High Pressures
    • Dahl, S.; Fredenslund, A.; Rasmussen, P. The MHV2 Model: A UNIFAC-Based Equation of State Model for Prediction of Gas Solubility and Vapor-Liquid Equilibria at Low and High Pressures. Ind. Eng. Chem. Res. 1991, 30, 1936-1945.
    • (1991) Ind. Eng. Chem. Res. , vol.30 , pp. 1936-1945
    • Dahl, S.1    Fredenslund, A.2    Rasmussen, P.3
  • 11
    • 0000473277 scopus 로고
    • Isothermal compressibilities of n-1-alcohols from methanol to 1-dodecanol at 298.15, 308.15, 318.15, and 333.15 K
    • Diaz Pefia, M.; Tardajos, G. Isothermal compressibilities of n-1-alcohols from methanol to 1-dodecanol at 298.15, 308.15, 318.15, and 333.15 K. J. Chem. Thermodyn. 1979, 11, 441-445.
    • (1979) J. Chem. Thermodyn. , vol.11 , pp. 441-445
    • Diaz Pefia, M.1    Tardajos, G.2
  • 13
    • 79956194942 scopus 로고
    • Tertiary Alkyl Ethers, Preparation and Properties
    • Evans, T. W.; Edlund, K. R. Tertiary Alkyl Ethers, Preparation and Properties. Ind. Eng. Chem. Res. 1936, 28, 1186-1188.
    • (1936) Ind. Eng. Chem. Res. , vol.28 , pp. 1186-1188
    • Evans, T.W.1    Edlund, K.R.2
  • 15
    • 0000827066 scopus 로고
    • Vapor-Liquid Equilibria from Total-Pressure Measurements. A New Apparatus
    • Gibbs, R. E.; Van Ness, H. C. Vapor-Liquid Equilibria from Total-Pressure Measurements. A New Apparatus. Ind. Eng. Chem. Fundam. 1972, 11, 410-413.
    • (1972) Ind. Eng. Chem. Fundam. , vol.11 , pp. 410-413
    • Gibbs, R.E.1    Van Ness, H.C.2
  • 19
    • 0016534375 scopus 로고
    • A Generalized Method for Predicting Second Virial Coefficients
    • Hayden, J. G.; O'Connell, J. P. A Generalized Method for Predicting Second Virial Coefficients. Ind. Eng. Chem. Process Des. Dev. 1975, 14, 209-216.
    • (1975) Ind. Eng. Chem. Process Des. Dev. , vol.14 , pp. 209-216
    • Hayden, J.G.1    O'Connell, J.P.2
  • 20
    • 0001853347 scopus 로고
    • Use TAME and heavier ethers to improve gasoline properties
    • Ignatius, J.; Järvelin, H.; Lindqvist, P. Use TAME and heavier ethers to improve gasoline properties. Hydrocarbon Process. 1995, 74, 51-53.
    • (1995) Hydrocarbon Process. , vol.74 , pp. 51-53
    • Ignatius, J.1    Järvelin, H.2    Lindqvist, P.3
  • 21
    • 0023455795 scopus 로고
    • A Modified UNIFAC Group-Contribution Model for Prediction of Phase Equilibria and Heats of Mixing
    • Larsen, B. L.; Rasmussen, P.; Fredenslund, A. A Modified UNIFAC Group-Contribution Model for Prediction of Phase Equilibria and Heats of Mixing. Ind. Eng. Chem. Res. 1987, 26, 2274-2286.
    • (1987) Ind. Eng. Chem. Res. , vol.26 , pp. 2274-2286
    • Larsen, B.L.1    Rasmussen, P.2    Fredenslund, A.3
  • 22
    • 0000403396 scopus 로고
    • Excess Molar Enthalpies of an Alkanol + a Brached Ether at the Temperature 298.15 K
    • Letcher, T. M.; Govender, P. U. Excess Molar Enthalpies of an Alkanol + a Brached Ether at the Temperature 298.15 K. J. Chem. Eng. Data 1995, 40, 997-1000.
    • (1995) J. Chem. Eng. Data , vol.40 , pp. 997-1000
    • Letcher, T.M.1    Govender, P.U.2
  • 23
    • 0020830378 scopus 로고
    • Extension of the Peng-Robinson Equation of State to Complex Mixtures: Evaluation of the Various Forms of the Local Composition Concept
    • Mathias, P. M.; Copeman, T. W. Extension of the Peng-Robinson Equation of State to Complex Mixtures: Evaluation of the Various Forms of the Local Composition Concept. Fluid Phase Equilib. 1983, 13, 91-108.
    • (1983) Fluid Phase Equilib. , vol.13 , pp. 91-108
    • Mathias, P.M.1    Copeman, T.W.2
  • 24
    • 0025402371 scopus 로고
    • Isobaric Vapor-Liquid Equilibrium in Two Binary Systems Involving tert-Amyl Methyl Ether
    • Palczewska-Tulinska, M.; Wyrzykowska-Stankiewicz, D. Isobaric Vapor-Liquid Equilibrium in Two Binary Systems Involving tert-Amyl Methyl Ether. Fluid Phase Equilib. 1990, 54, 57-68.
    • (1990) Fluid Phase Equilib. , vol.54 , pp. 57-68
    • Palczewska-Tulinska, M.1    Wyrzykowska-Stankiewicz, D.2
  • 25
    • 0001082370 scopus 로고
    • Experimental Vapor Pressures and Maximum-Likelihood Antoine-Equation Constants for 1,1,1-Methoxydimethylpropane, Thiacyclopentane and 1,4-Butanediol
    • Palczewska-Tulinska, M.; Cholinski, J.; Szafranski, A. M.; Wyrzykowska-Stankiewicz, D. Experimental Vapor Pressures and Maximum-Likelihood Antoine-Equation Constants for 1,1,1-Methoxydimethylpropane, Thiacyclopentane and 1,4-Butanediol. Fluid Phase Equilib. 1984, 15, 295-307.
    • (1984) Fluid Phase Equilib. , vol.15 , pp. 295-307
    • Palczewska-Tulinska, M.1    Cholinski, J.2    Szafranski, A.M.3    Wyrzykowska-Stankiewicz, D.4
  • 26
    • 0041613405 scopus 로고
    • Liquid-Vapor Phase Equilibrium in Binary Systems Formed by Methyl tert-Amyl Ether
    • Pavlova, I. P.; Saraeev, B. A.; Chaplits, D. N. Liquid-Vapor Phase Equilibrium in Binary Systems Formed by Methyl tert-Amyl Ether. Prom-st. Sint. Kauch. 1981, 5, 2-4.
    • (1981) Prom-st. Sint. Kauch. , vol.5 , pp. 2-4
    • Pavlova, I.P.1    Saraeev, B.A.2    Chaplits, D.N.3
  • 28
    • 0020809719 scopus 로고
    • Regression of Vapor-Liquid Equilibrium Data Based on Application of the Maximum-Likelihood Principle
    • Rubio, R. G.; Renuncio, J. A. R.; Diaz Peña, M. Regression of Vapor-Liquid Equilibrium Data Based on Application of the Maximum-Likelihood Principle. Fluid Phase Equilib. 1983, 12, 217-234.
    • (1983) Fluid Phase Equilib. , vol.12 , pp. 217-234
    • Rubio, R.G.1    Renuncio, J.A.R.2    Diaz Peña, M.3
  • 29
    • 0001149415 scopus 로고
    • Total Pressure Measurements of Binary Mixtures Containing tert-Amyl Methyl Ether and tert-Amyl Alcohol
    • Semar, S.; Sandler, S. I.; Antosik, M. Total Pressure Measurements of Binary Mixtures Containing tert-Amyl Methyl Ether and tert-Amyl Alcohol. J. Chem. Eng. Data 1995, 40, 712-718.
    • (1995) J. Chem. Eng. Data , vol.40 , pp. 712-718
    • Semar, S.1    Sandler, S.I.2    Antosik, M.3
  • 30
    • 47649111276 scopus 로고
    • Equilibrium Constants from a Modified Redlich-Kwong Equation of State
    • Soave, G. Equilibrium Constants from a Modified Redlich-Kwong Equation of State. Chem. Eng. Sci. 1972, 27, 1197-1203.
    • (1972) Chem. Eng. Sci. , vol.27 , pp. 1197-1203
    • Soave, G.1
  • 32
    • 0027668070 scopus 로고
    • Correlation and Prediction of the Vapor-Liquid Equilibria of the Binary and Ternary Systems involved in MTBE Synthesis
    • Vetere, A.; Miracca, I.; Cianci, F. Correlation and Prediction of the Vapor-Liquid Equilibria of the Binary and Ternary Systems involved in MTBE Synthesis. Fluid Phase Equilib, 1993, 90, 189-203.
    • (1993) Fluid Phase Equilib , vol.90 , pp. 189-203
    • Vetere, A.1    Miracca, I.2    Cianci, F.3


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.