-
1
-
-
0029487190
-
The ppT properties of ethanol + hexane
-
P. Sauermann, K. Holzapfel, J. Oprzynski, F. Kohler, W. Pool, Th.W. de Loos, The ppT properties of ethanol + hexane, Fluid Phase Equilibria 112 (1995) 249-272.
-
(1995)
Fluid Phase Equilibria
, vol.112
, pp. 249-272
-
-
Sauermann, P.1
Holzapfel, K.2
Oprzynski, J.3
Kohler, F.4
Pool, W.5
De Loos, T.W.6
-
2
-
-
33645652754
-
Zur Thermodynamik des Systems Wasser-Triaethylamin
-
F. Kohler, Zur Thermodynamik des Systems Wasser-Triaethylamin, Monatsh. Chem. 82 (1951) 913-925.
-
(1951)
Monatsh. Chem.
, vol.82
, pp. 913-925
-
-
Kohler, F.1
-
3
-
-
0024754934
-
Excess properties of mixtures of polar components and hydrocarbons of varying local polarisability
-
N. Van Nhu, F. Kohler, Excess properties of mixtures of polar components and hydrocarbons of varying local polarisability, Fluid Phase Equilibria 50 (1989) 267-296.
-
(1989)
Fluid Phase Equilibria
, vol.50
, pp. 267-296
-
-
Van Nhu, N.1
Kohler, F.2
-
4
-
-
0000746791
-
Model for alkanol + alkane mixtures: Extension and experimental verification
-
A. Liu, K. Pusicha, A.M. Demiriz, F. Kohler, Model for alkanol + alkane mixtures: extension and experimental verification, J. Sol. Chem. 20 (1991) 39-56.
-
(1991)
J. Sol. Chem.
, vol.20
, pp. 39-56
-
-
Liu, A.1
Pusicha, K.2
Demiriz, A.M.3
Kohler, F.4
-
5
-
-
0001277298
-
A model for the excess properties of 1 -alkanol + alkane mixtures containing chemical and physical terms
-
A. Liu, F. Kohler, L. Karrer, J. Gaube, P. Spellucci, A model for the excess properties of 1 -alkanol + alkane mixtures containing chemical and physical terms, Pure Appl. Chem. 61 (1989) 1441-1452.
-
(1989)
Pure Appl. Chem.
, vol.61
, pp. 1441-1452
-
-
Liu, A.1
Kohler, F.2
Karrer, L.3
Gaube, J.4
Spellucci, P.5
-
6
-
-
0027640672
-
Model for alkanol + alkane mixtures: Calculation of key systems
-
A. Liu, F. Kohler, Model for alkanol + alkane mixtures: calculation of key systems, Fluid Phase Equilibria 89 (1993) 243-252.
-
(1993)
Fluid Phase Equilibria
, vol.89
, pp. 243-252
-
-
Liu, A.1
Kohler, F.2
-
7
-
-
0022011277
-
A modification of Newton-Raphson algorithm for phase equilibria calculations using numerical differentiation of the Gibbs energy
-
U.K. Deiters, A modification of Newton-Raphson algorithm for phase equilibria calculations using numerical differentiation of the Gibbs energy, Fluid Phase Equilibria 19 (1985) 287-293.
-
(1985)
Fluid Phase Equilibria
, vol.19
, pp. 287-293
-
-
Deiters, U.K.1
-
8
-
-
0027642561
-
Application of an EOS chain association theory to the calculation of thermodynamic properties of (alkane + 1-alkanol) mixtures
-
U.K. Deiters, Application of an EOS chain association theory to the calculation of thermodynamic properties of (alkane + 1-alkanol) mixtures, Fluid Phase Equilibria 89 (1993) 229-242.
-
(1993)
Fluid Phase Equilibria
, vol.89
, pp. 229-242
-
-
Deiters, U.K.1
-
9
-
-
0023407755
-
Development of a new four-parameter cubic equation of state
-
M.A. Trebble, P.R. Bishnoi, Development of a new four-parameter cubic equation of state, Fluid Phase Equilibria 35 (1987) 1-18.
-
(1987)
Fluid Phase Equilibria
, vol.35
, pp. 1-18
-
-
Trebble, M.A.1
Bishnoi, P.R.2
-
10
-
-
0026191829
-
The impact of asymmetric equation of state mixing rules on thermodynamic property prediction for normal alkanol-hexane binaries
-
M.A. Trebble, The impact of asymmetric equation of state mixing rules on thermodynamic property prediction for normal alkanol-hexane binaries, Fluid Phase Equilibria 65 (1991) 73-88.
-
(1991)
Fluid Phase Equilibria
, vol.65
, pp. 73-88
-
-
Trebble, M.A.1
-
11
-
-
0022699554
-
PRSV: An improved Peng-Robinson equation of state for pure compounds and mixtures
-
R. Stryjek, J.H. Vera, PRSV: An improved Peng-Robinson equation of state for pure compounds and mixtures, Can. J. Chem. Eng. 64 (1986) 323-333.
-
(1986)
Can. J. Chem. Eng.
, vol.64
, pp. 323-333
-
-
Stryjek, R.1
Vera, J.H.2
-
12
-
-
0024703945
-
A density correction for the Peng-Robinson equation of state
-
P.M. Mathias, T. Naheiri, E.M. Oh, A density correction for the Peng-Robinson equation of state, Fluid Phase Equilibria 47 (1989) 77-87.
-
(1989)
Fluid Phase Equilibria
, vol.47
, pp. 77-87
-
-
Mathias, P.M.1
Naheiri, T.2
Oh, E.M.3
-
13
-
-
84955811077
-
Second virial coefficients of normal alkanes, linear 1-alkanols and their binaries
-
C. Tsonopoulos, J.H. Dymond, A.M. Szafranski, Second virial coefficients of normal alkanes, linear 1-alkanols and their binaries, Pure Appl. Chem. 61 (1989) 1387-1394.
-
(1989)
Pure Appl. Chem.
, vol.61
, pp. 1387-1394
-
-
Tsonopoulos, C.1
Dymond, J.H.2
Szafranski, A.M.3
-
14
-
-
0003849938
-
Enthalpies of vaporization of organic compounds,/IUPAC
-
Blackwell, Oxford
-
V. Majer, V. Svoboda, Enthalpies of vaporization of organic compounds,/IUPAC, Chem. Data Series No. 32. Blackwell, Oxford, 1985.
-
(1985)
Chem. Data Series No. 32.
, vol.32
-
-
Majer, V.1
Svoboda, V.2
-
15
-
-
0029276992
-
Acoustic determination of ideal-gas heat capacity and second virial coefficients of some refrigerants between 250 and 420 K
-
W. Beckermann, F. Kohler, Acoustic determination of ideal-gas heat capacity and second virial coefficients of some refrigerants between 250 and 420 K, Int. J. Thermophys. 16 (1995) 455-464.
-
(1995)
Int. J. Thermophys.
, vol.16
, pp. 455-464
-
-
Beckermann, W.1
Kohler, F.2
-
16
-
-
0043213877
-
-
Doctoral thesis, University of Rostock
-
T. Lober, p, p, T-Daten und abgeleitete Eigenschaften organischer Daempfe-Experimentelle Untersuchungen an n-Hexan und Benzen, Doctoral thesis, University of Rostock, 1991.
-
(1991)
P, P, T-Daten und Abgeleitete Eigenschaften Organischer Daempfe-Experimentelle Untersuchungen An N-Hexan und Benzen
-
-
Lober, T.1
-
19
-
-
0023409985
-
An interaction model for third virial coefficients which provides simplified equations for mixtures
-
D.R. McGregor, J.C. Holste, P.T. Eubank, K.N. Marsh, K.R. Hall, J. Schouten, An interaction model for third virial coefficients which provides simplified equations for mixtures, Fluid Phase Equilibria 35 (1987) 153-164.
-
(1987)
Fluid Phase Equilibria
, vol.35
, pp. 153-164
-
-
McGregor, D.R.1
Holste, J.C.2
Eubank, P.T.3
Marsh, K.N.4
Hall, K.R.5
Schouten, J.6
-
20
-
-
0000624441
-
Vapor-liquid equilibria at 25°C in the binary mixtures formed by hexane, benzene and ethanol
-
V.C. Smith, R.L. Robinson Jr., Vapor-liquid equilibria at 25°C in the binary mixtures formed by hexane, benzene and ethanol, J. Chem. Eng. Data 15 (1970) 391-395.
-
(1970)
J. Chem. Eng. Data
, vol.15
, pp. 391-395
-
-
Smith, V.C.1
Robinson Jr., R.L.2
-
21
-
-
0017518269
-
Vapor-liquid equilibria at 25°C for nine alcohol-hydrocarbon binary systems
-
S.-C. Hwang, R.L. Robinson Jr., Vapor-liquid equilibria at 25°C for nine alcohol-hydrocarbon binary systems, J. Chem. Eng. Data 22 (1977) 125-319.
-
(1977)
J. Chem. Eng. Data
, vol.22
, pp. 125-319
-
-
Hwang, S.-C.1
Robinson Jr., R.L.2
-
22
-
-
0000131334
-
Combinatorial entropy of mixing molecules that differ in size and shape. a simple approximation for binary and multicomponent mixtures
-
M.D. Donohue, J.M. Prausnitz, Combinatorial entropy of mixing molecules that differ in size and shape. A simple approximation for binary and multicomponent mixtures, Can. J. Chem. 53 (1975) 1586-1592.
-
(1975)
Can. J. Chem.
, vol.53
, pp. 1586-1592
-
-
Donohue, M.D.1
Prausnitz, J.M.2
-
23
-
-
0029328907
-
Equation of state modeling of refrigerant mixtures
-
H. Orbey, S.I. Sandier, Equation of state modeling of refrigerant mixtures, Ind. Eng. Chem. Res. 34 (1995) 2520-2525.
-
(1995)
Ind. Eng. Chem. Res.
, vol.34
, pp. 2520-2525
-
-
Orbey, H.1
Sandier, S.I.2
-
24
-
-
0026867521
-
A theoretically correct mixing rule for cubic equations of state
-
D.S.H. Wong, S.I. Sandler, A theoretically correct mixing rule for cubic equations of state. AlChE J. 38 (1992) 671-680.
-
(1992)
AlChE J.
, vol.38
, pp. 671-680
-
-
Wong, D.S.H.1
Sandler, S.I.2
-
25
-
-
0029386662
-
On the combination of equation of state and excess free energy models
-
H. Orbey, S.I. Sandier, On the combination of equation of state and excess free energy models. Fluid Phase Equilibria 111 (1995)53-70.
-
(1995)
Fluid Phase Equilibria
, vol.111
, pp. 53-70
-
-
Orbey, H.1
Sandier, S.I.2
|