화학공학소재연구정보센터
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No. Article
1 Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol plus dimethyl carbonate and the pressure dependency of the azeotropic point
Matsuda H, Negishi M, Iino S, Constantinescu D, Kurihara K, Tochigi K, Ochi K, Gmehling J
Fluid Phase Equilibria, 492, 101, 2019
2 SkaSim - Scalable HPC Software for Molecular Simulation in the Chemical Industry
Vrabec J, Bernreuther M, Bungartz HJ, Chen WL, Cordes W, Fingerhut R, Glass CW, Gmehling J, Hamburger R, Heilig M, Heinen M, Horsch MT, Hsieh CM, Hulsmann M, Jager P, Klein P, Knauer S, Koddermann T, Koster A, Langenbach K, Lin ST, Neumann P, Rarey J, Reith D, Rutkai G, Schappals M, Schenk M, Schedemann A, Schonherr M, Seckler S, Stephan S, Stobener K, Tchipev N, Wafai A, Werth S, Hasse H
Chemie Ingenieur Technik, 90(3), 295, 2018
3 Further Development of Modified UNIFAC (Dortmund): Revision and Extension 6 (vol 61, pg 2738, 2016)
Constantinescu D, Gmehling J
Journal of Chemical and Engineering Data, 62(7), 2230, 2017
4 Vapor-Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
Horstmann S, Constantinescu D, Gmehling J
Journal of Chemical and Engineering Data, 62(9), 2776, 2017
5 Present status of the group contribution equation of state VTPR and typical applications for process development
Schmid B, Gmehling J
Fluid Phase Equilibria, 425, 443, 2016
6 Further Development of Modified UNIFAC (Dortmund): Revision and Extension 6
Constantinescu D, Gmehling J
Journal of Chemical and Engineering Data, 61(8), 2738, 2016
7 Measurement, correlation and prediction of isothermal vapor-liquid equilibria of different systems containing vegetable oils
Belting PC, Gmehling J, Bolts R, Rarey J, Ceriani R, Chiavone O, Meirelles AJA
Fluid Phase Equilibria, 395, 15, 2015
8 About "New modified UNIFAC parameters using critically evaluated phase equilibrium data" by Jeong Won Karig, Vladimir Diky, Michael Frenkel [Fluid Phase Equilib. 388 (2015) 128-141]
Gmehling J
Fluid Phase Equilibria, 398, 98, 2015
9 (Vapour plus liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
Bahadur I, Pal A, Gmehling J, Hector T, Tumba K, Singh S, Ebenso EE
Journal of Chemical Thermodynamics, 90, 92, 2015
10 Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
Belting PC, Rarey J, Gmehling J, Ceriani R, Chiavone-Filho O, Meirelles AJA
Fluid Phase Equilibria, 361, 215, 2014