1 |
A combination of low-temperature reactive and extractive distillation for methoxy-2-propyl acetate synthesis and separation process: simulations and experiments Wang BH, Cai XL, Lu L, Ma J Journal of Chemical Technology and Biotechnology, 94(10), 3292, 2019 |
2 |
Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate plus propyl acetate plus dimethyl sulfoxide and binary systems of ethyl acetate plus dimethyl sulfoxide and propyl acetate plus dimethyl sulfoxide at 101.3 kPa Wang YL, Zhang HR, Pan XS, Yang JW, Cui PZ, Zhang FK, Gao J Journal of Chemical Thermodynamics, 135, 116, 2019 |
3 |
Energy-saving hybrid processes combining pressure-swing reactive distillation and pervaporation membrane for n-propyl acetate production Wang C, Zhang ZS, Zhang XK, Gao J, Stewart B Separation and Purification Technology, 221, 1, 2019 |
4 |
Liquid-liquid equilibrium of the ternary system water plus propargyl alcohol plus n-propyl acetate Sun C, Cao W, Wu J, Hu XP Fluid Phase Equilibria, 432, 85, 2017 |
5 |
Optimization of Enzymatic Synthesis of n-Propyl Acetate (Fruit Flavor Ester) - Effect of the Support on the Properties of Biocatalysts Corradini MCC, Gomes RAB, Luiz JHH, Mendes AA Chemical Engineering Communications, 203(11), 1432, 2016 |
6 |
Measurement and modelization of VLE of binary mixtures of propyl acetate, butyl acetate or isobutyl acetate with methanol at pressure of 0.6 MPa Susial P, Garcia D, Susial R, Clavijo YC, Martin A Chinese Journal of Chemical Engineering, 24(5), 630, 2016 |
7 |
Application of the UNIFAC models for prediction and description of excess molar enthalpies for binary mixtures of n-propanol, acetic acid, n-propyl acetate, and water Letyanina I, Tsvetov N, Toikka A Fluid Phase Equilibria, 427, 202, 2016 |
8 |
Isobaric (vapor plus liquid) equilibrium for n-propyl acetate with 1-butanol or 2-butanol. Binary mixtures at 0.15 and 0.6 MPa Susial P, Rodriguez-Henriquez JJ, Castillo VD, Estupinan E, Apolinario JC, Susial R Fluid Phase Equilibria, 385, 196, 2015 |
9 |
Solubility, liquid-liquid equilibrium and critical states for the system acetic acid plus n-propanol plus n-propyl acetate + water at 293.15 K and 303.15 K Toikka M, Samarov A, Toikka A Fluid Phase Equilibria, 375, 66, 2014 |
10 |
Excess molar enthalpies for binary mixtures of n-propanol, acetic acid, and n-propyl acetate at 313.15 K and atmospheric pressure Letyanina I, Tsvetov N, Zvereva I, Samarov A, Toikka A Fluid Phase Equilibria, 381, 77, 2014 |