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Thermodynamics and separation process for quaternary acrylic systems
38/38 checkable references clean · checked 2026-07-22
Every reference with a DOI in the deposited reference list resolved to a known work in Crossref or DataCite at the dated check, and none carried a retraction, withdrawal, or removal notice.
1 without a DOI — not checked. A reference deposited without a DOI is never matched by title or guessed at; it stays outside the checked set, and this line discloses that.
The 38 checked references that resolve
resolves10.1039/C5RA05133A
Preparation of Cs–La–Sb/SiO
<sub>2</sub>
catalyst and its performance for the synthesis of methyl acrylate by aldol condensation
resolves10.1016/j.apcata.2010.02.002
Performance of WO -added Mo–V–Te–Nb–O catalysts in the partial oxidation of propane to acrylic acid
resolves10.1002/cctc.201402608
The M1 Phase of MoVTeNbO as a Catalyst for Olefin Metathesis and Isomerization
resolves10.1021/ie501968g
Thermodynamics in Separation for the Ternary System 1,2-Ethanediol + 1,2-Propanediol + 2,3-Butanediol
resolves10.1021/ie9701175
Correlation of Vapor−Liquid Equilibrium Data for Methyl Acetate−Methanol−Water−Acetic Acid Mixtures
resolves10.1021/acs.iecr.5b01422
Reaction of Formalin with Acetic Acid over Vanadium–Phosphorus Oxide Bifunctional Catalyst
resolves10.1021/ie500371c
Catalysts, Kinetics, and Reactive Distillation for Methyl Acetate Synthesis
resolves10.1002/aic.10657
Structure, dynamics and thermodynamics in complex systems: Theoretical challenges and opportunities
resolves10.1016/j.fluid.2006.06.005
Isothermal vapour–liquid equilibrium with chemical reaction in the quaternary water+methanol+acetic acid+methyl acetate system, and in five binary subsystems
resolves10.1016/0378-3812(95)02728-W
LLE data for the systems water + (methanol or ethanol) + n-amyl acetate
resolves10.1021/je100077z
Liquid−Liquid Equilibrium of Ternary and Quaternary Systems Including Methyl Acetate, Benzene, Toluene, and Water at 283.2 K under Atmosphere
resolves10.1002/aic.14432
Separation of methanol‐tetrahydrofuran mixtures by heteroazeotropic distillation and pervaporation
resolves10.1002/aic.12677
A framework for synthesizing the optimal separation process of azeotropic mixtures
resolves10.1021/ie950049r
Global Stability Analysis and Calculation of Liquid−Liquid Equilibrium in Multicomponent Mixtures
resolves10.1021/je050374d
High-Pressure Phase Equilibrium for Ethylene + Methanol at 278.15 K and 283.65 K
resolves10.1021/je500160t
Investigation on Isobaric Vapor–Liquid Equilibrium for Water + Acetic Acid + <i>sec</i>-Butyl Acetate
resolves10.1002/aic.690440407
Improved direct and indirect systems of columns for ternary distillation
resolves10.1016/j.cherd.2008.07.017
Environmentally conscious design of chemical processes and products: Multi-optimization method
resolves10.1002/aic.690440616
Structure of Distillation Regions for Multicomponent Azeotropic Mixtures
resolves10.1021/je100932m
Vapor−Liquid Equilibrium and Liquid−Liquid Equilibrium of Methyl Acetate + Methanol + 1-Ethyl-3-methylimidazolium Acetate
resolves10.1021/je00017a071
Isobaric Vapor-Liquid Equilibrium for Methyl Acetate + Methanol + Water at 101.3 kPa
resolves10.1016/S0378-3812(97)00054-X
Isobaric vapor-liquid equilibria of the methanol, methyl acetate and methyl acrylate system at atmospheric pressure
resolves10.1039/C5GC00081E
An ionic liquid extraction process for the separation of indole from wash oil
resolves10.1002/aic.13731
Phase equilibria (LLE and VLE) of refining operations for enzymatic biodiesel production via quantum mechanical COSMO‐RS method
resolves10.1021/ie5013079
Process Simulation of Sulfuric Acid Recovery by Azeotropic Distillation: Vapor–Liquid Equilibria and Thermodynamic Modeling
resolves10.1021/i200020a020
Prediction of vapor-liquid equilibrium from ternary liquid-liquid equilibrium data
resolves10.1002/aic.690140124
Local compositions in thermodynamic excess functions for liquid mixtures
resolves10.1016/j.fluid.2014.06.025
Isobaric vapor–liquid equilibrium of ethanenitrile + water + 1,2-ethanediol + 1-ethyl-3-methylimidazolium chloride
resolves10.1021/je010015s
Effects of Lithium Nitrate on the Vapor−Liquid Equilibria of Methyl Acetate + Methanol and Ethyl Acetate + Ethanol
resolves10.1016/j.fluid.2004.05.009
Measurement and correlation of vapor–liquid equilibria and excess enthalpies of binary systems containing ionic liquids and hydrocarbons
resolves10.1016/j.fluid.2004.11.010
Measurement and prediction of vapor–liquid equilibria of ternary systems containing ionic liquids
resolves10.1021/i260068a028
Application of the UNIQUAC Equation to Calculation of Multicomponent Phase Equilibria. 1. Vapor-Liquid Equilibria
resolves10.1016/j.fluid.2007.05.026
Liquid–liquid equilibria for the quaternary system methyl isobutyl ketone–water–phenol–hydroquinone
resolves10.1016/j.fluid.2004.02.008
Interaction parameters for multi-component aromatic extraction with sulfolane
resolves10.1016/S0378-3812(00)00325-3
Regression of binary interaction parameters for thermodynamic models using an inside-variance estimation method (IVEM)
The 1 reference without a DOI — listed, not checked
no DOI — not checkedAzeotropic phenomenon in the five components mixture of Alcohol - Acrylate - H2O - β ether propionate - Acrylic acid
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