The Effect of the Liquid-Phase Activity Model on the Simulation of Ethyl Acetate Production by Reactive Distillation

2001 ◽  
Vol 40 (16) ◽  
pp. 3639-3646 ◽  
Author(s):  
Huseyin Okur ◽  
Mahmut Bayramoglu
Keyword(s):  
Liquid Phase ◽  
Ethyl Acetate ◽  
Reactive Distillation ◽  
Acetate Production ◽  
Activity Model ◽  
Phase Activity

scholarly journals Multi-Aspect Comparison of Ethyl Acetate Production Pathways: Reactive Distillation Process Integration and Intensification via Mechanical and Chemical Approach

Processes ◽  
2020 ◽  
Vol 8 (12) ◽  
pp. 1618
Author(s):  
Branislav Šulgan ◽  
Juraj Labovský ◽  
Zuzana Labovská
Keyword(s):  
Ethyl Acetate ◽  
Case Studies ◽  
Chemical Reaction ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Process Integration ◽  
Distillation Process ◽  
Acetate Production ◽  
Conventional Process ◽  
Set Up

This paper provides a multi-aspect comparison of selected methods of ethyl acetate production and shows the possibility of further reactive distillation process integration and sophisticated intensification including process stream regeneration. The production pathways were selected with respect to their practical applicability and sufficient experimental and feasibility studies already published. A total of four case studies were designed and compared: conventional process set-up (ethyl acetate is produced in a chemical reactor) is designed as a base case study; reactive distillation with a separation unit is derived from the conventional process set-up. The mechanical and chemical approach to reactive distillation process intensification and integration were assumed: reactive distillation column with a stripper and reactive distillation column with an auxiliary chemical reaction (ethylene oxide hydration). Process models were compiled in the Aspen Plus software. Complex process flowsheets of selected case studies including separation and regeneration were designed and optimized. Three different points of view were applied to evaluate the selected process benefits and drawbacks. Process energy, economy, and safety were assessed. As a result, a reactive distillation column with an auxiliary chemical reaction has been proven to be the most suitable pathway for ethyl acetate production assuming all three evaluated aspects.

scholarly journals Multi-Objective Assessment of Heat Pump-Assisted Ethyl Acetate Production

Processes ◽  
2021 ◽  
Vol 9 (8) ◽  
pp. 1380
Author(s):  
Branislav Šulgan ◽  
Juraj Labovský ◽  
Miroslav Variny ◽  
Zuzana Labovská
Keyword(s):  
Ethyl Acetate ◽  
Heat Pump ◽  
Distillation Column ◽  
Reactive Distillation ◽  
Process Models ◽  
Final Decision ◽  
Acetate Production ◽  
Separation Unit ◽  
Multi Objective ◽  
Conventional Process

Multi-objective (energy–economic–safety) assessment of ethyl acetate production involving a heat pump is presented in this paper. The heat pump is designed to intensify ethyl acetate separation and to reduce the total operating cost. Two ethyl acetate production pathways are upgraded using a heat pump, conventional process and reactive distillation column with a separation unit. Detailed process models including the heat pump environment have been compiled and optimized in the Aspen Plus software. Both benefits and drawbacks of including the heat pump in the processes are evaluated using three different points of view: process energy, economics, and safety. As a result, using a heat pump is highly recommended in both conventional process and reactive distillation column with a separation unit. As a higher level of process integration is achieved using a heat pump, economic aspects are improved; however, safety aspects deteriorate. The final decision on the suitability of using a heat pump depends on whether it is proposed for an existing plant, or a completely new plant is designed. In a new plant, the concept of a thermally coupled process (reactive distillation column with a stripper column) has been proven to be the most promising.

Reesterification of ethyl acetate by propanol catalysed by glycidyl methacrylate copolymers containing sulphonic acid groups

1981 ◽  
Vol 46 (8) ◽  
pp. 1941-1946 ◽  
Author(s):  
Karel Setínek
Keyword(s):  
Liquid Phase ◽  
Ethyl Acetate ◽  
Kinetic Study ◽  
Gas Phase ◽  
Nonlinear Regression ◽  
Kinetic Data ◽  
Glycidyl Methacrylate ◽  
Kinetic Equations ◽  
Methacrylate Copolymers ◽  
Styrene Divinylbenzene

A series of differently crosslinked macroporous 2,3-epoxypropyl methacrylate-ethylenedimethacrylate copolymers with chemically bonded propylsulphonic acid groups were used as catalysts for the kinetic study of reesterification of ethyl acetate by n-propanol in the liquid phase at 52 °C and in the gas phase at 90 °C. Analysis of kinetic data by the method of nonlinear regression for a series of equations of the Langmuir-Hinshelwood type showed that kinetic equations which describe best the course of the reaction are the same as for the earlier studied sulphonated macroporous styrene-divinylbenzene copolymers. Compared types of catalysts differ, however, in the dependence of their activity on the degree of crosslinking of the copolymer used.

scholarly journals Improving Ethyl Acetate Production in Baijiu Manufacture by Wickerhamomyces anomalus and Saccharomyces cerevisiae Mixed Culture Fermentations

2019 ◽  
Vol 2019 ◽  
pp. 1-11 ◽  
Author(s):  
Guangsen Fan ◽  
Chao Teng ◽  
Dai Xu ◽  
Zhilei Fu ◽  
Pengxiao Liu ◽  
...  
Keyword(s):  
Saccharomyces Cerevisiae ◽  
Ethyl Acetate ◽  
Mixed Culture ◽  
Nutrient Competition ◽  
Acetate Production ◽  
Mixed Fermentation ◽  
Wickerhamomyces Anomalus ◽  
Flavor Perception ◽  
Positive Effect

Ethyl acetate content has strong influence on the style and quality of Baijiu. Therefore, this study investigated the effect of Saccharomyces cerevisiae Y3401 on the production of ethyl acetate by Wickerhamomyces anomalus Y3604. Analysis of cell growth showed that Y3401 influences Y3604 by nutrient competition and inhibition by metabolites, while the effect of Y3604 on Y3401 was mainly competition for nutrients. Mixed fermentation with two yeasts was found to produce more ethyl acetate than a single fermentation. The highest yield of ethyl acetate was 2.99 g/L when the inoculation ratio of Y3401:Y3604 was 1:2. Synergistic fermentation of both yeasts improved ethyl acetate production and increased the content of other flavor compounds in liquid and simulated solid-state fermentation for Baijiu. Saccharomyces cerevisiae had a positive effect on ethyl acetate production in mixed culture and provides opportunities to alter the aroma and flavor perception of Baijiu.

The use of dilute acetic acid for butyl acetate production in a reactive distillation: Simulation and control studies

2008 ◽  
Vol 25 (6) ◽  
pp. 1252-1266 ◽  
Author(s):  
Amornchai Arpornwichanop ◽  
Chantarawadee Wiwittanaporn ◽  
Suthida Authayanun ◽  
Suttichai Assabumrungrat
Keyword(s):  
Acetic Acid ◽  
Butyl Acetate ◽  
Reactive Distillation ◽  
Acetate Production ◽  
Simulation And Control ◽  
Distillation Simulation ◽  
And Control
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