Exploring the impact of side‐reactions on triple‐column reactive‐extractive distillation
- 30 April 2024
- journal article
- research article
- Published by Wiley in Journal of Chemical Technology & Biotechnology
- Vol. 99 (7) , 1493-1503
Abstract
Background: Presently, there are no studies that examine the impact of side‐reactions of ethylene oxide hydration on triple‐column reactive‐extractive distillation (TC‐RED). This study addressed this gap by investigating how these side‐reactions influence the energy consumption, total annual cost (TAC), and CO2 emission of the TC‐RED process. Two case studies, which involve the ternary separation of tetrahydrofuran (THF)/ethanol (ETOH)/water and ethyl acetate (EA)/ETOH/water were conducted here.Results: Case studies 1 and 2 showed significant increase in energy consumption (39.68% and 16.56%), TAC (65.57% and 47.88%) and CO2 emission (21.15% and 12.89%) resulting from side‐reactions. The increase in energy consumption, TAC, and CO2 emission is primarily a consequence of the high boiling point of higher glycol product derivatives, altered chemical equilibrium behavior and increased reactant flowrates, which necessitate larger equipment sizes and incur higher capital costs. Notwithstanding this, TC‐RED with side‐reactions still outperforms pressure swing distillation (PSD) for separation of THF/ETOH/water and extractive distillation (ED) for separation of EA/ETOH/water. However, it falls short of double‐column reactive‐extractive distillation (DC‐RED) owing to the need for an additional column.Conclusion: Our study highlights the importance of considering side‐reactions in TC‐RED during process design. Although the decline in performance is a result of the additional complexities brought by side‐reactions, it is important to emphasize that the primary takeaway of this study is that the system model is more realistic. By incorporating side‐reactions into the simulation, we can model the system more comprehensively, providing future researchers with an opportunity to explore and address potential issues resulting from side‐reactions. © 2024 Society of Chemical Industry (SCI).Keywords
Funding Information
- Swinburne University of Technology Sarawak Campus (Account number: 9‐1372)
- Sunway University (GRTIN‐KSGS(02)‐DEN‐02‐2023)
This publication has 29 references indexed in Scilit:
- A perspective on the inevitable side reactions in ethylene-glycol based reactive-extractive distillationChemical Engineering Journal, 2023
- Are process-intensified extractive distillation always energetically more efficient?Chemical Engineering and Processing - Process Intensification, 2022
- Design and optimisation of novel hybrid side-stream reactive-extractive distillation for recovery of isopropyl alcohol and ethyl acetate from wastewaterChemical Engineering Journal, 2022
- Effect of side reactions in hybrid distillation system: Parallel production of ethyl acetate and glycolsChemical Engineering Journal, 2022
- Design and control of pressure‐swing distillation for separating ternary systems with three binary minimum azeotropesAIChE Journal, 2019
- Development of a techno‐economic framework for natural gas dehydration via absorption using Tri‐Ethylene Glycol: a comparative study on conventional and stripping gas dehydration processesJournal of Chemical Technology & Biotechnology, 2018
- Innovative Ethylene Glycol Diacetate synthesis process in a single reactive distillation columnChemical Engineering and Processing - Process Intensification, 2016
- Distillation Design and Control Using Aspen™ Simulation2013
- Reactive distillation design with considerations of heats of reactionAIChE Journal, 2006
- Synthesis of nonequilibrium reactive distillation processes by MINLP optimizationAIChE Journal, 1994