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Partial heat-integrated reactive distillation process for producing n-propyl acetate using a heat exchanger network.
- Source :
-
Energy Sources Part A: Recovery, Utilization & Environmental Effects . 2024, Vol. 46 Issue 1, p2284-2298. 15p. - Publication Year :
- 2024
-
Abstract
- In this work, a partial heat-integrated reactive distillation process was studied to yield n-propyl acetate. To optimize the operating parameters of two distinct processes, the sequential iteration optimization method was employed. The heat exchanger network (HEN) is an effective approach for the heat-integrated design of a distillation process. Compared with the conventional reactive distillation process, the total annual cost, CO2 emissions and total energy consumption of the partial heat-integrated reactive distillation process decreased by 20.7%, 31.1%, and 32.2%, respectively. The thermodynamic efficiencies of reactive distillation process and partial heatintegrated reactive distillation process were 4.33% and 9.86%, respectively. The significance of this paper is crucial in guiding the process of partial heatintegrated reactive distillation for the production of n-propyl acetate. [ABSTRACT FROM AUTHOR]
- Subjects :
- *REACTIVE distillation
*HEAT exchangers
*ENERGY consumption
*DISTILLATION
*ACETATES
Subjects
Details
- Language :
- English
- ISSN :
- 15567036
- Volume :
- 46
- Issue :
- 1
- Database :
- Academic Search Index
- Journal :
- Energy Sources Part A: Recovery, Utilization & Environmental Effects
- Publication Type :
- Academic Journal
- Accession number :
- 176345377
- Full Text :
- https://doi.org/10.1080/15567036.2024.2302960