The energy-efficient design based on co-process intensification for the transesterification of hexanol with n-butyl acetate
- DOI
- 10.2991/978-94-6463-415-0_14How to use a DOI?
- Keywords
- process intensification; co-process intensification principle; energy-efficient design; reactive double dividing-wall distillation column; process design
- Abstract
The transesterification of hexanol (HeOH) with n-butyl acetate (BuAc) has a low conversion rate and high energy consumption in reactor-separator system due to its unfavorable reaction kinetics and thermodynamic properties. The conventional reactive distillation column (CRDC) and the reactive single dividing-wall distillation column (R-SDWDC) consider the coupling between the reaction and separation operations, but their inherent structural deficiencies still prevent them from effectively reducing the irreversibility of separation operations. In this work, the recently proposed principle of co-process intensification is adopted for the process synthesis and design. Full consideration is given to process intensification of the remaining separation operations based on the non-sharp separation mode in the reaction column, resulting in a step-by-step derivation of the reactive double dividing-wall distillation column (R-DDWDC). The resultant outcomes indicate that the R-DDWDC is the optimal topological structure for implementing transesterification of HeOH with BuAc. The advantages are certainly attributed to the inclusion of the process intensification between the separation operations and its coordination with the process intensification between the reaction operation and associated separation operations involved. Although the proposed methodology is derived in terms of the transesterification of HeOH with BuAc, it has universal guiding significance for reaction systems with unfavorable kinetics and thermodynamic properties.
- Copyright
- © 2024 The Author(s)
- Open Access
- Open Access This chapter is licensed under the terms of the Creative Commons Attribution-NonCommercial 4.0 International License (http://creativecommons.org/licenses/by-nc/4.0/), which permits any noncommercial use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license and indicate if changes were made.
Cite this article
TY - CONF AU - Hao Li AU - Chenyang Fan AU - Shuaishuai Han AU - Kejin Huang AU - Haisheng Chen PY - 2024 DA - 2024/05/14 TI - The energy-efficient design based on co-process intensification for the transesterification of hexanol with n-butyl acetate BT - Proceedings of the 2023 9th International Conference on Advances in Energy Resources and Environment Engineering (ICAESEE 2023) PB - Atlantis Press SP - 131 EP - 138 SN - 2589-4943 UR - https://doi.org/10.2991/978-94-6463-415-0_14 DO - 10.2991/978-94-6463-415-0_14 ID - Li2024 ER -