
FOLLOWUS
Jiangsu Key Laboratory of Advanced Catalytic Materials and Technology, School of Petrochemical Engineering, Changzhou University, Changzhou 213164, China
Corresponding authors. E-mail addresses: lijinlong@cczu.edu.cn (J. Li)
Corresponding authors. E-mail addresses: huagonglou508@126.com (Q. Ye).
收稿:2025-07-14,
修回:2025-09-18,
录用:2025-09-19,
网络首发:2025-10-30,
纸质出版:2026-02
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Zhang Ruimin, Yang Shuang, Li Jinlong, 等. Sustainability evaluation of novel side-stream extractive distillation incorporating intermediate reboiler process for recovering ethyl acetate and methanol from wastewater based on multi-objective optimization[J]. 中国化学工程学报(英文), 2026,90(2):232-248.
Zhang Ruimin, Yang Shuang, Li Jinlong, et al. Sustainability evaluation of novel side-stream extractive distillation incorporating intermediate reboiler process for recovering ethyl acetate and methanol from wastewater based on multi-objective optimization[J]. Chinese Journal of Chemical Engineering, 2026, 90(2): 232-248.
Zhang Ruimin, Yang Shuang, Li Jinlong, 等. Sustainability evaluation of novel side-stream extractive distillation incorporating intermediate reboiler process for recovering ethyl acetate and methanol from wastewater based on multi-objective optimization[J]. 中国化学工程学报(英文), 2026,90(2):232-248. DOI:
Zhang Ruimin, Yang Shuang, Li Jinlong, et al. Sustainability evaluation of novel side-stream extractive distillation incorporating intermediate reboiler process for recovering ethyl acetate and methanol from wastewater based on multi-objective optimization[J]. Chinese Journal of Chemical Engineering, 2026, 90(2): 232-248. DOI:
Although side-stream extractive d
istillation (SED) is widely applied in azeotropic mixture separation due to its high efficiency and energy-saving advantages
the use of expensive high-pressure steam increases economic costs. The introduction of intermediate reboiler (IR) can reduce the consumption of high-pressure steam and thus reduce the operating cost. This work selects the extractive distillation process
using dimethyl sulfoxide (DMSO) as the solvent to separate ethyl acetate and methanol from wastewater. Based on the system characteristics
two SED processes are designed: SED-1 process directly obtains high-purity DMSO from the bottom of the SED column
whereas SED-2 process obtains a DMSO/water mixture at the bottom. To reduce high-pressure steam requirements
an IR is incorporated
leading to the proposal of SED-IR-1 and SED-IR-2 processes. Finally
heat-integrated processes (H-SEDIR-1 and H-SED-IR-2) are proposed based on the optimal SED-IR-1 and SED-IR-2 processes
which utilized the solvent stream waste heat to heat the IR to further reduce the energy consumption and operating cost. The results demonstrate that the H-SED-IR-1 process exhibits optimal economic performance with a 26.19% reduction in total annual cost compared with the conventional extractive distillation (CED) process
while the innovative H-SED-IR-2 process shows outstanding environmental benefits
achieving 38.78% and 39.97% reductions in CO
2
emissions and entropy generation
respectively
compared to the CED process.
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