
FOLLOWUS
Engineering Research Center of Preparation Technology of Ultra-Pure Chemicals for Integrated Circuits, Ministry of Education, Beijing University of Chemical Technology, Beijing 100029, China
State Key Laboratory of Chemical Resource Engineering, Beijing University of Chemical Technology, Beijing 100029, China
School of Materials Science and Engineering, Beihang University, Beijing 100191, China
Corresponding authors. E-mail addresses: buctlqs@126.com(Q. Li)
fengweiying@buaa.edu.cn(W. Feng)
2022500026@buct.edu.cn(H. Zhao).
收稿:2025-06-26,
修回:2025-08-03,
录用:2025-08-06,
网络首发:2025-09-01,
纸质出版:2026-01
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Feng Xuefeng, Lu Shuaishuai, Du Xuan, 等. Design and optimization of a high-efficiency distillation process for cellulosic fuel ethanol integrated with thermal coupling and molecular sieve adsorption[J]. 中国化学工程学报(英文), 2026,89(1):13-24.
Feng Xuefeng, Lu Shuaishuai, Du Xuan, et al. Design and optimization of a high-efficiency distillation process for cellulosic fuel ethanol integrated with thermal coupling and molecular sieve adsorption[J]. Chinese Journal of Chemical Engineering, 2026, 89(1): 13-24.
Feng Xuefeng, Lu Shuaishuai, Du Xuan, 等. Design and optimization of a high-efficiency distillation process for cellulosic fuel ethanol integrated with thermal coupling and molecular sieve adsorption[J]. 中国化学工程学报(英文), 2026,89(1):13-24. DOI:
Feng Xuefeng, Lu Shuaishuai, Du Xuan, et al. Design and optimization of a high-efficiency distillation process for cellulosic fuel ethanol integrated with thermal coupling and molecular sieve adsorption[J]. Chinese Journal of Chemical Engineering, 2026, 89(1): 13-24. DOI:
To address the challenges of high energy consumption and prominent costs in the traditional threecolumns distillation process for cellulosic fuel ethanol
a distillation—molecular sieve coupling separation process is proposed. This process integrates a three-column (crude distillation column
first distillation column
second distillation column) system with a 3A molecular sieve adsorption deep dehydration unit. A thermal coupling network is constructed
via
differential pressure design (steam from medium/high-pressure columns as mutual heat sources
reboiler l
iquid waste heat for feed preheating)
and molecular sieve adsorption conditions are optimized. The study first performs a thermodynamic consistency test on the ethanol—water system
determines optimal non-random two-liquid (NRTL) model binary interaction parameters
via
experimental data regression for Aspen Plus simulation. Aiming at minimum total annual cost (TAC)
Aspen Plus is used to optimize process parameters (theoretical tray number
feed location
reflux ratio
side-draw position
etc
.). Economic analysis shows this process reduces CO
2
emission costs by 27.56%
TAC by 15.58% (to 5.123 × 10
6
USD·a
- 1
)
and increases ethanol purity to >99.6%
providing an effective solution for green
efficient separation.
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