Yefei Liu

Dr. Yefei Liu

orcid

Research Focus & Metrics

Academic Career Length

10Years (2017-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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22 March 2017 in The Canadian Journal of Chemical Engineering
Verified
Journal Article
Closed access
PDF file
YHYang Han
Yang Han
YLYefei Liu
Yefei Liu
HJHong Jiang
Hong Jiang
WXWeihong Xing
Weihong Xing
RCRizhi Chen
Rizhi Chen

20 June 2021 in Industrial & Engineering Chemistry Research
Verified
Journal Article
Closed access
HJHong Jiang
Hong Jiang
YLYefei Liu
Yefei Liu
WXWeihong Xing
Weihong Xing
RCRizhi Chen
Rizhi Chen

16 October 2017 in Chemical Engineering & Technology
Verified
Journal Article
Closed access
PDF file
YLYefei Liu
Yefei Liu
YHYang Han
Yang Han
XLXiaoli Li
Xiaoli Li
HJHong Jiang
Hong Jiang
RCRizhi Chen
Rizhi Chen

16 May 2023 in Processes
Verified
Journal Article
Open access
PDF file
WCWeiye Chen
Weiye Chen
ZHZehua Hu
Zehua Hu
Xuechao GaoXuechao Gao
Xuechao Gao
YLYefei Liu
Yefei Liu
The multi-objective optimization of methanol distillation is a critical and complex issue in the methanol industry. The three-column methanol distillation scheme is first simulated with Aspen Plus to provide the initial value of the NSGA-III algorithm. The operating parameters are optimized through the Python-Aspen platform. The total annual cost and CO2 emissions are considered the objective function. A small value of indicator generational distance can be achieved by increasing the number of generations, which is helpful in improving algorithm convergence. The NSGA-III algorithm has good convergence and distribution performance. By comparing the optimized results with the original ones, the total annual cost and CO2 emissions are, respectively, reduced by 5.35% and 12.80% when the operating parameters of the methanol distillation sequence are optimized through NSGA-III. As a result, substantial economic and energy savings can be made, offering great potential to improve the performance of the three-column methanol distillation.

22 March 2018 in Journal of Chemical Technology & Biotechnology
Verified
Journal Article
Closed access
PDF file
YLYefei Liu
Yefei Liu
YHYang Han
Yang Han
XLXiaoli Li
Xiaoli Li
HJHong Jiang
Hong Jiang
RCRizhi Chen
Rizhi Chen

13 June 2022 in Molecules
Verified
Journal Article
Open access
PDF file
ZHZehua Hu
Zehua Hu
PLPeilong Li
Peilong Li
YLYefei Liu
Yefei Liu
Optimal synthesis of distillation sequence is a complex problem in chemical processes engineering, which involves process structure optimization and operation parameters optimization. The study of the synthesis of distillation sequence is a crucial step toward improving the efficiency of chemical processes and reducing greenhouse gas emissions. This work introduced the concept of binary tree to encode the distillation sequence. The performance of the six evolutionary algorithms was evaluated by solving a 14-component distillation sequence synthesis problem. The best algorithm was used to optimize the operation parameters of a triple-column distillation process. The total annual cost and CO2 emissions were considered as the metrics to evaluate the performance of triple-column distillation processes. As a result, NSGA-II-DE was found to be the best one of the six tested evolutionary algorithms. Then, NSGA-II-DE was applied to the distillation sequence optimization to find the best operating parameters, which led to a significant reduction in CO2 emission and total annual costs.