Xuechao Gao
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Xuechao Gao has a total of 132 co-authors. Here are the top co-authors by number of shared publications:
Xuehong Gu
14 shared publications- Suresh K. Bhatia
The University of Queensland
8 shared publications - Xuehong Gu
State Key Laboratory of Materials‐Oriented Chemical Engineering, College of Chemical Engineering Nanjing Tech University Nanjing China
8 shared publications Xiang Jin
7 shared publications- João Carlos Diniz da Costa
The University of Queensland, FIM2Lab—Functional Interfacial Materials and Membranes Laboratory, School of Chemical Engineering, Brisbane, QLD 4072, Australia
6 shared publications Chao Liu
Key Laboratory of Low-grade Energy Utilization Technologies and Systems, Ministry of Education, School of Energy and Power Engineering, Chongqing University, Chongqing 400044, China
5 shared publications
Latest Publications
- 12 April 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 750
Ag+-modulated T-type zeolite membrane with improved pervaporation stability for N, N-dimethylacetamide dehydration
- 12 April 2026
- Published by Elsevier in Journal of Membrane Science
- Vol. 750
Ag+-modulated T-type zeolite membrane with improved pervaporation stability for N, N-dimethylacetamide dehydration
- 27 January 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 720
A two-dimensional mathematical model for CO2/CH4 separation through high-permeable hollow fiber DD3R zeolite membranes
- 27 January 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 720
A two-dimensional mathematical model for CO2/CH4 separation through high-permeable hollow fiber DD3R zeolite membranes
- 22 January 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 720
Optimization of internal coupling process of NaA zeolite membrane in distillation column to separate ethanol/water mixture
- 22 January 2025
- Published by Elsevier in Journal of Membrane Science
- Vol. 720
Optimization of internal coupling process of NaA zeolite membrane in distillation column to separate ethanol/water mixture
- 19 October 2024
- Published by Elsevier in Chinese Journal of Chemical Engineering
- Vol. 77, 66-80
CPAM-assisted synthesis of NaA zeolite membrane on macroporous mullite hollow fiber for ethanol dehydration by pervaporation
- 19 October 2024
- Published by Elsevier in Chinese Journal of Chemical Engineering
- Vol. 77, 66-80
CPAM-assisted synthesis of NaA zeolite membrane on macroporous mullite hollow fiber for ethanol dehydration by pervaporation
- 1 September 2024
- Published by Springer Nature in Russian Chemical Bulletin
- Vol. 73 (9) , 2572-2582
Determination of intracrystalline diffusion coefficient of organic solvents in metal organic framework adsorbents by zero-length column method
- 1 September 2024
- Published by Springer Nature in Russian Chemical Bulletin
- Vol. 73 (9) , 2572-2582
Determination of intracrystalline diffusion coefficient of organic solvents in metal organic framework adsorbents by zero-length column method
- 28 May 2024
- Published by Elsevier in Journal of Membrane Science
- Vol. 706
Analysis of the gas transport resistance of CO2 and CH4 through ultra-thin DD3R zeolite membrane
- 28 May 2024
- Published by Elsevier in Journal of Membrane Science
- Vol. 706
Analysis of the gas transport resistance of CO2 and CH4 through ultra-thin DD3R zeolite membrane
- 3 April 2024
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 63 (15) , 6711-6724
A Novel Internal Coupling Process of a T-type Zeolite Membrane in a Distillation Column to Separate the PM/H2O Mixture
- 3 April 2024
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 63 (15) , 6711-6724
A Novel Internal Coupling Process of a T-type Zeolite Membrane in a Distillation Column to Separate the PM/H2O Mixture
- Open Access
Simulation and Multi-Objective Optimization of Three-Column Double-Effect Methanol Distillation by NSGA-III Algorithm
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.
Open AccessSimulation and Multi-Objective Optimization of Three-Column Double-Effect Methanol Distillation by NSGA-III Algorithm
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.