| 1 |
Multi-input single-output control for extending the operating range: Generalized split range control using the baton strategy
Reyes-Lua A, Skogestad S
Journal of Process Control, 91, 1, 2020 |
| 2 |
Potential of carbon dioxide transcritical power cycle waste-heat recovery systems for heavy-duty truck engines
Li XY, Tian H, Shu GQ, Zhao MR, Markides CN, Hu C
Applied Energy, 250, 1581, 2019 |
| 3 |
Manipulation and Control of Structure and Size of Inorganic Nanomaterials in Microchemical Systems
Luo GS, Du L, Wang YJ, Wang K
Chemical Engineering & Technology, 42(10), 1996, 2019 |
| 4 |
Optimization and control of a reactive and extractive distillation process for the synthesis of isopropyl acetate
Zhang QR, Yan S, Li HY, Xu PF
Chemical Engineering Communications, 206(5), 559, 2019 |
| 5 |
Optimization of decanter temperature in separating partially miscible homoazeotrope to reduce cost and energy consumption
Li X, Wang S, Wang YL, Cui PZ, Xu DM, Zhu ZY
Journal of Chemical Technology and Biotechnology, 94(6), 1998, 2019 |
| 6 |
Accounting for dynamics in self-optimizing control
Klemets JRA, Hovd M
Journal of Process Control, 76, 15, 2019 |
| 7 |
Self-optimizing control of an LNG liquefaction plant
Verheyleweghen A, Jaschke J
Journal of Process Control, 74, 63, 2019 |
| 8 |
Separation of ternary mixture with double azeotropic system by a pressure-swing batch distillation integrated with quasi-continuous process
Li X, Yang X, Wang S, Yang JW, Wang LL, Zhu ZY, Cui PZ, Wang YL, Gao J
Process Safety and Environmental Protection, 128, 85, 2019 |
| 9 |
Control of an energy-saving side-stream extractive distillation process with different disturbance conditions
Ma K, Yu MX, Dai Y, Ma YX, Gao J, Cui PZ, Wang YL
Separation and Purification Technology, 210, 195, 2019 |
| 10 |
Controllability comparisons of a reactive dividing-wall column for transesterification of methyl acetate and isopropanol
Feng SY, Ye Q, Xia H, Chen JX, Liu T, Wu WZ
Chemical Engineering Research & Design, 132, 409, 2018 |
