1 |
涂飞, 青红英, 罗雄麟, 等. 乙炔加氢反应器的先进控制(Ⅰ): 动态机理模型的建立[J]. 化工自动化及仪表, 2003, 30(1): 20-24.
|
|
Tu F, Qing H Y, Luo X L, et al. Advanced process control of acetylene hydrogenation reactor (Ⅰ): Construct dynamic model [J]. Control and Instruments in Chemical Industry, 2003, 30(1): 20-24.
|
2 |
Weiss G. Modeling and control of the acetylene converter [J]. Journal of Process Control, 1996, 6(1): 7-15.
|
3 |
Gobbo R, Soares R P, Lansarin M A, et al. Modeling, simulation, and optimization of a front-end system for acetylene hydrogenation reactors [J]. Brazilian Journal of Chemical Engineering, 2004, 21(4): 545-556.
|
4 |
Szukiewicz M, Kaczmarski K, Petrus R. Modeling of fixed-bed reactor: two models of industrial reactor for selective hydrogenation of acetylene [J]. Chemical Engineering Science, 1998, 53(1): 149-155.
|
5 |
罗雄麟, 刘建新, 许锋, 等. 乙炔加氢反应器二维非均相机理动态建模及分析[J]. 化工学报, 2008, 59(6): 1454-1461.
|
|
Luo X L, Liu J X, Xu F, et al. Hydrogenation, two-dimensional dynamic modeling and analysis of acetylene hydrogenation reactor [J]. Journal of Chemical Industry and Engineering (China), 2008, 59(6): 1454-1461.
|
6 |
田亮, 蒋达, 钱锋. 乙炔加氢反应系统操作优化策略[J]. 化工学报, 2015, 66(1): 373-377.
|
|
Tian L, Jiang D, Qian F. Reactor system switch strategy for acetylene hydrogenation process [J]. CIESC Journal, 2015, 66(1): 373-377.
|
7 |
田亮, 蒋达, 钱锋. 催化剂失活条件下的碳二加氢反应器模拟与优化[J]. 化工学报, 2012, 63(1): 185-192.
|
|
Tian L, Jiang D, Qian F. Simulation and optimization of acetylene converter with decreasing catalyst activity [J]. CIESC Journal, 2012, 63(1): 185-192.
|
8 |
Luo X L, Xia C K, Sun L. Margin design, online optimisation, and control approach of a heat exchanger network with bypasses [J]. Comput. Chem. Eng., 2013, 53(11): 102-121.
|
9 |
谢府命, 许锋, 梁志珊, 等. 乙炔加氢反应器全周期操作优化[J]. 化工学报, 2018, 69(3): 1081-1091.
|
|
Xie F M, Xu F, Liang Z S, et al. Full-cycle operation optimization of acetylene hydrogenation reactor [J]. CIESC Journal, 2018, 69(3): 1081-1091.
|
10 |
Narraway L T, Perkins J D. Selection of process control structure based on linear dynamic economics [J]. Ind. Eng. Chem. Res., 1993, 32(11): 2681-2692.
|
11 |
Narraway L T, Perkins J D, Barton G W. Interaction between process design and process control: economic analysis of process dynamics [J]. J. Process Contr., 1991, 1(5): 243-250.
|
12 |
Bahri P A, Romagnoli J A, Bandoni J A, et al. Back-off calculations in optimising control: a dynamic approach [J]. Comput. Chem. Eng., 1995, 19: 699-708.
|
13 |
Figueroa J L, Bahri P A, Bandoni J A, et al. Economic impact of disturbances and uncertain parameters in chemical processes - a dynamic back-off analysis [J]. Comput. Chem. Eng., 1996, 20(4): 453-461.
|
14 |
Kookos I K, Perkins J D. Control structure selection based on economics: generalization of the back-off methodology [J]. AIChE J., 2016, 62(9): 3056-3064.
|
15 |
Mehta S, Ricardez-Sandoval L A. Integration of design and control of dynamic systems under uncertainty: a new back-off approach [J]. Ind. Eng. Chem. Res., 2016, 55(2): 485-498.
|
16 |
Rafiei-Shishavan M, Mehta S, Ricardez-Sandoval L A. Simultaneous design and control under uncertainty: a back-off approach using power series expansions [J]. Comput. Chem. Eng., 2017, 99: 66-81.
|
17 |
Galvanin F, Barolo M, Bezzo F, et al. A backoff strategy for model-based experiment design under parametric uncertainty [J]. AIChE J., 2009, 56(8): 2088-2102.
|
18 |
Shi J, Biegler L T, Hamdan I, et al. Optimisation of grade transitions in polyethylene solution polymerization process under uncertainty [J]. Comput. Chem. Eng., 2016, 95: 260-279.
|
19 |
Koller R W, Ricardez-Sandoval L A, Biegler L T. Stochastic back-off algorithm for simultaneous design, control and scheduling of multi-product systems under uncertainty [J]. AIChE J., 2018, 64(13): 2379-2389.
|
20 |
Xu F, Luo X L, Wang R. Design margin and control performance analysis of a fluid catalytic cracking unit regenerator under model predictive control [J]. Industrial & Engineering Chemistry Research, 2014, 53(37): 14339-14350.
|
21 |
罗雄麟, 夏车奎, 孙琳. 有旁路换热网络全周期节能的动态优化控制实现方法[J]. 化工学报, 2013, 64(4): 1340-1350.
|
|
Luo X L, Xia C K, Sun L. A dynamic optimization control approach of life cycle energy saving for heat exchanger network with bypasses [J]. CIESC Journal, 2013, 64(4): 1340-1350.
|
22 |
夏车奎, 罗雄麟, 孙琳. 基于全周期节能的有旁路换热网络裕量优化设计[J]. 化工学报, 2012, 63(5): 1449-1458.
|
|
Xia C K, Luo X L, Sun L. Margin optimal design of heat exchanger network with bypasses based on life cycle energy saving [J]. CIESC Journal, 2012, 63(5): 1449-1458.
|
23 |
Xu F, Jiang H R, Wang R, et al. Influence of design margin on operation optimization and control performance of chemical processes [J]. Chinese Journal of Chemical Engineering, 2014, 22(1): 51-58.
|
24 |
Xie F M, Xu F, Liang Z S, et al. Full cycle dynamic optimisation maintaining the operation margin of acetylene hydrogenation fixed-bed reactor[J]. J. Taiwan Inst. Chem. E, 2020, 108: 29-42.
|
25 |
Pollard G P, Sargent R W H. Off line computation of optimum controls for a plate distillation column [J]. Automatica, 1970, 6(1): 59-76.
|
26 |
Morison K R, Sargent R W H. Optimization of multistage processes described by differential-algebraic equations [C]// Proceedings of the Fourth IIMAS. Berlin Heidelberg: Springer, 1984: 86-102.
|
27 |
Teo K L, Jennings L S, Lee H W J, et al. The control parameterization enhancing transform for constrained optimal control problems [J]. Journal of the Australian Mathematical Society, 1999, 40(3): 314-335.
|
28 |
Binder T, Cruse A, Villar C A C, et al. Dynamic optimization using a wavelet based adaptive control vector parameterization strategy [J]. Comput. Chem. Eng., 2000, 24(2): 1201-1207.
|
29 |
Chen T W C, Vassiliadis V S. Inequality path constraints in optimal control: a finite iteration ε-convergent scheme based on pointwise discretization [J]. J. Process Contr., 2005, 15(3): 353-362.
|
30 |
Hartwich A, Schlegel M, Würth L, et al. Adaptive control vector parameterization for nonlinear model-predictive control [J]. International Journal of Robust and Nonlinear Control, 2008, 18(8): 845-861.
|
31 |
Chen X, Du W L, Tianfield H, et al. Dynamic optimization of industrial processes with nonuniform discretization-based control vector parameterization [J]. IEEE T. Autom. Sci. Eng., 2014, 11(4): 1289-1299.
|