Control of Quaternary Ideal Endothermic Reactive Distillation with and without Internal Heat Integration

被引:8
作者
Mathew, Anish K. [1 ]
Kaistha, Nitin [2 ]
Kumar, M. V. Pavan [1 ]
机构
[1] Natl Inst Technol Calicut, Dept Chem Engn, Kozhikode 673601, Kerala, India
[2] Indian Inst Technol, Dept Chem Engn, Kanpur 208016, Uttar Pradesh, India
关键词
Control structure design; Decentralized control; Internal heat integration; Reactive distillation; STEADY-STATE MULTIPLICITIES; PROCESS INTENSIFICATION; AZEOTROPIC MIXTURE; DESIGN; COLUMNS; SIMULATION; ETHYL; CONTROLLABILITY; DYNAMICS; SYSTEM;
D O I
10.1002/ceat.201400785
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Decentralized control system design is evaluated for a basic and an internally heat-integrated generic, ideal, double-feed, two-product reactive distillation system. The internally heat-integrated reactive distillation column (HiRDC) is obtained via catalyst redistribution into the rectifying zone and feed tray relocation. For basic regulatory control, three two-point control structures with a fixed reflux rate or a fixed reflux ratio operation policy are synthesized and evaluated for their closed-loop disturbance rejection characteristics using rigorous dynamic simulations. To eliminate the purity offsets for on-target product purities, product purity composition controllers manipulating the reflux ratio and stripping tray temperature set point are implemented. Reactive tray section composition control is necessary for on-target product purity operation of HiRDC.
引用
收藏
页码:775 / 785
页数:11
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