有方面反应堆(SRC ) 的蒸馏列能在传统的反应蒸馏克服温度 / 压力失配,列在为蒸汽液体分离有利的温度 / 压力操作,当反应堆在为反应动力学有利的温度 / 压力操作时。根据光滑的操作和有方面反应堆(SRC ) 的蒸馏列的自动控制问题,设计,模拟计算和为 chlorobenzene 生产的 SCR 进程的动态控制在纸被讨论。第一,机制当模特儿,综合结构最佳的设计和过程模拟系统分别地被建立。然后 multivariable 控制计划被设计, SRC 过程的可控制性基于最佳的不变的综合结构被探索。对几骚乱的靠近环的系统的动态反应表演被讨论为 SRC 进程验证控制计划的有效性。模仿的结果证明控制用策略能有效地克服的常规控制组织在一个特定的范围喂骚乱。
The distillation column with side reactors (SRC) can overcome the temperature/pressure mismatch in the traditional reactive distillation, the column operates at temperature/pressure favorable for vapor-liquid separation, while the reactors operate at temperatures/pressures favorable for reaction kinetics. According to the smooth operation and automatic control problem of the distillation column with side reactors (SRC), the design, simulation calculation and dynamic control of the SCR process for chlorobenzene production are discussed in the paper. Firstly, the mechanism models, the integrated structure optimal design and process simulation systems are established, respectively. And then multivariable control schemes are designed, the controllability of SRC process based on the optimal steady-state integrated structure is explored. The dynamic response performances of closed-loop system against several disturbances are discussed to verify the effectiveness of control schemes for the SRC process. The simulating results show that the control structure using conventional control strategies can effectively overcome feeding disturbances in a specific range.