Internal Thermally Coupled Distillation Column(ITCDIC) is the research frontier of distillation energy saving . This paper investigates the principium design of ideal ITCDIC. A novel design model of ideal ITCDIC is de...Internal Thermally Coupled Distillation Column(ITCDIC) is the research frontier of distillation energy saving . This paper investigates the principium design of ideal ITCDIC. A novel design model of ideal ITCDIC is derived, which can not only directly achieve the system characteristics and comparative characteristics with conventional distillation columns, but also be used for further control and design studies. A series of detailed operation analyses are carried out, which pave the way for further research and practice application.展开更多
Based on the previous design model, degrees of freedom analysis and transient analysis are carried out. A PID control model is proposed. The results show that ITCDIC is a self-regulating process, and could be operated...Based on the previous design model, degrees of freedom analysis and transient analysis are carried out. A PID control model is proposed. The results show that ITCDIC is a self-regulating process, and could be operated smoothly with two PID controllers; the steady state design could be disassociate with the dynamic design. An optimization model of ITCDIC design parameters is derived, which can directly achieve the optimal design parameters providing the maximum energy savings and the product quality simultaneously. Benzene-toluene system is studied as an illustrative example.展开更多
Internal thermally coupled distillation column(ITCDIC) is a frontier in energy saving distillation research. In this paper, the optimal assessment on the energy saving and the operating cost for ITCDIC of nonideal mix...Internal thermally coupled distillation column(ITCDIC) is a frontier in energy saving distillation research. In this paper, the optimal assessment on the energy saving and the operating cost for ITCDIC of nonideal mixture is explored. An evaluating method is proposed, and the pertinent optimization model is then derived. The ethanol-water system is studied as an illustrative example. The optimization results show that the maximum energy saving in ITCDIC process is about 35% and the maximum operating cost saving in ITCDIC process is about 30%,as compared with a conventional distillation column(CDIC) under the minimum reflux ratio operating; the optimal operating pressure of the rectifying section is found to be around 0.25 MPa; the effects of the feed composition,operating pressure and the heat transfer rate on operation are also found and analyzed. It is revealed that ITCDIC process possesses high energy saving potential and promising economical prospect.展开更多
主要讨论和研究了高纯度热耦合精馏塔的优化控制问题。针对一个非线性的对象模型—苯-甲苯物系模型提出了基于非线性过程模型控制(NPM C,N on linear P rocess M odel Contro l)的控制方案,并与常规的P ID控制方案作了比较。结果表明:...主要讨论和研究了高纯度热耦合精馏塔的优化控制问题。针对一个非线性的对象模型—苯-甲苯物系模型提出了基于非线性过程模型控制(NPM C,N on linear P rocess M odel Contro l)的控制方案,并与常规的P ID控制方案作了比较。结果表明:非线性过程模型控制无论是在控制精度还是在响应时间上都优于传统的控制方案。展开更多
文摘Internal Thermally Coupled Distillation Column(ITCDIC) is the research frontier of distillation energy saving . This paper investigates the principium design of ideal ITCDIC. A novel design model of ideal ITCDIC is derived, which can not only directly achieve the system characteristics and comparative characteristics with conventional distillation columns, but also be used for further control and design studies. A series of detailed operation analyses are carried out, which pave the way for further research and practice application.
文摘Based on the previous design model, degrees of freedom analysis and transient analysis are carried out. A PID control model is proposed. The results show that ITCDIC is a self-regulating process, and could be operated smoothly with two PID controllers; the steady state design could be disassociate with the dynamic design. An optimization model of ITCDIC design parameters is derived, which can directly achieve the optimal design parameters providing the maximum energy savings and the product quality simultaneously. Benzene-toluene system is studied as an illustrative example.
基金Supported by National Natural Science Foundation of China(No.20106008)China Postdoctoral Science Foundation,Tsinghua University-Zhongda Group Postdoctoral Science Foundationthe National Environmental Protect Bureau of China(Huan-Ke-Ke,1997,
文摘Internal thermally coupled distillation column(ITCDIC) is a frontier in energy saving distillation research. In this paper, the optimal assessment on the energy saving and the operating cost for ITCDIC of nonideal mixture is explored. An evaluating method is proposed, and the pertinent optimization model is then derived. The ethanol-water system is studied as an illustrative example. The optimization results show that the maximum energy saving in ITCDIC process is about 35% and the maximum operating cost saving in ITCDIC process is about 30%,as compared with a conventional distillation column(CDIC) under the minimum reflux ratio operating; the optimal operating pressure of the rectifying section is found to be around 0.25 MPa; the effects of the feed composition,operating pressure and the heat transfer rate on operation are also found and analyzed. It is revealed that ITCDIC process possesses high energy saving potential and promising economical prospect.
文摘主要讨论和研究了高纯度热耦合精馏塔的优化控制问题。针对一个非线性的对象模型—苯-甲苯物系模型提出了基于非线性过程模型控制(NPM C,N on linear P rocess M odel Contro l)的控制方案,并与常规的P ID控制方案作了比较。结果表明:非线性过程模型控制无论是在控制精度还是在响应时间上都优于传统的控制方案。
