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Active-disturbance-rejection control method for temperature of a constant stirring polypropylene reaction kettle

A kind of technology of active disturbance rejection control and control method, applied in the direction of adaptive control, general control system, control/regulation system, etc., can solve the problems of practical limitation, difficult to obtain models, etc., and achieve rapid dynamic response and good adaptability and the effect of robustness

Inactive Publication Date: 2015-01-14
JIANGNAN UNIV
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  • Description
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Problems solved by technology

However, these methods all need to know the precise mathematical model of the system, and the mechanism modeling method involves a series of problems such as material balance, energy conservation and chemical reaction process. It is difficult to obtain a specific model in practice, and its practicability is greatly limited.

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  • Active-disturbance-rejection control method for temperature of a constant stirring polypropylene reaction kettle
  • Active-disturbance-rejection control method for temperature of a constant stirring polypropylene reaction kettle
  • Active-disturbance-rejection control method for temperature of a constant stirring polypropylene reaction kettle

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Embodiment Construction

[0031] The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

[0032] Taking the polypropylene production reaction model as the controlled object, in the MPCE multifunctional process and control platform, it communicates with the I / O of the slave station through the 4-20mA standard signal, transmits the field data in real time, and completes the functions of online monitoring, recording and query; The upper computer uses SIMATIC PCS7, which is a new generation of compact design controller from Siemens, which eliminates the redundant wiring between the automation station (AS), operator station (OS) and engineer station (ES), and uses a PROFIBUS-DP interface The CPU 416 as the central processing unit is connected with the modular I / O station ET200M through bus connectors and cables. The PCS7 BOX slave rack is equipped with a power supply module (PS), a communication interface module (IM153-2), an 8-channel analog inp...

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Abstract

The invention discloses an active-disturbance-rejection control method for the temperature of a constant stirring polypropylene reaction kettle. A discrete mode is adopted for the active-disturbance-rejection control method for the temperature of the constant stirring polypropylene reaction kettle, and a tracking differentiator module, an expanded state observer module and a non-linearity feedback controller module are involved. The method includes the steps that firstly, parameters of the tracking differentiator module and the expanded state observer module are set; then, a transient process is arranged, and disturbances are estimated; finally, an error signal is used for adjusting the non-linearity feedback controller module to control the temperature of the polypropylene reaction kettle. The control method has the advantages that the method is implemented on SIMATICPCS7 equipment without establishing a constant stirring polypropylene reaction kettle model, the dynamic response is rapid, and a system is high in adaptability and robustness under the working conditions of disturbances and variable loads.

Description

technical field [0001] The invention relates to an automatic disturbance rejection control method for the temperature of a continuously stirred polypropylene reactor, which belongs to the field of process control of chemical production. Background technique [0002] The industrial polypropylene reaction is an important batch production process, and its process technology is complex, with characteristics such as large lag, time variation and uncertainty. Polypropylene production is carried out in the industrially common stirred reactor (CSTR), which is a continuous polymerization process. The production requires that the reactants propylene and ethane undergo a polymerization reaction at a temperature of 70±1.0°C under the action of a catalyst to obtain a polypropylene product that meets the process requirements. [0003] Due to the strong stirring of the continuous stirring reactor, the solvent ethane plays a good role in dispersing and diluting, so the material flow state ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G05B13/04B01J19/18
Inventor 陶洪峰
Owner JIANGNAN UNIV
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