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A Multivariable Predictive Control Method for Air Separation Plant
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An air separation unit, predictive control technology, applied in general control system, adaptive control, control/regulation system, etc., can solve the problems of energy consumption and economic loss, complex process of air separation unit, serious coupling, etc., to reduce energy consumption Dissipation rate, reduction of extra cooling capacity, and improvement of extraction rate
Active Publication Date: 2020-08-25
盈德气体工程(浙江)有限公司
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[0005] The air separation unit has the characteristics of complex process and severe coupling; at the same time, in the production process of the air separation unit, the demand for the production gas of the external pipe network often presents the characteristics of periodicity, stages, and intermittent, and the dissipation of oxygen will cause unnecessary energy consumption and economic losses
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[0024] The present invention will be described in detail below in conjunction with accompanying drawing and specific embodiment: a kind of multivariable predictive control method that is used for air separation unit, described multivariable predictive control method is:
[0025] a) Add a host computer on the DCS system LAN of the air separation unit to create the MVPC server of the air separation unit, and the MVPC client is installed on the engineer station or operator station of the DCS;
[0026] b) Determination of variables: According to the optimization goals of the process flow of the air separation unit (such as reducing product flow fluctuations, reducing energy consumption, etc.), determine the controlled variable CV, operating variable MV, and disturbance variable DV;
[0027] c) The establishment principle of MVPC matrix size: select key parameters, as few variables as possible; at the same time determine the settings of CV and MV related restrictions; MVPC operating...
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Abstract
Disclosed is a multivariable predictive control method for an air separation device. The multivariate predictive control method comprises the steps that (a) an upper computer is additionally arranged on a DCS system local area network of the air separation device for creating an MVPC server of the air separation device; (b) variables are determined, specifically, according to the technological process optimizing target of the air separation device, the controlled variable (CV), the manipulating variable (MV) and the disturbance variable (DV) are determined; (c) the establishment principles of the size of an MVPC matrix are that key parameters are selected, the variables are controlled as less as possible, the valve opening degree, namely corresponding to the output of a PID controller under conventional control, is adjusted through the MV of an MVPC, when the MVPC works, the PID controller corresponding to the MV of the MVPC is in cascade control, the output of the PID controller tracks the MV of the MVPC, and when the MVPC does not work, the PID controller corresponding to the MV of the MVPC is in automatic control, and the MV of the MVPC tracks the output of the PID controller; (d) a model is built, specifically, an MVPC controller model is built in the air separation device, or independent MVPC controller models are built in different work sections in the air separation device; (e) the models are trained and adjusted, specifically, the gain K, the time constant Tau and the delay time Tdelay in the models are preliminarily set, and after the models are put into use, the optimized gain, time constant and delay time are provided by a system automatically; and (f) the models are put into use.
Description
technical field [0001] The invention relates to a multi-variable predictive control (MVPC: Multi-Variable Predictive Control) method for an air separation plant used in the air separation production process, and belongs to the technical field of automation control engineering. Background technique [0002] In the process flow of the air separation unit, the raw air enters the lower tower after a series of operations such as filtration, compression, precooling, purification, pressurization, expansion and heat exchange; Oxygen-enriched liquid air is obtained at the bottom of the tower, and pure liquid nitrogen is obtained at the top of the lower tower, which is subcooled by a subcooler and throttled into the upper tower. [0003] After further rectification in the upper tower, liquid oxygen is obtained at the bottom of the upper tower, which is compressed by the liquid oxygen pump and enters the main heat exchanger. Part of the liquid oxygen goes directly out of the cold box ...
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