System and method for proportional plus integral control in air separation energy saving process
A proportional-integral control and air separation technology, applied in electrical program control, comprehensive factory control, comprehensive factory control, etc., can solve problems such as poor robustness, low precision, and low efficiency
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Embodiment 1
[0034] refer to figure 1 with figure 2 , a proportional-integral control system for an air separation energy-saving process, comprising an on-site intelligent instrument 2 and a DCS system 12 directly connected to an air separation tower 1, and the DCS system 12 includes a storage device 4, a control station 5 and a host computer 6, so The on-site intelligent instrument 2 is connected with the storage device 4, the control station 5, and the host computer 6 in turn through the field bus and the data interface 3; Temperature, pressure data, described data interface is in order to realize the function of I / O module 8 namely the input and output of data, host computer 6 comprises the proportional-integral controller in order to solve proportional-integral control law and output control variable change value, so The proportional-integral controller described above includes a component estimation module 9 and a proportional-integral control law solution module 10 .
[0035] Desc...
Embodiment 2
[0045] refer to figure 1 with figure 2 , a proportional-integral control method of an air separation energy-saving process, said control method comprising the following steps:
[0046] 1) Determine the sampling period t, and the t value, the relative volatility of nitrogen and oxygen relative to argon α N 、α O , the Antony constant a N , b N 、c N 、a O , b O 、c O stored in the historical database;
[0047] 2) Set the control law parameter k 11 , k 12 , k 21 , k 22 and the set value of liquid nitrogen concentration at the top of the upper tower X 1, 1 * , the set value of the concentration of liquid oxygen at the bottom of the tower X 3,n * ;
[0048] 3) Detect the pressure P in the rectification section at time k r (k), each tray temperature T i (k), calculate the component concentration value of liquid nitrogen and liquid oxygen, adopt formula (1) (2) to obtain:
[0049] X i , N ...
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