Prediction control method for non-self-balancing system
A predictive control and non-self-balancing technology, which is applied in the direction of adaptive control, general control system, control/regulation system, etc., can solve the problems such as difficult to guarantee the stability of the control system, irregular adjustment of controller parameters, and difficult modeling
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Embodiment 1
[0105] For a 100,000-ton butadiene production plant in a certain factory, consider the following Figure 4 The extractive distillation column shown, the liquid level L of the extractive distillation column B 2 The flow F of tower A entering tower B is tested by a step signal to obtain the following process description
[0106] G ( s ) = K s e - θs
[0107] where K=0.2273, θ=10.
specific Embodiment approach
[0108] (1) According to the process characteristics, determine the system model parameter N=30 and the sampling time T s = 1s.
[0109] (2) Select the appropriate fitting point H=24, r=0, closed-loop response time T ref = 1s to verify the following formula
[0110] Σ i = 1 N + 1 | ( H + 1 ) ( Δ s ‾ i - ( r + 1 ) Δ s i - H ( Δ s ‾ i ...
Embodiment 2
[0119] Consider a non-self-balancing system structure described as:
[0120] G ( s ) = K s ( Ts + 1 ) e - θs
[0121] In the formula: K=1, T=4, θ=5.
[0122] Utilize the operation procedure similar to embodiment 1, select controller parameter H=14 under the nominal situation, T s = 1,T ref =1, r=0.
[0123] Apply the method of the present invention, control this non-self-balancing system when adding the load disturbance that amplitude is 0.1 at t=100 moment, the control output curve of its tracking unit step signal is shown in Image 6 shown by the solid line. From Image 6 It can be seen that the present invention can meet the requirement of tracking the set value in a relatively s...
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