Hydraulic press is designed for manufacturing of superhard materials using high temperature and high pressure.
The press DО138B produces a pressure of 6300кP. The measured values in control system are effective amperage I(kh) and voltage U(kh) in the circuit of heating, where h is the sampling time. The active power P(kh) is calculated as I(kh)*U(kh). The reference signal P*(kh) is a required value of active power. The actual value of P(kh) must follow the reference signal and change in accordance with specified cyclogram. This is provided by using of PID-controller.
The difficulty of control process is that the dynamical characteristic of heating process change for different materials. So, the controller must be tuned for each pattern to provide desired quality of control.
The adaptive PID-controller was designed on the base of proposed algorithm. This controller was tested for hydraulic press. The adaptation process consists of two steps. On the first step, the different values of control voltage were applied to the press and the active power settled in different levels. As the result, we calculated the time constant T = 0.2sec and delay τ =0.12sec. The comparison of real data (figure 1) and designed model (figure 2) is shown below:
The test cyclogram was specified for process of synthesis of superhard material. The nominal value of power of P = 1500 W was calculated for this cyclogram. The linearized model of heating process for P = 1500 W gave kp = 888.98
PID controller was designed by method of inner model under Kp = 888.98, T = 0.2sec and τ = 0.12sec. The results of system operation with designed controller is shown in figure:
The figure 5 shows that the real power follows reference signal and control error doesn’t exceed 1.3%.
We tested our controller with use of the experimental setup that imitates semi-industrial environment. This experimental setup includes an industrial controller WinCon-8000 and industrial computer Athena, which interact with each other through embedded DAC and ADC converters. Plant simulator is implemented in the industrial computer Athena. Self-tuning controller CHAR-25 is implemented in the industrial controller WinCon-8000. The scheme of experimental setup is shown on fig.2
1 – 2а – stage of self-tuning of test signal; 2б – stage of plant identification with test signal, controller calculation; 3 – plant output in the closed-loop system.
The figure shows that controller CHAR-25 provides required disturbance suppression.
We tested our controller with use of the experimental setup that imitates semi-industrial environment. This experimental setup includes an industrial controller WinCon-8000 and industrial computer Athena, which interact with each other through embedded DAC and ADC converters. Plant simulator is implemented in the industrial computer Athena. Self-tuning controller ST-PID-1 is implemented in the industrial controller WinCon-8000. The scheme of experimental setup is shown on fig.2
Simulated plant has the following form W(s) = K e-τs / (Tsog + 1), coefficients of the plant changed in accordance with the table 1 each 3500 s . External disturbance applied to the plant is the sum of meander with the frequency 0.1 rad/s and white noise: f(t) = SIGN( SIN(0.1t) ) + RAND. Amplitude of test signal is tuned such that the deviation of plant output, in compare with situation when the test signal is absent, does not exceed 15%
Number of mode |
I |
II |
III |
IV |
K |
6.14 |
4.77 |
3.75 |
1.78 |
T, s |
7.68 |
2.49 |
4.61 |
9.00 |
τ, s |
0.35 |
0.33 |
1.54 |
1.06 |
The plant output is shown on the fig.3, the magnified graphic of the fourth mode is shown on the fig.4
For clarification, see the figure 4. In the Iva interval + , the plant is controlled by the PID-controller that was tuned for the plant in the third mode. In the IVb interval the PID-controller was tuned. In the IVc interval the plant is controlled by the PID-controller that was tuned for the plant in the fourth mode.
If the control system works with the PID-controller that was tuned for the plant in the first mode and self-tuning of controller was disabled then the control system would be unstable in the third mode. The plant output for this case is shown in fig.5
Therefore, the controller ST-PID-1 provides stable operation of the system. The test signal is applied to the plant in the adaptation process only and gives the small deviation of plant output. .