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    • 1. 发明专利
    • PROCESS CONTROLLER FOR CLOSED LOOP SYSTEM INCLUDING PID ADJUSTER
    • JPH10312201A
    • 1998-11-24
    • JP13787597
    • 1997-05-12
    • MITSUBISHI HEAVY IND LTD
    • FUJIWARA TOSHIKATSUIWAI MASATAKA
    • G05B11/36G05B13/02
    • PROBLEM TO BE SOLVED: To provide a process controller for a closed loop including a PID adjuster by which the proportional gain of the PID adjuster is automatically calculated so as to obtain always proper value without being affected adversely by the secular change of a process characteristic. SOLUTION: The closed loop system including the PID adjuster consisting of the three operation of proportion, integration and differentiation for outputting a process and operation variable with respect to the process according to a target value is provided with a means setting the proportional gain of the PID adjuster with the target value and the output of a control gain adjuster arithmetic-processed based on a control variable outputted from the process at the time of varying the target value. To put it in the concrete, the proportional gain of the PID adjuster is made variable, at the time of varying the target value r(t)6, an error between them is inputted to an integrator so as to make the absolute value of the fine coefficient of the control variable y(t)4 close to a desirable value α* and the output of the integrator is made the proportional gain of the PID adjuster. Then, a desirable value α* is provided with a value only until some period passes after the fluctuation of a target value r(t)6 but becomes zero after then.
    • 2. 发明专利
    • DISTRIBUTION CONTROLLER
    • JPH0916203A
    • 1997-01-17
    • JP16622295
    • 1995-06-30
    • MITSUBISHI HEAVY IND LTD
    • FUJIWARA TOSHIKATSUMIYAGAWA HIROKAZUHIRAYAMA YUTAKA
    • G05B11/36
    • PURPOSE: To provide a distribution controller which makes the variation width of the state quantity of each process uniform and improves the control performance. CONSTITUTION: This distribution controller is equipped with a function generator which outputs commands of the state quantities of respective processes 2, 3, and 4 based on the value of disturbance which is already known, a subtracter which finds the deviations of the respective current state quantities of the processes 2, 3, and 4 from their commands, a multiplier which squares the respective deviations, an integrator which integrates the respective outputs, a 1st gain multiplier which finds the respective outputs of the integrators corresponding to the total of all the outputs as gains of the respective processes 2, 3, and 4 and multiplies them with the corresponding deviations, a 1st adder which adds all the outputs of the 1st gain multiplier, a 2nd gain multiplier which multiplies the output of the 1st adder by a gain regarding all the processes, and a 2nd adder 15 which adds the output of the 2nd gain multiplier to the output of a PID controller 14.
    • 5. 发明专利
    • STEAM TEMPERATURE CONTROLLER
    • JPH0484002A
    • 1992-03-17
    • JP19631390
    • 1990-07-26
    • MITSUBISHI HEAVY IND LTD
    • MASUDA MAKIOFUJIWARA TOSHIKATSUNAITO SHUZOMIYAGAWA HIROKAZU
    • F22B35/00
    • PURPOSE:To raise the response performance against a load variation by comparing outlet temperature target value signals for water wall third stage, fourth stage, and flue evaporator and the sensed temperature signals to obtain deviation signals and obtaining operation signals by carrying out proportional and differential control calculations and adding the signal given by addition and composition of the operation signals and the fuel feedforward signals to obtain fuel signals. CONSTITUTION:By pressure sensors 1A-1C, temperature sensors 2A-2C the outlet pressures and outlet temperatures of third stage and fourth stage of water wall and flue evaporator are detected. The outlet pressure signals 3A-3C of pressure sensors 1A-1C are inputted to function generators 5A-5C to obtain temperature target signals 4A-4C. To comparators 8A-8C function temperature target value signals 4A-4C and temperature detection value signals 6A-6C from temperature sensors 2A-2C are inputted to obtain deviation signals 7A-7C. The deviation signals 7A-7C are inputted to control and adjustment devices 10A-10C to carry out proportional and differential control calculations to obtain operational value signals 9A-9C. In an adder 20 the signal by addition and composition of respective operation value signals 9A-9C and fuel feedforward signal 18 are added and composed to obtain fuel signal 19 and steam temperature is controlled.
    • 6. 发明专利
    • FEEDFORWARD CONTROLLER
    • JPH0475101A
    • 1992-03-10
    • JP18785590
    • 1990-07-18
    • MITSUBISHI HEAVY IND LTD
    • FUJIWARA TOSHIKATSUHIROE TAKAHARU
    • G05B11/32G05B13/02
    • PURPOSE:To keep control performance with high accuracy even when known disturbance is fluctuated or when the characteristic of a process is changed in the lapse of time by finding a feedforward signal to prevent a controlled variable fluctuated by using the a mathematical model. CONSTITUTION:The dynamic characteristic of the process 1 is expressed in the mathematical model, and the parameter of the mathematical model is identified by a method of least square by fetching the controlled variable (y), the manipulated variable (u), and the known disturbance (d) of the process 1, and the feedforward signal can be found based on the parameter and the known disturbance (d). The feedforward signal is added on the output signal of a controller 2, and a result is inputted to the process 1 as the manipulated variable. Therefore, the feedforward signal to prevent the controlled variable (y) of the process fluctuated even when the known disturbance (d) is fluctuated can be found, and it is added on the output signal of the controller 2, and is supplied to the process 1 as the manipulated variable (u). Thereby, it is possible to stably perform the control of the process 1 even when the known disturbance is fluctuated.