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    • 2. 发明专利
    • CONTROL UNIT OF SEPARATE TYPE HEAT PIPE
    • JPS61252492A
    • 1986-11-10
    • JP9523185
    • 1985-05-02
    • MITSUBISHI HEAVY IND LTDKAWASAKI STEEL CO
    • HIRAYAMA YUTAKATAKANO HIDEKISOMA FUYUKI
    • F28D15/06F28D15/02
    • PURPOSE:To prevent the heat exchange efficiency due to air leakage caused by the negative pressure from deteriorating or to prevent the life of the heat pipe from shortening due to oxidation within the system by mounting a transmitter on a unit to be put into a negative pressure and controlling circulating water of a upstream side unit by detecting and transmitting the internal pressure of the transmitter. CONSTITUTION:When the temperature of an exhaust gas is lowered, the temperature of the exhaust gas at the inlet of a downstream side unit 14B lowers and the temperature of circulating water also lowers. Therefore, an output from a downstream apparatus internal pressure oscillator 8 becomes below an output from an apparatus internal pressure setter 9. Therefore, an output from a pressure deviation adjusting meter 10 becomes below the output from a water level deviation adjusting meter 7A of an upstream side evaporator. Therefore, the apparatus switched to the pressure control by a low level selector 11 and the downstream side unit is prevented from becoming a negative pressure. In a case where the downstream side unit 14B assumes a negative pressure even if the heat exchange in the upstream side unit 14A is put into a zero state, it is sufficient to form said downstream side unit in a construction similar to that of the upstream side unit.
    • 3. 发明专利
    • CONTROL METHOD OF SEPARATE TYPE HEAT PIPE
    • JPS61168791A
    • 1986-07-30
    • JP925785
    • 1985-01-23
    • MITSUBISHI HEAVY IND LTDKAWASAKI STEEL CO
    • TAKEUCHI YUICHIHIRAYAMA YUTAKATAKANO HIDEKISOMA FUYUKI
    • F28D15/06
    • PURPOSE:To perform continuous control that causes less thermal collision and better static characteristics by performing the water level adjustment for temperature control by means of a single closed cycle, and, when one range ability is exceeded, performing the heat exchange rate control with the next cycle. CONSTITUTION:The output of the difference adjusting gauge the receives outputs from the transmitter 6 of exhaust gas outlet temperature and the set value 7 becomes the set value of the water level of the A side vaporizer, and the output of the difference adjusting gause 9 that receives said water level set value and the output from the vaporizer water level transmitter 5a becomes the control signal for the circulating water control valve 4A. In said control system, if the exhaust gas temperature decreases, the setting value of the A side vaporizer water level is lowered to reduce the circulated water flow rate so as to reduce the heat exchanging rate in the vaporizer 1A. If the A side vaporizer water level becomes lower than the water level setting 10, the output of the subtracting unit 11 becomes plus and the output of the low limiter 13 also becomes plus. Therefore, the output of the subtracting unit 15 becomes smaller than the value of the B side vaporizer water level setting 14 to cause the water level of the B side vaporizer B to be lowered to reduce the heat exchanging rate, resulting in theincrease of the exhaust gas temperature.
    • 4. 发明专利
    • DISTRIBUTION CONTROLLER
    • JPH09134203A
    • 1997-05-20
    • JP29412095
    • 1995-11-13
    • MITSUBISHI HEAVY IND LTD
    • FUJIWARA TOSHIKATSUMIYAGAWA HIROKAZUHIRAYAMA YUTAKA
    • G05B13/02
    • PROBLEM TO BE SOLVED: To equalize the fluctuation of the respective state quantities of plural processes and to improve control performance. SOLUTION: Function generators 12-14 where the setting states of the state quantities of the respective processes 1a-1c are made to correspond to known disturbance (d) in the operation state of propotional-plus-integrad-plus-derivative (PID) control are provided. Three kinds of values obtained by differentiating deviations with the respective state quantity (x1) 4-state quantity (x3) 6 in differentiation units 49, 50 and 51, squaring them in multipliers 20, 33 and 38 and integrating them in integrators 21, 34 and 39 with the outputs of the function generators 12-14 as target values. The distribution of gains is decided by a value obtained by dividing the respective integral values by the total sum of the integral values. After the distribution of the gains is decided, a value obtained by adding all values obtained by multiplying the value of the deviation between the respective state quantities and the target values by the distribution value of the gain by the gains in coefficient units. Then, a value obtained by adding the value with the output of a PID controller 10 is set to be a manipulated variable (u).
    • 10. 发明专利
    • CONTROLLING CIRCUIT WITH CONTROL OUTPUT SUDDEN CHANGE PREVENTIVE FUNCTION
    • JPS62200402A
    • 1987-09-04
    • JP4313786
    • 1986-02-28
    • MITSUBISHI HEAVY IND LTD
    • HIRAYAMA YUTAKAFUJIWARA TOSHIKATSU
    • G05B11/36F22B35/00G05B17/02
    • PURPOSE:To prevent a sudden change in a model output at the time of switching a parameter of a linear model, and to improve the control performance, by installing a variation rate limiter for limiting a variation rate of an input of an integrator, in front of the integrator of the final stage for constituting a part of the linear model. CONSTITUTION:A variation rate limiter 3 for limiting a variation rate of an input of an integrator 4 is installed in front of the integrator 4 of the final stage. Therefore, when the variation rate of the variation rate limiter 3 is set in advance to the maximum variation rate value within a range in which modeling can be executed correctly at the time of a regular operation of a process being a controlled system, a control output is not brought to a sudden change exceeding a variation rate by which the process can be varied, even at the time of switching of a parameter 5 or a parameter 6 of a linear model by a model switching deciding circuit 7. Accordingly, an abnormal sudden change of a model output is prevented, and an output of the model moves smoothly. In this regard, the variation rate limiter 3 applies a limit to a variation rate of an input of the interrator 4, and sets the variation rate in advance to the maximum variation rate value by which a correct model output can be obtained at the time of a regular operation of the process being the controlled system.