JP2008282413A - Fluid temperature controller and control method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fluid temperature controller capable of coping with an individual difference in a flow control valve, capable of restraining satisfactorily overshooting, and capable of coping sufficiently with a load disturbance. <P>SOLUTION: A hydraulic fluid is cooled by cooling water in a heat exchanger, and is heated by a lamp heater to be brought into a target temperature. The flow control valve for the cooling water is controlled using two kinds of tables of the table for compensating a nonlinear cooling characteristic of the heat exchanger, and the table for compensating a nonlinear cooling characteristic of a proportional valve. The table for compensating the characteristic of the proportional valve defines a change rate of a flow rate generated when moved by one pulse from each pulse number position with respect to the position. The table for compensating the characteristic of the proportional valve is matched to a characteristic of the individual proportional valve, by applying a parameter expressing the individual difference of the proportional valve. The proportional valve is controlled in response to a change speed of a current temperature, in a transition period. The proportional valve is controlled to bring an output from the lamp heater within a prescribed proper output range, in a setting period. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to an apparatus for controlling the temperature of a fluid flowing through a pipe.

  One application in which a fluid temperature control device is used is temperature control of a vacuum chamber used in a semiconductor manufacturing apparatus. For example, in the case of the vacuum chamber 20 of the etching apparatus as shown in FIG. 1, generally, the outer wall 21 is in a high temperature region of 80 ° C. or higher, the lid 22 is in a low temperature of about −15 ° C., and the electrode 24 on which the wafer 23 is set is It needs to be controlled in a low temperature range of about −20 ° C. to 80 ° C. The temperature control of the outer wall 21, the lid 22, and the electrode 24 is performed by circulating a pipe around each place and flowing a temperature-controlled working fluid through each pipe. Here, water, ethylene glycol, or FLUORINERT (registered trademark) is used as the working fluid.

  For example, for temperature control in the low temperature range for the electrode 24, for example, a fluid temperature control device (hereinafter referred to as “low temperature machine”) 30 as shown in FIG. 2 can be used. Further, for example, a fluid temperature control device (hereinafter referred to as “high temperature machine”) 50 as shown in FIG. 3 can be used for temperature control in the high temperature range for the outer wall 21.

  In the cryogenic machine 30 shown in FIG. 2, there is a fluid circulation supply system 31, in which the working fluid circulates through the chiller (cooler) 32 or the bypass passage 35, the halogen lamp heater 33, and the vacuum chamber 20 in order. Yes. The working fluid is cooled when passing through a chiller (cooler) 32, then heated when passing through a heater 33, and supplied to the vacuum chamber 20. The opening control of the two flow control valves 34 and 36 provided in the chiller passage 37 and the bypass passage 35 and the output control of the halogen lamp heater 33 so that the temperature of the working fluid reaches the target temperature at the inlet of the vacuum chamber 20. Is done.

  The high-temperature machine 50 shown in FIG. 3 has a fluid circulation supply system 51 in which a working fluid is supplied to a heater / cooler 52 containing a halogen lamp heater and a cooling water channel, and a vacuum chamber 20 (for example, its outer wall 21). It circulates through in order. When the working fluid passes through the heater cooler 52, the working fluid is cooled by the cooling water, heated by the halogen lamp heater, and supplied to the vacuum chamber 20. The opening control of the cooling water flow rate control valve 62 and the output control of the halogen lamp are performed so that the temperature of the working fluid reaches the target temperature at the inlet of the vacuum chamber 20.

  In both the low temperature machine 30 and the high temperature machine 50, two types of heat exchangers are used to adjust the temperature of the working fluid. That is, a heat exchanger for cooling the working fluid with cooling water and a heat exchanger for heating the working fluid with a heater. Japanese Patent Application Laid-Open No. 2000-284832 discloses a conventional apparatus for controlling the temperature of a fluid by using such two types of heat exchangers.

  The conventional temperature control device described in Japanese Patent Laid-Open No. 2000-284832 performs control having the following characteristics.

  The first feature point relates to control of a flow rate control valve (for example, a proportional valve) for adjusting the flow rate of the working fluid or the cooling water. Generally, the opening / closing operation of the proportional valve is performed by a motor, and the opening / closing amount of the flow control valve is controlled by the operation amount (number of pulses) applied to the motor driver. However, the relationship between the number of applied pulses and the rate of change in flow rate (flow rate characteristics of the flow rate control valve) is non-linear. That is, the flow rate change rate when the same number of pulses is applied is not constant and varies depending on the opening position of the flow control valve. Therefore, in the conventional device, by introducing an opening-pulse number table having a characteristic that compensates for the nonlinear flow characteristic of the flow control valve, a certain ideal characteristic (the flow characteristic is reduced to a linear characteristic). Opening-flow rate characteristics with a gamma characteristic that increases the control resolution the smaller the value is). This eliminates the need to take into account the non-linear characteristics of the flow control valve in the calculation of the opening of the flow control valve, thereby simplifying the control process and improving the control accuracy.

  The second feature point relates to control at the time of transition (when the current temperature is away from the target temperature). For example, when the target temperature of the working fluid is changed and the deviation between the target temperature of the working fluid and the current temperature increases, the control operation of the conventional apparatus enters the rapid heating mode or the rapid cooling mode. In the rapid heating mode, the flow rate control valve for the cooling water or the flow rate control valve for the working fluid flowing through the chiller is closed to the minimum opening. In the rapid cooling mode, the flow rate control valve of the cooling water or the flow rate control valve of the working fluid flowing through the chiller is opened to the maximum opening. Responsiveness is improved by such rapid heating or rapid cooling operation in which the opening degree of the flow control valve is set to the minimum or maximum.

  The third feature point relates to control at the time of settling (when the current temperature is in the vicinity of the target temperature). When the current temperature enters a range near the target temperature, the control operation of the conventional apparatus enters the settling mode. In the settling mode, the opening value of the flow control valve for the coolant flow or the flow control valve for the working fluid flowing through the chiller is controlled to a predetermined value corresponding to the target temperature, so that the output value of the halogen lamp heater is a predetermined appropriate output. Keep within range. In this state, when a disturbance (temperature fluctuation due to heat generated in the process performed in the vacuum chamber) is added to the temperature of the working fluid, the disturbance is dealt with by adjusting the output power of the halogen lamp heater. Since the output power of the halogen lamp heater can be adjusted at high speed and with high accuracy, it is possible to respond to disturbances immediately and accurately, and it is easy to maintain the temperature of the working fluid at the target temperature.

JP 2000-284832 A

  The conventional apparatus described above has the following problems.

  First, there is a solid difference in the flow characteristics of the flow control valve. In other words, even with the same type of flow control valve, the flow characteristics of each product differ slightly. For this reason, the opening degree-pulse number table described above must have a wide margin to cover the distribution of flow rate characteristics due to individual differences. As a result, the opening-pulse number table is not necessarily optimal for individual flow control valve products.

  Second, the time from when the current temperature of the working fluid reaches the target temperature until the process can be started in the vacuum chamber is not sufficient enough to suppress overshoot (including undershoot). Is not yet short enough. One of the causes is that the cooling characteristics of the heat exchanger for exchanging heat between the working fluid and the cooling water are nonlinear. That is, even if the flow rate of the cooling water is the same, the cooling capacity varies depending on the temperature of the working fluid and the cooling water. The greater the temperature difference between the working fluid and the cooling water, the greater the cooling capacity. Therefore, the amount of cooling water for obtaining the same cooling capacity must be changed according to the temperature of the working fluid. Also, the cooling capacity for the same amount of cooling water varies depending on the temperature of the cooling water. Furthermore, as another cause, various heat sources such as a motor included in the apparatus also affect the temperature of the working fluid. However, the control method of the rapid heating or rapid cooling mode of the conventional apparatus is not enough to cope with such problems as the nonlinear characteristics of the heat exchanger and the influence of other heat sources, and suppresses overshoot sufficiently. Is difficult.

  Third, the ability to respond to disturbances is not sufficiently large. That is, in the conventional apparatus, the disturbance is dealt with by the output control of the halogen lamp heater. Therefore, it is difficult to completely cope with disturbance unless the margin of output capability of the halogen lamp heater is very large.

  Accordingly, an object of the present invention is to provide a fluid temperature control device that can satisfactorily suppress overshoot.

  Another object of the present invention is to provide a fluid temperature control device with a short settling time.

  Another object of the present invention is to provide a fluid temperature control apparatus that can sufficiently cope with disturbances.

The fluid temperature control device according to the first aspect of the present invention includes a heat exchanger for cooling the working fluid with the cooling fluid through which the working fluid and the cooling fluid flow, and a flow rate of the working fluid or the cooling fluid flowing through the heat exchanger. A flow control valve for controlling, an electric heater for heating the working fluid exiting the heat exchanger, and a heater control for operating the output power of the heater to control the temperature of the working fluid exiting the heater to the target temperature And a valve control unit for operating the flow rate control valve in order to control the cooling capacity of the heat exchanger. And the said valve control part is
(1) Transient valve control means for operating the flow rate control valve according to the rate of change of the current temperature during a transition before the current temperature of the working fluid reaches the target temperature;
(2) It has a settling time valve control means for operating the flow rate control valve so that the output power of the heater falls within a predetermined appropriate output range when settling after the current temperature reaches the target temperature.

  According to this fluid temperature control device, by performing valve control in accordance with the change rate of the current temperature at the time of transition, it is possible to more effectively suppress overshoot and shorten the settling time.

  In a preferred embodiment, the settling time valve control means includes means for feeding back the reference output power from the heater control section, and when the reference output power is outside the proper output range, the deviation between the reference output power and the proper output range. Means for operating the flow control valve according to the size. Thereby, the capability to cope with load disturbance is improved.

  In a preferred embodiment, the settling time valve control means calculates a manipulated variable of the flow control valve using a relatively large control gain during an overshoot immediately after the current temperature reaches the target temperature. And a means for calculating an operation amount of the flow control valve using a relatively small control gain after the overshoot is finished. Thereby, the overshoot can be more effectively suppressed, and the control can be stabilized after the overshoot ends.

  In a preferred embodiment, the settling time valve control means includes means for detecting the occurrence of hunting in which the output power of the heater oscillates with a width exceeding an appropriate output range, and operation of the flow control valve when hunting is detected. Means for reducing the control gain used to calculate the quantity. Thereby, hunting can be effectively suppressed.

  In a preferred embodiment, the heater control means calculates the operation amount of the heater output power by a speed type I-PD control method using a relatively large control gain at the time of transient and settling overshoot. And a means for calculating an operation amount of the output power of the heater by a PID control method using a relatively small control gain after the overshoot at the time of settling is completed.

  FIG. 4 shows a mechanical system configuration of the fluid temperature control apparatus according to the embodiment of the present invention.

  In the fluid temperature control apparatus 100, a path 101 indicated by a thick solid line is a path through which the working fluid circulates. There, the working fluid delivered from the tank 102 by the pump 103 is first divided into the main passage 104 and the bypass passage 105, which passes through the cooling heat exchanger 106 and then joins. Through a lamp heater (heat exchanger for heating) 108 using a halogen lamp, and is supplied to a load such as a vacuum chamber (not shown), and then returns to the tank 102 again. The bypass 105 has a flow sensor 107 that measures the flow rate of the working fluid flowing therethrough. At the outlet of the lamp heater 108 (the outlet of the fluid temperature control device 100), there is a temperature sensor 109 that measures the current temperature of the working fluid at the outlet (the current temperature of the working fluid supplied to the load). The working fluid always flows through this path 100 at a constant flow rate, is cooled when it passes through the heat exchanger 106, and is heated when it passes through the lamp heater 108, so that its temperature is controlled.

  A path 111 indicated by a thin solid line is a path through which cooling water for cooling the working fluid flows. In this case, the cooling water sent out by the pump 103 is first divided into the main passage 113 and the bypass passage 115, passes through the heat exchanger 106 in the main passage 113, joins, and is controlled by the constant flow valve 117. It is flowing at a constant flow rate. The main passage 113 and the bypass passage 115 are respectively provided with proportional valves 112 and 114 for controlling the flow rate of the cooling water.

  FIG. 5 shows a hardware configuration for performing the control operation of the fluid temperature control apparatus 100.

  As shown in the figure, the CPU board (controller) 121 takes in the detected value of the temperature of the working fluid supplied to the load from the temperature sensor 109 and the flow rate of the working fluid bypassing the heat exchanger 106 from the flow sensor 107. The detection value is captured, and the detection value of the current flowing through the lamp is captured from the lamp heater 108. Then, in order to make the temperature of the working fluid at the outlet coincide with a predetermined target temperature, the controller 121 performs arithmetic processing described later based on the detection value, and controls the flow rate of the cooling water according to the result. Therefore, the opening amount of the proportional valves 112 and 114 is controlled, and the output power of the lamp heater 108 is controlled. The controller 121 also starts and stops the pump 103. The controller 121 is connected to the operation panel 122 and the host computer 123, and performs the above-described start and end of the control operation, setting of the target temperature, and the like according to a command sent from the operation panel 122 or the host computer 123.

  FIG. 6 shows a basic functional configuration of the controller 121.

  The function of the controller 12 is roughly divided into a valve controller 131 and a lamp controller 132. The valve controller 131 controls the opening amounts of the proportional valves 112 and 114 that control the cooling water amount. The lamp controller 132 controls the output power of the lamp heater 108. The two types of control of the valve controller 131 and the lamp controller 132 are combined to control the current temperature (PV) at the outlet of the working fluid to the target temperature (SV). The control role of the controller 132 is different as follows.

  That is, it is the lamp heater 108 under the control of the lamp controller 132 that directly plays the role of controlling the current temperature (PV) of the working fluid to the target temperature (SV). Therefore, the lamp controller 132 inputs the current temperature (PV) and the target temperature (SV), performs PID calculation on the deviation between the two, and controls the output power of the lamp heater 108 so that the deviation becomes zero. . Since the output power of the lamp heater 108 can be controlled at high speed and with high accuracy, by controlling the temperature of the working fluid thereby, temperature control with high responsiveness and high accuracy becomes possible.

  On the other hand, the control of the cooling amount by the cooling water in the heat exchanger 106 has low responsiveness and low control accuracy. Therefore, the role of the cooling amount control performed by the valve controller 131 is to control the output power of the lamp heater 108 to be within a predetermined appropriate output range for the above-mentioned role. Therefore, the valve controller 131 inputs the target temperature (SV) and the current temperature (PV) of the working fluid and the output power of the lamp controller 132 (in particular, an integral component that is not easily affected by disturbance such as a temperature detection error). Then, arithmetic processing is performed by a method described later using these input amounts, and the proportional valves 112 and 114 are operated based on the result.

  In the basic configuration described above, the principle is applied to the present invention particularly in the specific control method of the proportional valves 112 and 114 performed by the valve controller 131. Therefore, in the following, a method for controlling the proportional valves 112 and 114 performed by the valve controller 131 will be described in detail.

  The main items newly adopted in the control of the proportional valves 112 and 114 are as follows.

  (1) Two types of tables are used: a table that compensates for nonlinear cooling characteristics of the heat exchanger 106, and a table that compensates for nonlinear flow characteristics of the proportional valves 112 and 114.

  (2) The table for compensating the flow rate characteristics of the proportional valves 112 and 114 is not the absolute value of the absolute flow rate for each pulse number position, but for each pulse number position, the number of pulses from that position is a unit quantity (for example, 1 It is defined by the relative value of the rate of change of flow rate that occurs when only (pulse) is changed (for example, the ratio of the flow rate change amount to the total flow rate of cooling water).

  (3) The table that compensates the flow characteristics of the proportional valves 112 and 114 is adapted to the individual proportional valves by applying the parameters representing the individuality (individual difference) of the individual proportional valves to this table. It is like that.

  (4) At the time of transition (when the deviation between the current temperature and the target temperature is large), proportional valve control is performed according to the change rate of the current temperature.

  (5) When settling (when the deviation between the current temperature and the target temperature is small), refer to the output power of the lamp heater 108 (particularly, the integral component that is not easily affected by disturbance such as temperature detection error) The proportional valve is controlled so that it falls within the proper output range. At that time, when the output power goes out of the proper output range, the proportional valve is operated according to the magnitude of the deviation between the two.

  (6) During settling (when the deviation between the current temperature and the target temperature is small), the overshoot is quickly suppressed and the settling time (from when the current temperature reaches the target temperature, even if a load disturbance is applied, that is, vacuum Even if the process is started in the chamber, the initial time until the ready state is reached in order to shorten the stable state in which the current temperature can be satisfactorily maintained at the target temperature (hereinafter referred to as the ready state). In the stage, the control gain is set higher than usual to increase the response of the proportional valve.

  (7) Has the function of suppressing hunting caused by the characteristics of the proportional valve.

  (8) There is an auto-tuning function that automatically detects the flow characteristics of the proportional valve used specifically, determines parameters suitable for the proportional valve, and applies the parameters to the proportional valve characteristic compensation table. .

  The following new items are also adopted for the output control of the lamp heater 108 performed by the lamp controller 132.

  (9) In the initial stage until the above-mentioned ready state at the time of transition and settling, the speed type I-PD control is adopted and the gain is set high, so that the overshoot is kept small. In addition, after entering the ready state, the gain is set low to ensure stability.

  Hereinafter, these new matters will be described in order.

  FIG. 7 shows the overall flow of proportional valve control performed by the valve controller 131.

  As shown in the figure, a transient / settling determination (step 141) is performed. As a result, if it is determined that the state is transient, the proportional valve control operation (step 142) is performed. Valve control (step 143) is executed. In the proportional valve control at the time of transition (step 142), a control calculation is performed on the deviation between the change rate of the current temperature of the working fluid and a predetermined target value (target conversion rate) for the change rate. On the other hand, in the proportional valve control at the time of settling (step 143), the output power (reference lamp output) of the lamp heater 108 fed back from the lamp control (step 149) performed by the lamp controller 132 and a predetermined appropriate lamp output width. Control calculation is performed on the deviation.

  The calculation result 144 of the proportional valve control shows the operation amount (the difference between the current cooling capacity and that after the operation) regarding the cooling capacity of the heat exchanger 106 at both the transition time and the settling time. Next, a table (heat exchanger compensation table) for compensating nonlinear cooling characteristics of the heat exchanger 106 is applied to the cooling capacity operation amount 144 (step 145). A numerical value 146 that appears as a result indicates an operation amount (a difference between the current cooling water flow rate and that after the operation) regarding the cooling water flow rate. Next, a table (proportional valve compensation table) for compensating the non-linear flow characteristics of the proportional valves 112 and 114 is applied to the cooling water flow rate manipulated variable 146 (step 147). Here, two types of proportional valve compensation tables adapted to the respective characteristics may be applied to the two proportional valves 112 and 114, respectively. However, for practical purposes, the processing is simplified. In addition, one type of table adapted to the characteristics of the proportional valve 112 on the main path that requires higher-precision control can be applied to both proportional valves 112 and 114. The numerical value 148 finally obtained by the above control processing is the operation amount of each of the proportional valves 112 and 114 (the number of pulses applied to the motor driver that drives each valve, and the current pulse number position and that after the operation. Difference).

  FIG. 8 shows the flow of one method example of the transient / settlement determination shown in step 141 of FIG.

  As shown in the figure, when the temperature adjustment of the working fluid is started (step 151), first, the current temperature (PV) of the working fluid is compared with a predetermined target temperature (SV) (step 152). If so, it is determined that the settling time is reached, and the proportional valve control operation (step 143) at the settling time is entered as described above. On the other hand, if the current temperature (PV) is different from the target temperature (SV), it is determined that the current temperature (PV) is in transition, and the proportional valve control operation in transition (step 142) is entered as described above.

  While performing the proportional valve control operation at the time of transition (step 142), the current temperature (PV) is periodically compared with a predetermined target temperature (SV) (step 153), and the current temperature (PV) is set as the target. As long as the temperature (SV) has not been reached, it is determined that it is still in transition, and the proportional valve control operation (step 142) at the time of transition is continued, and when the current temperature (PV) reaches the target temperature (SV). Then, it is determined that the settling time has been reached, and the proportional valve control operation at the settling time is entered (step 143).

  FIG. 9 shows the flow of another example method of transient / settlement determination.

  As shown in the figure, when the temperature adjustment of the working fluid is started (step 161), first, the current temperature (PV) of the working fluid is compared with a predetermined target temperature (SV) (step 162). If so, it is determined that the settling time is reached, and the proportional valve control operation (step 143) at the settling time is entered as described above. On the other hand, if the current temperature (PV) is different from the target temperature (SV), it is determined that the current temperature (PV) is in transition, and the proportional valve control operation in transition (step 142) is entered as described above.

  While the proportional valve control operation at the time of transition (step 142) is being performed, it is periodically determined whether the working fluid is being heated or lowered and whether the target temperature (SV) is 40 ° C. or more (or less). Step 163). Here, 40 ° C. is different depending on whether the temperature of the working fluid is higher or lower and whether the change in the coolant flow rate has a particularly large effect on the temperature change of the working fluid. This is a threshold value set as a guideline. As a result of the determination, if the temperature is decreasing and the target temperature (SV) is 40 ° C. or higher, then the time required for the current temperature (PV) to reach the target temperature (SV) is determined as the current temperature (PV). ) Is estimated from the current rate of change, and it is determined whether the estimated time required for arrival is 60 seconds or longer (step 164). Here, 60 seconds is a value determined as an approximate expected value of the delay time from when the operation of the proportional valve is stopped until the effect actually appears in the temperature of the working fluid. As a result of the determination, when the required arrival time is 60 seconds or more, it is determined that the transition is still in progress, and the proportional valve control operation at the transition (step 142) is continued. Thereafter, when the required travel time is less than 60 seconds, the process proceeds to step 166, and the proportional valve operation is stopped until the current temperature (PV) reaches the target temperature (SV) (step 166), and then the current temperature ( When PV reaches the target temperature (SV), it is determined that the settling time has been reached, and the proportional valve control operation during settling (step 143) is entered. Thus, when the temperature is decreasing and the target temperature (SV) is 40 ° C. or higher, the current temperature (PV) reaches the target temperature (SV) 60 seconds before the target temperature (SV). The reason why the control is turned off and the proportional valve operation is stopped until settling time is to effectively reduce the amount of overshoot (that is, undershoot) that is likely to occur when the temperature is lowered with a particularly large cooling capacity.

  On the other hand, if the result of the determination in step 163 is that the temperature is being increased or the target temperature (SV) is less than 40 ° C., the process proceeds to step 165 and, as in the method example shown in FIG. While PV) has not reached the target temperature (SV), it is determined that it is still in a transient state, and the proportional valve control operation (step 142) in the transient state is continued, and the current temperature (PV) becomes the target temperature (SV). ) Is reached, it is determined that the settling time has been reached, and the proportional valve control operation during settling (step 143) is entered.

  FIG. 10 shows the flow of proportional valve control during the transition shown in step 142 in FIGS.

  The proportional valve control at the time of transient increases or decreases the temperature (PV) of the working fluid toward a target temperature at a constant speed. As shown in the figure, the change rate of the current temperature (PV) of the working fluid is obtained, the deviation between this and the predetermined target change rate is calculated (step S171), and the deviation of the change rate is calculated for a predetermined period (for example, 250 ms). ) (Step 172), and PI calculation (or PID calculation) is performed on the sampled deviation using a predetermined control gain (Kp) (step 173). The result of this calculation indicates the operation amount of the cooling capacity of the heat exchanger 106 (difference between the present and after operation). Then, it is determined whether the temperature is currently being raised or lowered (step 174). When the temperature is being raised, the cooling capacity is increased with respect to the operation amount obtained by the PI calculation (the proportional valve on the main path). The amount of operation in the direction of opening 112 is cut, and a filter that passes only the amount of operation in the direction of reducing the cooling capacity (closing the proportional valve 112) is applied (step 175). Further, when the temperature is decreasing, the operation amount in the direction of decreasing the cooling capacity (closing the proportional valve 112) is cut with respect to the operation amount obtained by the PI calculation, and the cooling capacity is increased (opening the proportional valve 112). A filter that passes only the manipulated variable is applied (step 176). Next, regardless of whether the cooling capacity is increased or decreased with respect to the operation amount that has passed through the filter, the operation amount that has an absolute value greater than the predetermined limit value is cut, and the operation amount that has an absolute value that is less than or equal to the limit value. A limiter that passes only the light is applied (step 177). The operation amount that has passed through this limiter is the operation amount of the cooling capacity that is finally output.

  Here, the target change speed is set to a value substantially equal to the response speed of the temperature control by the lamp heater 108. Due to the delay due to the heat capacity of the heat exchanger 108 and the like, even after the current temperature reaches the target temperature, the temperature change due to the transient control performed until just before that continues gradually becoming gentler. If the target change speed is substantially equal to the response speed of the temperature control by the lamp heater 108, even if the temperature change continues at the same speed after reaching the target temperature, the temperature change is suppressed by the output control of the lamp heater 108. Can do. A small value is set for the control gain (Kp). As a result, the proportional valve is gently operated, and the excessive operation of the proportional valve (too much opening / closing, that is, too cold / not too cold) is suppressed.

  The filters in steps 175 and 176 mean that the proportional valve operation is not returned even if a slight overshoot occurs in the proportional valve operation. In order to maintain a constant temperature increase or decrease, in principle, it is necessary to continue the proportional valve operation in one direction. That is, in order to maintain a constant rate of temperature increase, the cooling capacity increases as the working fluid temperature increases at the same cooling water flow rate. Therefore, it is necessary to continue the operation of reducing the cooling water flow rate (closing the proportional valve 112). is there. In order to maintain a constant temperature drop, the cooling capacity decreases as the temperature decreases at the same cooling water flow rate, and therefore it is necessary to continue the operation of increasing the cooling water flow rate (opening the proportional valve 112). For this reason, even if there is a slight overshoot in the operation of closing the proportional valve 112 when the temperature rises, and a slight overshoot in the operation of opening the proportional valve 112 during the temperature drop, the overshoot operation is appropriate after a short time. It will coincide with the quantity manipulation. Therefore, even if the proportional valve operation is somewhat excessive, smooth control can be performed if it is not returned.

  The purpose of the limiter in step 177 is to prevent an extremely large cooling capacity operation that cannot be handled by the output capacity of the lamp heater 108. Therefore, the limit value of the limiter is set to a cooling capacity capability operation amount (cooling amount difference / second) corresponding to 100% output power (for example, 3 kW) of the lamp heater 108.

  FIG. 11 shows the flow of proportional valve control during settling shown in step 143 in FIGS.

  The proportional valve control during settling is to control the amount of cooling water by operating the proportional valve so that the output of the lamp heater 108 falls within a predetermined appropriate range. As shown in the figure, the reference lamp output fed back from the lamp controller 132 (see FIG. 6) is compared with an appropriate output range having a predetermined lower limit value UL and an upper limit value UH, and the reference lamp output falls below the lower limit value UL. The reference lamp output falls within the appropriate output range when the reference lamp output deviates from the lower limit value UL, the reference lamp output deviates from the upper limit value UH when the reference lamp output exceeds the upper limit value UH. If so, a deviation of zero is output (step 181). This deviation is sampled at a predetermined cycle (for example, 250 milliseconds). Then, it is determined whether or not it is currently ready (step 183). Here, the ready state means that after the current temperature (PV) reaches the target temperature (SV), a predetermined amount of heat (for example, 1.5 kw when the target temperature is 40 ° C. or higher and less than 40 ° C.). Means that the current temperature (PV) can be maintained at the target temperature (SV) with a predetermined accuracy (for example, ± 1 ° C.) even if a load disturbance of 1 kW) occurs. A specific method for determining the ready state will be described later.

  As a result of the ready determination, if it is not yet ready, PI calculation (or PID calculation) using a relatively large control gain (Kp1 / TI) is performed on the sampled deviation (step 184). If the state is ready, PI calculation using a relatively small control gain (Kp2 / TI) (for example, half the value of Kp1 / TI) is performed on the sampled deviation ( Step 185). The result of this PI calculation shows the operation amount (difference between the present and after operation) of the cooling capacity of the heat exchanger 106. Next, a limiter similar to step 177 already described in the control at the time of transition in FIG. 10 is applied to the cooling capacity operation amount (step 186). The operation amount that has passed through this limiter is the operation amount of the cooling capacity that is finally output.

  For the reference lamp output described above, the I (integral) component of the P, I, and D components obtained by the PID calculation in the lamp controller 132 is used in principle. This is because the integral component is hardly affected by disturbances such as temperature detection errors (reacts to external load disturbances), and most closely represents the current cooling amount by the cooling water. However, as will be described later, the PID control method of the lamp control is different between before and after the ready state, and since the position type PID control is performed after the ready state, the integral component is taken out independently. However, since the speed type I-PD control that easily suppresses the overshoot is performed before the ready state is entered, the integral component cannot be extracted independently. For this reason, the integral component is used as the reference lamp output after the ready state is reached. Before the ready state is reached, values including all the components of P, I, and D are used.

  The appropriate output range (lower limit UL and upper limit UH) in step 181 is, for example, the lower limit UL is 30% output power (for example, 0.9 kW) of the lamp heater 108, and the upper limit UL is 60% output power (for example, 1.8 kW). If the lamp output is greater than or equal to the lower limit value UL, the lamp will continue until the proportional valve responds even when an expected maximum amount (for example, 1.5 kW) of load disturbance (which increases the working fluid temperature) occurs. The target temperature can be maintained with a predetermined accuracy (for example, ± 1 ° C.) only by controlling the output. The difference between the lower limit value UL and the upper limit value UH (the width of the appropriate output range) indicates that the proportional valve operation is further advanced during the delay time from when the proportional valve operation is performed until the working fluid temperature actually changes. Hunting occurs in which the fluctuation of the lamp output goes too far, then the proportional valve operation is returned to correct it, and the lamp output goes too far backward due to the above delay time. It is set to prevent this from happening. In other words, the width of the appropriate output range is set to an appropriate width (for example, 30% lamp output for the purpose of preventing hunting by preventing the proportional valve control from reacting to fluctuations in lamp output within the width. (The smaller the width, the higher the possibility that hunting will occur). Although not shown in FIG. 11, in the proportional valve control at the time of settling (especially, control before becoming ready), processing for suppressing hunting by reducing the control gain should hunting occur. This hunting suppression process will be described later.

  The control gains (Kp1 / TI, Kp2 / TI) in steps 184 and 185 are set within a range in which the lamp control can follow. That is, if the control gain is too high, the ramp control cannot follow, and the fluctuation of the working fluid temperature at the time of proportional valve operation will be too large. The proportional gain (Kp1) before entering the ready state is set to be relatively high, whereby the response of the proportional valve becomes faster and it is easy to suppress overshoot. On the other hand, the proportional gain (Kp2) after the ready state is set is set to be relatively low, whereby the response of the proportional valve is delayed and the control is stabilized. The integration time TI is set to a value that roughly corresponds to the time constant of the temperature change in the heat exchanger 106.

  FIG. 12 shows the function of the heat exchanger compensation table used in step 145 of FIG.

  As shown in the figure, the heat exchanger compensation table 190 has a characteristic (Pcx-1) almost opposite to the non-linear cooling characteristic (Pcx) of the heat exchanger 106, and the operation amount of the cooling capacity is determined by the cooling water. It has a function to convert the flow rate into a manipulated variable. The characteristic (Pcx-1) of the heat exchanger compensation table 190 is a function of the current temperature (PV) of the working fluid. That is, the cooling water flow rate manipulated variable with respect to the same cooling capacity manipulated variable varies depending on the working fluid temperature (PV). On the heat exchanger compensation table 190, the cooling capacity manipulated variable is defined as a ratio [%] to the rated output power of the lamp heater 108, for example. The operation amount of the cooling water flow rate is defined by the ratio of the cooling water flow rate flowing through the heat exchanger 106 to the total cooling water flow rate (a constant value, for example, 10 L / min) (for example, 1% = 100 cc / min). Has been. The characteristic (Pcx-1) of the heat exchanger compensation table 190 is determined based on the actual measurement result or calculation result of the characteristic (Pcx) of the heat exchanger 106.

  FIG. 13 shows a specific example of the characteristic (Pcx-1) of the heat exchanger compensation table 190.

  In FIG. 13, the horizontal axis indicates the working fluid temperature (PV). The vertical axis indicates the cooling water flow rate operation amount (ratio of the operation amount with respect to the total flow rate (for example, 10 L / min)) necessary for generating a cooling capacity corresponding to 100% lamp output (for example, 3 kW). A solid line graph 191 in the figure indicates a set value of this table 190 (characteristic (Pcx-1) of this table 190). In addition, the circular dot plot and the square dot plot are the inverse of the actual characteristic (Pcx) of the heat exchanger 106 when the cooling water temperature is the expected minimum value 15 ° C. and the maximum value 30 ° C., respectively. The characteristics are shown.

  As shown in the figure, the set value in this table 190 substantially corresponds to the characteristic (Pcx) of the heat exchanger 106 when the cooling water temperature is the minimum value of 15 ° C. The reason why the table characteristic (Pcx-1) is adapted when the cooling water temperature is the minimum value of 15 ° C. is that when the cooling water temperature is the minimum value of 15 ° C., the heat exchanger 106 exhibits the greatest cooling capacity. Therefore, the highest precision is required for the proportional valve control. The higher the cooling water temperature, the more coarsely proportional valve control is allowed.

  By using this table 190, the cooling water flow rate manipulated variable can be obtained from the cooling capacity manipulated variable as follows. For example, when the current temperature (PV) of the working fluid is 50 ° C., the cooling capacity manipulated variable is calculated as 10%. According to this table 190, when the current temperature (PV) is 50 ° C., the cooling water flow rate manipulated variable for generating 100% cooling capacity is 15%. Therefore, the cooling water flow rate manipulated variable corresponding to the cooling capacity manipulated variable of 10% is 1.5%. Here, since the 100% cooling water flow rate manipulated variable is 10 L / min, the 1.5% cooling water flow rate manipulated variable is 0.15 L / min.

  FIG. 14 shows the function of the proportional valve compensation table used in step 147 of FIG.

  As shown in the figure, the proportional valve compensation table 200 has a characteristic (Pcv-1) that is almost the reverse of the nonlinear flow characteristic (Pcv) of the proportional valve. It has the function of converting to quantity (number of pulses). The characteristic (Pcv-1) of the proportional valve compensation table 200 is a function of the current position (current pulse number position) (PL) of the proportional valve. That is, the proportional valve operation amount with respect to the same cooling water flow rate operation amount varies depending on the proportional valve position (PL). On the proportional valve compensation table 200, the operation amount of the cooling water flow rate is, for example, the ratio of the flow rate of the cooling water flowing through the heat exchanger 106 to the total flow rate of the cooling water (a constant value, for example, 10 L / min) (for example, 1 % = 100 cc / min). The proportional valve operation amount is the number of pulses (relative value from the current position) to be applied to further open or close the valve from the current position. The characteristic (Pcv-1) of the proportional valve compensation table 200 is determined based on the actual measurement results of the characteristics (Pcv) of many proportional valves of the same model.

  FIG. 15 shows the result of actual measurement of the characteristics of a number of proportional valves of a certain model.

  In FIG. 15, the horizontal axis indicates the pulse number position of each proportional valve (absolute value with the fully closed state as the origin), and the vertical axis indicates the pressure loss (Cv value) of each proportional valve. A solid characteristic curve 201 in the figure indicates a characteristic curve of a number of actually measured proportional valves that is closest to the left side in the figure, and a dotted characteristic curve 202 indicates a characteristic curve of the number of actually measured proportional valves. Of these, the one on the right side in the figure is shown. The characteristic curve of the other proportional valve existed between the two characteristic curves 201 and 202 shown in the figure.

  What is found from the actual measurement results is that the characteristic curves of all proportional valves have substantially the same shape as the characteristic curves 201 and 202 shown in the figure. The difference between the solids is mainly the position in the horizontal axis direction (number of pulses). Only position). Therefore, it can be said that the individual difference in the flow characteristics of the proportional valve is substantially only the position shift in the horizontal axis direction in the figure. As shown by the shape of the characteristic curves 201 and 202 in the figure, when a pulse is applied from the fully closed state, the Cv value remains zero for a while, but the Cv value suddenly increases at certain pulse number positions 203 and 204. Stand up to. The pulse number positions 203 and 204 are referred to as “first sudden change portions” of the proportional valve characteristic in this specification. As pulses are further added, the Cv value is substantially constant for a while from the first sudden change portion, but the Cv value starts to increase at certain pulse number positions 205 and 206. The positions 205 and 206 are referred to as “second sudden change portions” of the proportional valve characteristic in this specification. From this second sudden change portion, the Cv value also increases as the number of pulses increases.

  FIG. 16 shows a specific example of the characteristic (Pcv-1) of the proportional valve compensation table 200 created based on the actual measurement characteristic shown in FIG.

  In FIG. 16, the horizontal axis indicates the pulse number position of each proportional valve when the first sudden change sections 203 and 204 of each proportional valve shown in FIG. The vertical axis shows the cooling of the main path that occurs when the proportional valve 112 of the main path is moved by one pulse from each pulse number position under the condition that the Cv value of the bypass path is constant (for example, = 1.5). The amount of water flow change is shown. The amount of change in the vertical axis is expressed as a ratio [%] (for example, 1% = 0.1 L / min) to the total flow rate of the cooling water (for example, 10 L / min). A thin solid characteristic curve 207 in the figure corresponds to one of the actually measured characteristic curves 201 and 202 shown in FIG. Since the position of the number of pulses of the first sudden change sections 203 and 204 is the origin of the horizontal axis, the individual differences in the proportional valve characteristics are removed, so that the characteristics of all proportional valves are almost the same as the characteristic curve 207 shown in the figure. Become. In this characteristic curve 207, a portion 208 is a first sudden change portion, and a portion 109 is a second sudden change portion. A characteristic curve 210 shown by a bold solid line in the figure is a set value of the proportional valve compensation table 200, that is, a characteristic (Pcv-1) of the proportional valve compensation table 200. The set value 210 of the proportional valve compensation table 200 has a simple shape for the convenience of mechanical processing, but is substantially the same as the actual characteristic 207 of all the proportional valves from which individual differences are removed.

  As is clear from the above description, the setting value 210 of the proportional valve compensation table 200 represents a common part obtained by removing individuality (individual difference) from the characteristics of all proportional valves of the same model. It can be commonly applied to proportional valves. Here, the individuality (individual difference) of each proportional valve is typically reflected in the absolute pulse positions of the first sudden change sections 203 and 204 of each proportional valve shown in FIG. Therefore, in the proportional valve compensation table 200, a numerical value representing the individuality of each proportional valve (for example, the absolute pulse position of the first sudden change sections 203 and 204) can be taken in as a parameter. In addition, other device characteristics (such as pressure loss) that affect the specific characteristics of the proportional valve can also be captured as parameters. The pulse number position of the table 200 (number of pulses shown in FIG. 16) is shifted by the number of pulses corresponding to the acquired parameter, thereby matching the characteristics of the proportional valve compensation table 200 to the individuality of each proportional valve. . The above parameters are automatically determined by performing auto tuning described later.

  As shown in FIG. 7, the heat exchanger compensation table 190 and the proportional valve compensation table 200 described above are used in combination in the latter stage of the proportional valve control process, so that the nonlinear cooling characteristics of the heat exchanger and the nonlinearity of the proportional valve are used. Therefore, it is possible to compensate for a good flow rate characteristic. Therefore, in the proportional valve control process, it is not necessary to consider the nonlinear characteristics of the heat exchanger and the proportional valve. In addition, if the specific model of the proportional valve or heat exchanger used is changed, it can be handled by changing only the corresponding table. Further, the heat exchanger compensation table 190 and the proportional valve compensation table 200 can be easily made from actual characteristics of the proportional valve and the heat exchanger, respectively, so that a highly accurate one can be obtained.

  In the proportional valve compensation table 200, the pulse number position is defined not by the absolute pulse number with the fully closed position as the origin, but by the relative pulse number with the first sudden change part for each proportional valve as the origin. The individuality of each proportional valve and the characteristics of the device environment in which the proportional valve is used (for example, pressure loss of piping) can be taken in as parameters and adapted to them. For this reason, there is no wide margin in consideration of individual differences as in the prior art, and control responsiveness is improved as compared with the prior art. In the proportional valve compensation table 200, the flow rate is not defined as an absolute flow rate at each pulse number position, but as a relative value indicating what percentage of the flow rate changes when one pulse is moved at each pulse number position. Therefore, it is robust against changes in proportional valve characteristics due to changes over time.

  By the way, as shown in FIG. 4, there are a proportional valve 112 of the main passage 113 and a proportional valve 114 of the bypass passage 115, and each of the two proportional valves 112, 114 has another proportionality adapted to each. A valve compensation table can be applied. However, in practice, one proportional valve compensation table adapted to the proportional valve 112 of the main path 113 is applied not only to the proportional valve 112 of the main path 113 but also to the proportional valve 114 of the bypass path 115. The process can be simplified. One reason for this is that, due to the action of the constant flow valve 117 shown in FIG. 4, the total flow rate of the cooling water is always constant regardless of the pressure loss of the two proportional valves 112 and 114, and This is because the valves 112 and 114 can be operated one by one, and when one is operated, the other is fully opened. Another reason is that, in most of the variable range of the target temperature (SV), only the proportional valve 112 of the main path 113 is operated for controlling the cooling capacity, and the target temperature ( This is because the proportional valve 114 of the bypass passage 115 is operated only in a part of the region where SV) is low, but the proportional valve operation in that region is sufficient with a coarse resolution, and high-definition operation is not required.

  FIG. 17 shows a processing flow of ready determination shown in step 183 in the proportional valve control during settling in FIG.

  As shown in the figure, when the temperature adjustment operation of the working fluid is started (step 211), it is first determined whether or not the current temperature (PV) of the working fluid has reached the target temperature (SV) (step 212). . Before reaching the target temperature (SV), the above-described proportional valve control during transition is performed, so there is no room for ready determination. When the current temperature (PV) passes the target temperature (SV), the above-described proportional valve control during settling is started. When the proportional valve control at the time of settling is started, after waiting for a time (for example, 1 second) that the proportional valve control surely enters operation (step 213), it is determined whether or not the overshoot has ended (step 214). ) Wait until the overshoot is over. When overshoot ends, ready determination (step 183) is entered.

  When the ready determination is entered, it is first determined whether the previous control at the time of transition was a temperature increase or a temperature decrease (step 215). If the temperature is lowered during the transition, the lamp output has become a large value since the overshoot (that is, the undershoot) has been suppressed so far when the overshoot is over (appropriate as shown in FIG. 11). The value is surely larger than the lower limit value UL of the lamp output range). Therefore, even if a load disturbance occurs immediately, the lamp output can be lowered to sufficiently absorb the load disturbance, so that it is immediately determined that the ready state has been reached (step 219).

  On the other hand, if the result of determination in step 215 is that the temperature has been raised during the transition, when the overshoot is over, the lamp output is low because the overshoot has been suppressed so far (FIG. 11). May be smaller than the lower limit UL of the appropriate lamp output range shown in FIG. In this case, unless the working fluid is cooled to some extent with the cooling water and the lamp output is increased to the lower limit UL or more by that amount, the ready state is not obtained. Therefore, first, in step 216, it is determined whether or not the pulse number position of the proportional valve 112 on the main path is greater than or equal to the second sudden change portion (see FIG. 15). When the position of the number of pulses of the proportional valve 112 is less than the second sudden change portion (on the left side of the second sudden change portion in FIG. 15), the proportional valve 112 cannot be opened immediately (even if a load disturbance occurs, the proportional valve 112 Cannot respond immediately). Therefore, in this case, it is determined whether the lamp output U is higher or lower than the lower limit value UL (step 217), and it is determined that the lamp output U has become ready after waiting until the lamp output U is reliably higher than the lower limit value UL. (Step 219).

  On the other hand, if the result of determination in step 216 is that the pulse number position of the proportional valve 112 is greater than or equal to the second sudden change portion (on the right side of the second sudden change portion in FIG. 15), the proportional valve 112 can be opened immediately and the load Even if a disturbance occurs, the proportional valve 112 can react immediately. Therefore, in that case, it is determined whether or not the lamp output U has exceeded a value slightly lower than the lower limit value UL (for example, 10%) (step 219). As soon as the value approaches the value UL, it is determined that the ready state has been reached (step 219).

  In this way, as soon as the state of the device is actually ready by determining whether it is in the ready state from the various states of the device such as lamp output, temperature change and proportional valve opening, the ready state The process of the vacuum chamber can be started quickly without waiting for time.

  FIG. 18 shows the flow of the hunting suppression process performed in the proportional valve control at the time of settling (in particular, control before the ready state is set).

  Here, hunting refers to a state in which the lamp output fluctuates beyond the above-described proper lamp output range (lower limit value UL and upper limit value UH) due to proportional valve operation. When hunting occurs, the proportional valve repeats opening and closing operations in a short time in order to suppress it, so that hunting can be detected by detecting the operation of such a proportional valve.

  As shown in FIG. 18, when the temperature adjustment operation of the working fluid is started (step 211), the transient / settling judgment is performed (step 212). When the settling time is judged, the proportional valve control at the time of settling described above (FIG. 18). 18 is omitted) and hunting suppression processing is started (step 213). In the hunting suppression process, first, the above-described ready determination result is referred to (step 214). As a result, if it is already in the ready state, there is no longer a possibility of occurrence of hunting, so this hunting suppression process is terminated.

  If the result of determination in step 214 is that the ready state has not yet been reached, it is next determined whether or not hunting has occurred (step 215). Here, for example, it is checked whether or not the set of the opening and closing of the proportional valve has been repeated three times or more within the last 60 seconds, and if so, it is determined that hunting has occurred (step 216). . If hunting has occurred, the proportional gain (Kp) of the control is reduced to half (that is, reduced to the same value as the control gain in the ready state (the value of block 185 in FIG. 11)) to suppress it. (Step 217).

  Thereafter, returning to step 214, if there are still more than three opening / closing operations in 60 seconds in step 215, it is determined that hunting is continuing (216), and the proportional gain (Kp) is lowered to half of the current value. (Step 217). Thus, the proportional gain (Kp) is decreased until the hunting converges. When the hunting converges (less than 3 times in step 215) and becomes ready in step 214, there is no longer a possibility of occurrence of hunting, so the proportional gain (Kp) is set to the specified value (block 185 in FIG. (Step 218), and this hunting suppression process is terminated.

  The control of the proportional valves 112 and 114 performed by the valve controller 131 (see FIG. 6) has been described above. Next, the control of the lamp heater 108 performed by the lamp controller 132 (see FIG. 6) will be described.

  FIG. 19 shows an overall flow of control of the lamp heater 108 performed by the lamp controller 132.

  As shown in the figure, when the temperature adjustment operation of the working fluid is started (step 231), first, a predetermined large gain value is set to the control gain (Kp) of PID control (step 232), and the large control gain ( Kp) is used to control the lamp output by the speed type I-PD control method (step 233). At the start of temperature adjustment, it is usually a transient state. Therefore, the ramp control during the transient state is performed by a speed type I-PD control method using a large control gain (Kp). When the state shifts from the transient state to the settling time, the ready determination 234 is performed as described above. As a result, the speed type I-PD control using the large control gain (Kp) is continued while the ready state is not yet established. Thereafter, when the ready state is entered, the control gain (Kp) is switched to a predetermined small value (for example, half of the initial gain value) (step 235), and the control method is switched to the position type PID control. The lamp output is controlled by the PID control method (step 236).

  In this way, the ramp control is performed by the speed type I-PD control method using a large control gain until the ready state at the settling time is reached after the transition time, and after the ready state at the settling time is reached. Is performed by a position type PID control method using a small control gain. Thereby, the amount of overshoot can be kept small before reaching the ready state, and the control can be stabilized after reaching the ready state.

  FIG. 20 shows the flow of lamp control by the method of speed type I-PD control, and FIG. 21 shows the flow of lamp control by the method of position type PID control.

  The method of speed type I-PD control and position type PID control itself is well known to those skilled in the art and will not be described here. The reference lamp output sent to the proportional valve control at the time of settling cannot be extracted only when the speed type I-PD control of FIG. 20 is performed before reaching the ready state as described above. , P, I, and D are all included values. On the other hand, when the position type PID control of FIG. 21 is performed after reaching the ready state, it has a value closest to the current cooling amount by the cooling water. Only I component.

  22 and 23 show a specific change in the current temperature (PV) of the working fluid with the passage of time, and a transition in the state of the ramp control and the proportional valve control. FIG. 22 shows the case when the temperature is raised, and FIG. 23 shows the case when the temperature is lowered.

  In these drawings, a thick solid line curve indicates a change in the current temperature (PV), a thick one-dot chain line curve indicates a change in the proportional valve opening, and a thick two-dot chain line curve indicates a change in lamp output.

  As shown in FIG. 22, at the time of temperature increase, the proportional valve control at the time of transition is performed from time t1 until the current temperature (PV) reaches the target temperature (SV) until the time t1. Proportional valve control is performed. Overshoot occurs from time t1, and overshoot ends at time t2 when the current temperature (PV) returns to the target temperature (SV) again. Thereafter, at time t3 when the lamp output increases and reaches the lower limit value UL of the appropriate lamp output width, it is determined that the ready state has been reached, and the lamp control is switched from the large gain I-PD control to the small gain PID control. The gain of proportional valve control during settling also switches from a large value to a small value.

  As shown in FIG. 23, when the temperature falls, the transient state continues from the start of temperature adjustment until time t2 when the current temperature (PV) reaches the target temperature (SV), but the current temperature is reached in another 60 seconds before that. At the predicted time t1 when (PV) reaches the target temperature (SV), the proportional valve control during the transition ends, and thereafter, the proportional valve is not operated until time t2. Proportional valve control during settling is performed from time t2. At time t3 when overshoot occurs from time t2 and the current temperature (PV) returns to the target temperature (SV) again, it is determined that the overshoot is completed and at the same time the ready state is reached. The PD control is switched to the small gain PID control, and the gain of the proportional valve control at the time of settling is also switched from a large value to a small value.

  This is the end of the description of the control during normal temperature adjustment. Finally, auto-tuning processing for adapting the proportional valve compensation table to specific proportional valve characteristics will be described.

  FIG. 24 shows the overall flow of the auto tuning process.

  In auto tuning, the lamp output control is performed so that the working fluid temperature is controlled to a predetermined target temperature, and the proportional valve 112 on the main path is operated by a certain number of pulses, and the fluctuation of the lamp output due to the operation is monitored. Thus, by detecting the pulse number position of the first sudden change portion of the proportional valve 112 and setting it as a parameter in the proportional valve compensation table 200, the characteristics of the proportional valve compensation table 200 are adapted to the individuality of the proportional valve 112. Is. This auto-tuning process can be performed at any time as necessary.

  As shown in FIG. 24, when the auto-tuning process is started (step 271), first, the proportional valves 112 and 114 of both the main path and the bypass path are fully opened (step 272), the pump 103 is operated and the working fluid and Flowing cooling water (step 273), and wait for 1 minute in that state (step 276) When the flow is stabilized, the current temperature (PV) of the working fluid enters a predetermined low temperature range (for example, 40 ° C. or less). It is checked whether or not there is (step 275). If the current temperature (PV) is 40 ° C. or less, the flow rate of the working fluid is measured (step 276), and the lamp control PID constant is set based on the flow rate value (step 277). Here, the flow rate of the working fluid is measured after the current temperature (PV) becomes 40 ° C. or less because of the characteristics of the flow sensor, the higher the working fluid temperature, the smaller the flow rate is actually measured. This is because the flow rate is accurately measured at a low temperature.

  Thereafter, the proportional valve 112 of the main path to be measured is fully closed (step 278), the lamp control method is the position type PID control (step 279), and the target temperature (SV) is set to a predetermined high temperature (for example, 80 ° C.). ) (Step 280) and a temperature raising operation is performed (step 281). When it is confirmed that the current temperature (PV) of the working fluid has reached a target temperature (SV) (for example, 80 ° C.) (step 282), a proportional valve flow rate characteristic tuning process is performed (step 283). This proportional valve flow rate characteristic tuning process is to monitor the fluctuation of the lamp output while operating the proportional valve 112 on the main path in increments of a predetermined number of pulses (for example, 10 pulses). This is a process of determining the pulse number position of the unit and setting it as a parameter in the proportional valve compensation table. Here, the reason why this proportional valve flow rate characteristic tuning process is performed under a high target temperature (SV) such as 80 ° C. is that the heat generation amount inside the apparatus (such as a pump) is larger than the heat generation amount at such a high temperature. This is because, even if the proportional valve is in the fully closed state (that is, without cooling), the working fluid temperature can be controlled to be the target temperature constant only by the lamp control.

  When the proportional valve flow characteristic tuning process is finished, the auto tuning process is finished (step 284), the target temperature (SV) is returned to the original value before starting the auto tuning process (step 285), and then the normal operation is started. (Step S286).

  FIG. 25 shows the flow of the proportional valve flow rate characteristic tuning process shown at step 283 in FIG.

  As shown in the figure, first, 120 pulses are applied to the proportional valve 112 in the fully closed state of the main path, and the proportional valve 112 is opened to an absolute pulse number position (VP) of 120 pulses (S291). Then, the operation is continued for one minute without operating the proportional valve 112 (step 293), and the fluctuation amount of the lamp output is integrated and recorded (that is, the fluctuation amount of the integral component of the position type PID control in that one minute is calculated). (Step 292). After one minute has passed, 10 pulses are further applied to the proportional valve 112 to advance the absolute pulse number position (VP) of the proportional valve 112 by 10 pulses (step 296). Similarly, the operation is continued for one minute without operating the proportional valve 112 (step 293), and the fluctuation amount of the lamp output is integrated and recorded (step 292).

  Thus, starting from the absolute position (VP) of 120 pulses, the proportional valve 112 is opened every 10 pulses, and the operation of integrating and recording the lamp output fluctuation amount for 1 minute at that position is repeated. If this operation is performed until the absolute position (VP) of the proportional valve 112 reaches 270 pulses (step 294), the integrated value of the lamp output fluctuation amount recorded at each absolute position in increments of 10 pulses is compared. The absolute position (VP) having the maximum value is determined as the first sudden change portion, and the absolute position of the first sudden change portion is set as a parameter of the proportional valve compensation table 200 (step 297). This completes the proportional valve flow characteristic tuning process.

  Although one embodiment of the present invention has been described above, the above embodiment is merely an example for explaining the present invention, and is not intended to limit the present invention only to the above embodiment. Therefore, the present invention can be implemented in various forms other than the above-described embodiment.

  For example, in the above embodiment, the proportional valve control has been described by taking the case where the amount of cooling water is controlled by a proportional valve as an example. However, the proportional valve control of the present invention is also used when the flow rate of the working fluid is controlled by a proportional valve. The method can be applied.

Sectional drawing which shows schematic structure of the general vacuum chamber used with a semiconductor manufacturing apparatus. The block diagram which shows the structure of the conventional fluid temperature control apparatus (low temperature machine) used for temperature control of the low temperature part of the vacuum chamber of FIG. The block diagram which shows the structure of another conventional fluid temperature control apparatus (high temperature machine) used for temperature control of the high temperature part of the vacuum chamber of FIG. The block diagram which shows the mechanical system structure of the fluid temperature control apparatus concerning one Embodiment of this invention. FIG. 2 is a block diagram showing a hardware configuration for performing a control operation of the fluid temperature control apparatus 100. FIG. 2 is a block diagram showing a basic functional configuration of a controller 121. The figure which shows the whole flow of the proportional valve control which the valve controller 131 performs. The figure which shows the flow of one method example of the transient / settling judgment shown to step 141 of FIG. The figure which shows the flow of another method example of the transient / settling judgment shown to step 141 of FIG. The figure which shows the flow of the proportional valve control at the time of the transition shown by step 142 in FIGS. The figure which shows the flow of the proportional valve control at the time of the stabilization shown by FIG. The figure which shows the function of the heat exchanger compensation table used by step 145 of FIG. The figure which shows the specific example of the characteristic (Pcx-1) of the heat exchanger compensation table 190. FIG. The figure which shows the function of the proportional valve compensation table used by step 147 of FIG. The figure which showed the result of having measured the characteristic of many proportional valves of a certain model. The figure which shows the specific example of the characteristic (Pcv-1) of the proportional valve compensation table 200 produced based on the actual measurement characteristic shown in FIG. The figure which shows the processing flow of the ready determination shown by step 183 in the proportional valve control at the time of settling of FIG. The figure which shows the flow of the hunting suppression process performed by the proportional valve control at the time of settling (especially control before becoming a ready state). The figure which shows the whole flow of control of the lamp heater 108 which the lamp controller 132 performs. The figure which shows the flow of the lamp control by the method of speed type | mold I-PD control. The figure which shows the flow of the lamp control by the method of position type PID control. The figure which shows the change of the present temperature (PV) of a working fluid at the time of temperature rising, and the transition of the state of ramp control and proportional valve control. The figure which shows the change of the present temperature (PV) of a working fluid at the time of temperature fall, and the transition of the state of ramp control and proportional valve control. The figure which shows the whole flow of the process of auto tuning. The figure which shows the flow of the proportional valve flow characteristic tuning process shown by step 283 in FIG.

Explanation of symbols

DESCRIPTION OF SYMBOLS 100 Fluid temperature control apparatus 101 Circulation path | route of a working fluid 106 Heat exchanger for cooling 108 Lamp heater (heat exchanger for heating)
107 Flow Sensor 109 Temperature Sensor 111 Cooling Water Path 112, 113 Proportional Valve 117 Constant Flow Valve 121 Controller 131 Valve Controller 132 Lamp Controller 142 Transient Proportional Valve Control 143 Settling Proportional Valve Control 190 Heat Exchanger Compensation Table 200 Proportional Valve compensation table

Claims (6)

A heat exchanger for cooling the working fluid with the coolant, in which the working fluid and the coolant flow;
A flow rate control valve for controlling the flow rate of the working fluid or coolant flowing through the heat exchanger;
An electrical heater for heating the working fluid exiting the heat exchanger;
A heater controller for operating the output power of the heater to control the temperature of the working fluid exiting the heater to a target temperature;
In order to control the cooling capacity of the heat exchanger, a valve control unit for operating the flow control valve,
The valve control unit is
A transient valve control means for operating the flow rate control valve according to a change speed of the current temperature at a transition before the current temperature of the working fluid reaches the target temperature;
Fluid temperature control having a settling time valve control means for operating the flow rate control valve so that the output power of the heater falls within a predetermined appropriate output range at the time of settling after the current temperature reaches the target temperature. apparatus. The settling time valve control means,
Means for feeding back reference output power from the heater controller;
2. The fluid according to claim 1, further comprising means for operating the flow rate control valve in accordance with a magnitude of deviation between the reference output power and the appropriate output range when the reference output power is outside the appropriate output range. Temperature control device. The settling time valve control means,
Means for calculating an operation amount of the flow control valve using a relatively large control gain during an overshoot immediately after the current temperature reaches the target temperature;
Means for calculating the manipulated variable of the flow control valve using a relatively small control gain after the overshoot is completed;
The fluid temperature control device according to claim 1, comprising: The settling time valve control means,
Means for detecting the occurrence of hunting in which the output power of the heater vibrates with a width exceeding the appropriate output range;
The fluid temperature control device according to claim 1, further comprising means for reducing a control gain used for calculating an operation amount of the flow control valve when the hunting is detected. The heater control means;
Means for calculating an operation amount of the output power of the heater by a speed type I-PD control method using a relatively large control gain at the time of transient and overshoot at the time of settling;
2. The fluid temperature control device according to claim 1, further comprising means for calculating an operation amount of the output power of the heater by a method of PID control using a relatively small control gain after the overshoot at the settling time. . The flow rate of the working fluid or coolant flowing through the heat exchanger is controlled by a flow control valve, and the temperature of the working fluid is controlled by heating the working fluid that has exited the heat exchanger with an electric heater. In the method
A heater control step of operating the output power of the heater to control the temperature of the working fluid exiting the heater to a target temperature;
A valve control step of operating the flow rate control valve to control the cooling capacity of the heat exchanger;
The valve control step comprises:
A transient valve control step of operating the flow rate control valve according to a change speed of the current temperature at a transition time before the current temperature of the working fluid reaches the target temperature;
A fluid temperature control having a settling time valve control step of operating the flow rate control valve so that the output power of the heater falls within a predetermined appropriate output range at the time of settling after the current temperature reaches the target temperature. Method.

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