Patent Number: 043222676
Section: description

DESCRIPTION OF THE PREFERRED EMBODIMENT FIG. 1 shows an embodiment of this invention. Steam W.sub.M generated in the reactor 1 is normally fed to a main turbine, not shown, via a main steam conduit C.sub.M and isolation valves IV immediately inside and outside a container vessel PV. When a fault occurs inside or outside the reactor 1 and when the reactor 1 is scrammed by a mechanism, not shown, with the result that the isolation valves IV are closed, the decay heat Q.sub.R generated in the reactor core 25 is taken out or dissipated by an RHR (residual heat removal) system shown in FIG. 1. Schematically, the RHR system has such a constitution as follows: the steam generated in the reactor 1 is led to a heat exchanger 4 and condensed there into water 5 and the condensed water 5 is fed back into the reactor 1 by a pump 10 driven by a turbine 12 actuated by the reactor steam so as to cool the reactor core 25. A control valve 3 is controlled by a condensate flow control apparatus A, which is well known and easily obtainable. The function of this condensate flow control apparatus A is as follows: the reactor steam generated by the decay heat Q.sub.R is led through the control valve 3 to the heat exchanger 4 and condensed into water 5 at a rate of a flow W.sub.H by a cooling pipe assembly 6 in the heat exchanger 4, and the pressure P.sub.H in the heat exchanger 4 is controlled to the value (P.sub.H).sub.ref set by a reference pressure setting means 22 by means of a pressure detector 14, a pressure controller 15 and the regulation valve 3 so that the condensate flow W.sub.H from the heat exchanger 4 may be stabilized. Make-up water flow W.sub.c from a make-up water tank 8 is added to the condensate flow W.sub.H at the point J and the resultant flow, i.e. feedwater flow, W.sub.F is fed to the pump 10. A check valve 9 serves to prevent the return of the supplied make-up water to the make-up water tank 8. The aperture of a control valve 7 is controlled by a make-up water control apparatus C. The feed water W.sub.F is pressurized by the pump 10 and supplied into the reactor 1 through a check valve 11. The pump 10 is driven by the turbine 12 and the flow W.sub.TB of steam to drive the turbine 12 is controlled by a regulation valve 13 near the inlet of the turbine 12, which valve is in turn controlled by a feedwater flow control apparatus B. According to this invention, the problems concerning the lowering of the reactor water level and the temperature fall rates can be solved by the combination of the control apparatuses B and C described above. Namely, the RHR system as an embodiment of this invention operates as follows. In the case of scram, the reactor water level lowers since the steam W.sub.TB to drive the turbine 12 is exhausted out of the system. To compensate the exhausted steam, i.e. reactor water, the make-up water control apparatus C is used to change the pressure at the outlet of the make-up water tank 8 according to the change in the reactor water level so that a required amount of make-up water W.sub.c is supplied into the reactor 1 and also the condensate flow W.sub.H is decreased. On the other hand, the temperature fall rates in the reactor 1 vary owing to the supply of the make-up water and the change in the decay heat with time. Accordingly, the residual heat is removed safely during a shortest period of time by controlling the feedwater flow W.sub.F by the feedwater control apparatus B in such a manner that the maximum one of the temperature fall rates at several points in the reactor 1 always equals the preset desired value. First, the control of the reactor water level by the make-up water control apparatus will be explained. The level L.sub.R of the reactor water is detected by a water level detector 31. A water level controller 32 determines the desired value (P.sub.s).sub.ref for the pressure at the outlet of the make-up water tank 8 in accordance with the difference between the detected level L.sub.R and the preset value (L.sub.R).sub.ref set by a reference water level setting means 33. Then, the pressure P.sub.s at the outlet of the make-up water tank 8 is controlled to the desired value (P.sub.s).sub.ref by the combined operations of a pressure detector 16, a pressure controller 17 and the control valve 7. The relationships between the signals at points in the control apparatus C, the various flows and the level of the reactor water are as shown in FIG. 2. Now, reference should be had to FIG. 2. Suppose that the RHR system is started at an instant and that the level L.sub.R of the reactor water lowers as shown in diagram (a). The references value (L.sub.R).sub.ref set by the reference water level setting means 33 is made approximately equal to the reactor water level L.sub.R assumed before the instant t.sub.0 and the water level controller 32 receives an input (L.sub.R).sub.ref =L.sub.R and in turn delivers a constant desired value, i.e. reference pressure (P.sub.s).sub.ref before the instant t.sub.0. The pressure P.sub.s detected at the joining point J by the pressure detector 16 is slightly higher than a pressure P.sub.c to open the check valve 9 before t.sub.0 since the RHR system is not operating before t.sub.0. The pressure P.sub.s increases rapidly after the start of the operation of the RHR system but remains lower than (P.sub.s).sub.ref. The pressure controller 17 receives an input (P.sub.s).sub.ref -P.sub.s &gt;0 and controls the aperature V of the control valve 7 to the fully opened state. Consequently, the detected pressure P.sub.s is higher than the pressure P.sub.c to open the check valve 9 and it therefore follows that W.sub.c =0 and W.sub.H =W.sub.F. When the level L.sub.R of the reactor water lowers at t.sub.0 and the condition that (L.sub.R).sub.ref -L.sub.R .gtoreq.0 is reached, the pressure setter 32 decreases the value (P.sub.s).sub.ref. When the condition that (P.sub.s).sub.ref -P.sub.s &lt;0 is reached at t.sub.1, the pressure controller 17 starts to close the control valve 7. As the aperture of the valve 7 decreases, the pressure P.sub.s at the point J lowers. At an instant t.sub.2, the pressure P.sub.c to open the check valve 9 exceeds the pressure P.sub.s, that is, P.sub.c &gt;P.sub.s so that make-up water starts to flow at a rate W.sub.c from the tank 8 via the check valve 9. The expression (3) given below shows the relationship between the flow W.sub.c and the pressure P.sub.s. ##EQU3## where k is the coefficient of friction loss of the make-up water pipe, P.sub.o the pressure in the make-up water tank 8, H.sub.c the difference between the potential heads at the surface of the make-up water in the tank 8 and at the position of the feedwater pipe, and .gamma..sub.w the specific weight of the make-up water, all these quantities being constant. Accordingly, W.sub.c varies depending only upon P.sub.s, as shown in FIG. 3. If the value under the radical sign in (3) is negative, as occurs in the case where P.sub.s exceeds P.sub.c, then the check valve 9 is completely closed so that W.sub.c =0. After t.sub.2, it is seen that W.sub.F =W.sub.c +W.sub.H. It should here be noted that W.sub.F remains constant before, at and after t.sub.2 since W.sub.F is controlled to a roughly constant value by the control apparatus B governing the operation of the pump 10, that is, since W.sub.H is decreased by an amount equal to the increment of W.sub.c. As a result of the above control that make-up water more than the exhausted water is supplied into the RHR system, the reactor water recovers its initial level (L.sub.R).sub.ref. The instant t at which the water level L.sub.R returns to the value at t.sub.0, is theoretically equal to the instant, i.e. t.sub.3 in FIG. 2(a), when the exhausted amount ##EQU4## becomes identical with the compensated amount ##EQU5## Until the instant t.sub.3, before which (L.sub.R).sub.ref &gt;L.sub.R, both the preset value (P.sub.s).sub.ref and the aperture V of the valve 7 decrease. But after t.sub.3, the condition that (L.sub.R).sub.ref &lt;L.sub.R is reached so that (P.sub.s).sub.ref begins to increase. The actual change in the pressure P.sub.s lags behind the preset value (P.sub.s).sub.ref and therefore P.sub.s starts to increase in retard of (P.sub.s).sub.ref. At this time, (P.sub.s).sub.ref &gt;P.sub.s so that the aperture V of the valve 7 continues to increase for a certain time after t.sub.3. When P.sub.s increases until P.sub.s &gt;P.sub.c at t.sub.4, the check valve 9 is completely closed and thereafter W.sub.c =0. After t.sub.4, the water level L.sub.R lowers owing to the exhaustion of W.sub.TB and the condition that (L.sub.R).sub.ref &gt;L.sub.R is again reached at t.sub.5. The operation after t.sub.5 is substantially the same as that after t.sub.0 in the initial stage and the description of the further operation will be omitted. The control apparatus C attempts to stabilize the reactor water level by repeating the control operation in the period from t.sub.0 to t.sub.5. In FIG. 2, although the level fluctuation appears considerable, this is for the convenience of explanation and the actual fluctuation can be confined within a very small range. Now, consider the operation of the control apparatus A while the control apparatus A is at operation. In the control apparatus A, the pressure detected by the detector 14 increases upon closure of the valve 7 so that the regulation valve 3 is choked to decrease the internal pressure of the heat exchanger 4. Consequently, the pressure at the inlet of the control valve 3 increases to decrease the flow W.sub.H. The control apparatus C performs the control of reactor water level and the control of pressure in cascade, but only the control of water level is basically necessary so that it is only necessary to control directly the aperture of the control valve 7 by the pressure setter 32. In practice, however, the response to the change in the variable to be controlled is slow if the water level control system alone is employed. Therefore, the provision of the pressure control system as a minor control loop will improve the stability of control. Next, the feedwater flow control apparatus B will be described. When the RHR system is started, the control apparatus B controls the temperature fall rates at various points in the reactor to be smaller than their corresponding, preset values. Namely, since the rate (-.DELTA.Temp/.DELTA.t) of the fall of the reactor water temperature as one of the typical temperature fall rates associated with a reactor is expressed such that ##EQU6## the flow W.sub.F of feed water into the reactor must be varied in accordance with the variations with time of Q.sub.R and W.sub.c in order to keep the temperature fall rate (-.DELTA.Temp/.DELTA.t) of the reactor water constant at a desired value. The symbols appearing in the expression (4) are the same as those used in the expression (2), W.sub.c (i.sub.f -i.sub.F) being an amount of heat required to make the make-up water flow W.sub.c saturated in the reactor and W.sub.c (i.sub.g -i.sub.f) to turn the saturated water W.sub.c into steam. To achieve such a control as described above, temperature detectors 34 and 35 detect temperatures at different points in the reactor 1 and the respective temperature fall rates (-.DELTA.Temp/.DELTA.t) are calculated by temperature fall rate calculator 36 and 37. The most critical one of the temperature fall rates is selected by a maximum temperature fall rate selector 38. On the basis of the difference between the above selected value and the value (-.DELTA.Temp/.DELTA.t).sub.ref set by a reference temperature-fall-rate setting means 39, the set value (W.sub.F).sub.ref for the flow of feed water supplied into the reactor 1 is determined by a function generator 40. The function generator 40 decreases the value for (W.sub.F).sub.ref if the temperature fall rate in question is excessive while it increases (W.sub.F).sub.ref in case of the rate being insufficient. The actual feedwater flow W.sub.F is controlled by controlling the flow W.sub.TB of steam supplied to the turbine 12 on the basis of the value (W.sub.F).sub.ref. Namely, on the basis of the difference between the flow W.sub.F detected by a flow detector 18 and the value (W.sub.F).sub.ref set by the function generator 40, a function generator 19 generates a turbine speed reference signal (N.sub.T).sub.ref. Consequently, the flow W.sub.TB of steam supplied to the turbine 12 is controlled by the combined operation of a turbine speed detector 20, a turbine speed controller 21 and the control valve 13 so that the turbine speed N.sub.T is controlled to make W.sub.F equal to (W.sub.F).sub.ref. As a result, the temperature fall rate (-.DELTA.Temp/.DELTA.t) in (4) is controlled to a desired value. For example, if the temperature fall rate is excessive, the function generator 40 delivers an output for decreasing (W.sub.F).sub.ref so that (N.sub.T).sub.ref decreases to decrease the feedwater flow W.sub.F by choking the valve 13. As a result of this control, the value W.sub.F (i.sub.g -i.sub.F) in (4) decreases so that (-.DELTA.Temp/.DELTA.t) decreases. On the other hand, if the temperature fall rate is insufficient, the function generator 40 delivers an output for increasing (W.sub.F).sub.ref so that (N.sub.T).sub.ref increases to increase the flow W.sub.F by opening the valve 13. Accordingly, W.sub.F (i.sub.g -i.sub.F) in (4) increases to increase (-.DELTA.Temp/.DELTA.t). The control hereafter is continued until the condition that (-.DELTA.Temp/.DELTA.t).apprxeq.(-.DELTA.Temp/.DELTA.t).sub.ref has been reached. In the feedwater control apparatus B, the function generators 40 and 19 may be replaced by blind controllers which receive deviation signals. The control apparatus B is a cascade control system comprising a temperature fall rate control section, a flow control section and a speed control section, but it may be only a temperature control system in which the control valve 13 for the turbine steam flow is directly controlled by the output of the function generator 40. The provision of the minor loops for flow and speed with the temperature fall rate control system will improve the stability and the response speed of the overall control system. As described above with the control apparatuses A, B and C of the RHR system shown in FIG. 1, if each of the fluctuations of the reactor water level and the temperature fall rate occurs separately, the corresponding individual control apparatus operates to compensate the fluctuation. It should here be noted that each of the water level controller 32 and the function generator 40 must have suitable sensitive thresholds and that only when they receive inputs in excess of the thresholds, they control the aperture of the valves 7 and 13. With this constitution, the control of too frequent and negligible fluctuations can be prevented from taking place. Now, the effects of the combination of the control apparatuses B and C will be considered. As seen from FIGS. 2a to 2d, the control apparatus C controls the make-up water flow W.sub.c only during a period ranging from t.sub.2 to t.sub.4 and the control apparatus B operates alone for the time other than the above period. Therefore, there is a possibility only during the period t.sub.2 to t.sub.4, that both the control apparatuses B and C operate jointly. In such a case, the most severe conditions are the following two: (a) the temperature fall rate is excessive and the reactor water level lowers, and (b) the rate is insufficient with elevated level. Consider first the former case (a). According to this invention, since the flow of steam going out of the reactor equals W.sub.H +W.sub.TB and the flow W.sub.F of feed water supplied into the reactor equals W.sub.H +W.sub.c, the following reasoning will hold. Since the temperature fall rate is excessive, the control tends toward decreasing W.sub.F. On the other hand, since the reactor water level L.sub.R lowers, P.sub.s decreases (the aperture of the value lessens) to decrease W.sub.H. The decrease in P.sub.s causes W.sub.c to increase. As a result, W.sub.F (i.sub.g -i.sub.F) in FIG. 4 decreases and W.sub.c (i.sub.f -i.sub.F) in (4) increases to decrease the temperature fall rate. The water level L.sub.R rises since W.sub.c in excess of W.sub.TB is supplied into the closed loop (i.e. feedwater pipe). Thus, the temperature fall rate-.DELTA.Temp/.DELTA.t and the reactor water level L.sub.R can both resume desired values. In the latter case (b) mentioned above, the insufficient rate of the fall of the reactor temperature causes W.sub.F to increase while the elevated water level L.sub.R causes the decrease in W.sub.c. Since in the RHR system having a closed loop, L.sub.R is determined depending only on W.sub.c, the transient rise of the water level returns to its initial level after the condition that W.sub.c =0 has been reached. The temperature fall rate in this case increases with the increase in W.sub.F (i.sub.g -i.sub.F). Also, the control apparatuses B and C can operate jointly in the two cases as follows: (c) insufficient temperature fall rate with lowered water level and (d) excessive temperature fall rate with elevated water level. In either case, the joint control serves to stabilize both the fluctuations. This will be briefly described below. Since the temperature fall rate is determined depending on both W.sub.H and W.sub.c, the control apparatus B is affected by the control apparatus C. However, after the condition that W.sub.c =0 has been reached, the control apparatus B operates alone. In addition to this, the control apparatus operates intermittently so that the above influence takes place only for a short period. This is how (-.DELTA.Temp/.DELTA.t) can be shifted toward stabilization. On the other hand, since the RHR system has a closed loop, the water level L.sub.R is normally determined depending on both W.sub.c and W.sub.TB (whereas the transient fluctuation of L.sub.R is caused by the variation of W.sub.F). When the control apparatus C is operating, W.sub.c &gt;W.sub.TB. It is considered that the control apparatus C is seldom affected by the control apparatus B during this while. Thus, the water level L.sub.R is also stabilized. In conclusion, the simultaneous operation of the control apparatuses B and C also functions to stabilize both L.sub.R and (-.DELTA.Temp/.DELTA.t). FIGS. 4a to 4c show the performance characteristics of an RHR system as an embodiment of this invention. If the above described control is performed with (W.sub.F).sub.ref set at W.sub.F shown in FIG. 4a, the reactor water level can be kept constant while the temperature fall rate is maintained at a desired value. Namely, the reactor water level L.sub.R can be always kept constant by the supply of make-up water (FIG. 4c) and also the reactor temperature Temp can be lowered at the maximum fall rate, i.e. during the shortest period, except in the period of several tens of minutes after scram. Immediately after scram, Q.sub.R becomes very much, as shown in FIG. 2, and in order to attain the temperature fall rate having a usual value, the feedwater flow W.sub.F must be very large so that the turbine and the pump are overloaded. To prevent this overload, W.sub.F must be prevented from becoming too large by setting the maximum limit allowable to the output (W.sub.F).sub.ref of the function generator 40. As described above, according to this invention, the reactor water level can be stably kept constant and moreover the temperature fall rates can be kept at desired values smaller than the corresponding maximum values allowable, so that the reactor can be cooled down at the maximum speed (i.e. double the speed attainable by the conventional control system) without deteriorating the pressure vessel etc. Further, according to this invention, the automated system contributes much to the reduction of human labor. Although in the above embodiment the temperature of the saturated water in the reactor is directly detected, this invention can be equally applied to the system in which the pressure of the saturated steam in the reactor vessel is detected and converted to temperature to determine the temperature of the reactor water. This type of the embodiment will enjoy a higher control capability since the response of pressure to the rapid change in the variables of the reactor is faster than that of temperature. Furthermore, in the above embodiment, the temperature fall rates are obtained at several points in the reactor and the flow of feedwater into the reactor is determined depending on the maximum one of the temperature fall rate. In the case, however, where the reactor vessel, the flange of the reactor vessel, the feedwater nozzle etc. have their individual allowable temperature fall rates different from one another, a system may be employed in which reference values (W.sub.F).sub.ref are set for the respective members in the reactor and the flow of feedwater is determined by choosing the minimum one of the reference values. In this case, the temperature fall rate at the weakest member is controlled so that the reliability can be improved. In addition to the above merits, the following advantages can be obtained according to this invention. (1) Since the reactor water level can be stably kept constant, the thermal impacts which are inherent to the operation of the ECCS can be prevented so that the deterioration of the strength of the reactor structure can be suppressed. (2) Since the temperature fall rates at several points in the reactor can be set smaller than their allowable limiting values, the reactor can be cooled down in the shortest time without degrading the characteristics of instruments. (3) The automated constitution can reduce human labor and improve the operating reliability as well.