AIR FLOW CONTROL SYSTEM IN PFBC PLANTS

Abstract: Air flow control in a PFBC plant comprising a combustor (1) and a pressure vessel (2) as well as a two-shaft gas turbine consisting of a low-pressure compressor LC (3) and a low-pressure turbine LT (7) interconnected by a shaft and a high-pressure compressor HC (5) and a high-pressure turbine (6) interconnected by a shaft, wherein air is sucked into LC, is passed on to HC and via an intercept valve (22) into the pressure vessel and the combustor, whereafter the return flow is passed via the intercept valve to HT and further to LT, from where the return flow is released into the free environment, and wherein the set value (Gset) of the air flow control is calculated on the basis of the bed level and the actual value (Gactual) is calculated from the available process parameters, and wherein both are supplied to the regulator (13) of the air flow control, the output of which regulator controls the executive member of the control in the form of a guide vane ring, provided at the inlet to LT, with adjustable guide vanes (11).

Description: Air flow control system in PFBC plants TECHNICAL FIELD The present invention relates to methods and devices to ensure that the pressure vessel and the combustor of a PFBC plant are, at all times, pressurized with the aid of air flow control and that the proper quantity of air is supplied in each load case. BACKGROUND ART, THE PROBLEMS PFBC plants have been described in a great number of publi¬ cations and patent specifications . One example of such a description is given in EP 0124842 entitled "Power plant with a fluidized bed combustion chamber". A so-called PFBC plant includes a compressor unit and a turbine unit which are adapted such that a low-pressure compressor and a low- pressure turbine are interconnected via a first shaft and a high-pressure compressor and a high-pressure turbine are interconnected via a second shaft. In a PFBC plant there is a relatively clear-cut relationship between the bed level of the combustor and the load. To be able to maintain this relationship and to obtain optimum operation, a large number of more or less connected systems are required. To cover the fuel consumed during the combus¬ tion, the proper quantity of fuel must be continuously supplied to the combustor. This is done with the aid of a fuel supply control. The combustion of supplied mass for optimum use thereof and for keeping the waste gases within permissible limits etc. requires that the air flow to the pressure vessel and the bed of the PFBC plant is at all times the correct one. According to the above, the present invention comprises a control system whose duty it is to satisfy these requirements. SUBSTITUTE SHEET Upon a change of load, in addition to both the fuel supply and the air flow being changed, also the bed level must be adapted to the new load. The bed level may be adjusted in several ways, among other things by feeding bed material from the bed either out into a storage vessel located outside the bed, or from the storage vessel into the bed. This method is described, inter alia, in the above-mentioned EP specification. The system which supplies the combustor with compressed air comprises a two-shaft gas turbine in which, as mentioned above, the low-pressure compressor (LC) and the low-pressure turbine (LT) are interconnected by a fixed shaft and the high-pressure compressor (HC) and the high-pressure turbine (HT) are interconnected by a fixed shaft. The high-pressure unit drives a generator via star gear. In addition to the system mentioned, PFBC plants comprise control of bed temperature, feedwater etc., which are all in different ways connected in dependence on the prevailing load and load changes. Most of these systems have limita¬ tions from the point of view of process engineering. For the air flow control these comprise the difference pressure between the pressure vessel and the bed vessel as well as the pressure ratio between the inlets and outlets of com¬ pressors, the minimum and maximum speed of the low-pressure shaft, the rate of change of several of the controlled quantities etc. which become active and influence each other. The passage of the air through the compressors and up to the fluidized bed as well as the passage of the corresponding waste gases through the turbines and out into the free environment are part of the prior art and will therefore only be briefly described here. Air is admitted into the low-pressure compressor and is passed on via an intermediate cooler to the high-pressure compressor. From there the air is passed into the pressure vessel which thereby becomes SUBSTITUTESHEET pressurized with a certain overpressure in relation to the combustor. The waste gases which are generated during the combustion are now passed from the combustor via cyclones to the high-pressure turbine and from there on to the low- pressure turbine from where the gases are released, possibly after cleaning and cooling, into the free environment. The air and gas passage through the compressor and turbine units, as described above, need not, of course, be associ- ated with a fluidized bed plant. SE 8602003-9 entitled "A method for operation of a turbine unit" describes how such a turbine unit may be used together with other types of com- bustors for, for example, operation of an electric generator connected to the common shaft for the high-pressure co - pressor and the high-pressure turbine. From the design of this plant it can be deduced that the executive member for control of the power of the generator consists of a guide vane ring, connected to the inlet of the low-pressure tur¬ bine, with adjustable guide vanes through which the gas flow from the high-pressure turbine and to the low-pressure tur¬ bine has to pass. Otherwise, it is of interest to note that the above SE patent only mentions devices for air supply under pressure to the combustor and does not disclose any form of control of the air flow. As far as is known, no individual control of the air flow in known PFBC plants exists at present. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 shows the parts of a PFBC plant to which the invention is directed, with the measuring points required for the different controls . Figure 2 shows a summary of the controls and limiting signals which are included in the air flow control system. SUBSTITUTE SHEET Figure 3 shows the configuration of the selection system whic determines what control is to be switched on. SUMMARY OF THE INVENTION Figure 1 shows the parts of a PFBC plant which constitute the most important components of an air flow system, as largely described also in the above-mentioned patent docu¬ ments. Numeral 1 designates a combustor inside a pressure vessel 2. Air is sucked into the low-pressure compressor 3 and passes through an intermediate cooler 4 on its way to a high-pressure compressor 5. From there the air is passed into the pressure vessel 2. The gas outlet from the com¬ bustor is passed via cyclones (not shown) to a high-pressure turbine 6 and on its way out into the free environment the gas passes through a low-pressure turbine 7. The figure also shows a storage vessel 8 with bed material for adjustment of the bed level "h" in connection with load changes. Fuel is intended to be injected at the inlets 9- To the high- pressure shaft there is connected an electric machine 10 which upon start-tp may operate as a motor and which in normal operation may operate as a generator. Output of power from tubes present in the bed is not shown in the figure. An air flow control according to the invention comprises a new concept for such a control since as executive member in the air flow control there is used a cjuide vane ring 11 with adjustable guide vanes on the input side of the low-pressure turbine. This means that the air flow is regulated by influencing the gas flow by means of the guide vane ring. The guide vane ring is the same as that which according to SΞ 86020O3-9 is used as executive member for power control of the electric generator included therein. The operating member of the guide vane ring is shown at 12 and this member is influenced by the PID-connected air flow regulator 13. In the usual manner the air flow control has a set value, G se t- and an actual value, Gactual• The air flow is normally measured in kg/s. SUBSTITUTESHEET The control concept described in Figure 1 constitutes an exceedingly simplified picture of the actual control system for the air flow control. The reason for this are the above- mentioned limitations which such a system must take into consideration. These will be described in greater detail below under the description of embodiments of the invention. An important problem in an air flow control system is that the set value must automatically and at all times correspond to the current load, that is, also correspond to the bed level. The relationship between air flow requirement G se t and load or bed level may for a certain fuel material be calculated as a function where also the temperature of the bed and the thermal value of the fuel etc. are included as parameters. Thus, for a certain given fuel the set value may be written as G set = (h) Whether the calculation of the necessary air quantity is based on the load or the bed level is largely irrelevant. It should be noted, however, that the load can be measured relatively accurately with more or less conventional measuring methods. However, obtaining a measure of the current bed level is more difficult. One way is to measure the pressure difference between the pressure, Pβ, in the bottom of the combustor and the pressure P$ in the so-called freeboard. The reason is that there is a given relationship between the difference pressure and the bed level "h" . Pressure gauges for this purpose are shown at 14 and 15 in Figure 1. Another and equally important requirement is to obtain a reliable measure of the actual value of the air flow. Among other things because direct-measuring air flow meters give rise to pressure drops across the meter itself, the current measured value is instead formed with the aid of known cal¬ culable relationships between measurable parameters. In that SUBSTITUTE SHEET connection, a normalized speed N n for the high-pressure compressor is first calculated according to the following relationship where H is the physical speed, that is, the speed measured directly on the high-pressure shaft, and where T3 is the temperature of the air in kelvin before the high-pressure compressor. The respective measuring means are shown at 16 and 17 in Figure 1. With the aid of produced multitudes of curves for different normalized speeds, the normalized compressor air flow G n versus the pressure ratio P3/P 4 across the high-pressure compressor can be determined. This pressure ratio is called π-value within the current techni¬ cal field and will come into the picture in a most obvious way in some of the limiting controls which will be described below. Measuring means for these pressures are shown at 18 and 19 in Figure 1. The air flow through the high-pressure compressor can then be calculated according to the following relationship Gactual = G n P 5 N n /3, 63 where P3 is the pressure of the air immediately before the high-pressure compressor. The speed Nτ,c of the low-pressure unit must not be below a given minimum value or above a certain maximum value. The measured value for this speed is included in the limiting control which continuously ensures that the speed lies within permissible limits. The measured value is obtained by a measured value transducer shown at 20 in Figure 2. The limiting controls also comprise the difference pressure between the pressure vessel and the combustor. A measured value of this difference pressure DP may be obtained with the difference pressure gauge 21. SUBSTITUTESHEET Figure 1 also shows a so-called intercept valve 22 through which the air flow to the pressure vessel and the gas flow from the combustor can be influenced. The task of the value will be explained in greater detail below under the description of the embodiments. The different control limitations such as the π-control, the speed control of the low-pressure compressor, the difference pressure control etc. are included together with the main control with the PID-connected air flow regulator in a selection system according to the invention and the output signal of which corresponds to the most predominant of the controls and which is the signal which is finally supplied to the operating device 11 according to Figure 1 for control of the adjustable guide vanes of the guide vane ring. The selection system works with analog signals when it comes to deciding what control is to be switched on. In addition, the selection system comprises logic signals which are related to the switching on and off of the air flow control, start- up and run-down of the plant as well as various faults which may occur. The configuration of the selection system will be described in greater detail under the description of the embodiment . It is, of course, important in a control concept as the one described here that the change between the different control systems when these relieve each other takes place as smoothly as possible and without too violent "jumps" in the signal to the executive member. To accomplish this according to the invention, the output signal from the selection system, that is, the control signal to the executive member, independently of what control is switched on, is fed back to all the control systems as a follow-up set value which ensures that the outputs of all the regulators have an output signal which only by a given small margin differs from the output of that regulator which is switched on. SUBSTITUTE SHEET DESCRIPTION OF THE PREFERRED EMBODIMENTS Figure 2 shows a summary of the measurement and control signals which are included in the air flow control and the limiting controls which are associated therewith. Under the "Summary of the Invention" a description is given of how both the set value and the actual value for the air flow control are produced. The production of these quantities are therefore shown only symbolically in Figure 2 in the form of the set value calculator 23 and the actual value calculator 24. Input signal to the set value transducer is, in the example shown, the bed level "h" which is assumed to have been produced in some known way, for example via the pressure difference measurement between PQ and PB as previously described. The determination of the actual value for the air flow is performed, as mentioned above, with the aid of measured values for pressure upstream and downstream of the high- pressure compressor, the temperature downstream of the high- pressure compressor and the speed of the high-pressure unit, which values are supplied to the actual value calculator which, with access to stored characteristics for normalized air flow of the high-pressure compressor for different π- values for normalized speeds thereof, may supply an actual value for air flow. Figure 2 also shows the PID-connected air flow regulator 13 according to Figure 1. The output of the regulator, that is, the control signal to the operating member of the guide vane if this control is switched on, is supplied to the selection system 25 which will be described in detail below. As mentioned, the selection system determines which control system is to be switched on and the output signal from the selection system is supplied to the operating device 11 of the guide vane according to Figure 1. To avoid an inter¬ mittent transition between the different control systems when the selection system determines that another control is SUBSTITUTESHEET to become activated, each control will be supplied with a follow-up set value Fset, as described above and shown in Figure 2, which continuously ensures that each control system receives a control output signal which differs, by a small deviation only, from the control signal which is activated. Under normal operation the compressors must operate within a certain operating range. If the working point approaches the limits of the working range, problems with so-called surging and choking may arise. These phenomena may lead to conside¬ rable damage on the compressor and must therefore be avoi¬ ded. If the working point of the compressor should arrive outside the working range and below the curve corresponding to the choking limit, choking occurs, and if the working point should arrive outside the working range and above the curve corresponding to the surging limit, surging occurs. The air flow control is therefore supplemented by a limiting control referred to as ππc-control, symbolically shown at 26 in Figure 2. To obtain a certain margin to the actual limit curves, this control is based on a π-surging limit curve which lies below the actual limit curve for surging and a π- choking limit curve which lies above the actual limit curve for choking. As is otherwise clear from Figure 2, this control has as input signal the t H c-value and the normalized speed N of the high-pressure compressor, which both values are obtained in connection with the production of the actual value for the air flow control as well as the pressure after the high-pressure compressor. The π*_ιc-control comprises two regulators, one of which supplies a control signal "Min π" and the other a control signal "Max π" which, when the operating range starts to approach the respective limit regions, exert an influence on the air flow control in such a way that these signals, via the selection system, are determining for the position of the guide vane ring. In the same way as for the PID regulator, the JTHC-regulators are supplied with the follow-up set value F se t to avoid distur- SUBSTITUTE SHEET bing jerks in the control when any of these controls is switched on. A brief description as to when the surging and choking problems arise and how the Max-π and Min-π values are obtained for the different air flows will now be given . On each one of the curves for normalized speeds in the multi¬ tude of curves which provides the relationship between π and the compressor air flow there is a point where surging and choking, respectively, are initiated. If the points for surging on all the curves in the multitude of curves are linked together, a coherent curve is obtained which is called the surging curve, and if in similar manner the points for choking are linked together, a coherent choking curve is obtained. The region between these two curves defines the permissible working range of the compressor. To provide margins to these limit curves, π-limit curves according to the above have been decided. The Max-π regula¬ tor then sees to it that a set value for the Max-π control is generated which has such a value that the working point of the compressor by a certain margin does not come too close to the π-εurging limit curve, that is, lies below the π-surging limit curve. Suitably, a maximum curve is assumed which is determined by a curve equal to 0.9 times the π- surging limit curve. In a corresponding manner, the Min-π regulator provides a set value for Min-π control when an operating position approaching the region for choking is about to be obtained. For reasons of process technique a margin in relation to the π-choking limit curve has been selected, which is dependent on the pressure after the high- pressure compressor, that is, 4 , and for that reason also a measured value for this pressure is supplied to the π- regulator. When the pressure after the high-pressure com¬ pressor is greater than a certain pressure, for example 3.5 bar, a Min-π value is used which is determined by the π- choking limit curve and when the pressure is lower, a curve which is a few per cent lower than the π-choking limit curve- is used. However, this value, of course, also permits a SUBSTITUTESHEET satisfactory margin in relation to the actual choking limit curve. As already mentioned, the low-pressure unit is not allowed to operate at speeds below a certain minimum speed or above a certain maximum speed. If there are tendencies in that direction, the limitation is to take over the control of the guide vane ring via the selection system. The measured value for the speed of the low-pressure unit, as it can be obtained from the transducer 20 in Figure 1, is therefore supplied to the LC control 27 in Figure 2. From there a signal "Minspeed LC" is obtained if the actual speed drops to the lowest permissible speed and a signal "Maxspeed LC" is obtained if the speed is increased to the highest permissible. One of these signals will determine the mode of running of the air flow system via the selection system if this signal is the predominant one of all control signals. As is clear from the figure, also this control is supplied with the follow-up set value F set . As previously described, an electric machine 10 according to Figure 1 is connected to the shaft of the high-pressure unit. During normal operation this machine operates as a generator and delivers electrical power to the power net- work. The same machine may also advantageously be used as a motor for start-up of the high-pressure unit and then draws power from the network. In order not to overload the shaft between the high-pressure compressor and the turbine, however, the power from the network to the machine operating as a motor must be limited. A measured value of this power is therefore supplied to a maximum power control 28 accor¬ ding to Figure 2. This control operates in exactly the same way as the DP control. This means that the output signal follows the output signal of the selection system because of the follow-up set value F set for as long as the input sig¬ nal, that is MW, lies below a maximally allowed value set in advance. When the supplied power amounts to the maximally; allowed value, a control signal "Max MW" is obtained which, SUBSTITUTE SHEET in the same way as for the other control systems, s supplied to the selection system. The air flow which is supplied to the pressure vessel tends to give this vessel an overpressure in relation to the com¬ bustor. The difference pressure must be limited to a maximum value and the measured value DP of the difference pressure DP, obtained with the aid of the transducer 21 according to Figure 1, is therefore supplied to the difference pressure control 29 according to Figure 2. This control operates in the same way as the other control systems in that the output signal, for as long as the difference pressure is below a permissible maximum value set in advance with a certain mar¬ gin, because of the follow-up set value delivers a signal which follows the signal which is currently switched on. If, on the other hand, the input signal, that is DP, exceeds the set value, the DP control delivers a "Max DP" signal which, if the other conditions are fulfilled, is allowed to deter¬ mine the movement of the guide vanes via the selection system. The maximum permissible difference pressure in a plant designed according to the invention has been set at 0.55 bar. The status of the fuel injection concerns the operating state of the whole PFBC plant and information about the condition (FO) must therefore be supplied to the selec¬ tion system. If, for some reason, the gas turbine unit comes outside its permissible working range so that, for example, surging of the low-pressure compressor and surging of the high-pressure compressor occur, that the maximum speed of the low-pressure compressor is exceeded, that vibrations occur on the units, etc., a function called GT trip is triggered. Upon a GT trip, special measures must be taken and it is therefore important that the selection system is informed of this (GT) . SUBSTITUTE SHEET As mentioned above, during start-up of the plant the high- pressure unit is driven by the electric machine, connected to the common shaft and fed from the network. Only when the speed of the unit has reached the speed which corresponds to the necessary speed to be able to phase the machine into the network, is it opened for air supply to the pressure chamber and also for gas outlet from the combustor. This opening is performed with the intercept valve 22 according to Figure 1. It is therefore important for the selection system to know whether the intercept valve has opened or not (10) . Information about the states of the above functions is obtained in the form of logical 0- and 1-signals which are supplied to the selection system. That part of the selec- tion system which is to process these input signals must then be designed for logic processing and is for this purpose designed such that the 0- and 1-signals have the following meaning: Fuel injection, OFF Yes = 1, No = 0 Intercept valve, ON Yes = 1, No = 0 GT trip Yes = 1, No = 0 The selection system 25 according to Figure 2 can be desig¬ ned in a plurality of different ways depending on the desi¬ red control and protection strategy and whether input and output signals are analog and/or digital signals. The selec- tion system may also be built up in a more or less integra¬ ted form within the scope of the invention. A preferred embodiment is shown in Figure 3. Since the input signals in the described embodiment consist of both analog and digital signals, the selection system must comprise both analog and digital selectors for the logic decisions that are to be made. All the digital selectors in Figure 3 are drawn in a position in which the activation signal from the logic inputs are 0. SUBSTITUTESHEET Selector VI is a first minimum selector whose output signal Ul is the smaller of the control signal and the signal Minspeed LC. The output signal is passed to a maximum selector V2 whose output signal U2 consists of that of the input signals thereto which is the greater. Besides Ul, the input signals also comprise the signals from Min-π, Maxspeed LC and the signals U3 and U4 from a first digital selector Dl, and a reference signal al = 0. When Dl is not activated, both U3 and U4 will have the value zero because of the reference signal a2 = 0. The first digital selector is activated, as is clear from Figure 3, by the signal Fuel injection when this changes from 0 to 1. U3 will then be equal to a Max MW signal filtered in the filter F and U4 will be equal to the Max DP signal. The greatest of all the input signals to V2 will now, as the signal U2, be supplied to a second minimum selector V3. To this there are also supplied the signal from Max-π and a reference signal a3 = 100. The output signal from V3, that is U5 according to Figure 3, consists of the control signal which is passed to the operating device of the guide vane unless the logical signals from Intercept or GT trip are activated and request otherwise. If none of a second digital selector D2 and a third digital selector D3 is activated, the output signal U6 from D3, because the reference a4 of D2 corresponds to the maximum control signal to the operating device of the guide vane, will thus be guided towards an open guide vane ring. In such a state the control signal U5 to the operating device will be disconnected. If D3 is activated, that is, if a GT trip is obtained, the output signal U6 from D3, because of the feedback according to the figure, will retain the value of the signal prevailing prior to the activation independently of the state of D2. As is clear, the signal U5 also forms the follow-up set value F set . SUBSTITUTESHEET The activation state of the digital selector D2 is deter¬ mined by the logical signals from Intercept and GT trip. As is clear from the figure, these signals are passed to a memory M with a subsequent time lag element T. The relation- ship between the input signals to the S- and R-inputs on the memory and its output is clear from the following summary: Intercept signal S 0 1 0 1 GT trip R 0 0 1 1 . M signal Ml 0 1 0 0 As will be clear, it is only the combination of S = 1 and R = 0, that is, normal operating state with a switched-on intercept valve and no GT trip, that may trigger D2, which can be done at the earliest after a certain time determined by the time lag element T. This means that during normal operation the two control signals U5 and U6 have the same value, and if a GT trip should occur, D3 will be locked to the control signal pricr to the occurrence cf a GT trip. Then when a GT trip has been corrected, that is, the GT trip signal becomes zero, U6 is increased 100 % . Only when the intercept valve is opened, does the normal control switch in U6=U5. SUBSTITUTE SHEET

Claims: CLAIMS 1. A method for air flow control in a PFBC plant which, in addition to a combustor (1) and a pressure vessel (2) , comprises a two-shaft gas turbine consisting of a low- pressure compressor LC (3) and a low-pressure turbine LT (7) interconnected by a shaft as well as a high-pressure com¬ pressor HC (5) and a high-pressure turbine HT (6) inter¬ connected by a shaft, wherein air is sucked into LC, is passed on to HC and via an intercept valve (22) into the pressure vessel and the combustor, whereafter the return flow is passed via the intercept valve to HT and further to LT from where the return flow is released into the free environment, the inlet to LT being provided with a guide vane ring with adjustable guide vanes, which method is characterized in that the set value (G set ) of the air flow control for the current fuel is formed from the relationship between the level of the bed material in the combustor, the bed level h, and the necessary air flow, and that the actual value (Gac t ua l ) of the air flow is formed from known calculable relationships between measurable parameters and that the set and actual values are supplied to a regulator (13) , the output signal of which controls the executive member of the air flow control which is in the form of the guide vane ring (11) with the rotatable guide vanes. 2. A method according to claim 1 wherein an electric machine (10) via a gear unit is connected to the same shaft as HC and HT and wherein information about the power (MW) supplied to the machine during start-up of the PFBC plant is supplied to the air flow control system together with infor¬ mation about the speed (N C) of LC and information about the difference pressure (DP) between the pressure vessel and the combustor, which method is characterized in that the air flow control system comprises a limiting control for ππc from which control signals (Min-π, Max-π) are delivered, which are switched into the air flow control if the working SUBSTITUTESHEET point for HC approaches the limit area for choking or surging, a limiting control for the speed N L c of LC from which control signals (Minspeed LC, Maxspeed LC) are delivered which are switched into the air flow control when the speed of LC starts approaching the respective limit values, a limiting control for maximum allowed supplied power to the electric machine during start-up, from which a control signal (Max MW) is delivered which is switched into the air flow control when the supplied power starts approaching the maximum allowed value and a limiting control for maximum allowed difference pressure (DP) between pressure vessel and combustor from which a control signal (Max DP) is delivered which is switched into the air flow control when the difference pressure starts approaching the maximum allowed value. 3. A method according to claim 1 wherein the air flow control system is supplied with signals with information as to whether fuel injection is being performed or not (FO) , information as to whether a GT trip has occurred or not (GT) as well as in.formation as to whether the intercept valve is switched on or not (10) , which method is characterized in that the signals FO, GT and 10 are used for interlocking/blocking of the air flow control system. . A method for air flow control in a PFBC plant according to the preceding claims, which method is characterized in that the air flow control system comprises a selection system (25) which is supplied with the control signal from the PID regulator (13), the signals Min-π, Max-π, Minspeed LC, Maxspeed LC, Max MW and Max DP from the limiting controls as well as the interlock/blocking signals FO, GT and 10 and that the selection system is adapted such that its output signal consists of the most predominant one of the input signals, which output signal is the control signal which is finally supplied to the .operating device (12) for the operation of the guide vanes. SUBSTITUTESHEET 5. A method for air flow control in a PFBC plant according to the preceding claims, which method is characterized in that all the regulators included in the control are supplied with a follow-up set value F set equal to the control signal to the operating device and which controls the outputs of all regulators, except the one that is switched on, to a value which is somewhat lower or higher than the current control signal. 6. A method for air flow control in a PFBC plant according to the preceding claims, which method is characterized in that the actual value (G act ua l ) of the air flow is formed from the relationship between the speed (N-J) of HC, the temperature (T3) of the air flow before HC, the normalized speed (N n ) for HC, the pressure before (P3) and after (P 4 ) KC and the normalized compressor air flow (GN) as a function of the pressure ratio ππc (P4/P3) . 7. A device for carrying out the method for air flow control according to claim 1 in a PFBC plant which, in addition to a combustor (1) and a pressure vessel (2), comprises a two-shaft gas turbine consisting of a low- pressure compressor LC (3) and a low-pressure turbine LT (7) interconnected by a shaft and a high-pressure compressor HC (5) and a high-pressure turbine HT (6) interconnected by a shaft, and an intercept valve (22) , a guide vane ring (11) with adjustable guide vanes being provided at the inlet to LT, which device is characterized, in that it comprises devices for forming a set value (23) and an actual value (24) for the air flow and an air flow regulator (13), and that the guide vane ring with adjustable guide vanes (11) controlled by the air flow regulator is arranged as an executive member in the air flow control. 8. A device according to claim 6, characterized in that for limiting control of the air flow control the device comprises a regulator (26) for minimum and maximum limita¬ tion of the ratio between the pressure after (P 4 ) and before SUBSTITUTESHEET (P 3 ) HC and which is adapted to supply control signals Min-π and Max-π, a regulator (27) for minimum and maximum limita¬ tion of the speed (NLC) of LC and which is adapted to supply control signals Minspeed LC and Maxspeed LC, a regulator (28) for maximizing the supplied power to a machine (10) connected to the same shaft as HC and HT in connection with start-up of the PFBC plant and which is adapted to deliver a control signal Max MW and a regulator (29) for maximizing the difference pressure (DP) between the pressure vessel and the combustor and which is adapted to deliver a control signal Max DP. 9. A device according to claim 6, characterized in that for evaluation of which control system is to be switched on or whether interlock/blocking signals with information about the status of the fuel injection (FO) , GT trip (GT) or an intercept valve (10) included in the system should be deter¬ mining for the control of the guide vanes of the guide vane ring, the device is provided with a selection system with input signals from the control systems and from the interlock/blocking, the selection system comprising analog minimum selectors (VI, V3) and maximum selectors (V2) as well as digital selectors (Dl, D2, D3) which are connected to deliver, as output signal from the selection system, a signal which is determined by the most predominant one of the input signals of the selection system, which signal constitutes the control signal for the guide vanes of the guide vane ring. SUBSTITUTE SHEET

Inventors: ALMHEM PAER, NEVESTVEIT HJALMAR, ALMHEM, PAER, NEVESTVEIT, HJALMAR
Applicants: ABB CARBON AB
Application year: 1992
Main classification: F02C9
IPC codes: F01K23, F02C9