CA2425577A1 - Method of and system for controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process - Google Patents
Method of and system for controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process Download PDFInfo
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- CA2425577A1 CA2425577A1 CA002425577A CA2425577A CA2425577A1 CA 2425577 A1 CA2425577 A1 CA 2425577A1 CA 002425577 A CA002425577 A CA 002425577A CA 2425577 A CA2425577 A CA 2425577A CA 2425577 A1 CA2425577 A1 CA 2425577A1
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- 238000000034 method Methods 0.000 title claims abstract description 36
- 230000008569 process Effects 0.000 title claims description 12
- 230000004044 response Effects 0.000 claims abstract description 28
- 238000002485 combustion reaction Methods 0.000 claims abstract description 15
- 238000012544 monitoring process Methods 0.000 claims description 23
- 230000008859 change Effects 0.000 claims description 20
- 239000012530 fluid Substances 0.000 claims description 14
- 239000000567 combustion gas Substances 0.000 claims 2
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 description 89
- 230000001351 cycling effect Effects 0.000 description 15
- 238000010586 diagram Methods 0.000 description 6
- 238000005259 measurement Methods 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000010355 oscillation Effects 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004890 malting Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N5/00—Systems for controlling combustion
- F23N5/02—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium
- F23N5/022—Systems for controlling combustion using devices responsive to thermal changes or to thermal expansion of a medium using electronic means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D19/00—Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
- F02D19/02—Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with gaseous fuels
- F02D19/021—Control of components of the fuel supply system
- F02D19/023—Control of components of the fuel supply system to adjust the fuel mass or volume flow
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02D—CONTROLLING COMBUSTION ENGINES
- F02D19/00—Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
- F02D19/02—Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with gaseous fuels
- F02D19/026—Measuring or estimating parameters related to the fuel supply system
- F02D19/027—Determining the fuel pressure, temperature or volume flow, the fuel tank fill level or a valve position
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N1/00—Regulating fuel supply
- F23N1/02—Regulating fuel supply conjointly with air supply
- F23N1/022—Regulating fuel supply conjointly with air supply using electronic means
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D11/00—Control of flow ratio
- G05D11/02—Controlling ratio of two or more flows of fluid or fluent material
- G05D11/13—Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means
- G05D11/131—Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means by measuring the values related to the quantity of the individual components
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N5/00—Systems for controlling combustion
- F23N5/18—Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel
- F23N2005/181—Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel using detectors sensitive to rate of flow of air
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N5/00—Systems for controlling combustion
- F23N5/18—Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel
- F23N2005/185—Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel using detectors sensitive to rate of flow of fuel
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2225/00—Measuring
- F23N2225/08—Measuring temperature
- F23N2225/16—Measuring temperature burner temperature
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2235/00—Valves, nozzles or pumps
- F23N2235/02—Air or combustion gas valves or dampers
- F23N2235/06—Air or combustion gas valves or dampers at the air intake
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23N—REGULATING OR CONTROLLING COMBUSTION
- F23N2235/00—Valves, nozzles or pumps
- F23N2235/12—Fuel valves
- F23N2235/16—Fuel valves variable flow or proportional valves
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Regulation And Control Of Combustion (AREA)
- Feedback Control In General (AREA)
- Flow Control (AREA)
Abstract
In a method of and system for controlling the air/gas ratio in a lag-lead combustion plant the lead and lag parameters are monitored to provide lead and lag signals representative of the values of the parameters. These are compared to provide an error signal representative of the deviation of the ratio of the lead and lag parameters from a preselected ratio. The lag parameter is then adjusted to reduce the deviation in response to the deviation exceeding a preselected deviation.
Description
Method of And System For Controlling The Ratio of A Variable Lead Parameter And An Adjustable Lag Parameter For A Lag-lead Process The present invention relates to a method of and system for controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process and particularly, but not exclusively, to apparatus for controlling the aix/gas ratio iri a~gas combustion plant.
It is known that the air/gas ratio (AGR) in a gas combustion plant should be maintained substantially constant to achieve optimum combustion efficiency of the plant.
Air/gas ratio controllers are used in the plant to maintain the air/gas ratio when the gas flow rate is increased or decreased. To achieve this, the air/gas ratio controller monitors the gas flow rate and adjusts the air flow rate accordingly, usually by adjusting a valve in an air supply line.
A problem with existing air/gas ratio control is the difficulty in adjusting the air flow rate to match accurately the gas flow rate. The present invention aims to provide an improved method and system for air/gas ratio control.
Accordingly, the present invention provides a method of controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process, the method comprising: monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter; monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter; comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from apreselected ratio; and adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
In a preferred form of the invention said error signal is compared with a preselected threshold value and said lag parameter is adjusted in response to said error signal exceeding said preselected threshold value. Advantageously, the error signal is compared with an error range defined by a first, upper preselected threshold value and a second, lower preselected threshold value and said lag parameter is adjusted in response to said error signal falling outside said error range.
The present invention also provides a control system for providing lag-lead control of a process having a variable lead parameter and an adjustable lag parameter, the system comprising: lead monitoring means for monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter; lag monitoring means for monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter; comparator means for comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio; and adjusting means for adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
Advantageously, the system fwther comprises threshold value means for providing a preselectable threshold value and comparator means for comparing said error signal with said preselectable threshold value. The adjusting means is operable to adjust said lag parameter in response to said error signal exceeding said preselectable threshold value.
Preferably, said threshold value means comprises a first, upper threshold value means for providing a first, upper preselected threshold value and a second, lower threshold value means for providing a second, lower preselectable threshold value, thereby to define an error range; said compaxator means is operable to compare said~error signal with said upper and lower preselectable threshold values; and said adjusting means is operable to adjust said lag parameter in response to said error signal falling outside said error range.
The present invention will now be described, by way of example only, with reference to the accompanying drawings in which:
Figure 1 is a schematic block diagram showing a typical gas combustion plant;
It is known that the air/gas ratio (AGR) in a gas combustion plant should be maintained substantially constant to achieve optimum combustion efficiency of the plant.
Air/gas ratio controllers are used in the plant to maintain the air/gas ratio when the gas flow rate is increased or decreased. To achieve this, the air/gas ratio controller monitors the gas flow rate and adjusts the air flow rate accordingly, usually by adjusting a valve in an air supply line.
A problem with existing air/gas ratio control is the difficulty in adjusting the air flow rate to match accurately the gas flow rate. The present invention aims to provide an improved method and system for air/gas ratio control.
Accordingly, the present invention provides a method of controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process, the method comprising: monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter; monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter; comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from apreselected ratio; and adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
In a preferred form of the invention said error signal is compared with a preselected threshold value and said lag parameter is adjusted in response to said error signal exceeding said preselected threshold value. Advantageously, the error signal is compared with an error range defined by a first, upper preselected threshold value and a second, lower preselected threshold value and said lag parameter is adjusted in response to said error signal falling outside said error range.
The present invention also provides a control system for providing lag-lead control of a process having a variable lead parameter and an adjustable lag parameter, the system comprising: lead monitoring means for monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter; lag monitoring means for monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter; comparator means for comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio; and adjusting means for adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
Advantageously, the system fwther comprises threshold value means for providing a preselectable threshold value and comparator means for comparing said error signal with said preselectable threshold value. The adjusting means is operable to adjust said lag parameter in response to said error signal exceeding said preselectable threshold value.
Preferably, said threshold value means comprises a first, upper threshold value means for providing a first, upper preselected threshold value and a second, lower threshold value means for providing a second, lower preselectable threshold value, thereby to define an error range; said compaxator means is operable to compare said~error signal with said upper and lower preselectable threshold values; and said adjusting means is operable to adjust said lag parameter in response to said error signal falling outside said error range.
The present invention will now be described, by way of example only, with reference to the accompanying drawings in which:
Figure 1 is a schematic block diagram showing a typical gas combustion plant;
2 Figure 2 is a schematic block diagram of an air/gas ratio controller used in the plant of Figure 1;
Figure 3 is a schematic block diagram of a control system having a preferred form of air/gas ratio controller according to one aspect of the present invention;
Figure 4 is a schematic block diagram of a preferred form of air/gas ratio controller according to another aspect of the present invention;
Figure 5 is a schematic~block diagram of a modification to the controller of fig. 4;
Figure 6 is a graph showing the change in valve position with applied control voltage;
Figure 7 is a graph showing the derivative of the valve characteristic of Figure,6; and Figure 8 is a graph showing the relationship between the valve derivative and total deadband value.
A typical gas combustion plant 10 is shown in Figure 1. The plant 10 consists of three main parts, a temperature controller 12, an air/gas ratio control system 20 and a burner 40 within, for example, a kiln or furnace 41.
The temperature controller 12 is able to control the temperature of the furnace 41, either by following a predetermined temperature profile or by allowing a user to define the desired temperature profile. To increase the temperature of the fiunace, for example, the controller 12 adjusts the valve in the gas supply line to increase the flow rate of the gas supplied to the burner and the air/gas ratio control system 20 adjusts the air flow rate to attempt to maintain the ratio between the flow rates of the air and the gas supplied to the burner substantially constant. A typical configuration for an air/gas ratio control system is shown in Figure 2.
Figure 3 is a schematic block diagram of a control system having a preferred form of air/gas ratio controller according to one aspect of the present invention;
Figure 4 is a schematic block diagram of a preferred form of air/gas ratio controller according to another aspect of the present invention;
Figure 5 is a schematic~block diagram of a modification to the controller of fig. 4;
Figure 6 is a graph showing the change in valve position with applied control voltage;
Figure 7 is a graph showing the derivative of the valve characteristic of Figure,6; and Figure 8 is a graph showing the relationship between the valve derivative and total deadband value.
A typical gas combustion plant 10 is shown in Figure 1. The plant 10 consists of three main parts, a temperature controller 12, an air/gas ratio control system 20 and a burner 40 within, for example, a kiln or furnace 41.
The temperature controller 12 is able to control the temperature of the furnace 41, either by following a predetermined temperature profile or by allowing a user to define the desired temperature profile. To increase the temperature of the fiunace, for example, the controller 12 adjusts the valve in the gas supply line to increase the flow rate of the gas supplied to the burner and the air/gas ratio control system 20 adjusts the air flow rate to attempt to maintain the ratio between the flow rates of the air and the gas supplied to the burner substantially constant. A typical configuration for an air/gas ratio control system is shown in Figure 2.
3 The system 20 includes a gas valve 22 connected to the gas supply line 24 for varying the gas flow rate along the line. A gas flow measurement sensor 26 is positioned downstream of the gas valve 22 for monitoring the gas flow rate along the line. Similarly, an air valve 28 is positioned at a point in the air supply line 30 for varying the air flow rate along the line and an air flow measurement sensor 32 is positioned downstream of the air valve 28 for monitoring the air flow rate along the air line. -The gas valve 22 is connected to receive an input signal from the temperature controller 12 to adjust the flow rate of the gas: The air valve 28 is connected to receive an input from an air/gas ratio controller 34 to adjust the flow rate of the air in dependence on the gas flow rate.
The air/gas ratio controller 34 receives an input from both of the gas and air measurement sensors 26, 32 and compares the flow rates of the gas and the air and adjusts the air valve to maintain the required air/gas ratio.
It can be seen that if the combustion process is to function with the maximum possible efficiency, the air/gas ratio controller 34 must control the air valve to follow changes in the gas valve as closely as possible.
Such a system is commonly l~nown as a lag-lead system. In a lag-lead system when a lead parameter (the gas flow rate) varies, a lag parameter (in this case the air flow rate) is adjusted to maintain the ratio of the parameters substantially constant.
The flow rate of the air and the gas axe monitored by the measurement sensors of the air/gas ratio control system 20. These preferably sample the flow rate at a predetermined samplilig rate. The lead parameter (here the gas flow rate) and the lag parameter (here the air flow rate) are sampled at regular time intervals. The lead parameter is sampled usually at a faster rate than the lag parameter and can be sampled as fast as once every 20ms. The sample rate of the lag parameter would be adjusted to suit the lead parameter sample rate and in tlus instance would be typically once every 120ms. A typical sample range for the lag parameter would be between 100ms and SOOms. In a natural gas combustion system the air/gas ratio
The air/gas ratio controller 34 receives an input from both of the gas and air measurement sensors 26, 32 and compares the flow rates of the gas and the air and adjusts the air valve to maintain the required air/gas ratio.
It can be seen that if the combustion process is to function with the maximum possible efficiency, the air/gas ratio controller 34 must control the air valve to follow changes in the gas valve as closely as possible.
Such a system is commonly l~nown as a lag-lead system. In a lag-lead system when a lead parameter (the gas flow rate) varies, a lag parameter (in this case the air flow rate) is adjusted to maintain the ratio of the parameters substantially constant.
The flow rate of the air and the gas axe monitored by the measurement sensors of the air/gas ratio control system 20. These preferably sample the flow rate at a predetermined samplilig rate. The lead parameter (here the gas flow rate) and the lag parameter (here the air flow rate) are sampled at regular time intervals. The lead parameter is sampled usually at a faster rate than the lag parameter and can be sampled as fast as once every 20ms. The sample rate of the lag parameter would be adjusted to suit the lead parameter sample rate and in tlus instance would be typically once every 120ms. A typical sample range for the lag parameter would be between 100ms and SOOms. In a natural gas combustion system the air/gas ratio
4 is typically required to be maintained in the order of 10:1, known as the stoichiometric/gas ratio. Changes in the temperature reference signal result in the gas valve being adjusted by the temperature controller 12. This changes the gas flow rate and thus the air/gas ratio from the desired value. This change in the gas flow rate is monitored by the controller 34 which acts to~adjust the air valve 28 to return the air/gas ratio to the desired value.
If a change in the air/gas ratio is detected (i.e. the a3r/gas ratio moves away from the desired value) by the air/gas ratio controller during a particular sampling of the air and gas flow the controller will move the air valve in the required direction (either towards its fully open or fully closed position) until the next sample is taken.
However, if the error in the air/gas ratio is smaller than the change in the air/gas ratio effected by the air valve movement over one sample interval (the period between one sample time and the next) the valve will overshoot the desired position and the desired air flow rate will not be achieved. At the next sampling, the controller 34 will detect a reverse error and will move the valve in the opposite direction i.e. it will move the valve towards its closed position if the previous error caused the valve to be moved towards its open position, and vice versa.
Again, the valve will be moved too far in the reverse direction during the sample interval and will stop at or close to its initial position i.e. the position from which it was first moved in response to the originally monitored error in the air/gas ratio. This opening and closing of the valve, known as hunting, will repeat for as long as the error in the air/gas ratio remains substantially the same as or smaller than the change effected by movement of the air valve over one sampling interval. The air valve and consequently the air flow rate will thus oscillate about the level required to achieve the desired air/gas ratio. These oscillations are known as limit cycles.
It can be seen that if the error in the air/gas ratio exceeds a particular threshold level (being defined by the change in the air/gas ratio effected by the air valve movement over one sample interval) then no limit cycling will occur. However, if the error lies below the threshold level then limit cycling will occur. For valves with linear characteristics i.e.
wluch exhibit a linear response, the threshold level is constant throughout the valve's operating range. However, many electromagnetically operated valves exhibit a non-linear response where the air flow rate through the valve varies non-linearly in relation to the applied control signal. Thus, the change in the air flow through the valve during movement of the valve towards its fully open or fully closed position over a single sample interval will be different depending on the position of the valve within its operating range (Figure 6). Consequently, the threshold level defining the area value below which limit cycling occurs will vary over the operating range of the valve.
Since the motor driving the valve acts as an integrator, the change in flow over one sampling interval can be found by differentiating the valve characteristic (Figure 7).
The differential curve of the valve characteristic shows how much the valve moves (and thus by how much the air flow rate will alter) during one sample interval, depending on the initial position of the valve in the valve operating range. Since errors in the air/gas ratio can have negative as well as positive values, it is necessary to establish both positive and negative derivative curves centred around a zero value in order to establish the threshold level.
As shown in Figure 8, this effectively produces an "error envelope" within which limit cycling occurs (Figure 8). Thus limit cycling will occur where:
E(Ts, u) ~ ~ I s(tt) I .........................................(1) where:
8(u) is the derivative of the valve characteristic at any given valve position (u) and 2*8(u) represents the deadband value;
Ts is the sample time; and a is the valve position.
Conversely, limit cycling will not occur where:
E(Ts, u) ~ Z ~ S~u~ I ........................................~2~
In order to reduce or substantially eliminate limit cycling in the air/gas ratio controller, it is therefore desirable to ensure that the air valve is not adjusted when the error lies within the error envelope of the valve. In other words when equation 1 applies. In a preferred form of the invention, this is achieved by implementing a so-called "deadband" as described below.
Fig. 3 is a schematic block diagram of part of a control system 90 having a preferred form of air/gas ratio controller 100. The controller 100 has a first comparator 102 which is connected to receive two input signals, the first from the gas flow sensor 26 being connected to a non-inverting input of the comparator 102 and the second from the air flow sensor 32 connected to an inverting input. An output of the first comparator 102 is connected firstly to a non-inverting input of a second comparator 104 and secondly to an inverting input of a third comparator 106.
Positive and negative fixed threshold value circuits 108, 110; the purpose of which is described below, are connected to non-inverting and inverting inputs of the second acid third comparators 104, 106 respectively. An output of each of the second and third comparators 104, 106 is connected to a respective operational amplifier 112, 114. An output of each operational amplifier is connected to a respective relay 116, 118 which actuate movement of the air valve 28.
During operation of the combustion plant 10, the flow rates of the gas and the air supplied to the burner 40 are measured by the flow sensors 26, 32 each of which generates a signal S~, Sa corresponding to the respective flow rate and sends the signal to the air/gas ratio controller '100.
The gas flow signal Sg and the air flow signal Sa are fed to the first comparator 102, the gas flow signal Sg to the non-inverting input and the air flow signal Sa to the inverting input. The comparator 102 compares the two signals and generates an error signal E as a function of the comparison.
The error signal E represents the difference between the actual air flow measured by the sensor 32 and the desired air flow to produce a stoichiometric air/gas ratio with the current gas flow rate. Since the sensor 32 would normally produce an air signal Sa which is a magnitude of 10 greater than the gas signal Sg produced by the gas sensor 26 for a stoichiometric ratio (i.e. an air flow rate which is a magnitude of 10 greater than the gas flow rate) the value of the air signal Sa is adjusted to the same level as the gas signal Sg for a stoichiornetric ratio. This can be effected by a simple voltage divider in the air flow sensor 32.
The error signal E is fed to the non-inverting input of the second comparator 104 and to the inverting input of the third comparator 106, each of which compares the error signal E value with fixed positive and negative threshold values generated by the positive and negative threshold value circuits 108, 110 respectively.
If the error signal value is greater than or equal to the positive threshold value, then the comparator 104 applies an actuation signal through the first operational amplifier 112 to the first relay 116 which energises the air valve 28 to move in a first direction, towards its fully closed position. Similarly, if the error signal value is less than or equal to the negative threshold value, the comparator 106 applies an actuation signal through the second operational amplifier 114 to the second relay 116 which energises the air valve 28 to move in the opposite direction towards its fully open position.
If, however, the error signal value is less than the positive threshold value and greater than the negative threshold value, the second and third comparators are unaffected and the air valve is not adjusted.
The threshold value circuits 108,110 set an error signal range within which the controller 100 takes no corrective action. Thus, if the gas flow rate is changed in order to increase or decrease the temperature of the burner 40 this will 'result in an air/gas ratio which moves away from the desired value. This will result in an error signal being generated by the comparator 102, the error signal representing the difference between the actual air/gas ratio and the desired airlgas ratio. It will therefore be appreciated that if the change in the air flow rate which is required to return the air/gas ratio to the desired level is less than the change represented by the error signal range set by the threshold value circuits 108, 110 then the error signal E will fall within this range and the air valve 28 will remain unactuated. The error is in effect deemed to be zero and the air valve is not adjusted. The threshold range set by the threshold circuits 108, 110 is termed a "deadband". In practice, this reduces the occurrence of limit cycling in the air flow and allows the desired air/gas ratio to be maintained more closely.
The value of the deadband affects the performance of the air/gas ratio controller 100 which in turn affects the efficiency of the combustion plant. Selection of the correct value for the deadband is therefore important. By malting the deadband value high, limit cycle oscillations are reduced, but the accuracy of control of the air valve to provide the desired air/gas ratio is reduced. Conversely, a low threshold value gives good accuracy but increases the occurrence of limit cycling. It is preferable, therefore to malce the deadband as small as possible, without causing limit cycling.
It is apparent from the above description that if the deadband value represents a change in air flow rate which is slightly larger than the movement of the air valve (change in air flow rate) in a single sample interval, then adjustment of the valve can be made without limit cycling occurring. A constant deadband value can therefore be used for valves with linear characteristics. However, for non-linear valves having an error envelope such as that shown iri Figure 8, the use of a constant deadband value is ineffective since limit cycling may occur in some parts of the~operating range of the valve even though a deadband is used.
A solution is to vary the value of the deadband according to the valve characteristic over the valve's operating range. It is found that the optimum deadband value for a given valve position is equal to twice the value of the differential of the valve characteristic at that position. Since the deadband is centred around a zero value the upper and lower threshold levels of the deadband (set by the positive and negative threshold circuits 108, 110) correspond to the positive and negative derivative curves of the valve. Thus, the deadband is chosen to map exactly the error envelope of the valve. Thus, the controller will adjust the air valve in the instance where:
E(Ts, u) ( Z D a where D(u) = 8 (u) and represents the deadband value defined by the error envelope at a given valve position (u) which is the region within which limit cycling does not occur even in the absence of a deadband since the value of an error within which region is greater than or equal to the change in flow caused by adjustment of the valve during one sample interval.
Conversely,'the controller will not adjust the air valve in the instance where:
I E(Ts, u) ~ ~ D a In this case, the error lies within the deadband which is the region in which limit cycling would occur if the air valve were adjusted and the deadband were not present.
A solution is to vary the value of the deadband in dependence on the valve characteristic over the operating range of the valve.
Figure 4 shows a second embodiment of air/gas ratio controller 200 as part of a control system 190. In figures, 3, 4 and 5 like reference numerals indicate like parts. As can be seen, the controller 200 is similar in form to the controller 100 of Figure 3 but with the fixed threshold value circuits replaced by variable threshold value circuits 208, 210 each of which i0 comprises a look-up table. The variable threshold value circuits 208, 210 are connected to receive a signal from an air valve position sensor 222 via an operational amplifier 220. The valve position sensor 222 can be of the form which simply monitors the voltage applied to the valve to drive the valve bettveen its open and closed positions.
Before the control system is put into operation the characteristic of the air valve is measured and the differential curve shown in Figure 7 determined for the valve in order to provide the error envelope shown in Figure 8. A number of different threshold values or levels are then taken from the envelope of Figure 8, a positive and a negative value for selected valve positions. The positive values are stored in the look-up table of the threshold value circuit 208 and the negative values are stored in the look-up table of the threshold value circuit 210.
During operation, as the valve position changes, the threshold value in the look-up table which is compared with the error signal is selected according to the position signal from the air valve position sensor.
The value generated by each variable threshold value circuit 208, 210 is thus a function of the position of the air valve 28 and thus of the air flow rate. As the position of the air valve varies, the change in the air flow rate which occurs during each sample interval also varies.
The air valve characteristics are effectively stored in the look-up table in each threshold circuit 208, 210. The look-up table therefore gives the characteristic at a given valve position and thus determines the deadband value for that position. The deadband is thus varied according to the instantaneous position of the air valve 28.
As in the previous embodiment, if the error signal E calculated by cornparator 202, lies within the range defined by the instantaneous positive and negative threshold values generated by the threshold circuits 208, 210, then the error is deemed to be zero and no corrective action is made to air valve 28.
If, however, the error value.lies on or outside the error envelope, the air valve 28 is adjusted as described previously.
Since the deadband value is always greater than the change in air flow effected by movement of the air valve during one sample interval, the occurrence of limit cycling is 'minimised. In addition, the accuracy of the air/gas ratio controller 200 is increased. This results in a significant improvement in combustion efficiency of the gas combustion plant since the airlgas ratio is maintained at an optimum.
It will be apparent that various modifications and improvements can be made to the present invention.
The present invention may be modified such that the movement of the air valve 28 is continuously monitored to determine whether the characteristics of the valve have changed owing to wear, for example. If the valve characteristics have changed, this information can be fed to the variable threshold value circuits to modify the deadband value fox each position of the valve. An example of such a modification to the present invention is shown in fig.
If a change in the air/gas ratio is detected (i.e. the a3r/gas ratio moves away from the desired value) by the air/gas ratio controller during a particular sampling of the air and gas flow the controller will move the air valve in the required direction (either towards its fully open or fully closed position) until the next sample is taken.
However, if the error in the air/gas ratio is smaller than the change in the air/gas ratio effected by the air valve movement over one sample interval (the period between one sample time and the next) the valve will overshoot the desired position and the desired air flow rate will not be achieved. At the next sampling, the controller 34 will detect a reverse error and will move the valve in the opposite direction i.e. it will move the valve towards its closed position if the previous error caused the valve to be moved towards its open position, and vice versa.
Again, the valve will be moved too far in the reverse direction during the sample interval and will stop at or close to its initial position i.e. the position from which it was first moved in response to the originally monitored error in the air/gas ratio. This opening and closing of the valve, known as hunting, will repeat for as long as the error in the air/gas ratio remains substantially the same as or smaller than the change effected by movement of the air valve over one sampling interval. The air valve and consequently the air flow rate will thus oscillate about the level required to achieve the desired air/gas ratio. These oscillations are known as limit cycles.
It can be seen that if the error in the air/gas ratio exceeds a particular threshold level (being defined by the change in the air/gas ratio effected by the air valve movement over one sample interval) then no limit cycling will occur. However, if the error lies below the threshold level then limit cycling will occur. For valves with linear characteristics i.e.
wluch exhibit a linear response, the threshold level is constant throughout the valve's operating range. However, many electromagnetically operated valves exhibit a non-linear response where the air flow rate through the valve varies non-linearly in relation to the applied control signal. Thus, the change in the air flow through the valve during movement of the valve towards its fully open or fully closed position over a single sample interval will be different depending on the position of the valve within its operating range (Figure 6). Consequently, the threshold level defining the area value below which limit cycling occurs will vary over the operating range of the valve.
Since the motor driving the valve acts as an integrator, the change in flow over one sampling interval can be found by differentiating the valve characteristic (Figure 7).
The differential curve of the valve characteristic shows how much the valve moves (and thus by how much the air flow rate will alter) during one sample interval, depending on the initial position of the valve in the valve operating range. Since errors in the air/gas ratio can have negative as well as positive values, it is necessary to establish both positive and negative derivative curves centred around a zero value in order to establish the threshold level.
As shown in Figure 8, this effectively produces an "error envelope" within which limit cycling occurs (Figure 8). Thus limit cycling will occur where:
E(Ts, u) ~ ~ I s(tt) I .........................................(1) where:
8(u) is the derivative of the valve characteristic at any given valve position (u) and 2*8(u) represents the deadband value;
Ts is the sample time; and a is the valve position.
Conversely, limit cycling will not occur where:
E(Ts, u) ~ Z ~ S~u~ I ........................................~2~
In order to reduce or substantially eliminate limit cycling in the air/gas ratio controller, it is therefore desirable to ensure that the air valve is not adjusted when the error lies within the error envelope of the valve. In other words when equation 1 applies. In a preferred form of the invention, this is achieved by implementing a so-called "deadband" as described below.
Fig. 3 is a schematic block diagram of part of a control system 90 having a preferred form of air/gas ratio controller 100. The controller 100 has a first comparator 102 which is connected to receive two input signals, the first from the gas flow sensor 26 being connected to a non-inverting input of the comparator 102 and the second from the air flow sensor 32 connected to an inverting input. An output of the first comparator 102 is connected firstly to a non-inverting input of a second comparator 104 and secondly to an inverting input of a third comparator 106.
Positive and negative fixed threshold value circuits 108, 110; the purpose of which is described below, are connected to non-inverting and inverting inputs of the second acid third comparators 104, 106 respectively. An output of each of the second and third comparators 104, 106 is connected to a respective operational amplifier 112, 114. An output of each operational amplifier is connected to a respective relay 116, 118 which actuate movement of the air valve 28.
During operation of the combustion plant 10, the flow rates of the gas and the air supplied to the burner 40 are measured by the flow sensors 26, 32 each of which generates a signal S~, Sa corresponding to the respective flow rate and sends the signal to the air/gas ratio controller '100.
The gas flow signal Sg and the air flow signal Sa are fed to the first comparator 102, the gas flow signal Sg to the non-inverting input and the air flow signal Sa to the inverting input. The comparator 102 compares the two signals and generates an error signal E as a function of the comparison.
The error signal E represents the difference between the actual air flow measured by the sensor 32 and the desired air flow to produce a stoichiometric air/gas ratio with the current gas flow rate. Since the sensor 32 would normally produce an air signal Sa which is a magnitude of 10 greater than the gas signal Sg produced by the gas sensor 26 for a stoichiometric ratio (i.e. an air flow rate which is a magnitude of 10 greater than the gas flow rate) the value of the air signal Sa is adjusted to the same level as the gas signal Sg for a stoichiornetric ratio. This can be effected by a simple voltage divider in the air flow sensor 32.
The error signal E is fed to the non-inverting input of the second comparator 104 and to the inverting input of the third comparator 106, each of which compares the error signal E value with fixed positive and negative threshold values generated by the positive and negative threshold value circuits 108, 110 respectively.
If the error signal value is greater than or equal to the positive threshold value, then the comparator 104 applies an actuation signal through the first operational amplifier 112 to the first relay 116 which energises the air valve 28 to move in a first direction, towards its fully closed position. Similarly, if the error signal value is less than or equal to the negative threshold value, the comparator 106 applies an actuation signal through the second operational amplifier 114 to the second relay 116 which energises the air valve 28 to move in the opposite direction towards its fully open position.
If, however, the error signal value is less than the positive threshold value and greater than the negative threshold value, the second and third comparators are unaffected and the air valve is not adjusted.
The threshold value circuits 108,110 set an error signal range within which the controller 100 takes no corrective action. Thus, if the gas flow rate is changed in order to increase or decrease the temperature of the burner 40 this will 'result in an air/gas ratio which moves away from the desired value. This will result in an error signal being generated by the comparator 102, the error signal representing the difference between the actual air/gas ratio and the desired airlgas ratio. It will therefore be appreciated that if the change in the air flow rate which is required to return the air/gas ratio to the desired level is less than the change represented by the error signal range set by the threshold value circuits 108, 110 then the error signal E will fall within this range and the air valve 28 will remain unactuated. The error is in effect deemed to be zero and the air valve is not adjusted. The threshold range set by the threshold circuits 108, 110 is termed a "deadband". In practice, this reduces the occurrence of limit cycling in the air flow and allows the desired air/gas ratio to be maintained more closely.
The value of the deadband affects the performance of the air/gas ratio controller 100 which in turn affects the efficiency of the combustion plant. Selection of the correct value for the deadband is therefore important. By malting the deadband value high, limit cycle oscillations are reduced, but the accuracy of control of the air valve to provide the desired air/gas ratio is reduced. Conversely, a low threshold value gives good accuracy but increases the occurrence of limit cycling. It is preferable, therefore to malce the deadband as small as possible, without causing limit cycling.
It is apparent from the above description that if the deadband value represents a change in air flow rate which is slightly larger than the movement of the air valve (change in air flow rate) in a single sample interval, then adjustment of the valve can be made without limit cycling occurring. A constant deadband value can therefore be used for valves with linear characteristics. However, for non-linear valves having an error envelope such as that shown iri Figure 8, the use of a constant deadband value is ineffective since limit cycling may occur in some parts of the~operating range of the valve even though a deadband is used.
A solution is to vary the value of the deadband according to the valve characteristic over the valve's operating range. It is found that the optimum deadband value for a given valve position is equal to twice the value of the differential of the valve characteristic at that position. Since the deadband is centred around a zero value the upper and lower threshold levels of the deadband (set by the positive and negative threshold circuits 108, 110) correspond to the positive and negative derivative curves of the valve. Thus, the deadband is chosen to map exactly the error envelope of the valve. Thus, the controller will adjust the air valve in the instance where:
E(Ts, u) ( Z D a where D(u) = 8 (u) and represents the deadband value defined by the error envelope at a given valve position (u) which is the region within which limit cycling does not occur even in the absence of a deadband since the value of an error within which region is greater than or equal to the change in flow caused by adjustment of the valve during one sample interval.
Conversely,'the controller will not adjust the air valve in the instance where:
I E(Ts, u) ~ ~ D a In this case, the error lies within the deadband which is the region in which limit cycling would occur if the air valve were adjusted and the deadband were not present.
A solution is to vary the value of the deadband in dependence on the valve characteristic over the operating range of the valve.
Figure 4 shows a second embodiment of air/gas ratio controller 200 as part of a control system 190. In figures, 3, 4 and 5 like reference numerals indicate like parts. As can be seen, the controller 200 is similar in form to the controller 100 of Figure 3 but with the fixed threshold value circuits replaced by variable threshold value circuits 208, 210 each of which i0 comprises a look-up table. The variable threshold value circuits 208, 210 are connected to receive a signal from an air valve position sensor 222 via an operational amplifier 220. The valve position sensor 222 can be of the form which simply monitors the voltage applied to the valve to drive the valve bettveen its open and closed positions.
Before the control system is put into operation the characteristic of the air valve is measured and the differential curve shown in Figure 7 determined for the valve in order to provide the error envelope shown in Figure 8. A number of different threshold values or levels are then taken from the envelope of Figure 8, a positive and a negative value for selected valve positions. The positive values are stored in the look-up table of the threshold value circuit 208 and the negative values are stored in the look-up table of the threshold value circuit 210.
During operation, as the valve position changes, the threshold value in the look-up table which is compared with the error signal is selected according to the position signal from the air valve position sensor.
The value generated by each variable threshold value circuit 208, 210 is thus a function of the position of the air valve 28 and thus of the air flow rate. As the position of the air valve varies, the change in the air flow rate which occurs during each sample interval also varies.
The air valve characteristics are effectively stored in the look-up table in each threshold circuit 208, 210. The look-up table therefore gives the characteristic at a given valve position and thus determines the deadband value for that position. The deadband is thus varied according to the instantaneous position of the air valve 28.
As in the previous embodiment, if the error signal E calculated by cornparator 202, lies within the range defined by the instantaneous positive and negative threshold values generated by the threshold circuits 208, 210, then the error is deemed to be zero and no corrective action is made to air valve 28.
If, however, the error value.lies on or outside the error envelope, the air valve 28 is adjusted as described previously.
Since the deadband value is always greater than the change in air flow effected by movement of the air valve during one sample interval, the occurrence of limit cycling is 'minimised. In addition, the accuracy of the air/gas ratio controller 200 is increased. This results in a significant improvement in combustion efficiency of the gas combustion plant since the airlgas ratio is maintained at an optimum.
It will be apparent that various modifications and improvements can be made to the present invention.
The present invention may be modified such that the movement of the air valve 28 is continuously monitored to determine whether the characteristics of the valve have changed owing to wear, for example. If the valve characteristics have changed, this information can be fed to the variable threshold value circuits to modify the deadband value fox each position of the valve. An example of such a modification to the present invention is shown in fig.
5 in which like reference numerals indicate like parts.
In Figure 5 one of the relays, in this case relay 116 which actuates the valve towards its fully closed position, is connected to an input of a multiplexer 300. An output of the air flow sensor 32 and the valve position sensor 222 are also connected to the multiplexer 300.
The output from the multiplexer 300 is connected to aparameter estimator 302 whose output in turn is connected to the variable threshold value circuits 208, 210.
The parameter estimator 302 may be a microprocessor running, for example, MATLAB.
Before the control system is put into operation the characteristic of the air valve is measured and the response curve shown in Figure 6 is stored in a store in the parameter estimator 302.
This can be effected by moving the valve from one of a fully open and closed position to the other and monitoring the signals from the valve position sensor 222 and the air flow rate sensor 32 which are then stored in the parameter estimator 302 as continuously variable values or discrete values.
When relay 116 is actuated to move the air flow valve 28 towards its fully closed position the parameter estimator 302 is also enabled. During closing of the valve 28 the parameter estimator 302 processes the outputs from the air flow rate and position sensors 32, 222 and compares the monitored flow rate with the previously stored flow rate. If there is a deviation between the monitored flow rate with the previously stored flow rate this would suggest, for example, wear in the valve mechanism. The parameter estimator 302 then adjusts the threshold values in the look up tables in the threshold value circuits 208, 210 which relate to the monitored valve position to take account of changes in the valve characteristics which have occurred. It will be appreciated that equally the movement of the valve towards its fully open position may be used to update the look up tables to take account of wear, in which case the estimator 302 would be enabled with relay 118.
Whilst the above description is made with reference to a lag-lead control system wherein the lead parameter is the gas flow rate and the lag parameter is the air flow rate, it will be appreciated that the invention is equally applicable to systems wherein the lead parameter is the air flow rate and the lag parameter is the gas flow rate, or any other lag-lead system.
It Will also be appreciated that whilst the preferred form of the invention has been described with reference to an air/gas combustion plant or fiunace, the invention is equally applicable to lag-lead control systems for controlling the ratio of two fluids where the fluids may be in gas or liquid form.
In Figure 5 one of the relays, in this case relay 116 which actuates the valve towards its fully closed position, is connected to an input of a multiplexer 300. An output of the air flow sensor 32 and the valve position sensor 222 are also connected to the multiplexer 300.
The output from the multiplexer 300 is connected to aparameter estimator 302 whose output in turn is connected to the variable threshold value circuits 208, 210.
The parameter estimator 302 may be a microprocessor running, for example, MATLAB.
Before the control system is put into operation the characteristic of the air valve is measured and the response curve shown in Figure 6 is stored in a store in the parameter estimator 302.
This can be effected by moving the valve from one of a fully open and closed position to the other and monitoring the signals from the valve position sensor 222 and the air flow rate sensor 32 which are then stored in the parameter estimator 302 as continuously variable values or discrete values.
When relay 116 is actuated to move the air flow valve 28 towards its fully closed position the parameter estimator 302 is also enabled. During closing of the valve 28 the parameter estimator 302 processes the outputs from the air flow rate and position sensors 32, 222 and compares the monitored flow rate with the previously stored flow rate. If there is a deviation between the monitored flow rate with the previously stored flow rate this would suggest, for example, wear in the valve mechanism. The parameter estimator 302 then adjusts the threshold values in the look up tables in the threshold value circuits 208, 210 which relate to the monitored valve position to take account of changes in the valve characteristics which have occurred. It will be appreciated that equally the movement of the valve towards its fully open position may be used to update the look up tables to take account of wear, in which case the estimator 302 would be enabled with relay 118.
Whilst the above description is made with reference to a lag-lead control system wherein the lead parameter is the gas flow rate and the lag parameter is the air flow rate, it will be appreciated that the invention is equally applicable to systems wherein the lead parameter is the air flow rate and the lag parameter is the gas flow rate, or any other lag-lead system.
It Will also be appreciated that whilst the preferred form of the invention has been described with reference to an air/gas combustion plant or fiunace, the invention is equally applicable to lag-lead control systems for controlling the ratio of two fluids where the fluids may be in gas or liquid form.
Claims (28)
1 A method of controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process, the method comprising:
monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter;
monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter;
comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio;
and adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter;
monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter;
comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio;
and adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
2 A method as claimed in claim 1 comprising comparing said error signal with a preselected threshold value and adjusting said lag parameter in response to said error signal exceeding said preselected threshold value.
3 A method as claimed in claim 1 or 2 comprising comparing said error signal with an error range. defined by a first, upper preselected threshold value and a second, lower preselected threshold value and adjusting said lag parameter in response to said error signal falling outside said error range.
4 A method as claimed in claim 3 comprising:
adjusting said lag parameter to reduce said ratio in response to said error signal being above said error range;
and adjusting said lag parameter to increase said ratio in response to said error signal being below said error range.
adjusting said lag parameter to reduce said ratio in response to said error signal being above said error range;
and adjusting said lag parameter to increase said ratio in response to said error signal being below said error range.
A method as claimed in claim 4 wherein:
said first, upper preselected threshold value is a positive value and said second, lower preselected threshold value is a negative value;
a positive error signal indicates an increase in said ratio from said preselected ratio and a negative error signal indicates a decrease in said ratio from said preselected ratio;
and the method comprises:
adjusting said lag parameter to reduce said ratio in response to said error signal being positive and exceeding said first, upper preselected threshold value;
and adjusting said lag parameter to increase said ratio in response to said error signal being negative and exceeding said second, lower preselected threshold value.
said first, upper preselected threshold value is a positive value and said second, lower preselected threshold value is a negative value;
a positive error signal indicates an increase in said ratio from said preselected ratio and a negative error signal indicates a decrease in said ratio from said preselected ratio;
and the method comprises:
adjusting said lag parameter to reduce said ratio in response to said error signal being positive and exceeding said first, upper preselected threshold value;
and adjusting said lag parameter to increase said ratio in response to said error signal being negative and exceeding said second, lower preselected threshold value.
6 A method as claimed in any of claims 2 to 5 wherein the or each said threshold value is a fixed value.
7 A method as claimed in any of claims 2 to 5 wherein the or each said threshold value is a function of the value of said lag parameter.
8 A method as claimed in claim 7 wherein the step of comparing said error signal with the or each threshold value comprises adjusting said threshold value in dependence on the value of said lag parameter and comparing said error signal with said adjusted threshold level.
9 A method as claimed in claim 8 comprising:
providing a look up table for storing a plurality of threshold values;
and the step of adjusting said threshold value comprising selecting one of said threshold values in dependence on the value of said lag parameter.
providing a look up table for storing a plurality of threshold values;
and the step of adjusting said threshold value comprising selecting one of said threshold values in dependence on the value of said lag parameter.
A method as claimed in claim 7 wherein:
the or each threshold value comprises a plurality of threshold levels;
and the step of comparing said error signal with the or each threshold value comprises selecting a threshold level for said threshold value in dependence on the value of said lag parameter and comparing said error signal with said selected threshold level.
the or each threshold value comprises a plurality of threshold levels;
and the step of comparing said error signal with the or each threshold value comprises selecting a threshold level for said threshold value in dependence on the value of said lag parameter and comparing said error signal with said selected threshold level.
11 A method as claimed in claim 10 comprising:
providing a look up table for storing said plurality of threshold levels;
and the step of adjusting said threshold value comprising selecting one of said threshold levels in dependence on the value of said lag parameter.
providing a look up table for storing said plurality of threshold levels;
and the step of adjusting said threshold value comprising selecting one of said threshold levels in dependence on the value of said lag parameter.
12 A method as claimed in any of claims 1 to 11 wherein:
said lead and lag parameters are lead and lag fluid flow rates for said industrial process;
and said method comprises:
providing lag valve means for controlling flow of said lag fluid;
monitoring the position of said lag valve means during opening or closing of said valve means;
monitoring the flow rate of said lag fluid during opening or closing of said valve means;
comparing the change in position of said valve means with the change in said flow rate of said lag fluid;
and adjusting said threshold value in response to said comparison indicating a change in the characteristic of said valve means.
said lead and lag parameters are lead and lag fluid flow rates for said industrial process;
and said method comprises:
providing lag valve means for controlling flow of said lag fluid;
monitoring the position of said lag valve means during opening or closing of said valve means;
monitoring the flow rate of said lag fluid during opening or closing of said valve means;
comparing the change in position of said valve means with the change in said flow rate of said lag fluid;
and adjusting said threshold value in response to said comparison indicating a change in the characteristic of said valve means.
13 A method as claimed in claim 12 when appendant to claim 9 or 11 wherein the step of adjusting said threshold value comprises adjusting the threshold values or levels in said loop up table.
14 A method as claimed in any of claims 1 to 13 wherein:
said lead parameter is the flow rate of a combustion gas;
said lag parameter is the flow rate of air;
and said process is a combustion process.
said lead parameter is the flow rate of a combustion gas;
said lag parameter is the flow rate of air;
and said process is a combustion process.
15 A control system (34) for providing lag-lead control of a process having a variable lead parameter and an adjustable lag parameter, the system comprising:
lead monitoring means (26) for monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter;
lag monitoring means (32) for monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter;
comparator means ( 102) for comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio;
and adjusting means (116, 118) for adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
lead monitoring means (26) for monitoring said lead parameter and providing a lead signal representative of the value of said lead parameter;
lag monitoring means (32) for monitoring said lag parameter and providing a lag signal representative of the value of said lag parameter;
comparator means ( 102) for comparing said lead and lag signals and providing an error signal representative of the deviation of the ratio of said lead and lag parameters from a preselected ratio;
and adjusting means (116, 118) for adjusting said lag parameter to reduce said deviation in response to said deviation exceeding a preselected deviation.
16 A control system as claimed in claim 15 further comprising:
threshold value means (108, 110) for providing a preselectable threshold value;
comparator means (104, 106) for comparing said error signal with said preselectable threshold value;
and wherein said adjusting means (116, 118) is operable to adjust said lag parameter in response to said error signal exceeding said preselectable threshold value.
threshold value means (108, 110) for providing a preselectable threshold value;
comparator means (104, 106) for comparing said error signal with said preselectable threshold value;
and wherein said adjusting means (116, 118) is operable to adjust said lag parameter in response to said error signal exceeding said preselectable threshold value.
17 A control system as claimed in claim 16 wherein:
said threshold value means comprises a first, upper threshold value means (108) for providing a first, upper preselected threshold value and a second, lower threshold value means (110) for providing a second, lower preselectable threshold value, thereby to define an error range;
said comparator means (104, 106) is operable to compare said error signal with said upper and lower preselectable threshold values;
and said adjusting means (116, 118) is operable to adjust said lag parameter in response to said error signal falling outside said error range.
said threshold value means comprises a first, upper threshold value means (108) for providing a first, upper preselected threshold value and a second, lower threshold value means (110) for providing a second, lower preselectable threshold value, thereby to define an error range;
said comparator means (104, 106) is operable to compare said error signal with said upper and lower preselectable threshold values;
and said adjusting means (116, 118) is operable to adjust said lag parameter in response to said error signal falling outside said error range.
18 A control system as claimed in claim 17 wherein:
said adjusting means (116, 118) is operable to adjust said lag parameter to reduce said ratio in response to said error signal being above said error range and to adjust said lag parameter to increase said ratio in response to said error signal being below said error range.
said adjusting means (116, 118) is operable to adjust said lag parameter to reduce said ratio in response to said error signal being above said error range and to adjust said lag parameter to increase said ratio in response to said error signal being below said error range.
19 A control system as claimed in claim 18 wherein:
said first, upper preselected threshold value is a positive value and said second, lower preselected threshold value is a negative value;
a positive error signal indicates an increase in said ratio from said preselected ratio and a negative error signal indicates a decrease in said ratio from said preselected ratio;
and said adjusting means (116, 118) is operable reduce said ratio in response to said error signal being positive and exceeding said first, upper preselected threshold value and to increase said ratio in response to said error signal being negative and exceeding said second, lower preselected threshold value.
said first, upper preselected threshold value is a positive value and said second, lower preselected threshold value is a negative value;
a positive error signal indicates an increase in said ratio from said preselected ratio and a negative error signal indicates a decrease in said ratio from said preselected ratio;
and said adjusting means (116, 118) is operable reduce said ratio in response to said error signal being positive and exceeding said first, upper preselected threshold value and to increase said ratio in response to said error signal being negative and exceeding said second, lower preselected threshold value.
20 A control system as claimed in any of claims 16 to 19 wherein the or each said threshold value is a fixed value.
21 A control system as claimed in any of claims 16 to 19 wherein the or each said threshold value is a function of the value of said lag parameter.
22 A control system as claimed in claim 21 further comprising adjusting means (222) for adjusting said threshold value in dependence on the value of said lag parameter and wherein said comparator means (104,106) is operable to compare said error signal with said adjusted threshold value.
23 A control system as claimed in claim 22 wherein:
said threshold value means comprises a look up table (208, 210) for storing a plurality of threshold values;
and said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold values in dependence on the value of said lag parameter.
said threshold value means comprises a look up table (208, 210) for storing a plurality of threshold values;
and said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold values in dependence on the value of said lag parameter.
24 A control system as claimed in claim 21 further comprising:
adjusting means (222) for adjusting said threshold value in dependence on the value of said lag parameter;
and wherein:
the or each threshold value comprises a plurality of threshold levels;
said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold levels in dependence on the value of said lag parameter;
and said comparator means (104, 106) is operable to compare said error signal with said selected threshold level.
adjusting means (222) for adjusting said threshold value in dependence on the value of said lag parameter;
and wherein:
the or each threshold value comprises a plurality of threshold levels;
said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold levels in dependence on the value of said lag parameter;
and said comparator means (104, 106) is operable to compare said error signal with said selected threshold level.
25 A control system as claimed in claim 24 wherein:
said threshold value means comprises a look up table (208, 210) for storing a plurality of threshold values;
and said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold values in dependence on the value of said lag parameter.
said threshold value means comprises a look up table (208, 210) for storing a plurality of threshold values;
and said threshold value adjusting means (222) is operable to adjust said threshold value by selecting one of said threshold values in dependence on the value of said lag parameter.
26 A control system as claimed in my of claims 15 to 25 wherein:
said lead and lag parameters are lead and lag fluid flow rates for said process;
and said control system comprises:
lag valve means (28) for controlling the flow of said lag fluid;
position monitoring means (322) for monitoring the position of said lag valve means (28) during opening or closing of said lag valve means and providing a position signal representative thereof;
wherein:
said lag monitoring means (32) is operable to monitor the flow rate of said lag fluid during opening or closing of said lag valve means (28) and provide a flow rate signal representative thereof;
and said control system further comprises:
storage means (302) for storing sampled values of said position and flow rate signals representing a preselected characteristic of said lag valve means;
second comparator means (302) for comparing the valve position of said lag valve means (28) and lag fluid flow rate during movement of said lag valve means with the stored values;
and second adjusting means (302) for adjusting said threshold value in response to said comparison indicating a change in the characteristic of said lag valve means (28).
said lead and lag parameters are lead and lag fluid flow rates for said process;
and said control system comprises:
lag valve means (28) for controlling the flow of said lag fluid;
position monitoring means (322) for monitoring the position of said lag valve means (28) during opening or closing of said lag valve means and providing a position signal representative thereof;
wherein:
said lag monitoring means (32) is operable to monitor the flow rate of said lag fluid during opening or closing of said lag valve means (28) and provide a flow rate signal representative thereof;
and said control system further comprises:
storage means (302) for storing sampled values of said position and flow rate signals representing a preselected characteristic of said lag valve means;
second comparator means (302) for comparing the valve position of said lag valve means (28) and lag fluid flow rate during movement of said lag valve means with the stored values;
and second adjusting means (302) for adjusting said threshold value in response to said comparison indicating a change in the characteristic of said lag valve means (28).
27 A control system as claimed in any of claims 15 to 25 wherein:
said lead and lag parameters are lead and lag fluid flow rates for said process;
and said control system comprises:
lag valve means (28) for controlling the flow of said lag fluid;
position monitoring means (322) for monitoring the position of said lag valve means during opening or closing of said lag valve means and providing a position signal representative thereof;
wherein:
said lag monitoring means (32) is operable to monitor the flow rate of said lag fluid during opening or closing of said valve means (28) and provide a flow rate signal representative thereof;
and said control system further comprises:
storage means (302) for storing sampled values of said position and flow rate signals representing a preselected characteristic of said lag valve means;
second comparator means (302) for comparing the lag fluid flow rate during movement of said valve means with stored value corresponding to the monitored position of said lag valve means;
and second adjusting means (302) for adjusting said threshold value in response to said comparison indicating a change in the characteristic of said valve means.
said lead and lag parameters are lead and lag fluid flow rates for said process;
and said control system comprises:
lag valve means (28) for controlling the flow of said lag fluid;
position monitoring means (322) for monitoring the position of said lag valve means during opening or closing of said lag valve means and providing a position signal representative thereof;
wherein:
said lag monitoring means (32) is operable to monitor the flow rate of said lag fluid during opening or closing of said valve means (28) and provide a flow rate signal representative thereof;
and said control system further comprises:
storage means (302) for storing sampled values of said position and flow rate signals representing a preselected characteristic of said lag valve means;
second comparator means (302) for comparing the lag fluid flow rate during movement of said valve means with stored value corresponding to the monitored position of said lag valve means;
and second adjusting means (302) for adjusting said threshold value in response to said comparison indicating a change in the characteristic of said valve means.
28 A control system as claimed in any of claims 15 to 27 wherein:
said lead parameter is the flow rate of a combustion gas;
said lag parameter is the flow rate of air;
and said process is a combustion process.
said lead parameter is the flow rate of a combustion gas;
said lag parameter is the flow rate of air;
and said process is a combustion process.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GBGB0025231.2A GB0025231D0 (en) | 2000-10-14 | 2000-10-14 | Air/fuel ratio control |
| GB0025231.2 | 2000-10-14 | ||
| PCT/GB2001/004586 WO2002033499A1 (en) | 2000-10-14 | 2001-10-15 | Method of and system for controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2425577A1 true CA2425577A1 (en) | 2002-04-25 |
Family
ID=9901301
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002425577A Abandoned CA2425577A1 (en) | 2000-10-14 | 2001-10-15 | Method of and system for controlling the ratio of a variable lead parameter and an adjustable lag parameter for a lag-lead process |
Country Status (17)
| Country | Link |
|---|---|
| US (1) | US20070082304A1 (en) |
| CN (1) | CN1285982C (en) |
| AU (2) | AU9404501A (en) |
| BG (1) | BG107801A (en) |
| CA (1) | CA2425577A1 (en) |
| CZ (1) | CZ20031074A3 (en) |
| EE (1) | EE200300181A (en) |
| GB (2) | GB0025231D0 (en) |
| HU (1) | HUP0302298A2 (en) |
| LT (1) | LT5091B (en) |
| LV (1) | LV13096B (en) |
| NO (1) | NO20031689L (en) |
| NZ (1) | NZ525305A (en) |
| PL (1) | PL361302A1 (en) |
| SK (1) | SK4922003A3 (en) |
| WO (1) | WO2002033499A1 (en) |
| YU (1) | YU28103A (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7802984B2 (en) | 2006-04-07 | 2010-09-28 | Thomas & Betts International, Inc. | System and method for combustion-air modulation of a gas-fired heating system |
| US20110269081A1 (en) * | 2010-05-03 | 2011-11-03 | Bayer Materialscience Llc | Systems and processes for improved combustion control |
| US9851103B2 (en) | 2011-12-15 | 2017-12-26 | Honeywell International Inc. | Gas valve with overpressure diagnostics |
| US9557059B2 (en) | 2011-12-15 | 2017-01-31 | Honeywell International Inc | Gas valve with communication link |
| US9846440B2 (en) * | 2011-12-15 | 2017-12-19 | Honeywell International Inc. | Valve controller configured to estimate fuel comsumption |
| US9645584B2 (en) | 2014-09-17 | 2017-05-09 | Honeywell International Inc. | Gas valve with electronic health monitoring |
| CN106287806B (en) * | 2016-09-29 | 2019-01-08 | 长沙开元仪器股份有限公司 | A kind of automatic flow control system and its working method of high temperature combustion furnace |
| US11073281B2 (en) | 2017-12-29 | 2021-07-27 | Honeywell International Inc. | Closed-loop programming and control of a combustion appliance |
| US10697815B2 (en) | 2018-06-09 | 2020-06-30 | Honeywell International Inc. | System and methods for mitigating condensation in a sensor module |
| WO2020183117A1 (en) * | 2019-03-11 | 2020-09-17 | Thermal Recycling (Uk) Ltd | Kiln control |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4585161A (en) * | 1984-04-27 | 1986-04-29 | Tokyo Gas Company Ltd. | Air fuel ratio control system for furnace |
| US5222887A (en) * | 1992-01-17 | 1993-06-29 | Gas Research Institute | Method and apparatus for fuel/air control of surface combustion burners |
| US5904131A (en) * | 1995-12-28 | 1999-05-18 | Cummins Engine Company, Inc. | Internal combustion engine with air/fuel ratio control |
| JP3765617B2 (en) * | 1996-06-25 | 2006-04-12 | 本田技研工業株式会社 | Air-fuel ratio control device for internal combustion engine |
-
2000
- 2000-10-14 GB GBGB0025231.2A patent/GB0025231D0/en not_active Ceased
-
2001
- 2001-10-15 HU HU0302298A patent/HUP0302298A2/en unknown
- 2001-10-15 GB GB0312659A patent/GB2385154B/en not_active Expired - Fee Related
- 2001-10-15 NZ NZ525305A patent/NZ525305A/en unknown
- 2001-10-15 YU YU28103A patent/YU28103A/en unknown
- 2001-10-15 US US10/399,374 patent/US20070082304A1/en not_active Abandoned
- 2001-10-15 AU AU9404501A patent/AU9404501A/en active Pending
- 2001-10-15 CA CA002425577A patent/CA2425577A1/en not_active Abandoned
- 2001-10-15 AU AU2001294045A patent/AU2001294045B2/en not_active Ceased
- 2001-10-15 PL PL01361302A patent/PL361302A1/en unknown
- 2001-10-15 WO PCT/GB2001/004586 patent/WO2002033499A1/en active IP Right Grant
- 2001-10-15 CN CNB018188362A patent/CN1285982C/en not_active Expired - Fee Related
- 2001-10-15 CZ CZ20031074A patent/CZ20031074A3/en unknown
- 2001-10-15 EE EEP200300181A patent/EE200300181A/en unknown
- 2001-10-15 SK SK492-2003A patent/SK4922003A3/en unknown
-
2003
- 2003-04-11 NO NO20031689A patent/NO20031689L/en not_active Application Discontinuation
- 2003-05-05 LT LT2003032A patent/LT5091B/en not_active IP Right Cessation
- 2003-05-12 BG BG107801A patent/BG107801A/en unknown
- 2003-05-12 LV LVP-03-46A patent/LV13096B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| CN1474965A (en) | 2004-02-11 |
| BG107801A (en) | 2004-07-30 |
| AU9404501A (en) | 2002-04-29 |
| HUP0302298A2 (en) | 2003-10-28 |
| CN1285982C (en) | 2006-11-22 |
| YU28103A (en) | 2004-07-15 |
| NZ525305A (en) | 2004-09-24 |
| SK4922003A3 (en) | 2003-10-07 |
| LV13096B (en) | 2004-02-20 |
| WO2002033499A1 (en) | 2002-04-25 |
| NO20031689L (en) | 2003-06-11 |
| LT5091B (en) | 2004-01-26 |
| LT2003032A (en) | 2003-09-25 |
| GB2385154B (en) | 2004-06-30 |
| AU2001294045B2 (en) | 2005-09-08 |
| PL361302A1 (en) | 2004-10-04 |
| GB0312659D0 (en) | 2003-07-09 |
| US20070082304A1 (en) | 2007-04-12 |
| GB0025231D0 (en) | 2000-11-29 |
| CZ20031074A3 (en) | 2003-09-17 |
| GB2385154A (en) | 2003-08-13 |
| EE200300181A (en) | 2003-06-16 |
| NO20031689D0 (en) | 2003-04-11 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| FZDE | Discontinued |