CN109002068B - Temperature optimization control method for flame path - Google Patents
Temperature optimization control method for flame path Download PDFInfo
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- CN109002068B CN109002068B CN201811042776.4A CN201811042776A CN109002068B CN 109002068 B CN109002068 B CN 109002068B CN 201811042776 A CN201811042776 A CN 201811042776A CN 109002068 B CN109002068 B CN 109002068B
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- 238000005457 optimization Methods 0.000 title claims abstract description 7
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- 230000004069 differentiation Effects 0.000 claims abstract description 4
- 230000010354 integration Effects 0.000 claims abstract description 4
- 239000011159 matrix material Substances 0.000 claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 6
- 230000008859 change Effects 0.000 claims description 5
- 238000004364 calculation method Methods 0.000 claims description 3
- 238000012417 linear regression Methods 0.000 claims description 3
- 238000007781 pre-processing Methods 0.000 claims description 3
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- 238000005259 measurement Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 14
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000571 coke Substances 0.000 description 3
- 238000004939 coking Methods 0.000 description 3
- 238000003763 carbonization Methods 0.000 description 2
- 239000003034 coal gas Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
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- 239000002918 waste heat Substances 0.000 description 1
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- G—PHYSICS
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- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D23/00—Control of temperature
- G05D23/19—Control of temperature characterised by the use of electric means
- G05D23/20—Control of temperature characterised by the use of electric means with sensing elements having variation of electric or magnetic properties with change of temperature
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B21/00—Heating of coke ovens with combustible gases
- C10B21/10—Regulating and controlling the combustion
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Abstract
The invention discloses a flame path temperature optimization control method, which is characterized in that a flame path temperature detection model based on an improved PLS (partial least squares) is utilized to detect the problem of the flame path at the current moment, and the temperature of the flame path is controlled by adopting fuzzy PID (proportion integration differentiation) with variable universe of discourse according to a preset target value of the temperature of the flame path. The flame path temperature detection model based on the improved PLS realizes indirect measurement of the flame path temperature, reduces the cost, improves the efficiency, and simultaneously utilizes the fuzzy PID of the variable universe of discourse, thereby realizing the advantages of short temperature adjustment time, high steady-state precision, small steady-state error, small overshoot and the like.
Description
Technical Field
The invention relates to a temperature control method, in particular to a temperature optimization control method of a flame path.
Background
Coke ovens are complex industrial kilns in the metallurgical industry and are composed of a plurality of alternately arranged coking chambers and combustion chambers. The coal gas and the air enter the combustion chamber for diffusion and combustion after being preheated by the heat storage chamber, and the generated heat is transferred to the carbonization chamber through the furnace wall; the coal is subjected to high-temperature dry distillation in the carbonization chamber to form coke, waste gas generated by combustion is discharged after waste heat of the regenerator is recovered, and the flow directions of coal gas, air and the waste gas are exchanged once every 20 min. In the coking process, the flame path temperature is a crucial process parameter and is directly related to the coke quality and the service life of a furnace body, but the measurement of the flame path temperature is mainly carried out by a warm thermocouple at present, but the installation is difficult, and the coking temperature is too high and is easy to damage, and meanwhile, the control of the flame path temperature mostly depends on manual experience or a simple PID control algorithm, so that the precision is lower, and the adjustment time is too long.
Disclosure of Invention
In order to solve the problems that the direct measurement of the temperature of the flame path in the prior art is high in cost and easy to cause problems, and the control of the temperature of the flame path is not optimized enough, the invention aims to provide a temperature optimization control method of the flame path.
The technical scheme adopted by the invention for solving the technical problems is as follows:
a temperature optimization control method of a flame path is characterized by comprising the following steps: (1) establishing a flame path temperature detection model based on the improved PLS according to the heating gas flow, the top temperature of the regenerator, the pressure of a gas main pipe, the gas flow of the gas, the temperature of a flue and historical data of the variables; (2) collecting the variables in real time, and calculating a flame path temperature deviation value according to a flame path detection value of the flame path temperature detection model based on the improved PLS and a preset flame path temperature target value; (3) and controlling the temperature of the flame path by using fuzzy PID (proportion integration differentiation) with variable discourse domains according to the deviation value of the temperature of the flame path.
Wherein the step (1) of establishing a flame path temperature detection model based on the improved PLS comprises the following steps:
(a) historical data of variables such as heating gas flow X1, regenerator top temperature X2, gas main pipe pressure X3, furnace gas flow X4 and flue temperature X5 are collected as input variables X which are sample data of the model, and flue temperature Y1 is used as output variables Y of the model;
(b) preprocessing the input variable X, firstly, carrying out standardized transformation on the input variable X to eliminate the influence of data dimension, and secondly, removing large error data;
(c) establishing a flame path temperature detection model based on the improved PLS according to the preprocessed input variables:
assuming that an input variable X is linearly related to an output variable Y, namely Y is XB + E, wherein B is a regression coefficient matrix, and E is a residual error matrix;
when the PLS modeling is improved, X and Y are decomposed to obtainWherein T, U is a score matrix, P, Q is a load matrix, and E1 and E2 are residual matrixes;
according to the formula II, the vectors are in relation with each other by linear regression: u ═ CT + R, where R is the residual matrix, C is the regression factor: c ═ UTT/(TTT), so that a regression coefficient matrix of
In order to ensure the prediction accuracy of the model, the model is verified by using the mean square error and the root mean square error.
When a new collected sample is received, fault judgment calculation needs to be carried out on the new sample, and input variables of the two standardized sample data are respectively set as Zi={zi1,zi1,,zim},Zj={zj1,zj1,,zjmThe failure judgment is related to two coefficients, wherein the coefficient 1 is:Lij1 is 2 samples more consistent, Lij0 is the inconsistency of the two samples; the coefficient 2 is:wherein EmaxIs a set value, Mij2 samples are the same for 1, MijTwo samples differ by 0. According to the two coefficients, the calculated value is: j ═ α Lij+(1-α)MijWhere α ∈ (0, 1). By calculating the calculated value, the flame path temperature detection based on the improved PLS is carried out after the calculated value meets the set threshold value, so that the accuracy of temperature prediction can be effectively ensured, error control caused by faults in a sensor is prevented, and the stable control of the system is improved.
The design of the fuzzy PID of the change domain comprises the following steps:
(A) the selection of the expansion factor of the input and output discourse domain, the basic discourse domain of the error e and the error change rate ec of the flame path temperature are respectively set as follows:then the input scale factor isWherein lambda belongs to (0,1) and is the value range of the domain of discourseThe envelope coefficient reflects the precision of a control system, and the larger the lambda is, the more obvious the domain compression is; output scaling factor
(B) Fuzzification treatment: selecting 7 fuzzy subsets { NB, NM, NS, ZE, PS, PM, PB } to perform fuzzification processing;
(C) determining a membership function: selecting a triangular membership function at the zero point, and selecting a Gaussian membership function at the position close to the boundary of the fuzzy domain;
(D) establishing a fuzzy control rule table and fuzzy reasoning:
when e is larger, Kp is increased, response speed is increased, overshoot is avoided, and Kd is also increased properly; to reduce integral saturation, Ki is reduced;
when the Kp is moderate, the Kp is reduced, the overshoot is reduced, the Ki is increased, the stability is improved, and the value of the Kd is moderate;
when e is smaller, Ki needs to be increased to ensure stability, reduce Kp and improve steady-state precision, and when ec is larger, Kd is reduced, and when ec is smaller, Kd is increased;
Drawings
Fig. 1 is a schematic diagram of the temperature-optimized control of a flame path.
Detailed Description
The technical solution of the present invention is further described below with reference to the accompanying drawings and examples.
As shown in fig. 1, a method for controlling optimal temperature of a flue is characterized by comprising the following steps: (1) establishing a flame path temperature detection model based on the improved PLS according to the heating gas flow, the top temperature of the regenerator, the pressure of a gas main pipe, the gas flow of the gas, the temperature of a flue and historical data of the variables; (2) collecting the variables in real time, and calculating a flame path temperature deviation value according to a flame path detection value of the flame path temperature detection model based on the improved PLS and a preset flame path temperature target value; (3) and controlling the temperature of the flame path by using fuzzy PID (proportion integration differentiation) with variable discourse domains according to the deviation value of the temperature of the flame path.
Wherein the step (1) of establishing a flame path temperature detection model based on the improved PLS comprises the following steps:
(a) historical data of variables such as heating gas flow X1, regenerator top temperature X2, gas main pipe pressure X3, furnace gas flow X4 and flue temperature X5 are collected as input variables X which are sample data of the model, and flue temperature Y1 is used as output variables Y of the model;
(b) preprocessing the input variable X, firstly, carrying out standardized transformation on the input variable X to eliminate the influence of data dimension, and secondly, removing large error data;
(c) establishing a flame path temperature detection model based on the improved PLS according to the preprocessed input variables:
assuming that an input variable X is linearly related to an output variable Y, namely Y is XB + E, wherein B is a regression coefficient matrix, and E is a residual error matrix;
when the PLS modeling is improved, X and Y are decomposed to obtainWherein T, U is a score matrix, P, Q is a load matrix, and E1 and E2 are residual matrixes;
according to the formula II, the vectors are in relation with each other by linear regression: u ═ CT + R, where R is the residual matrix, C is the regression factor: c ═ UTT/(TTT), so that a regression coefficient matrix of
In order to ensure the prediction accuracy of the model, the model is verified by using the mean square error and the root mean square error.
When a new collected sample is received, fault judgment calculation needs to be carried out on the new sample, and input variables of the two standardized sample data are respectively set as Zi={zi1,zi1,,zim},Zj={zj1,zj1,,zjmThe failure judgment is related to two coefficients, wherein the coefficient 1 is:Lij1 is 2 samples more consistent, Lij0 is the inconsistency of the two samples; the coefficient 2 is:wherein EmaxIs a set value, Mij2 samples are the same for 1, MijTwo samples differ by 0. According to the two coefficients, the calculated value is: j ═ α Lij+(1-α)MijWhere α ∈ (0, 1). By calculating the calculated value, the flame path temperature detection based on the improved PLS is carried out after the calculated value meets the set threshold value, so that the accuracy of temperature prediction can be effectively ensured, error control caused by faults in a sensor is prevented, and the stable control of the system is improved.
The design of the fuzzy PID of the change domain comprises the following steps:
(A) the selection of the expansion factor of the input and output discourse domain, the basic discourse domain of the error e and the error change rate ec of the flame path temperature are respectively set as follows:then the input scale factor isWherein, the lambda belongs to (0,1) and is a value range coefficient of the domain of discourse, which reflects the precision of the control system, and the larger the lambda is, the more obvious the domain of discourse compression is; output scaling factor
(B) Fuzzification treatment: selecting 7 fuzzy subsets { NB, NM, NS, ZE, PS, PM, PB } to perform fuzzification processing;
(C) determining a membership function: selecting a triangular membership function at the zero point, and selecting a Gaussian membership function at the position close to the boundary of the fuzzy domain;
(D) establishing a fuzzy control rule table and fuzzy reasoning: PID parameter tuning is achieved based on experience as follows,
when e is larger, Kp is increased, response speed is increased, overshoot is avoided, and Kd is also increased properly; to reduce integral saturation, Ki is reduced;
when the Kp is moderate, the Kp is reduced, the overshoot is reduced, the Ki is increased, the stability is improved, and the value of the Kd is moderate;
when e is smaller, Ki needs to be increased to ensure stability, reduce Kp and improve steady-state precision, and when ec is larger, Kd is reduced, and when ec is smaller, Kd is increased;
a fuzzy control rule table is obtained according to the above experience, as shown in table 1:
TABLE 1 fuzzy control rules Table
Claims (2)
1. A temperature optimization control method of a flame path is characterized by comprising the following steps:
(1) according to historical data of variables such as heating gas flow, regenerator top temperature, gas main pipe pressure, gas flow and flue temperature, a flame path temperature detection model based on the improved PLS is established;
(2) collecting the variables in real time, and calculating a flame path temperature deviation value according to a flame path detection value of the flame path temperature detection model based on the improved PLS and a preset flame path temperature target value;
(3) controlling the temperature of the flame path by using fuzzy PID (proportion integration differentiation) with variable discourse domains according to the deviation value of the temperature of the flame path;
the step (1) of establishing a flame path temperature detection model based on the improved PLS comprises the following steps:
(a) historical data of variables such as heating gas flow X1, regenerator top temperature X2, gas main pipe pressure X3, furnace gas flow X4 and flue temperature X5 are collected as input variables X which are sample data of the model, and flue temperature Y1 is used as output variables Y of the model;
(b) preprocessing the input variable X, firstly, carrying out standardized transformation on the input variable X to eliminate the influence of data dimension, and secondly, removing large error data;
(c) establishing a flame path temperature detection model based on the improved PLS according to the preprocessed input variables:
assuming that an input variable X is linearly related to an output variable Y, namely Y is XB + E, wherein B is a regression coefficient matrix, and E is a residual error matrix;
when the PLS modeling is improved, X and Y are decomposed to obtainWherein T, U is a score matrix, P, Q is a load matrix, and E1 and E2 are residual matrixes;
according to the formula II, the vectors are in relation with each other by linear regression: u ═ CT + R, where R is the residual matrix, C is the regression factor: c ═ UTT/(TTT), so that a regression coefficient matrix of
And (3) controlling the temperature of the flame path by using a variable universe fuzzy PID according to the temperature deviation value of the flame path, wherein the design of the variable universe fuzzy PID comprises the following steps:
(A) the selection of the expansion factor of the input and output discourse domain, the basic discourse domain of the error e and the error change rate ec of the flame path temperature are respectively set as follows:then the input scale factor isOutput scaling factor
(B) Fuzzification treatment: selecting 7 fuzzy subsets { NB, NM, NS, ZE, PS, PM, PB } to perform fuzzification processing;
(C) determining a membership function: selecting a triangular membership function at the zero point, and selecting a Gaussian membership function at the position close to the boundary of the fuzzy domain;
(D) establishing a fuzzy control rule table and fuzzy reasoning:
when e is larger, Kp is increased, response speed is increased, overshoot is avoided, and Kd is also increased properly; to reduce integral saturation, Ki is reduced;
when the Kp is moderate, the Kp is reduced, the overshoot is reduced, the Ki is increased, the stability is improved, and the value of the Kd is moderate;
when e is smaller, Ki needs to be increased to ensure stability, reduce Kp and improve steady-state precision, and when ec is larger, Kd is reduced, and when ec is smaller, Kd is increased;
(E) the integral quantity delta K of PID can be obtained by clarifying the fuzzy quantityp、ΔKi、ΔKdThen the PID parameters are:wherein Kp0、Ki0、Kd0Is the initial value of PID parameter;
wherein upon receiving a new collected sample, it is requiredCarrying out fault judgment calculation on the new sample, and setting the input variables of the two standardized sample data as Zi={zi1,zi1,,zim},Zj={zj1,zj1,,zjmThe failure judgment is related to two coefficients, wherein the coefficient 1 is:Lij1 is 2 samples more consistent, Lij0 is the inconsistency of the two samples; the coefficient 2 is:wherein EmaxIs a set value, Mij2 samples are the same for 1, MijTwo samples differ for 0, and the calculated value is obtained from the two coefficients: j ═ α Lij+(1-α)MijAnd alpha belongs to (0,1), and the calculated value is calculated, and the flame path temperature detection based on the improved PLS is carried out after the calculated value meets the set threshold, so that the accuracy of temperature prediction can be effectively ensured, error control caused by the fault condition in the sensor is prevented, and the stable control of the system is improved.
2. The method for controlling the optimal temperature of the flame path according to claim 1, wherein the initial value of the PID parameter is as follows: kp0=7、Ki0=5、Kd0=2。
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