CN103605287A - Bed temperature prediction system and method of circulating fluidized bed boiler - Google Patents

Bed temperature prediction system and method of circulating fluidized bed boiler Download PDF

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CN103605287A
CN103605287A CN201310335800.4A CN201310335800A CN103605287A CN 103605287 A CN103605287 A CN 103605287A CN 201310335800 A CN201310335800 A CN 201310335800A CN 103605287 A CN103605287 A CN 103605287A
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bed temperature
training sample
variable
independent variable
predicted value
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CN103605287B (en
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吴家标
刘兴高
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Zhejiang University ZJU
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Abstract

The invention discloses a bed temperature prediction system and a method of a circulating fluidized bed boiler. The system comprises a field intelligent instrument, a database, a data interface, a control station and an upper computer which are connected with the circulating fluidized bed boiler, the field intelligent instrument is connected with the control station, the database and the upper computer, wherein the upper computer comprises a standardized processing module used for collecting training samples of a key variables from the database and performing standardized processing, a prediction mechanism forming module used for establishing a prediction model, a prediction execution module used for predicting bed temperature in real time, a model update module, a signal acquisition module, and a result display module. The bed temperature prediction system and the method of the circulating fluidized bed boiler predict the bed temperature according to operating conditions and operating variables of the circulating fluidized bed boiler, facilitating suggestions and guidance for operation, thereby controlling the bed temperature in an optimal range, effectively ensuring the safe and environment-friendly operation of the circulating fluidized bed boiler, and laying a foundation for further optimization of operation efficiency.

Description

Circulating Fluidized Bed Temperature prognoses system and method
Technical field
The present invention relates to energy project field, especially, relate to a kind of Circulating Fluidized Bed Temperature prognoses system and method.
Background technology
Circulating Fluidized Bed Boiler has the advantages such as pollutant emission is few, fuel tolerance wide, Load Regulation ability is strong, obtains applying more and more widely in recent years in the industries such as electric power, heat supply.Circulating Fluidized Bed Temperature is one directly affect the important parameter that can boiler safe and continuous move, also directly affect desulfuration efficiency in boiler operatiopn and the generation of oxides of nitrogen simultaneously, this is external when Circulating Fluidized Bed Boiler operational efficiency is optimized, and bed temperature is the important restrictions condition that needs are considered.Set up the prognoses system of Circulating Fluidized Bed Temperature, significant to the safety of Circulating Fluidized Bed Boiler, environmental protection operation and operation optimization.
Summary of the invention
The object of the invention is to for the deficiencies in the prior art, a kind of Circulating Fluidized Bed Boiler heat loss due to exhaust gas prognoses system and method are provided.
The technical solution adopted for the present invention to solve the technical problems is: a kind of Circulating Fluidized Bed Temperature prognoses system, comprises the field intelligent instrument, database, data-interface, control station and the host computer that are connected with Circulating Fluidized Bed Boiler; Field intelligent instrument is connected with control station, database and host computer, and described host computer comprises:
Standardization module, for gather the historical record of operating condition variable and performance variable from database, the training sample matrix X that forms independent variable, gather the historical record of corresponding average bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
x ‾ j = 1 n Σ i = 1 n x ij , (i=1,2,…,n;j=1,2,…,p) (1)
y ‾ = 1 n Σ i = 1 n y i , (i=1,2,…,n) (2)
1.2) ask standard deviation
s x , j = 1 n Σ i = 1 n ( x ij - x ‾ j ) 2 , (i=1,2,…,n;j=1,2,…,p) (3)
s y = 1 n Σ i = 1 n ( y i - y ‾ ) 2 , (i=1,2,…,n) (4)
1.3) standardization
x ij * = x ij - x ‾ j s x , j , (i=1,2,…,n;j=1,2,…,p) (5)
y i * = y i - y ‾ s y , (i=1,2,…,n) (6)
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number,
Figure BDA00003617732700017
Figure BDA00003617732700018
for the average of training sample, s x,j, s yfor the standard deviation of training sample,
Figure BDA00003617732700022
for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable.
Forecasting mechanism forms module, and for setting up forecast model, implementation step is as follows:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) predictive coefficient vector β is transmitted and stores into prediction execution module.
Prediction execution module, for predicting bed temperature according to the performance variable of the operating condition of Circulating Fluidized Bed Boiler and setting, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
x ( t ) j * = x ( t ) j - x ‾ j s x , j , (j=1,2,…,p) (8)
Wherein, x (t) jfor t moment j independent variable initial value,
Figure BDA00003617732700024
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample,
Figure BDA00003617732700025
for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
y ^ ( t ) * = x ( t ) 1 * x ( t ) 2 * . . . x ( t ) p * β - - - ( 9 )
Wherein,
Figure BDA00003617732700027
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
y ^ ( t ) = y ^ ( t ) * · s y + y ‾ - - - ( 10 )
Wherein,
Figure BDA00003617732700029
former dimension predicted value for t moment bed temperature.
As preferred a kind of scheme: described host computer also comprises: model modification module, be used for by the time interval of setting actual bed temperature and predicted value comparison, if relative error is greater than 10%, new data is added to training sample data, re-execute standardization module and forecasting mechanism and form module.
Further, described host computer also comprises:
Signal acquisition module, for the sampling time interval by setting, gathers real time data from field intelligent instrument, and from database, gathers historical data.
Result display module, for reading parameters from control station, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, adjusting operation condition, is controlled at optimum range by bed temperature in time, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler.Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively.
As preferred another kind of scheme: described independent variable comprises: operating condition variable: main steam flow, environment temperature, feed temperature, combustion chamber draft, bed pressure, coal-fired moisture, coal-fired volatile matter, coal-fired ash content, coal-fired sulphur content; Performance variable: wind total blast volume, Secondary Air total blast volume.
A Circulating Fluidized Bed Temperature Forecasting Methodology, described Forecasting Methodology comprises the following steps:
1) from database, gather the historical record of operating condition variable and performance variable, the training sample matrix X that forms independent variable, gather the historical record of corresponding average bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, and variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
x ‾ j = 1 n Σ i = 1 n x ij , (i=1,2,…,n;j=1,2,…,p) (1)
y ‾ = 1 n Σ i = 1 n y i , (i=1,2,…,n) (2)
1.2) ask standard deviation
s x , j = 1 n Σ i = 1 n ( x ij - x ‾ j ) 2 , (i=1,2,…,n;j=1,2,…,p) (3)
s y = 1 n Σ i = 1 n ( y i - y ‾ ) 2 , (i=1,2,…,n) (4)
1.3) standardization
x ij * = x ij - x ‾ j s x , j , (i=1,2,…,n;j=1,2,…,p) (5)
y i * = y i - y ‾ s y , (i=1,2,…,n) (6)
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number,
Figure BDA00003617732700037
Figure BDA00003617732700038
for the average of training sample, s x,j, s yfor the standard deviation of training sample,
Figure BDA00003617732700039
Figure BDA000036177327000310
for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable.
2) the standardized training sample obtaining is set up to forecast model by following process:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) preserve the predictive coefficient vector β obtaining.
3) using the performance variable of the operating condition variable of Circulating Fluidized Bed Boiler and setting as input signal, according to predictive coefficient vector, bed temperature to be predicted, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
x ( t ) j * = x ( t ) j - x ‾ j s x , j , (j=1,2,…,p) (8)
Wherein, x (t) jfor t moment j independent variable initial value,
Figure BDA00003617732700041
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample,
Figure BDA00003617732700042
for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
y ^ ( t ) * = x ( t ) 1 * x ( t ) 2 * . . . x ( t ) p * β - - - ( 9 )
Wherein,
Figure BDA00003617732700044
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
y ^ ( t ) = y ^ ( t ) * · s y + y ‾ - - - ( 10 )
Wherein,
Figure BDA00003617732700046
former dimension predicted value for t moment bed temperature.
As preferred a kind of scheme: described method also comprises: 4) by the sampling time interval of setting, collection site intelligent instrument signal, by the actual bed temperature obtaining and predicted value comparison, if relative error is greater than 10%, new data is added to training sample data, re-execute step 1), 2), so that forecast model is upgraded.
Further, in described step 3), from control station, read parameters, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, timely adjusting operation condition, bed temperature is controlled to optimum range, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler.Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively.
As preferred another kind of scheme: described independent variable comprises: operating condition variable: main steam flow, environment temperature, feed temperature, combustion chamber draft, bed pressure, coal-fired moisture, coal-fired volatile matter, coal-fired ash content, coal-fired sulphur content; Performance variable: wind total blast volume, Secondary Air total blast volume.
Beneficial effect of the present invention is mainly manifested in: the bed temperature to Circulating Fluidized Bed Boiler is predicted, advises and guiding production operation, and bed temperature is controlled to optimum range, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler.
Accompanying drawing explanation
Fig. 1 is the hardware structure diagram of system proposed by the invention.
Fig. 2 is the functional block diagram of host computer of the present invention.
Embodiment
Below in conjunction with drawings and Examples, the invention will be further described.
Embodiment 1
With reference to Fig. 1, Fig. 2, a kind of Circulating Fluidized Bed Temperature prognoses system, comprise the field intelligent instrument 2, data-interface 3, database 4, control station 5 and the host computer 6 that are connected with Circulating Fluidized Bed Boiler 1, field intelligent instrument 2 is connected with fieldbus, data bus is connected with data-interface 3, data-interface 3 is connected with database 4, control station 5 and host computer 6, and described host computer 6 comprises:
Standardization module 7, for gather the historical record of operating condition variable and performance variable from database, the training sample matrix X that forms independent variable, gather the historical record of corresponding average bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
x ‾ j = 1 n Σ i = 1 n x ij , (i=1,2,…,n;j=1,2,…,p) (1)
y ‾ = 1 n Σ i = 1 n y i , (i=1,2,…,n) (2)
1.2) ask standard deviation
s x , j = 1 n Σ i = 1 n ( x ij - x ‾ j ) 2 , (i=1,2,…,n;j=1,2,…,p) (3)
s y = 1 n Σ i = 1 n ( y i - y ‾ ) 2 , (i=1,2,…,n) (4)
1.3) standardization
x ij * = x ij - x ‾ j s x , j , (i=1,2,…,n;j=1,2,…,p) (5)
y i * = y i - y ‾ s y , (i=1,2,…,n) (6)
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number, for the average of training sample, s x,j, s yfor the standard deviation of training sample,
Figure BDA00003617732700058
Figure BDA00003617732700059
for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable.
Forecasting mechanism forms module 8, and for setting up forecast model, implementation step is as follows:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) predictive coefficient vector β is transmitted and stores into prediction execution module.
Prediction execution module 9, for predicting bed temperature according to the performance variable of the operating condition of Circulating Fluidized Bed Boiler and setting, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
x ( t ) j * = x ( t ) j - x ‾ j s x , j , (j=1,2,…,p) (8)
Wherein, x (t) jfor t moment j independent variable initial value,
Figure BDA000036177327000511
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample,
Figure BDA000036177327000512
for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
y ^ ( t ) * = x ( t ) 1 * x ( t ) 2 * . . . x ( t ) p * β - - - ( 9 )
Wherein,
Figure BDA000036177327000514
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
y ^ ( t ) = y ^ ( t ) * · s y + y ‾ - - - ( 10 )
Wherein,
Figure BDA00003617732700062
former dimension predicted value for t moment bed temperature.
Described host computer 6 also comprises: signal acquisition module 11, for the sampling time interval by setting, gathers real time data from field intelligent instrument, and from database, gather historical data.
Described host computer 6 also comprises: model modification module 12, be used for by the time interval of setting actual bed temperature and predicted value comparison, if relative error is greater than 10%, new data is added to training sample data, re-execute standardization module and forecasting mechanism and form module.
Described host computer 6 also comprises: result display module 10, for reading parameters from control station, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, adjusting operation condition, is controlled at optimum range by bed temperature in time, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler.Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively.
The hardware components of described host computer 6 comprises: I/O element, for the collection of data and the transmission of information; Data-carrier store, the data sample that storage running is required and operational factor etc.; Program storage, the software program of storage practical function module; Arithmetical unit, executive routine, realizes the function of appointment; Display module, shows the parameter, the operation result that arrange, and provides suggestion for operation.
Embodiment 2
With reference to Fig. 1, Fig. 2, a kind of Circulating Fluidized Bed Temperature Forecasting Methodology, described Forecasting Methodology comprises the following steps:
1) from database, gather the historical record of operating condition variable and performance variable, the training sample matrix X that forms independent variable, gather the historical record of corresponding average bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, and variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
x ‾ j = 1 n Σ i = 1 n x ij , (i=1,2,…,n;j=1,2,…,p) (1)
y ‾ = 1 n Σ i = 1 n y i , (i=1,2,…,n) (2)
1.2) ask standard deviation
s x , j = 1 n Σ i = 1 n ( x ij - x ‾ j ) 2 , (i=1,2,…,n;j=1,2,…,p) (3)
s y = 1 n Σ i = 1 n ( y i - y ‾ ) 2 , (i=1,2,…,n) (4)
1.3) standardization
x ij * = x ij - x ‾ j s x , j , (i=1,2,…,n;j=1,2,…,p) (5)
y i * = y i - y ‾ s y , (i=1,2,…,n) (6)
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number,
Figure BDA00003617732700072
for the average of training sample, s x,j, s yfor the standard deviation of training sample,
Figure BDA00003617732700073
Figure BDA00003617732700074
for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable.
2) the standardized training sample obtaining is set up to forecast model by following process:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) preserve the predictive coefficient vector β obtaining.
3) using the performance variable of the operating condition variable of Circulating Fluidized Bed Boiler and setting as input signal, according to predictive coefficient vector, bed temperature to be predicted, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
x ( t ) j * = x ( t ) j - x ‾ j s x , j , (j=1,2,…,p) (8)
Wherein, x (t) jfor t moment j independent variable initial value,
Figure BDA00003617732700076
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample,
Figure BDA00003617732700077
for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
y ^ ( t ) * = x ( t ) 1 * x ( t ) 2 * . . . x ( t ) p * β - - - ( 9 )
Wherein,
Figure BDA00003617732700079
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
y ^ ( t ) = y ^ ( t ) * · s y + y ‾ - - - ( 10 )
Wherein,
Figure BDA000036177327000711
former dimension predicted value for t moment bed temperature.
Described method also comprises: 4) by the sampling time interval of setting, collection site intelligent instrument signal, by the actual bed temperature obtaining and predicted value comparison, if relative error is greater than 10%, new data is added to training sample data, re-execute step 1), 2), so that forecast model is upgraded.
In described step 3), from control station, read parameters, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, adjusting operation condition, is controlled at optimum range by bed temperature in time, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler.Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively.
Described independent variable comprises: operating condition variable: main steam flow, environment temperature, feed temperature, combustion chamber draft, bed pressure, coal-fired moisture, coal-fired volatile matter, coal-fired ash content, coal-fired sulphur content; Performance variable: wind total blast volume, Secondary Air total blast volume.
Circulating Fluidized Bed Temperature prognoses system and method proposed by the invention, by above-mentioned concrete implementation step, be described, person skilled obviously can be within not departing from content of the present invention, spirit and scope to device as herein described with method of operating is changed or suitably change and combination, realize the technology of the present invention.Special needs to be pointed out is, all similar replacements and change apparent to one skilled in the artly, they all can be deemed to be included in spirit of the present invention, scope and content.

Claims (1)

1. a Circulating Fluidized Bed Temperature prognoses system, is characterized in that, comprises the field intelligent instrument, database, data-interface, control station and the host computer that are connected with Circulating Fluidized Bed Boiler; Field intelligent instrument is connected with control station, database and host computer, and described host computer comprises:
Standardization module, for gather the historical record of operating condition variable and performance variable from database, the training sample matrix X that forms independent variable, gather the historical record of corresponding bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
Figure DEST_PATH_FDA0000444775250000011
Figure DEST_PATH_FDA0000444775250000012
1.2) ask standard deviation
Figure DEST_PATH_FDA0000444775250000013
Figure DEST_PATH_FDA0000444775250000014
1.3) standardization
Figure DEST_PATH_FDA0000444775250000015
Figure DEST_PATH_FDA0000444775250000016
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number,
Figure DEST_PATH_FDA0000444775250000017
for the average of training sample, s x,j, s yfor the standard deviation of training sample,
Figure DEST_PATH_FDA0000444775250000018
for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable;
Forecasting mechanism forms module, and for setting up forecast model, implementation step is as follows:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) predictive coefficient vector β is transmitted and stores into prediction execution module;
Prediction execution module, for predicting bed temperature according to the performance variable of the operating condition of Circulating Fluidized Bed Boiler and setting, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
Figure DEST_PATH_FDA0000444775250000021
Wherein, x (t) jfor t moment j independent variable initial value,
Figure DEST_PATH_FDA0000444775250000022
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample, for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
Figure DEST_PATH_FDA0000444775250000024
Wherein,
Figure DEST_PATH_FDA0000444775250000025
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
Wherein,
Figure DEST_PATH_FDA0000444775250000027
former dimension predicted value for t moment bed temperature;
Described host computer also comprises:
Signal acquisition module, for the sampling time interval by setting, gathers real time data from field intelligent instrument, and from database, gathers historical data;
Model modification module, by actual bed temperature and predicted value comparison, if relative error is greater than 10%, adds new data training sample data for the time interval by setting, and re-executes standardization module and forecasting mechanism and forms module;
Result display module, for reading parameters from control station, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, adjusting operation condition, is controlled at optimum range by bed temperature in time, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler; Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively;
Described independent variable comprises: operating condition variable: main steam flow, environment temperature, feed temperature, combustion chamber draft, bed pressure, coal-fired moisture, coal-fired volatile matter, coal-fired ash content, coal-fired sulphur content; Performance variable: wind total blast volume, Secondary Air total blast volume.2, the bed temperature Forecasting Methodology that use Circulating Fluidized Bed Temperature prognoses system claimed in claim 1 realizes, is characterized in that, described Forecasting Methodology comprises the following steps:
1) from database, gather the historical record of operating condition variable and performance variable, the training sample matrix X that forms independent variable, gather the historical record of corresponding bed temperature signal, form dependent variable training sample vector Y, training sample X, Y are carried out to standardization, the average that makes each variable is 0, and variance is 1, obtains independent variable training sample matrix X after standardization *dependent variable training sample vector Y after (n * p), standardization *(n * 1), adopts following process to complete:
1.1) average:
Figure DEST_PATH_FDA0000444775250000028
1.2) ask standard deviation
Figure DEST_PATH_FDA0000444775250000031
Figure DEST_PATH_FDA0000444775250000032
1.3) standardization
Figure DEST_PATH_FDA0000444775250000033
Figure DEST_PATH_FDA0000444775250000034
Wherein, x ij, y ifor the initial value of training sample point, n is training sample number, and p is independent variable number,
Figure DEST_PATH_FDA0000444775250000035
for the average of training sample, s x,j, s yfor the standard deviation of training sample, for the standardized value of training sample point, wherein subscript i, j represent respectively i training sample point, a j independent variable;
2) the standardized training sample obtaining is set up to forecast model by following process:
2.1) by (7) formula, ask predictive coefficient vector β:
β=(X *TX *) -1X *TY * (7)
Wherein, subscript: T ,-1 is transposition, the inverse of a matrix of representing matrix respectively;
2.2) preserve the predictive coefficient vector β obtaining;
3) using the performance variable of the operating condition variable of Circulating Fluidized Bed Boiler and setting as input signal, according to predictive coefficient vector, bed temperature to be predicted, implementation step is as follows:
3.1) the independent variable signal of input is processed by (8) formula:
Figure DEST_PATH_FDA0000444775250000037
Wherein, x (t) jfor t moment j independent variable initial value,
Figure DEST_PATH_FDA0000444775250000038
be the average of j independent variable training sample, s x,jbe the standard deviation of j independent variable training sample,
Figure DEST_PATH_FDA0000444775250000039
for t moment j independent variable nondimensionalization value, t represents that time, unit are second;
3.2) by following formula, ask the nondimensionalization predicted value of bed temperature:
Figure DEST_PATH_FDA00004447752500000310
Wherein,
Figure DEST_PATH_FDA00004447752500000311
nondimensionalization predicted value for t moment bed temperature;
3.3) by following formula, ask the former dimension predicted value of bed temperature:
Figure DEST_PATH_FDA00004447752500000312
Wherein,
Figure DEST_PATH_FDA00004447752500000313
former dimension predicted value for t moment bed temperature;
Described method also comprises: 4) by the sampling time interval of setting, collection site intelligent instrument signal, by the actual bed temperature obtaining and predicted value comparison, if relative error is greater than 10%, new data is added to training sample data, re-execute step 1), 2), so that forecast model is upgraded;
In described step 3), from control station, read parameters, and bed temperature predicted value is passed to control station show, and provide suggestion for operation: under current operating mode, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, so that control station staff, according to bed temperature predicted value and suggestion for operation, adjusting operation condition, is controlled at optimum range by bed temperature in time, effectively guarantees safety, the environmental protection operation of Circulating Fluidized Bed Boiler; Wherein, how performance variable is adjusted is conducive to bed temperature to be controlled at optimum range most, and a short-cut method is by the multiple combination value of performance variable, and substitution bed temperature prognoses system, obtains corresponding bed temperature predicted value, thereby by big or small, obtain very intuitively;
Described independent variable comprises: operating condition variable: main steam flow, environment temperature, feed temperature, combustion chamber draft, bed pressure, coal-fired moisture, coal-fired volatile matter, coal-fired ash content, coal-fired sulphur content; Performance variable: wind total blast volume, Secondary Air total blast volume.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105485674A (en) * 2016-01-21 2016-04-13 山西大学 Water supply instruction building method for supercritical low-calorific-value circulating fluidized bed boiler
WO2017063178A1 (en) * 2015-10-15 2017-04-20 Accenture Global Services Limited System and method for selecting controllable parameters for equipment operation safety
CN109426144A (en) * 2017-08-22 2019-03-05 邢台国泰发电有限责任公司 Flue gas in power station boiler method of denitration based on Random Forest model

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060085098A1 (en) * 2004-10-20 2006-04-20 Childress Ronald L Jr Predictive header pressure control
CN101017373A (en) * 2006-12-28 2007-08-15 浙江大学 Industrial process multiresolution softsensoring instrument and method thereof
CN101286044A (en) * 2008-05-12 2008-10-15 杭州电子科技大学 Coal-burning boiler system mixing modeling method
CN102194057A (en) * 2011-05-05 2011-09-21 浙江宜景环保科技有限公司 Method for updating model of waste plastic oil refining combustion optimization
CN102494336A (en) * 2011-12-16 2012-06-13 浙江大学 Combustion process multivariable control method for CFBB (circulating fluidized bed boiler)
CN103197549A (en) * 2013-03-04 2013-07-10 华北电力大学 Soft measurement method and optimal control method of sulfur dioxide in circulating fluidized bed boiler smoke

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060085098A1 (en) * 2004-10-20 2006-04-20 Childress Ronald L Jr Predictive header pressure control
CN101017373A (en) * 2006-12-28 2007-08-15 浙江大学 Industrial process multiresolution softsensoring instrument and method thereof
CN101286044A (en) * 2008-05-12 2008-10-15 杭州电子科技大学 Coal-burning boiler system mixing modeling method
CN102194057A (en) * 2011-05-05 2011-09-21 浙江宜景环保科技有限公司 Method for updating model of waste plastic oil refining combustion optimization
CN102494336A (en) * 2011-12-16 2012-06-13 浙江大学 Combustion process multivariable control method for CFBB (circulating fluidized bed boiler)
CN103197549A (en) * 2013-03-04 2013-07-10 华北电力大学 Soft measurement method and optimal control method of sulfur dioxide in circulating fluidized bed boiler smoke

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
吴家标 等: "循环流化床锅炉效率相关参数的建模研究", 《计算机与应用化学》 *
吴家标 等: "循环流化床锅炉节能的操作优化", 《江南大学学报 (自然科学版)》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017063178A1 (en) * 2015-10-15 2017-04-20 Accenture Global Services Limited System and method for selecting controllable parameters for equipment operation safety
CN109643087A (en) * 2015-10-15 2019-04-16 埃森哲环球服务有限公司 System and method for selecting the controllable parameter for equipment operation safety
US10545465B2 (en) 2015-10-15 2020-01-28 Accenture Global Services Limited System and method for selecting controllable parameters for equipment operation safety
CN109643087B (en) * 2015-10-15 2021-09-10 埃森哲环球服务有限公司 System and method for selecting controllable parameters for operational safety of a device
CN105485674A (en) * 2016-01-21 2016-04-13 山西大学 Water supply instruction building method for supercritical low-calorific-value circulating fluidized bed boiler
CN109426144A (en) * 2017-08-22 2019-03-05 邢台国泰发电有限责任公司 Flue gas in power station boiler method of denitration based on Random Forest model
CN109426144B (en) * 2017-08-22 2021-07-16 邢台国泰发电有限责任公司 Power station boiler flue gas denitration method based on random forest model

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