CN103439468A - Method for indirectly monitoring oxygen content in industrial furnace group - Google Patents

Method for indirectly monitoring oxygen content in industrial furnace group Download PDF

Info

Publication number
CN103439468A
CN103439468A CN2013104049474A CN201310404947A CN103439468A CN 103439468 A CN103439468 A CN 103439468A CN 2013104049474 A CN2013104049474 A CN 2013104049474A CN 201310404947 A CN201310404947 A CN 201310404947A CN 103439468 A CN103439468 A CN 103439468A
Authority
CN
China
Prior art keywords
oxygen
sampling
industrial furnace
analyser
value
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN2013104049474A
Other languages
Chinese (zh)
Other versions
CN103439468B (en
Inventor
陈在平
倪建云
贾超
刘峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin University of Technology
Original Assignee
Tianjin University of Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin University of Technology filed Critical Tianjin University of Technology
Priority to CN201310404947.4A priority Critical patent/CN103439468B/en
Publication of CN103439468A publication Critical patent/CN103439468A/en
Application granted granted Critical
Publication of CN103439468B publication Critical patent/CN103439468B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Regulation And Control Of Combustion (AREA)

Abstract

The invention discloses a method for indirectly monitoring oxygen content in an industrial furnace group. According to the method, sample data of an oxygen analyzer are analyzed, the judgment of ending a sampling switching process is completed by adopting a time and data combination drive method, and then the problem of sample data missing caused by alternative sampling in an oxygen monitoring system is solved by using a difference value average strategy. By adopting the method, indirect monitoring that the oxygen analyzer alternatively samples oxygen contents in oxygen monitoring systems of multiple industrial furnaces can be realized.

Description

A kind of industrial furnace group oxygen content indirect monitoring method
Technical field
The present invention relates to oxygen content indirect monitoring technology in the industrial furnace monitoring system, this technology relates to a kind of monitoring technology by many industrial furnace oxygen contents of an oxygen analyser alternating sampling.
Background technology
More and more pay attention to the problems such as industrial energy saving and environmental protection along with China, its monitoring requirement of real-time to large and medium-sized enterprise's industrial furnace operation conditions is more and more higher.In a large amount of existing industrial furnace supervisory systems, what in situation, its supervisory system was mainly considered mostly is the technological requirement of industrial furnace combustion process, for energy consumption and burning efficiency, does not take into full account.Therefore, in the process to industrial furnace combustion position monitoring system transformation, adopt online oxygen analyser to be sampled to industrial furnace, realize that real-time monitoring to industrial furnace is to improve burning efficiency.At present, in the monitoring system that many industrial furnace oxygen contents of an oxygen analyser alternating sampling are arranged, there is no a kind of suitable method for solving judgement and the sampling process shortage of data problem in alternating sampling process sampling switching.
Summary of the invention
The objective of the invention is the problems referred to above that exist for solving prior art, a kind of industrial furnace group oxygen content indirect monitoring method is provided.
The zirconia that the inventive method is installed at ad-hoc location according to technological requirement by the industrial furnace group and be the oxygen analyser of energy consumption monitoring installation, determine the statistics rule between the oxygen content that zirconia and oxygen analyser detect respectively, form a kind of based on data and time combination drive and difference Average Strategy, realization is to the industrial furnace sample handoff procedure oxygen content indirect monitoring of mining massively, and the method comprises the following steps:
1, a kind of industrial furnace group oxygen content indirect monitoring method, it is characterized in that, the zirconia that the method is installed at ad-hoc location according to technological requirement by the industrial furnace group and be the oxygen analyser of energy consumption monitoring installation, determine the statistics rule between the oxygen content that zirconia and oxygen analyser detect respectively, form the combination drive method of a kind of time-based and data, the oxygen analyser sampled data is analyzed to sampling time and the rule relation between sampled data and the difference Average Strategy drawn.Realization is the indirect monitoring for oxygen content in the sampling handoff procedure to the industrial furnace flock-mate, comprises the following steps:
The 1st step, the oxygen content of utilizing Mind on statistics to detect respectively zirconia and oxygen analyser are analyzed
After the 1.1st step, the sample of industrial furnace being mined massively at oxygen analyser complete one-period, sampled value to this cycle of oxygen analyser is analyzed, judge the residing stabilized zone of sampled value in the time of can normally reflecting industrial furnace Actual combustion situation, thereby determine that the analyser sampled value is started through peak value to the time of experiencing when the stabilized zone by sampling
Figure 2013104049474100002DEST_PATH_IMAGE002
;
The 1.2nd step, when the oxygen analyser sampled value, during in stabilized zone, calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure 2013104049474100002DEST_PATH_IMAGE004
,
Figure 2013104049474100002DEST_PATH_IMAGE006
,
Figure 2013104049474100002DEST_PATH_IMAGE008
mean that data start in stabilized zone to finish the oxygen analyser sampling number to sampling;
The 1.3rd step, according to the analysis of oxygen analyser sampled data, determine the oxygen analyser sampled value in the stabilized zone time difference value
Figure 632682DEST_PATH_IMAGE004
maximal value and minimum value scope
Figure 2013104049474100002DEST_PATH_IMAGE010
;
The 2nd step, employing time and data mixing drive method to be judged the end of sampling handoff procedure
When the 2.1st step, oxygen analyser are sampled again to selected industrial furnace, in the oxygen monitoring system, time delay sampled afterwards;
After the 2.2nd step, oxygen monitoring system start sampling, calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure 2013104049474100002DEST_PATH_IMAGE012
,
Figure 2013104049474100002DEST_PATH_IMAGE014
,
Figure 2013104049474100002DEST_PATH_IMAGE016
expression from
Figure 629642DEST_PATH_IMAGE002
constantly sampling starts to be switched and determined to sampling that to finish be oxygen analyser sampled value oxygen analyser sampling number can truly reflect the industrial furnace oxygen content time;
The 2.3rd step, according to the difference range determined in the 1.3rd step
Figure 428971DEST_PATH_IMAGE010
, to calculating each of gained
Figure 952356DEST_PATH_IMAGE012
the size of value is judged according to the 2.4th and the 2.5th step;
If the 2.4th step
Figure 2013104049474100002DEST_PATH_IMAGE018
, continue difference judged;
If the 2.5th step
Figure 2013104049474100002DEST_PATH_IMAGE020
, think that this moment oxygen analyser sampled value can reflect this industrial furnace Actual combustion situation, the sampling handoff procedure is judged end, in the oxygen monitoring system, each oxygen content value constantly of industrial furnace is the oxygen analysis actual sample value.
The 3rd step, employing difference strategy carry out indirect monitoring to the missing data of sampling process
The 3.1st step, after the sampling handoff procedure judge to finish, when in the oxygen monitoring system, the industrial furnace oxygen content is the oxygen analyser actual sample value, continue to calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure 2013104049474100002DEST_PATH_IMAGE022
,
Figure 2013104049474100002DEST_PATH_IMAGE024
,
Figure 2013104049474100002DEST_PATH_IMAGE026
expression is switched and determined and finishes to finish the oxygen analyser sampling number to the sampling process to this industrial furnace from sampling;
The 3.2nd step, when oxygen analyser finishes this industrial furnace sampling process, calculate whole differences in the oxygen monitoring system
Figure 935411DEST_PATH_IMAGE022
mean value
Figure 2013104049474100002DEST_PATH_IMAGE028
;
The 3.3rd step, when oxygen analyser is switched to the sampling of another industrial furnace, this industrial furnace oxygen content in the oxygen monitoring system
Figure 2013104049474100002DEST_PATH_IMAGE030
with zirconia sampled value and the difference mean value calculated
Figure 335168DEST_PATH_IMAGE028
sum means.
advantage of the present invention and beneficial effect
The technical scheme adopted by the invention described above can be found out, this method adopts time and data mixing to drive and the difference averaging method, complete the indirect monitoring to oxygen content in industrial furnace sampling handoff procedure, the method has higher practicality for the system by an oxygen analyser alternating sampling industrial furnace group oxygen content.
The accompanying drawing explanation
Fig. 1 is oxygen analyser sampling process flow diagram.
Fig. 2 is the oxygen analyser working timing figure.
Fig. 3 is oxygen analyser sampled value change curve.
Fig. 4 is oxygen content difference change curve.
Fig. 5 is sampling handoff procedure decision flowchart.
Fig. 6 is difference method of average calculation flow chart.
Fig. 7 is system displayed value and analyser sampled value correlation curve figure.
Embodiment
The concrete steps of industrial furnace group oxygen content indirect monitoring method provided by the invention are as follows:
The 1st step, the oxygen content of utilizing Mind on statistics to detect respectively zirconia and oxygen analyser are analyzed
Fig. 1 is system oxygen analyser sampling process flow diagram, adopt two industrial furnace oxygen contents of an oxygen analyser alternating sampling in the oxygen monitoring system, each sampling process maintains 30 minutes, after oxygen analyser has been sampled to an industrial furnace oxygen content, be switched to another industrial furnace is sampled through blowback, gas storage process, in blowback, gas storage process, in oxygen analyser, mixed air.Therefore, when oxygen analyser is switched to when another industrial furnace oxygen content is sampled, initial analyser sampled value can not truly reflect the Actual combustion situation of industrial furnace.
Fig. 2 is the oxygen analyser working timing figure,
Figure 40956DEST_PATH_IMAGE002
the sampled value that means oxygen analyser is passed through the time that peak value extremely experiences when stabilized zone by starting to sample.
Figure DEST_PATH_IMAGE032
mean the oxygen analyser sampling handoff procedure judgement period.Within this period, oxygen analyser has been switched to is sampled to an industrial furnace, but because analyser experiences blowback, gas storage process in a upper sampling process, make the initial sampled value of analyser finally just enter stabilized zone by reaching gently peak value, and can not truly reflect the actual state of this industrial furnace burning. mean that the analyser sampled value can truly reflect the industrial furnace combustion position period.
Figure DEST_PATH_IMAGE036
when the expression analyser is switched to another industrial furnace sampling after completing this industrial furnace being sampled, in the oxygen monitoring system, the period of sampled data disappearance appears in this industrial furnace.
Oxygen analyser sampled value change curve as shown in Figure 3, can roughly be judged sampled value by starting sampling through the peak value time required to stabilized zone according to curve map
Figure 500756DEST_PATH_IMAGE002
it is 600 seconds.During in stabilized zone, calculate the poor of synchronization zirconia sampled value and oxygen analyser sampled value when sampled value
Figure 291994DEST_PATH_IMAGE004
.The difference change curve as shown in Figure 4, is determined the analyser sampled value in the stabilized zone time difference value with this
Figure 370809DEST_PATH_IMAGE004
minimum value and peaked scope
Figure DEST_PATH_IMAGE038
.
The judgement that the 2nd step, employing time and data mixing have driven the sampling handoff procedure to finish
As shown in Figure 2, the analyser sampling process in
Figure 993420DEST_PATH_IMAGE032
in the time of in time period, according to the analysis to last cycle analyser sampled value change curve, utilize time and the data mixing driving method handoff procedure of being sampled to judge.Fig. 5 is sample handoff procedure decision flowchart, wherein,
Figure DEST_PATH_IMAGE040
Figure DEST_PATH_IMAGE042
for the oxygen analyser sampled value, expression from
Figure 840339DEST_PATH_IMAGE002
sampling constantly starts to be switched and determined and to finish to sampling, oxygen analyser sampling number when the oxygen analyser sampled value can truly reflect the industrial furnace oxygen content; for the oxygen content of zirconia collection, before be switched and determined finishing in sampling, within every 1 second, calculate the poor of zirconia collection value once and oxygen analyser sampled value,
Figure 199962DEST_PATH_IMAGE030
for industrial furnace oxygen content displayed value in the oxygen monitoring system.
Concrete operation step is described below.When oxygen analyser is sampled to this industrial furnace, postpone after 600 seconds to be sampled again, within every 1 second, calculate the poor of primary oxygen analyser sampled value and zirconia sampled value during in stabilized zone in sampled value
Figure 204827DEST_PATH_IMAGE012
, and this difference size is judged, until
Figure DEST_PATH_IMAGE046
, draw
Figure DEST_PATH_IMAGE048
.Now, think that the oxygen analyser sampled value can normally reflect the Actual combustion situation of this industrial furnace, oxygen content displayed value in the oxygen monitoring system
Figure 705079DEST_PATH_IMAGE030
for the actual sample value of oxygen analyser, the sampling handoff procedure is judged end.
The 3rd step, employing difference strategy carry out indirect monitoring to the missing data of sampling process
As shown in Figure 2, mean that oxygen analyser completes and is switched to when another industrial furnace is sampled the sampling of this industrial furnace, the time period of shortage of data phenomenon appears in this industrial furnace.Analyzed according to the sampled data to the last cycle, adopt the difference Average Strategy to carry out indirect monitoring to the sampled data disappearance process of this industrial furnace.
Concrete operation step is as follows.Fig. 6 is difference method of average calculation flow chart.After monitoring system completes the judgement to the sampling handoff procedure, during actual sample value that the monitoring system displayed value is oxygen analyser, in this sampling process, system proceeds as follows:
(1)
Figure DEST_PATH_IMAGE054
(2)
Wherein,
Figure DEST_PATH_IMAGE056
mean the rear oxygen analyser sampled value of sampling handoff procedure judgement,
Figure DEST_PATH_IMAGE058
mean phase zirconia collection value in the same time,
Figure 933288DEST_PATH_IMAGE022
mean to calculate in every 1 second the poor of oxygen analyser sampled value once and zirconia sampled value, expression from the sampling handoff procedure judge to finish to the sampling number of rear oxygen analyser that this industrial furnace has been sampled.This periodic sampling data analysis is obtained
Figure DEST_PATH_IMAGE060
, when oxygen analyser finishes to this heating furnace is sampled from sampling is switched and determined, sampled altogether 1200 times.
After oxygen analyser is switched to another industrial furnace is sampled, the system oxygen content value of this industrial furnace
Figure 34285DEST_PATH_IMAGE030
meet following relational expression:
Figure DEST_PATH_IMAGE062
(3)
As shown in Fig. 7 system displayed value and analyser sampled value correlation curve figure, by this method, monitoring system has completed the indirect monitoring to industrial furnace group oxygen content, and has very high practicality.Should use the same method and carry out indirect monitoring for the oxygen content of another industrial furnace.
The present invention is applicable to the system by an oxygen analyser alternating sampling industrial furnace group oxygen content, for similar system, has very high practicality.

Claims (1)

1. an industrial furnace group oxygen content indirect monitoring method, it is characterized in that, the zirconia that the method is installed at ad-hoc location according to technological requirement by the industrial furnace group and be the oxygen analyser of energy consumption monitoring installation, determine the statistics rule between the oxygen content that zirconia and oxygen analyser detect respectively, form the combination drive method of a kind of time-based and data, the oxygen analyser sampled data is analyzed to sampling time and the rule relation between sampled data and the difference Average Strategy drawn; Realization is the indirect monitoring for oxygen content in the sampling handoff procedure to the industrial furnace flock-mate, comprises the following steps:
The 1st step, the oxygen content of utilizing Mind on statistics to detect respectively zirconia and oxygen analyser are analyzed
After the 1.1st step, the sample of industrial furnace being mined massively at oxygen analyser complete one-period, sampled value to this cycle of oxygen analyser is analyzed, judge the residing stabilized zone of sampled value in the time of can normally reflecting industrial furnace Actual combustion situation, thereby determine that the analyser sampled value is started through peak value to the time of experiencing when the stabilized zone by sampling
Figure 2013104049474100001DEST_PATH_IMAGE002
;
The 1.2nd step, when the oxygen analyser sampled value, during in stabilized zone, calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure 2013104049474100001DEST_PATH_IMAGE004
,
Figure DEST_PATH_IMAGE006
,
Figure DEST_PATH_IMAGE008
mean that data start in stabilized zone to finish the oxygen analyser sampling number to sampling;
The 1.3rd step, according to the analysis of oxygen analyser sampled data, determine the oxygen analyser sampled value in the stabilized zone time difference value maximal value and minimum value scope
Figure DEST_PATH_IMAGE010
;
The 2nd step, employing time and data mixing drive method to be judged the end of sampling handoff procedure
When the 2.1st step, oxygen analyser are sampled again to selected industrial furnace, in the oxygen monitoring system, time delay sampled afterwards;
After the 2.2nd step, oxygen monitoring system start sampling, calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure DEST_PATH_IMAGE012
,
Figure DEST_PATH_IMAGE014
,
Figure DEST_PATH_IMAGE016
expression from
Figure 500005DEST_PATH_IMAGE002
constantly sampling starts to be switched and determined to sampling that to finish be oxygen analyser sampled value oxygen analyser sampling number can truly reflect the industrial furnace oxygen content time;
The 2.3rd step, according to the difference range determined in the 1.3rd step , to calculating each of gained
Figure 771903DEST_PATH_IMAGE012
the size of value is judged according to the 2.4th and the 2.5th step;
If the 2.4th step
Figure DEST_PATH_IMAGE018
, continue difference
Figure 656683DEST_PATH_IMAGE012
judged;
If the 2.5th step
Figure DEST_PATH_IMAGE020
, think that this moment oxygen analyser sampled value can reflect this industrial furnace Actual combustion situation, the sampling handoff procedure is judged end, in the oxygen monitoring system, each oxygen content value constantly of industrial furnace is the oxygen analysis actual sample value;
The 3rd step, employing difference strategy carry out indirect monitoring to the missing data of sampling process
The 3.1st step, after the sampling handoff procedure judge to finish, when in the oxygen monitoring system, the industrial furnace oxygen content is the oxygen analyser actual sample value, continue to calculate the poor of synchronization oxygen analyser sampled value and zirconia sampled value
Figure DEST_PATH_IMAGE022
,
Figure DEST_PATH_IMAGE024
,
Figure DEST_PATH_IMAGE026
expression is switched and determined and finishes to finish the oxygen analyser sampling number to the sampling process to this industrial furnace from sampling;
The 3.2nd step, when oxygen analyser finishes this industrial furnace sampling process, calculate whole differences in the oxygen monitoring system
Figure 110667DEST_PATH_IMAGE022
mean value
Figure DEST_PATH_IMAGE028
;
The 3.3rd step, when oxygen analyser is switched to the sampling of another industrial furnace, this industrial furnace oxygen content in the oxygen monitoring system
Figure DEST_PATH_IMAGE030
with zirconia sampled value and the difference mean value calculated sum means.
CN201310404947.4A 2013-09-09 2013-09-09 A kind of industrial furnace group oxygen content indirect monitoring method Expired - Fee Related CN103439468B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310404947.4A CN103439468B (en) 2013-09-09 2013-09-09 A kind of industrial furnace group oxygen content indirect monitoring method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310404947.4A CN103439468B (en) 2013-09-09 2013-09-09 A kind of industrial furnace group oxygen content indirect monitoring method

Publications (2)

Publication Number Publication Date
CN103439468A true CN103439468A (en) 2013-12-11
CN103439468B CN103439468B (en) 2015-08-26

Family

ID=49693172

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310404947.4A Expired - Fee Related CN103439468B (en) 2013-09-09 2013-09-09 A kind of industrial furnace group oxygen content indirect monitoring method

Country Status (1)

Country Link
CN (1) CN103439468B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030120444A1 (en) * 2001-08-13 2003-06-26 Sempra Energy Solutions System and method for environmental data acquisition
CN1485602A (en) * 2002-09-26 2004-03-31 马克文 Method and apparatus for measuring chimney heat exchanger air leakage ratio
CN103257205A (en) * 2013-04-22 2013-08-21 鞍山翰玛传感技术有限公司 Coke oven group oxynitride detection method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20030120444A1 (en) * 2001-08-13 2003-06-26 Sempra Energy Solutions System and method for environmental data acquisition
CN1485602A (en) * 2002-09-26 2004-03-31 马克文 Method and apparatus for measuring chimney heat exchanger air leakage ratio
CN103257205A (en) * 2013-04-22 2013-08-21 鞍山翰玛传感技术有限公司 Coke oven group oxynitride detection method

Also Published As

Publication number Publication date
CN103439468B (en) 2015-08-26

Similar Documents

Publication Publication Date Title
EP2661546B1 (en) Internal combustion engine with exhaust after treatment and its method of operation
CN102397875B (en) Production method of longitudinal thickness-variable steel plate
CN104728989B (en) Air conditioner defrosting control method and the air conditioner for performing the defrosting control method
CN102880795A (en) Method for acquiring target values of boiler optimized operation economic parameters
Yang et al. Research on optimum method to eliminate backfire of hydrogen internal combustion engines based on combining postponing ignition timing with water injection of intake manifold
Zhou et al. Capturing CO2 from cement plants: A priority for reducing CO2 emissions in China
MX337765B (en) Dry sorbent injection during non-steady state conditons in dry scrubber.
CN204536959U (en) A kind of FGD device Predictive Control System for coal-burning power plant
CN111795584B (en) Control method and device for reducing content of nitrogen oxides in combustion waste gas of heating furnace
CN105298602A (en) Particle trap real-time online updating regeneration control method
CN111242469B (en) Method and system for coupling ultralow emission and high-efficiency energy-saving operation of boiler or kiln
CN104933874A (en) Traffic light self-adaptive control method and device
CN108958031B (en) Post combustion CO2Coordinated prediction control method for trapping coal-fired power generation system
CN105688531A (en) A pressure difference-timing sequence mixed control method for a bag type dust collector
CN103439468A (en) Method for indirectly monitoring oxygen content in industrial furnace group
CN103322640B (en) Air conditioner energy saving control method, system and air-conditioning switching system that synthesis energy saving is built
Dong et al. Future zero carbon ammonia engine: Fundamental study on the effect of jet ignition system characterized by gasoline ignition chamber
Li et al. CO2 capture modelling for pulverised coal-fired power plants: A case study of an existing 1 GW ultra-supercritical power plant in Shandong, China
CN103759458A (en) Flue gas waste heat recovery system based on absorption-type heat pump technology
CN102706098B (en) Hot start method for boost expander
CN205619266U (en) Annealing stove gas controlling means
CN102363827B (en) Method and system for coordinative production of electric arc furnace and waste heat recovery device
CN115301056A (en) Denitration flue gas interlocking control system and denitration process
CN102231056B (en) Timer sharing method
CN203550273U (en) Flue gas waste heat recovery system based on absorption heat pump technology

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150826

Termination date: 20160909