CN105160479A - Method for measuring boiler dry flue gas volume based on coal caloric values and exhaust fume oxygen amount - Google Patents

Method for measuring boiler dry flue gas volume based on coal caloric values and exhaust fume oxygen amount Download PDF

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Publication number
CN105160479A
CN105160479A CN201510567705.6A CN201510567705A CN105160479A CN 105160479 A CN105160479 A CN 105160479A CN 201510567705 A CN201510567705 A CN 201510567705A CN 105160479 A CN105160479 A CN 105160479A
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China
Prior art keywords
flue gas
coal
dry flue
content
calorific value
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CN201510567705.6A
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Inventor
郝勇生
韦思超
周志成
苏志刚
王培红
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Southeast University
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Southeast University
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Priority to CN201510567705.6A priority Critical patent/CN105160479A/en
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/80Management or planning
    • Y02P90/84Greenhouse gas [GHG] management systems

Abstract

The invention discloses a method for measuring boiler dry flue gas volume based on coal caloric values and exhaust fume oxygen amount. The exhaust fume oxygen amount can be acquired from the database of a power plant decentralized control system DCS, the coal caloric values are obtained from a power plant coal industrial analysis report, an excess air coefficient is obtained through the calculation based on the exhaust fume oxygen amount, and the CO2 theoretical maximum value is obtained through the calculation based on the coal caloric values. The content of CO2 in the dry flue gas is obtained through the calculation based on the excess air coefficient and the CO2 theoretical maximum value, and the volume and the mass of the dry flue gas are respectively obtained through the calculation based on the content of CO2 in the dry flue gas and the coal caloric values. The measuring method can effectively prevent the strict requirement that the coal component element analysis needs to be calculated based on national standard, simplifies the calculating model of the dry flue gas, and can meet the needs for the online calculation of the dry flue gas of a boiler.

Description

A kind of method measuring boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas
Technical field
The present invention relates to a kind of assay method of boiler dry flue gas amount, belong to soft-measuring technique field.
Background technology
Boiler dry flue gas amount, as parameter important in boiler combustion process, is directly connected to the discharge capacity of boiler economics and pollutant.At present, boiler dry flue gas amount normally calculates based on the master pattern in GB10184-88, namely determines exhaust gas volumn by the ultimate analysis of coal-fired composition.
But the dry flue gas amount computing method of national Specification are general only for boiler thermal output test or boiler performance certification test.Because power plant does not possess the ability of coal-fired component element analysis, therefore the computing method of the dry flue gas amount of national Specification can not be used for the operating analysis of power plant.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, the invention provides a kind of method measuring boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas, can realize the dry flue gas amount of other measured operating parameter boilers by coal-fired calorific value and boiler.
Technical scheme: for achieving the above object, the technical solution used in the present invention is:
A kind of method measuring boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas, oxygen content in exhaust gas is obtained from the database of DCS of Power Plant DCS, the coal-fired calorific value of coal is obtained from power plant coal quality industrial analysis report, calculate excess air coefficient according to described oxygen content in exhaust gas, calculate CO according to described coal-fired calorific value 2theoretical maximum; According to described excess air coefficient and CO 2theoretical maximum calculates CO 2content in dry flue gas, according to described CO 2content in dry flue gas and coal-fired calorific value calculate volume and the quality of dry flue gas respectively.
Concrete calculation procedure is as follows:
Step 1: obtain oxygen content in exhaust gas O from the database of DCS of Power Plant DCS 2py, from power plant coal quality industrial analysis report, obtain the coal-fired calorific value Q of low level of coal dy;
Step 2: the excess air coefficient α calculating fume side:
α = 21 21 - O 2 p y
Step 3: calculate CO 2content in dry flue gas:
(1) CO is calculated 2theoretical maximum CO 2max:
CO 2 m a x = ( 0.10162 + 0.04399 × Q d y / 1000 ) ( 0.44971 + 0.23825 × Q d y / 1000 ) × 100 %
(2) CO is calculated 2content CO in dry flue gas 2:
CO 2 = CO 2 max α × 100 %
Step 4: the volume V calculating dry flue gas lywith quality μ ly:
(1) dry flue gas volume V is calculated ly:
V ly=(1.1296-0.02028×Q dy/1000)+(0.10162+0.04399×Q dy/1000)/CO 2
(2) dry flue gas quality μ is calculated ly:
μ ly=(0.96569+0.00707×Q dy/1000)+(0.13139+0.05699×Q dy/1000)/CO 2
Beneficial effect: the present invention is based on coal-fired calorific value and calculate dry flue gas amount, effectively prevent national standard and calculate the rigors needing coal-fired component element to analyze, simplify the computation model of dry flue gas amount, the needs in line computation of boiler dry flue gas amount can be met.
Accompanying drawing explanation
Fig. 1 is method flow diagram of the present invention.
Embodiment
Below in conjunction with accompanying drawing, the present invention is further described.
Be illustrated in figure 1, a kind of method measuring boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas, oxygen content in exhaust gas is obtained from the database of DCS of Power Plant DCS, the coal-fired calorific value of coal is obtained from power plant coal quality industrial analysis report, calculate excess air coefficient according to described oxygen content in exhaust gas, calculate CO according to described coal-fired calorific value 2theoretical maximum; According to described excess air coefficient and CO 2theoretical maximum calculates CO 2content in dry flue gas, according to described CO 2content in dry flue gas and coal-fired calorific value calculate volume and the quality of dry flue gas respectively.
The present invention, for 1000MW boiler, as follows to the detailed step of dry flue gas quantitative determination:
Step 1: obtain oxygen content in exhaust gas O from the database of DCS DCS of Power Plant DCS 2py, the operating condition down smoke-discharging oxygen amount value O in certain moment 2pyfor: 4.0%, from power plant coal quality industrial analysis report, obtain the coal-fired calorific value Q of low level of coal dy, the coal-fired calorific value Q of low level of coal dy: 20742.0kJ/kg;
Step 2: the excess air coefficient α calculating fume side:
α = 21 21 - O 2 p y = 1.2353
Step 3: calculate CO 2content in dry flue gas:
(1) CO is calculated according to the derivation of thermal engineering atlas curve 2theoretical maximum CO 2maxformula:
CO 2 m a x = ( 0.10162 + 0.04399 × Q d y / 1000 ) ( 0.44971 + 0.23825 × Q d y / 1000 ) × 100 % = 18.81 %
(2) CO is calculated 2content CO in dry flue gas 2%:
CO 2 = CO 2 max α k 100 % = 15.26 %
Step 4: the volume V calculating dry flue gas lywith quality μ ly:
(1) dry flue gas volume V is calculated according to the derivation of thermal engineering atlas curve lyformula:
V ly=(1.1296-0.02028×Q dy/1000)+(0.10162+0.04399×Q dy/1000)/CO 2=7.369m 3/kg
(2) dry flue gas quality μ is calculated according to the derivation of thermal engineering atlas curve lyformula:
μ ly=(0.96569+0.00707×Q dy/1000)+(0.13139+0.05699×Q dy/1000)/CO 2=9.7389kg/kg
The above is only the preferred embodiment of the present invention; be noted that for those skilled in the art; under the premise without departing from the principles of the invention, can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.

Claims (2)

1. one kind measures the method for boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas, it is characterized in that: from the database of DCS of Power Plant DCS, obtain oxygen content in exhaust gas, the coal-fired calorific value of coal is obtained from power plant coal quality industrial analysis report, calculate excess air coefficient according to described oxygen content in exhaust gas, calculate CO according to described coal-fired calorific value 2theoretical maximum; According to described excess air coefficient and CO 2theoretical maximum calculates CO 2content in dry flue gas, according to described CO 2content in dry flue gas and coal-fired calorific value calculate volume and the quality of dry flue gas respectively.
2. a kind of method measuring boiler dry flue gas amount based on coal-fired calorific value and oxygen content in exhaust gas according to claim 1, is characterized in that: concrete calculation procedure is as follows:
Step 1: obtain oxygen content in exhaust gas O from the database of DCS of Power Plant DCS 2py, from power plant coal quality industrial analysis report, obtain the coal-fired calorific value Q of low level of coal dy;
Step 2: the excess air coefficient α calculating fume side:
α = 21 21 - O 2 p y
Step 3: calculate CO 2content in dry flue gas:
(1) CO is calculated 2theoretical maximum CO 2max:
CO 2 m a x = ( 0.10162 + 0.04399 × Q d y / 1000 ) ( 0.44971 + 0.23825 × Q d y / 1000 ) × 100 %
(2) CO is calculated 2content CO in dry flue gas 2:
Step 4: the volume V calculating dry flue gas lywith quality μ ly:
(1) dry flue gas volume V is calculated ly:
V ly=(1.1296-0.02028×Q dy/1000)+(0.10162+0.04399×Q dy/1000)/CO 2
(2) dry flue gas quality μ is calculated ly:
μ ly=(0.96569+0.00707×Q dy/1000)+(0.13139+0.05699×Q dy/1000)/CO 2
CN201510567705.6A 2015-09-08 2015-09-08 Method for measuring boiler dry flue gas volume based on coal caloric values and exhaust fume oxygen amount Pending CN105160479A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105467086A (en) * 2015-12-28 2016-04-06 国网山东省电力公司电力科学研究院 Method for measuring flue gas amount of boiler of power station
CN106596861A (en) * 2016-12-22 2017-04-26 湖南工程学院 Offshore generating host flue gas amount measuring and calculating method
CN108460243A (en) * 2018-02-02 2018-08-28 国网福建省电力有限公司 A kind of Industrial Analysis calculating elements analysis method using coal of small sample
CN112966216A (en) * 2021-02-08 2021-06-15 龙源(北京)碳资产管理技术有限公司 Method for calculating heat value of fuel coal based on hydrocarbon element and application thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102012968A (en) * 2010-11-24 2011-04-13 东北电力大学 Method for monitoring thermal efficiency and coal quality data of pulverized coal fired boiler in real time
CN103208035A (en) * 2013-03-25 2013-07-17 吉林省电力有限公司电力科学研究院 Energy-saving dispatching optimization method for sets
CN103995987A (en) * 2014-06-05 2014-08-20 中冶华天工程技术有限公司 Heat efficiency calculating method for pulverized coal boiler with blending combustion of blast furnace gas
CN104008297A (en) * 2014-06-05 2014-08-27 中冶华天工程技术有限公司 Method for calculating thermal efficiency of coal dust and blast furnace gas co-combustion boiler

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102012968A (en) * 2010-11-24 2011-04-13 东北电力大学 Method for monitoring thermal efficiency and coal quality data of pulverized coal fired boiler in real time
CN103208035A (en) * 2013-03-25 2013-07-17 吉林省电力有限公司电力科学研究院 Energy-saving dispatching optimization method for sets
CN103995987A (en) * 2014-06-05 2014-08-20 中冶华天工程技术有限公司 Heat efficiency calculating method for pulverized coal boiler with blending combustion of blast furnace gas
CN104008297A (en) * 2014-06-05 2014-08-27 中冶华天工程技术有限公司 Method for calculating thermal efficiency of coal dust and blast furnace gas co-combustion boiler

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张小桃 等: "一种新的锅炉效率的计算模型", 《电站系统工程》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105467086A (en) * 2015-12-28 2016-04-06 国网山东省电力公司电力科学研究院 Method for measuring flue gas amount of boiler of power station
CN105467086B (en) * 2015-12-28 2017-03-22 国网山东省电力公司电力科学研究院 Method for measuring flue gas amount of boiler of power station
CN106596861A (en) * 2016-12-22 2017-04-26 湖南工程学院 Offshore generating host flue gas amount measuring and calculating method
CN108460243A (en) * 2018-02-02 2018-08-28 国网福建省电力有限公司 A kind of Industrial Analysis calculating elements analysis method using coal of small sample
CN108460243B (en) * 2018-02-02 2021-09-28 国网福建省电力有限公司 Small sample industrial analysis and calculation element analysis method using coal
CN112966216A (en) * 2021-02-08 2021-06-15 龙源(北京)碳资产管理技术有限公司 Method for calculating heat value of fuel coal based on hydrocarbon element and application thereof

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