CN108053330A - A kind of computational methods and system of pollutant uncontrollable discharge amount - Google Patents
A kind of computational methods and system of pollutant uncontrollable discharge amount Download PDFInfo
- Publication number
- CN108053330A CN108053330A CN201711292874.9A CN201711292874A CN108053330A CN 108053330 A CN108053330 A CN 108053330A CN 201711292874 A CN201711292874 A CN 201711292874A CN 108053330 A CN108053330 A CN 108053330A
- Authority
- CN
- China
- Prior art keywords
- pollutant
- dirty
- amorphous
- temperature
- coke oven
- 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
Links
- 239000003344 environmental pollutant Substances 0.000 title claims abstract description 124
- 231100000719 pollutant Toxicity 0.000 title claims abstract description 87
- 238000000205 computational method Methods 0.000 title claims abstract description 23
- 239000000571 coke Substances 0.000 claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 238000004939 coking Methods 0.000 claims abstract description 3
- 238000001514 detection method Methods 0.000 claims description 28
- 238000004364 calculation method Methods 0.000 claims description 11
- 230000017525 heat dissipation Effects 0.000 claims description 6
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000013618 particulate matter Substances 0.000 claims description 4
- 229910001385 heavy metal Inorganic materials 0.000 claims description 3
- 230000005855 radiation Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241001062472 Stokellia anisodon Species 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06Q—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
- G06Q50/00—Information and communication technology [ICT] specially adapted for implementation of business processes of specific business sectors, e.g. utilities or tourism
- G06Q50/04—Manufacturing
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F22/00—Methods or apparatus for measuring volume of fluids or fluent solid material, not otherwise provided for
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
- Y02P90/30—Computing systems specially adapted for manufacturing
Landscapes
- Engineering & Computer Science (AREA)
- General Physics & Mathematics (AREA)
- Business, Economics & Management (AREA)
- Physics & Mathematics (AREA)
- Primary Health Care (AREA)
- General Health & Medical Sciences (AREA)
- Human Resources & Organizations (AREA)
- Marketing (AREA)
- Economics (AREA)
- Strategic Management (AREA)
- Tourism & Hospitality (AREA)
- Health & Medical Sciences (AREA)
- General Business, Economics & Management (AREA)
- Manufacturing & Machinery (AREA)
- Theoretical Computer Science (AREA)
- Fluid Mechanics (AREA)
- Coke Industry (AREA)
Abstract
The invention discloses a kind of computational methods and system of pollutant uncontrollable discharge amount, and in coking industry enterprise production process, coke oven is discharged pollutants in the form of inorganization, and the computational methods specifically include：The temperature of the outer surface of the coke oven and the temperature of external environment are detected, obtains surface temperature TTableWith environment temperature TRing；Calculate the area S of the top surface of the coke oven and perimeter P；Detect the amorphous concentration C of the pollutant in external environmentIt is dirty；According to the surface temperature TTable, the environment temperature TRing, the area S and perimeter P calculate and add the thermogenetic pollutant amorphous volume V the coke oven each secondIt is dirty；According to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the amorphous discharge capacity Q of the pollutantIt is dirty.By detecting the amorphous concentration C of the pollutant in external environmentIt is dirty, the amorphous discharge capacity Q of pollutant is calculatedIt is dirty, realize the accurate calculating of pollutant uncontrollable discharge amount.
Description
Technical field
Pollutant discharge amount field in being produced the present invention relates to coking industry, more particularly to a kind of pollutant inorganization
The computational methods and system of discharge capacity.
Background technology
The amorphous discharge capacity of pollutant is being calculated using material balance method in the prior art, need to accurately measure input coefficient
Material total amount, the material total amount that is lost in the product of system output and the total amount of byproduct, system, by by input coefficient
Material total amount subtracts the material total amount being lost in the total amount and system of the product of system output, byproduct and draws inorganization in system
The total amount of the substance of form discharge.Since the proportion that uncontrollable discharge amount accounts in material total amount is very small, discharge characteristics is unknown
Really, the resultant error obtained by the method for counting and calculating is larger, and the result for causing pollutant uncontrollable discharge amount is inaccurate,
Error is larger.
The content of the invention
The object of the present invention is to provide a kind of pollutants of the accuracy for the result of calculation that can improve uncontrollable discharge amount
The computational methods and system of uncontrollable discharge amount.
To achieve the above object, the present invention provides following schemes：
A kind of computational methods of pollutant uncontrollable discharge amount, during metal smelt, coke oven discharges pollutants
Inorganization, the computational methods specifically include：
The temperature of the outer surface of the coke oven and the temperature of external environment are detected, obtains surface temperature TTableAnd environment temperature
TRing；
Calculate the area S of the top surface of the coke oven and perimeter P；
Detect the amorphous concentration C of the pollutant in external environmentIt is dirty；
According to the surface temperature TTable, the environment temperature TRing, the area S and the perimeter P calculate the coke oven
Add the thermogenetic pollutant amorphous volume V each secondsIt is dirty；
According to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the pollutant
Amorphous discharge capacity QIt is dirty。
Optionally, the amorphous concentration C of the pollutant in the detection external environmentIt is dirtyIt specifically includes：
One detection faces is set at 0.5 meter of the top surface higher than the coke oven, and the size and shape of the detection faces is equal
It is identical with the top surface；
The n amorphous test points of pollutant are uniformly arranged in the detection faces, wherein n represents the test point
Number, n=3,4,5 ...；
The detection amorphous concentration of pollutant is respectively C at the position of the n test points1、C2......Cn；
The amorphous concentration of pollutant
Optionally, described be uniformly arranged specifically includes：Straight uniform layout or diagonal uniform layout or symmetric configuration.
Optionally, it is described according to the surface temperature TTable, the environment temperature TRing, the area S and the perimeter P calculate
Add the thermogenetic pollutant amorphous volume V the coke oven each secondsIt is dirtyIt specifically includes：
According to the surface temperature TTable, the environment temperature TRing, calculate qualitative temperature
According to the area S and the perimeter P, characteristic length is calculated
According to the qualitative temperature TIt is fixedDetermine the pollutant inorganization in the qualitative temperature TIt is fixedUnder thermal conductivity factor λ,
Dynamic viscosity μ, kinematic viscosity υ, planck number Pr；
Grashof number
Nusselt number
Heat transfer coefficient
Heat dissipation capacity φ caused by convection currentIt is right=Sh (TTable-TRing)；
Radiation-induced heat dissipation capacity φSpoke=S ε σ (TTable 4-TRing 4), wherein, ε represents the amorphous transmitting of pollutant
Rate, σ=5.67W/ (m2·k4)；
Add the thermogenetic pollutant amorphous volume the coke oven each second
Wherein, c represents the amorphous specific heat capacity of pollutant, and ρ represents the dirt
Contaminate the amorphous density of object.
Optionally, it is described according to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyIt calculates
The amorphous discharge capacity Q of pollutantIt is dirtyIt specifically includes：
The amorphous discharge capacity Q of pollutantIt is dirty=VIt is dirty×CIt is dirty× 60 seconds.
Optionally, the pollutant inorganization specifically includes：At least one in particulate matter, heavy metal and gaseous pollutant
Person.
Optionally, the concentration C of the gaseous pollutantDirty gas=CIt is dirty× A, wherein A are represented in the qualitative temperature TIt is fixedUnder institute
State the conversion ratio of gaseous pollutant.To achieve these goals, the invention also discloses a kind of pollutant uncontrollable discharge amounts
Computing system, the computing system specifically include：
Temperature acquisition module for detecting the temperature of the temperature of the outer surface of the coke oven and external environment, obtains table
Face temperature TTableWith environment temperature TRing；
Area and circumference calculating module, for calculating the area S of the top surface of the coke oven and perimeter P；
Concentration detection module, for detecting the amorphous concentration C of the pollutant in external environmentIt is dirty；
Volume calculation module is connected with the area and circumference calculating module and the temperature acquisition module, is used for respectively
According to the surface temperature TTable, the environment temperature TRing, the area S and perimeter P calculate the heating coke oven each second production
The amorphous volume V of the raw pollutantIt is dirty；
Emission amount calculation module is connected respectively with the concentration detection module and the volume calculation module, for basis
The amorphous volume V of pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the amorphous discharge of the pollutant
Measure QIt is dirty。
The specific embodiment provided according to the present invention, the invention discloses following technique effects：The invention discloses one kind
The computational methods and system of pollutant uncontrollable discharge amount, by detecting the amorphous concentration of the pollutant in external environment
CIt is dirty, and according to the surface temperature TTable, the environment temperature TRing, that the area S and the perimeter P calculate the coke oven is per second
Clock adds the amorphous volume V of the thermogenetic pollutantIt is dirty, finally draw the amorphous discharge capacity Q of pollutantIt is dirty, realize nothing
Organize the accurate calculating of discharge capacity.
Above-mentioned computational methods can realize accurate calculating to the material of each batch or the total amount of product.
Description of the drawings
It in order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to institute in embodiment
Attached drawing to be used is needed to be briefly described, it should be apparent that, the accompanying drawings in the following description is only some implementations of the present invention
Example, for those of ordinary skill in the art, without having to pay creative labor, can also be according to these attached drawings
Obtain other attached drawings.
Fig. 1 is a kind of flow chart of the computational methods of pollutant uncontrollable discharge amount of the present invention；
Fig. 2 is the schematic diagram that the n amorphous test points of pollutant are uniformly arranged in the detection faces；
Fig. 3 is a kind of structure diagram of the computing system of pollutant uncontrollable discharge amount of the present invention.
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, instead of all the embodiments.Based on this
Embodiment in invention, the every other reality that those of ordinary skill in the art are obtained without making creative work
Example is applied, belongs to the scope of protection of the invention.
The object of the present invention is to provide a kind of pollutants of the accuracy for the result of calculation that can improve uncontrollable discharge amount
The computational methods and system of uncontrollable discharge amount.
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, it is below in conjunction with the accompanying drawings and specific real
Applying mode, the present invention is described in further detail.
Fig. 1 is a kind of flow chart of the computational methods of pollutant uncontrollable discharge amount of the present invention, as shown in Figure 1, of the invention
A kind of computational methods of the pollutant uncontrollable discharge amount provided, during metal smelt, coke oven discharges pollutants nothing
Tissue, the computational methods specifically include：
Step 100：The temperature of the outer surface of the coke oven and the temperature of external environment are detected, obtains surface temperature TTableWith
Environment temperature TRing；
Step 200：Calculate the area S of the top surface of the coke oven and perimeter P；
Step 300：Detect the amorphous concentration C of the pollutant in external environmentIt is dirty；
Step 400：According to the surface temperature TTable, the environment temperature TRing, the area S and the perimeter P calculate institute
It states coke oven and adds the thermogenetic pollutant amorphous volume V each secondIt is dirty；
Step 500：According to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate institute
State the amorphous discharge capacity Q of pollutantIt is dirty。
Step 300：The amorphous concentration C of the pollutant in the detection external environmentIt is dirtyIt specifically includes：
One detection faces is set at 0.5 meter of the top surface higher than the coke oven, and the size and shape of the detection faces is equal
It is identical with the top surface；
The n amorphous test points of pollutant are uniformly arranged in the detection faces, wherein n represents the test point
Number, n=3,4,5 ...；
The detection amorphous concentration of pollutant is respectively C at the position of the n test points1、C2......Cn；
The amorphous concentration of pollutant
As shown in Fig. 2, 3 amorphous test points of pollutant are uniformly arranged in the detection faces, it is described uniform
Setting specifically includes：Straight uniform layout or diagonal uniform layout or symmetric configuration, as shown in Fig. 2-1, the straight uniform cloth
Office, linear distribution of shapes set a test point 8, test point 9 and test point in the center position of the detection faces 7
10 is equal with the distance of the test point 8, and the test point 8, test point 9 and test point 10 are in a straight line, described straight
Line is parallel to the long side of the detection faces.
As shown in Fig. 2-2, the diagonal layout, in cornerwise distribution of shapes, in the center position of the detection faces 7
One test point 8 is set, and test point 9 and test point 10 are equal with the distance of the test point 8, the test point 9 and test point
10 are arranged on the diagonal of the detection faces.
As Figure 2-3, in the shape that the symmetric configuration, the test point 8, test point 9 and test point 10 form
The position of heart point is the center position of the detection faces.
Step 400：It is described according to the surface temperature TTable, the environment temperature TRing, the area S and perimeter P calculate institute
It states coke oven and adds the thermogenetic pollutant amorphous volume V each secondIt is dirtyIt specifically includes：
According to the surface temperature TTable, the environment temperature TRingCalculate qualitative temperature
Characteristic length is calculated according to the area S and perimeter P
According to the qualitative temperature TIt is fixedThe pollutant inorganization can be obtained by looking into dry air thermophysical property table under atmospheric pressure
In the qualitative temperature TIt is fixedUnder thermal conductivity factor λ, dynamic viscosity μ, kinematic viscosity υ, planck number Pr；
Grashof number
Nusselt number
Heat transfer coefficient
Heat dissipation capacity φ caused by convection currentIt is right=Sh (TTable-TRing),
Radiation-induced heat dissipation capacity φSpoke=S ε σ (TTable 4-TRing 4), wherein, ε represents the amorphous transmitting of pollutant
Rate, σ=5.67W/ (m2·k4)；
Add the thermogenetic pollutant amorphous volume the coke oven each second
Wherein, c represents the amorphous specific heat capacity of pollutant, and ρ represents the dirt
Contaminate the amorphous density of object.
Step 500：It is described according to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyMeter
Calculate the amorphous discharge capacity Q of the pollutantIt is dirtyIt specifically includes：
The amorphous discharge capacity Q of pollutantIt is dirty=VIt is dirty×CIt is dirty× 60 seconds.
Optionally, the pollutant inorganization specifically includes：At least one in particulate matter, heavy metal and gaseous pollutant
Person, the scope of the diameter of the particulate matter is 1-75 microns.
Optionally, the concentration C of the gaseous pollutantDirty gas=CIt is dirty× A, wherein A are represented in the qualitative temperature TIt is fixedUnder institute
The conversion ratio of gaseous pollutant is stated, the gaseous pollutant includes hydrogen sulfide, sulfur dioxide, nitrogen oxides, carbon dioxide, volatilization
Property organic pollution, benzene homologues, since gaseous pollutant has different conversion ratios under different temperature environments.
To achieve these goals, it is described the present invention also provides a kind of computing system of pollutant uncontrollable discharge amount
Computing system specifically includes：
As shown in figure 3, temperature acquisition module 1, for detecting the temperature of the outer surface of the coke oven and external environment
Temperature obtains surface temperature TTableWith environment temperature TRing；
Area and circumference calculating module 2, for calculating the area S of the top surface of the coke oven and perimeter P；
Concentration detection module 3, for detecting the amorphous concentration C of the pollutant in external environmentIt is dirty；
Volume calculation module 4 is connected respectively with the area and circumference calculating module 2 and the temperature acquisition module 1, is used
According to the surface temperature TTable, the environment temperature TRing, the area S and perimeter P calculate heating coke oven each second
The amorphous volume V of the pollutant generatedIt is dirty；
Emission amount calculation module 5 is connected respectively with the concentration detection module 3 and the volume calculation module 4, for root
According to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the amorphous row of the pollutant
High-volume QIt is dirty。
Each embodiment is described by the way of progressive in this specification, the highlights of each of the examples are with other
The difference of embodiment, just to refer each other for identical similar portion between each embodiment.For system disclosed in embodiment
For, since it is corresponded to the methods disclosed in the examples, so description is fairly simple, related part is said referring to method part
It is bright.
Specific case used herein is set forth the principle of the present invention and embodiment, and above example is said
It is bright to be only intended to help the method and its core concept for understanding the present invention；Meanwhile for those of ordinary skill in the art, foundation
The thought of the present invention, in specific embodiments and applications there will be changes.In conclusion this specification content is not
It is interpreted as limitation of the present invention.
Claims (8)
1. a kind of computational methods of pollutant uncontrollable discharge amount, in coking industry enterprise production process, coke oven discharge is dirty
Contaminate object inorganization, which is characterized in that the computational methods specifically include：
The temperature of the outer surface of the coke oven and the temperature of external environment are detected, obtains surface temperature TTableWith environment temperature TRing；
Calculate the area S of the top surface of the coke oven and perimeter P；
Detect the amorphous concentration C of the pollutant in external environmentIt is dirty；
According to the surface temperature TTable, the environment temperature TRing, that the area S and the perimeter P calculate the coke oven is per second
Clock adds the amorphous volume V of the thermogenetic pollutantIt is dirty；
According to the amorphous volume V of the pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyThe pollutant is calculated without group
The discharge capacity Q knittedIt is dirty。
A kind of 2. computational methods of pollutant uncontrollable discharge amount according to claim 1, which is characterized in that the detection
The amorphous concentration C of the pollutant in external environmentIt is dirtyIt specifically includes：
One detection faces is set at 0.5 meter of the top surface higher than the coke oven, and the size and shape of the detection faces is and institute
It is identical to state top surface；
The n amorphous test points of pollutant are uniformly arranged in the detection faces, wherein n represents of the test point
Number, n=3,4,5 ...；
The detection amorphous concentration of pollutant is respectively C at the position of the n test points1、C2......Cn；
The amorphous concentration of pollutant
3. the computational methods of a kind of pollutant uncontrollable discharge amount according to claim 2, which is characterized in that described uniform
Setting specifically includes：Straight uniform layout or diagonal uniform layout or symmetric configuration.
A kind of 4. computational methods of pollutant uncontrollable discharge amount according to claim 1, which is characterized in that the basis
The surface temperature TTable, the environment temperature TRing, the area S and the perimeter P calculate the heating coke oven each second production
The amorphous volume V of the raw pollutantIt is dirtyIt specifically includes：
According to the surface temperature TTable, the environment temperature TRing, calculate qualitative temperature
According to the area S and the perimeter P, characteristic length is calculated
According to the qualitative temperature TIt is fixedDetermine the pollutant inorganization in the qualitative temperature TIt is fixedUnder thermal conductivity factor λ, power
Viscosity, mu, kinematic viscosity υ, planck number Pr；
Grashof number
Nusselt number
Heat transfer coefficient
Heat dissipation capacity φ caused by convection currentIt is right=Sh (TTable-TRing)；
Radiation-induced heat dissipation capacity φSpoke=S ε σ (TTable 4-TRing 4), wherein, ε represents the amorphous emissivity of pollutant, σ
=5.67W/ (m2·k4)；
Add the thermogenetic pollutant amorphous volume the coke oven each second
Wherein, c represents the amorphous specific heat capacity of pollutant, and ρ represents the pollutant
Amorphous density.
A kind of 5. computational methods of pollutant uncontrollable discharge amount according to claim 1, which is characterized in that the basis
The amorphous volume V of pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the amorphous discharge of the pollutant
Measure QIt is dirtyIt specifically includes：
The amorphous discharge capacity Q of pollutantIt is dirty=VIt is dirty×CIt is dirty× 60 seconds.
A kind of 6. computational methods of pollutant uncontrollable discharge amount according to claim 1, which is characterized in that the pollution
Object inorganization specifically includes：At least one of particulate matter, heavy metal and gaseous pollutant.
A kind of 7. computational methods of pollutant uncontrollable discharge amount according to claim 6, which is characterized in that the gaseous state
The concentration C of pollutantDirty gas=CIt is dirty× A, wherein A are represented in the qualitative temperature TIt is fixedUnder the gaseous pollutant conversion ratio.
8. a kind of computing system of pollutant uncontrollable discharge amount, which is characterized in that the computing system specifically includes：
Temperature acquisition module for detecting the temperature of the temperature of the outer surface of the coke oven and external environment, obtains surface temperature
Spend TTableWith environment temperature TRing；
Area and circumference calculating module, for calculating the area S of the top surface of the coke oven and perimeter P；
Concentration detection module, for detecting the amorphous concentration C of the pollutant in external environmentIt is dirty；
Volume calculation module is connected respectively with the area and circumference calculating module and the temperature acquisition module, for basis
The surface temperature TTable, the environment temperature TRing, the area S and the perimeter P calculate the heating coke oven each second production
The amorphous volume V of the raw pollutantIt is dirty；
Emission amount calculation module is connected respectively with the concentration detection module and the volume calculation module, for according to
The amorphous volume V of pollutantIt is dirtyWith the amorphous concentration C of the pollutantIt is dirtyCalculate the amorphous discharge capacity Q of the pollutantIt is dirty。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711292874.9A CN108053330B (en) | 2017-12-08 | 2017-12-08 | Method and system for calculating unorganized emission of pollutants |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711292874.9A CN108053330B (en) | 2017-12-08 | 2017-12-08 | Method and system for calculating unorganized emission of pollutants |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108053330A true CN108053330A (en) | 2018-05-18 |
| CN108053330B CN108053330B (en) | 2020-10-27 |
Family
ID=62122896
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711292874.9A Active CN108053330B (en) | 2017-12-08 | 2017-12-08 | Method and system for calculating unorganized emission of pollutants |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108053330B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110645481A (en) * | 2018-06-27 | 2020-01-03 | 广州发展集团股份有限公司 | Danger control method for gas pipeline leakage |
| CN111521754A (en) * | 2020-04-22 | 2020-08-11 | 中国科学院地理科学与资源研究所 | Preliminary investigation and stationing method for soil pollution in coking enterprise site |
| CN112034800A (en) * | 2020-08-30 | 2020-12-04 | 上海市环境科学研究院 | Method, system, medium and terminal for calculating unorganized emission of volatile organic pollutants |
| CN112241800A (en) * | 2019-07-16 | 2021-01-19 | 宝山钢铁股份有限公司 | Method for calculating VOCs pollutant emission of coke oven |
| CN115392623A (en) * | 2022-06-27 | 2022-11-25 | 河南鑫安利安全科技股份有限公司 | Enterprise safety production hidden danger investigation system |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20070255515A1 (en) * | 2006-05-01 | 2007-11-01 | Hansa Consult Of North America, Llc | Methods, systems, and computer program products for automatically detecting leaks in a type III hydrant fuel piping system |
| CN101586918A (en) * | 2009-06-24 | 2009-11-25 | 哈尔滨金鑫电气有限责任公司 | The multi-stage waste heat recovery device of industrial furnace high-temperature flue gas |
| CN102003985A (en) * | 2009-08-31 | 2011-04-06 | 宝山钢铁股份有限公司 | Method for measuring inorganization discharge amount of dust in stock ground |
| CN103697946A (en) * | 2013-12-05 | 2014-04-02 | 贵州电网公司电力调度控制中心 | Method for calculating flue gas flow of coal-fired boiler in heat-engine plant and method for controlling pollutant discharge amount |
| US20140196534A1 (en) * | 2003-09-25 | 2014-07-17 | Deka Products Limited Partnership | Metering System and Method for Aerosol Delivery |
| CN103954322A (en) * | 2014-05-09 | 2014-07-30 | 中国石油化工股份有限公司 | Oil gas emission testing system of oil storage tank |
| CN106198881A (en) * | 2016-07-26 | 2016-12-07 | 中冶长天国际工程有限责任公司 | A kind of ignition furnace furnace roof CO detection device and detection method |
| CN106841087A (en) * | 2017-04-17 | 2017-06-13 | 中国石油化工股份有限公司 | Petrochemical enterprise uncontrollable discharge source VOCS discharges method for measuring and calculating |
| CN106932543A (en) * | 2017-04-27 | 2017-07-07 | 广西科技大学鹿山学院 | Thermal power plant's environment flue gas monitoring early warning system |
-
2017
- 2017-12-08 CN CN201711292874.9A patent/CN108053330B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140196534A1 (en) * | 2003-09-25 | 2014-07-17 | Deka Products Limited Partnership | Metering System and Method for Aerosol Delivery |
| US20070255515A1 (en) * | 2006-05-01 | 2007-11-01 | Hansa Consult Of North America, Llc | Methods, systems, and computer program products for automatically detecting leaks in a type III hydrant fuel piping system |
| CN101586918A (en) * | 2009-06-24 | 2009-11-25 | 哈尔滨金鑫电气有限责任公司 | The multi-stage waste heat recovery device of industrial furnace high-temperature flue gas |
| CN102003985A (en) * | 2009-08-31 | 2011-04-06 | 宝山钢铁股份有限公司 | Method for measuring inorganization discharge amount of dust in stock ground |
| CN103697946A (en) * | 2013-12-05 | 2014-04-02 | 贵州电网公司电力调度控制中心 | Method for calculating flue gas flow of coal-fired boiler in heat-engine plant and method for controlling pollutant discharge amount |
| CN103954322A (en) * | 2014-05-09 | 2014-07-30 | 中国石油化工股份有限公司 | Oil gas emission testing system of oil storage tank |
| CN106198881A (en) * | 2016-07-26 | 2016-12-07 | 中冶长天国际工程有限责任公司 | A kind of ignition furnace furnace roof CO detection device and detection method |
| CN106841087A (en) * | 2017-04-17 | 2017-06-13 | 中国石油化工股份有限公司 | Petrochemical enterprise uncontrollable discharge source VOCS discharges method for measuring and calculating |
| CN106932543A (en) * | 2017-04-27 | 2017-07-07 | 广西科技大学鹿山学院 | Thermal power plant's environment flue gas monitoring early warning system |
Non-Patent Citations (2)
| Title |
|---|
| 江梅 等: ""我国挥发性有机物定义和控制指标的探讨"", 《环境科学》 * |
| 钱惠国 等: ""热加工车间热污染回收能力分析"", 《环境工程学报》 * |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110645481A (en) * | 2018-06-27 | 2020-01-03 | 广州发展集团股份有限公司 | Danger control method for gas pipeline leakage |
| CN112241800A (en) * | 2019-07-16 | 2021-01-19 | 宝山钢铁股份有限公司 | Method for calculating VOCs pollutant emission of coke oven |
| CN112241800B (en) * | 2019-07-16 | 2022-10-21 | 宝山钢铁股份有限公司 | Method for calculating VOCs pollutant emission amount of coke oven |
| CN111521754A (en) * | 2020-04-22 | 2020-08-11 | 中国科学院地理科学与资源研究所 | Preliminary investigation and stationing method for soil pollution in coking enterprise site |
| CN111521754B (en) * | 2020-04-22 | 2021-04-13 | 中国科学院地理科学与资源研究所 | Preliminary investigation and stationing method for soil pollution in coking enterprise site |
| CN112034800A (en) * | 2020-08-30 | 2020-12-04 | 上海市环境科学研究院 | Method, system, medium and terminal for calculating unorganized emission of volatile organic pollutants |
| CN115392623A (en) * | 2022-06-27 | 2022-11-25 | 河南鑫安利安全科技股份有限公司 | Enterprise safety production hidden danger investigation system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108053330B (en) | 2020-10-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108053330A (en) | A kind of computational methods and system of pollutant uncontrollable discharge amount | |
| CN103792253B (en) | The measuring method of one-dimensional material thermal contact resistance | |
| CN102288641A (en) | Method for measuring high temperature thermal conductivity coefficient | |
| CN104237298A (en) | Method for testing shrinkage rate of electronic flat glass | |
| CN108226219B (en) | Method for detecting heat generation uniformity of film resistor | |
| CN109752113A (en) | Location determining method and circuit design method in web temperature sensor and its application | |
| Wu et al. | Flexible and anisotropic strain sensors based on highly aligned carbon fiber membrane for exercise monitoring | |
| CN103940845A (en) | Measuring method for thermal conductivity of metal at high temperature | |
| Järvinen et al. | Extending the Faraday cup aerosol electrometer based calibration method up to 5 µm | |
| CN105021650B (en) | A kind of Guarded hot plate heat conductivity measuring device | |
| Cui et al. | Design and fabrication of a thermopile-based thin film heat flux sensor, using a lead—substrate integration method | |
| CN107309515A (en) | A kind of high temperature chain-conveyer furnace brazing temperature evaluating method for curve | |
| Zou et al. | A thermal conductivity sensor based on mixed carbon material modification for hydrogen detection | |
| WO2016128000A1 (en) | A method of directly determining the water balance in fuel cells | |
| CN106679848B (en) | A method of utilizing ordinary temp sensor quick temperature measurement | |
| CN110567606B (en) | Noise thermometer and method for measuring temperature | |
| CN103267775A (en) | Micro-nano-scale material seebeck coefficient online measurement method | |
| CN106248259A (en) | A kind of system corrects the dynamic temperature measurement method of hot thermocouple inertial drift | |
| CN1339667A (en) | Method and device for detecting boiler heat efficiency | |
| CN104897306B (en) | Transient radiation heat-flow measurement method based on circle paper tinsel heat-flow meter | |
| CN105785102B (en) | Thermoelectrical potential measuring circuit, platform and the method for minute yardstick sample | |
| Berning et al. | Applying hot wire anemometry to directly measure the water balance in a proton exchange membrane fuel cell–Part 1: Theory | |
| CN103529073B (en) | A kind of asymmetric hot plate instrument | |
| Fu et al. | Simultaneous measurements of high-temperature total hemispherical emissivity and thermal conductivity using a steady-state calorimetric technique | |
| CN207232257U (en) | A kind of alternating temperature four-point probe measurment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Lingna Inventor after: Ma Zhaokun Inventor before: Ma Zhaokun Inventor before: Li Lingna |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240220 Address after: No. 506 Liantong Road, Zhoucun District, Zibo City, Shandong Province, 255020 Patentee after: Li Lingna Country or region after: China Address before: Room 0805, 8th Floor, Huaxia International, No. 137 Gourmet Street, Zhangdian District, Zibo City, Shandong Province, 255000 Patentee before: SHANDONG PAITEFEI ENVIRONMENTAL TECHNOLOGY Co.,Ltd. Country or region before: China |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240326 Address after: No. 506, Liantong Road, Zhoucun District, Zibo City, Shandong Province Patentee after: ZIBO VOCATIONAL INSTITUTE Country or region after: China Address before: No. 506 Liantong Road, Zhoucun District, Zibo City, Shandong Province, 255020 Patentee before: Li Lingna Country or region before: China |