CN204536317U - A kind of biomass gasification furnace gas humidity on-line measurement system - Google Patents
A kind of biomass gasification furnace gas humidity on-line measurement system Download PDFInfo
- Publication number
- CN204536317U CN204536317U CN201520262754.4U CN201520262754U CN204536317U CN 204536317 U CN204536317 U CN 204536317U CN 201520262754 U CN201520262754 U CN 201520262754U CN 204536317 U CN204536317 U CN 204536317U
- Authority
- CN
- China
- Prior art keywords
- gas
- temperature
- fuel gas
- dry
- temperature fuel
- 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.)
- Active
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 17
- 238000002309 gasification Methods 0.000 title claims abstract description 11
- 238000005259 measurement Methods 0.000 title claims abstract description 11
- 239000002737 fuel gas Substances 0.000 claims abstract description 65
- 239000007789 gas Substances 0.000 claims abstract description 42
- 239000000567 combustion gas Substances 0.000 claims abstract description 27
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
Abstract
The utility model provides a kind of biomass gasification furnace gas humidity on-line measurement system, comprise combustion gas stopple coupon, high temperature rise pressure fan, high-temperature fuel gas flowmeter, high-temperature fuel gas temperature detector, high-temperature fuel gas pressure detector, gas cooler, dry gas meter, dry fuel gas temperature detecting device, dry gaseous-pressure detecting device, PLC, combustion gas stopple coupon and the female pipe of high-temperature fuel gas are connected in parallel, combustion gas stopple coupon is provided with high temperature rise pressure fan along inlet end successively to outlet side, gas cooler, pipeline between inlet end to gas cooler is provided with the high-temperature fuel gas flow be connected with PLC, high-temperature fuel gas temperature detector and high-temperature fuel gas pressure detector, pipeline between gas cooler to outlet side is provided with the dry gas meter be connected with PLC, dry fuel gas temperature detecting device, dry gaseous-pressure detecting device.The utility model can realize biomass high-temperature combustion gas humidity real time on-line monitoring.
Description
Technical field
The utility model relates to biomass energy and utilizes technical field, specifically a kind of biomass gasification furnace gas humidity on-line measurement system.
Background technology
Gasification of biomass high-temperature fuel gas contains a large amount of as reducing gas compositions such as CO relative to common flue gas, unavailable by the method for oxygen determination humidity.Simultaneously because fuel gas temperature is higher, humidity cannot be analyzed by measuring conductance.
Summary of the invention
The utility model provides a kind of biomass gasification furnace gas humidity on-line measurement system, can the humidity of real time on-line monitoring biomass high-temperature combustion gas.
A kind of biomass gasification furnace gas humidity on-line measurement system, comprise combustion gas stopple coupon, high temperature rise pressure fan, high-temperature fuel gas flowmeter, high-temperature fuel gas temperature detector, high-temperature fuel gas pressure detector, gas cooler, dry gas meter, dry fuel gas temperature detecting device, dry gaseous-pressure detecting device, PLC, described combustion gas stopple coupon and the female pipe of high-temperature fuel gas are connected in parallel, described combustion gas stopple coupon is provided with high temperature rise pressure fan along inlet end successively to outlet side, gas cooler, pipeline between inlet end to gas cooler is provided with the high-temperature fuel gas flow be connected with PLC, high-temperature fuel gas temperature detector and high-temperature fuel gas pressure detector, pipeline between gas cooler to outlet side is provided with the dry gas meter be connected with PLC, dry fuel gas temperature detecting device, dry gaseous-pressure detecting device.
The utility model uses different flow score Ce Ding the standard state flow of high-temperature fuel gas and cooled dry combustion gas, compares the scheme calculating humidity afterwards, achieves biomass high-temperature combustion gas humidity real time on-line monitoring.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model biomass gasification furnace gas humidity on-line measurement system.
In figure: 1-high-temperature fuel gas mother pipe, 2-combustion gas stopple coupon, 3-high temperature rise pressure fan, 4-high-temperature fuel gas flowmeter, 5-high-temperature fuel gas temperature detector, 6-high-temperature fuel gas pressure detector, 7-gas cooler, 8-dry gas meter, 9-dry fuel gas temperature detecting device, 10-dry gaseous-pressure detecting device, 11-PLC.
Embodiment
Below in conjunction with the accompanying drawing in the utility model, the technical scheme in the utility model is clearly and completely described.
Figure 1 shows that the structural representation of the utility model biomass gasification furnace gas humidity on-line measurement system, described biomass gasification furnace gas humidity on-line measurement system comprises combustion gas stopple coupon 2, high temperature rise pressure fan 3, high-temperature fuel gas flowmeter 4, high-temperature fuel gas temperature detector 5, high-temperature fuel gas pressure detector 6, gas cooler 7, dry gas meter 8, dry fuel gas temperature detecting device 9, dry gaseous-pressure detecting device 10, PLC 11.
Described combustion gas stopple coupon 2 is connected in parallel with the female pipe 1 of high-temperature fuel gas, and namely the inlet end of described combustion gas stopple coupon 2 accesses high-temperature fuel gas from the female pipe 1 of high-temperature fuel gas, and high-temperature fuel gas is recycled to the female pipe 1 of high-temperature fuel gas by outlet side.Described combustion gas stopple coupon 2 is provided with high temperature rise pressure fan 3 along inlet end successively to outlet side, gas cooler 7, pipeline between inlet end to gas cooler 7 is provided with high-temperature fuel gas flow 4, high-temperature fuel gas temperature detector 5 and high-temperature fuel gas pressure detector 6, pipeline between gas cooler 7 to outlet side is provided with dry gas meter 8, dry fuel gas temperature detecting device 9, dry gaseous-pressure detecting device 10, high-temperature fuel gas flow 4, high-temperature fuel gas temperature detector 5, high-temperature fuel gas pressure detector, dry gas meter 8, dry fuel gas temperature detecting device 9, dry gaseous-pressure detecting device 10 is all connected with PLC 11.
Principle of work of the present utility model:
From the female pipe 1 of high-temperature fuel gas, enter combustion gas stopple coupon 2 by high temperature rise pressure fan 3 extraction section high-temperature fuel gas sample gas, combustion gas is successively by returning the female pipe 1 of high-temperature fuel gas after high-temperature fuel gas flowmeter 4, gas cooler 7, dry gas meter 8.High-temperature fuel gas flowmeter 4 records flow value and sends into PLC 11, and the temperature and pressure correction then recorded through high-temperature fuel gas temperature detector 5 and high-temperature fuel gas pressure detector 6 calculates its standard state flow; High-temperature fuel gas is cooled to after below 50 DEG C through gas cooler 7, contained moisture condenses precipitation naturally, form dry combustion gas, the flow value that dry gas meter 8 is measured sends into PLC 11, the temperature and pressure correction recorded through dry fuel gas temperature detecting device 9, dry gaseous-pressure detecting device 10 calculates the standard state flow of dry combustion gas, high-temperature fuel gas standard state flow is deducted the result of dry combustion gas standard state flow divided by high-temperature fuel gas standard state flow by PLC 11, can obtain combustion gas humidity.
The utility model uses different flow score Ce Ding the standard state flow of high-temperature fuel gas and cooled dry combustion gas, compare the scheme calculating humidity afterwards, achieve biomass high-temperature combustion gas humidity real time on-line monitoring, according to on-the-spot actual arrangement situation, the on-line measurement system of biomass gasifying furnace high-temperature fuel gas humidity can be installed at the applicable position of the female pipe of combustion gas.
The above; be only embodiment of the present utility model; but protection domain of the present utility model is not limited thereto; anyly belong to those skilled in the art in the technical scope that the utility model discloses; the change that can expect easily or replacement, all should be encompassed within protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claim.
Claims (1)
1. a biomass gasification furnace gas humidity on-line measurement system, is characterized in that: comprise combustion gas stopple coupon (2), high temperature rise pressure fan (3), high-temperature fuel gas flowmeter (4), high-temperature fuel gas temperature detector (5), high-temperature fuel gas pressure detector (6), gas cooler (7), dry gas meter (8), dry fuel gas temperature detecting device (9), dry gaseous-pressure detecting device (10), PLC (11), described combustion gas stopple coupon (10) is managed (1) with high-temperature fuel gas mother and is connected in parallel, and described combustion gas stopple coupon (2) is provided with high temperature rise pressure fan (3) successively along inlet end to outlet side, gas cooler (7), the pipeline between inlet end to gas cooler (7) is provided with the high-temperature fuel gas flow (4) be connected with PLC (11), high-temperature fuel gas temperature detector (5) and high-temperature fuel gas pressure detector (6), the pipeline between gas cooler (7) to outlet side is provided with the dry gas meter (8) be connected with PLC (11), dry fuel gas temperature detecting device (9), dry gaseous-pressure detecting device (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520262754.4U CN204536317U (en) | 2015-04-27 | 2015-04-27 | A kind of biomass gasification furnace gas humidity on-line measurement system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520262754.4U CN204536317U (en) | 2015-04-27 | 2015-04-27 | A kind of biomass gasification furnace gas humidity on-line measurement system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204536317U true CN204536317U (en) | 2015-08-05 |
Family
ID=53750303
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520262754.4U Active CN204536317U (en) | 2015-04-27 | 2015-04-27 | A kind of biomass gasification furnace gas humidity on-line measurement system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204536317U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057749A (en) * | 2016-08-04 | 2017-08-18 | 石化盈科信息技术有限责任公司 | The online soft sensor system and measuring method of gasoline stabilizer separation accuracy |
| CN110108595A (en) * | 2019-04-15 | 2019-08-09 | 中国辐射防护研究院 | A kind of gas-vapour mixing method humidity detection device |
-
2015
- 2015-04-27 CN CN201520262754.4U patent/CN204536317U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057749A (en) * | 2016-08-04 | 2017-08-18 | 石化盈科信息技术有限责任公司 | The online soft sensor system and measuring method of gasoline stabilizer separation accuracy |
| CN107057749B (en) * | 2016-08-04 | 2018-12-07 | 石化盈科信息技术有限责任公司 | The online soft sensor system and measurement method of gasoline stabilizer separation accuracy |
| CN110108595A (en) * | 2019-04-15 | 2019-08-09 | 中国辐射防护研究院 | A kind of gas-vapour mixing method humidity detection device |
| CN110108595B (en) * | 2019-04-15 | 2021-09-24 | 中国辐射防护研究院 | Humidity monitoring device adopting gas-steam mixing method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203350238U (en) | Humidity monitor | |
| CN103646176A (en) | Comprehensive calculation method for energy-saving effect after steam turbine steam seal modification | |
| CN202033058U (en) | Real-time measuring device for air supply flow of boiler | |
| CN102156065A (en) | Gas analytical system | |
| CN204536317U (en) | A kind of biomass gasification furnace gas humidity on-line measurement system | |
| CN102967491B (en) | Particle sampling device and utilize this device to carry out the method for particle detection | |
| CN102288459A (en) | On-line analytical system for garbage incineration flue gas | |
| CN101561426B (en) | Humidity measuring method and measuring device used for CEMS system | |
| CN202853655U (en) | Flue gas monitoring system | |
| CN201892654U (en) | On-line shutdown corrosion detection device for heating power equipment | |
| CN102997967A (en) | Blowing flow real time measuring device and method for pipeline with rectangular section | |
| CN108332975B (en) | 1.5-stage turbine rotating disc cavity flow heat transfer foundation test bed | |
| CN103499371A (en) | Method for measuring flow of air leaked into condenser and vacuum system | |
| CN202974350U (en) | Air supply flow real-time detection device for rectangular section pipeline | |
| CN203053778U (en) | Device for detecting leakage of waste heat recovery heat exchanger | |
| WO2021174785A1 (en) | Method for monitoring effect of ammonia escape from denitration on downstream rotary air preheater | |
| CN204422280U (en) | A kind of sampling probe for hot and humid many cloud of dust gas | |
| CN204241032U (en) | A kind of stationary combustion source greenhouse gas emission on-line monitoring system | |
| CN201413262Y (en) | Humidity measurement device used for CEMS system | |
| CN104458149B (en) | Air preheater air leakage calculation method | |
| CN105466645A (en) | System and method for quickly detecting air leakage factor of boiler tail flue | |
| CN204649662U (en) | A kind of acid dew point instrument detection probe dust prevention system | |
| CN209342489U (en) | A kind of flue gas desulfurization pretreatment unit | |
| CN209432735U (en) | A kind of online water analysis system | |
| CN204421994U (en) | A kind of engine consumption test gas-oil separation and exhaust apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Hangzhou Juneng Boiler Co., Ltd. Assignor: GUODIAN CHANGYUAN HUBEI BIOMASS GASIFICATION TECHNOLOGY CO., LTD. Contract record no.: 2016420000008 Denomination of utility model: Biomass gasification stove gas humidity on line measurement system Granted publication date: 20150805 License type: Common License Record date: 20160406 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Guodian Longyuan Environment Protection Engrg. Co., Ltd., Beijing Assignor: GUODIAN CHANGYUAN HUBEI BIOMASS GASIFICATION TECHNOLOGY CO., LTD. Contract record no.: 2017420000021 Denomination of utility model: Biomass gasification stove gas humidity on line measurement system Granted publication date: 20150805 License type: Common License Record date: 20170905 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Wuhan Wu pan Energy Engineering Co., Ltd. Assignor: GUODIAN CHANGYUAN HUBEI BIOMASS GASIFICATION TECHNOLOGY CO., LTD. Contract record no.: 2018420000003 Denomination of utility model: Biomass gasification stove gas humidity on line measurement system Granted publication date: 20150805 License type: Common License Record date: 20180404 |
|
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Harbin Boiler Company Limited Assignor: GUODIAN CHANGYUAN HUBEI BIOMASS GASIFICATION TECHNOLOGY CO., LTD. Contract record no.: 2018420000014 Denomination of utility model: Biomass gasification stove gas humidity on line measurement system Granted publication date: 20150805 License type: Common License Record date: 20180604 |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211028 Address after: 430077 national energy building, No. 63, Xudong street, Hongshan District, Wuhan City, Hubei Province Patentee after: National Energy Group Changyuan Power Co.,Ltd. Address before: 448040 No. 80 Bai Lu Road, Jingmen, Hubei Patentee before: GUODIAN CHANGYUAN HUBEI BIOMASS GASIFICATION TECHNOLOGY Co.,Ltd. |