CN108644789A - A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device - Google Patents
A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device Download PDFInfo
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- CN108644789A CN108644789A CN201810458843.4A CN201810458843A CN108644789A CN 108644789 A CN108644789 A CN 108644789A CN 201810458843 A CN201810458843 A CN 201810458843A CN 108644789 A CN108644789 A CN 108644789A
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- flue
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- decarburization
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- 239000007789 gas Substances 0.000 title claims abstract description 114
- 238000005261 decarburization Methods 0.000 title claims abstract description 28
- 239000003245 coal Substances 0.000 title claims abstract description 23
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 23
- 239000001257 hydrogen Substances 0.000 title claims abstract description 23
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 238000002485 combustion reaction Methods 0.000 claims abstract description 20
- 230000008676 import Effects 0.000 claims abstract description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 31
- 239000003546 flue gas Substances 0.000 claims description 29
- 238000009825 accumulation Methods 0.000 claims description 21
- 239000002918 waste heat Substances 0.000 claims description 17
- 239000011148 porous material Substances 0.000 claims description 15
- 230000009977 dual effect Effects 0.000 claims description 7
- 230000008020 evaporation Effects 0.000 claims description 7
- 238000001704 evaporation Methods 0.000 claims description 7
- 235000019504 cigarettes Nutrition 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 239000011819 refractory material Substances 0.000 claims description 2
- 206010022000 influenza Diseases 0.000 claims 1
- 239000010815 organic waste Substances 0.000 abstract description 11
- 230000007613 environmental effect Effects 0.000 abstract description 7
- 239000012855 volatile organic compound Substances 0.000 abstract description 7
- 238000004134 energy conservation Methods 0.000 abstract description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 8
- 239000003345 natural gas Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000002360 explosive Substances 0.000 description 3
- 239000002737 fuel gas Substances 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 210000000038 chest Anatomy 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
- F23G7/066—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
- F23G7/068—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator using regenerative heat recovery means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2204/00—Supplementary heating arrangements
- F23G2204/10—Supplementary heating arrangements using auxiliary fuel
- F23G2204/103—Supplementary heating arrangements using auxiliary fuel gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/14—Gaseous waste or fumes
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
Abstract
The present invention relates to a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating devices, single unit system uses vertical layout, incinerator adiabatic furnace is connected to insulated combustion chamber, insulated combustion chamber is connected to by first order gas reversal chamber with the first flue, first flue is connected to by second level gas reversal chamber with the second flue, second flue is connected to by third level gas reversal chamber with third flue, the end of third flue and exhaust gas entrance chamber, exhaust gas entrance chamber is equipped with decarburization resolution gas import, low-temperature zone preheater is located in exhaust gas entrance chamber, middle-temperature section preheater is located in the second flue, high temperature section preheater is located in the first flue, high temperature section preheater is connected to incinerator adiabatic furnace, low-temperature zone preheater is additionally provided with exhanst gas outlet.The present invention uses direct combustion processing mode, leads to too small amount of outside resources and ignites, using the available energy of VOCs itself, by thoroughly destroying by fire for volatile organic waste gas, qualified discharge, energy conservation and environmental protection.
Description
Technical field
The invention belongs to volatile organic waste gas incineration technology fields, are related to volatile organic waste gas environmental protection and energy saving burning
Technology, and in particular to arrive a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device.
Background technology
Since economic speedup develops, modern manufacturing industry, which seeks the requirement of hydrogen, increasingly to be increased, and coal hydrogen producing technology is sent out therewith
Exhibition is also very rapid.In recent years since industrial development is rapid, the energy consume excessively and environmental pollution phenomenon cross be it is serious, realize
Energy-saving and emission-reduction are imperative.Coal hydrogen manufacturing decarburization resolution gas is VOCs（Volatile organic gases）, contain H2, N2, CO, CH4Equal gas
Body, fuel gas content is few, which carefully analyzes such gas distinguishing, have it is flammable, have
Energy has calorific value, is unable to the features such as independent burning.If direct emission not only causes atmosphere pollution, environmental disruption, but also wastes
The available energy.The direct incineration technology of decarburization resolution gas does not use generally because of the less feature of its fuel gas content at present,
Have using direct incineration technology instead because of the king-sized feature of gas flow more waste of energy instead, therefore, for organic
The volatile organic waste gas direct fired technology of component content rareness is not yet ripe, and existing processing volatile organic waste gas mostly uses greatly
The technology of mode is burned in RTO accumulation of heats, and RTO accumulation of heats burn mode because of preheating, burning, the switching repeatedly of purge, need to arrange
Gas piping valve it is more, it is difficult to close tight that switching, which causes valve, repeatedly, causes gas easily to reveal, since volatility is organic
The flammable explosive gas such as exhaust gas most hydrogeneous, methane, carbon monoxide, not only environmental protection cannot be up to standard for valve leaks, but also because containing
Flammable explosive gas has quite high danger, while RTO accumulation of heat incineration system takes up a large area, and has larger limitation,
The inflammable and explosive volatile organic waste gas such as hydrogeneous, methane, carbon monoxide should not be promoted the use of.
Invention content
To solve the above-mentioned problems, the present invention provides a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating devices, using straight
Processing mode is fired, the advantages of RTO accumulation of heats are burned has been drawn and volatile organic waste gas is preheated, is heated, it is only logical too small amount of
The available energy that outside resources are ignited and generated using VOCs itself burnings, it is up to standard by thoroughly destroying by fire for organic exhaust gas
Discharge, energy conservation and environmental protection.
In order to achieve the above object, using following technical scheme：A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device, including
Incinerator, waste heat boiler and organic exhaust gas preheater, incinerator include incinerator adiabatic furnace, insulated combustion chamber, waste heat boiler
Including level-one steam-generating bank, dual evaporation tube bank, economizer and boiler drum, organic exhaust gas preheater is by heat-exchanging tube bundle, upper plate
Pipe, lower perforated plate and intermediate bulkhead form and are divided into low-temperature zone preheater, middle-temperature section preheater, high temperature section preheater；Single unit system
Using vertical layout, waste heat boiler is above incinerator, and organic exhaust gas preheater is mounted in waste heat boiler, incinerator heat insulation furnace
It is connected to by the uniform accumulation of heat flower pore wall a of flue gas between thorax and insulated combustion chamber, insulated combustion chamber passes through first order gas reversal chamber
It is connected to the first flue, the first flue is connected to by second level gas reversal chamber with the second flue, and the second flue passes through the third level
Gas reversal chamber is connected to third flue, and the end of third flue is given up also by outer connecting pipe road and exhaust gas entrance chamber
It is connected at the top of gas inlet chamber and the second flue, exhaust gas entrance chamber is equipped with decarburization resolution gas import, and low-temperature zone preheater is located at
In exhaust gas entrance chamber, middle-temperature section preheater is located in the second flue, and high temperature section preheater is located in the first flue, and high temperature section is pre-
Hot device is connected to incinerator adiabatic furnace, and low-temperature zone preheater is additionally provided with exhanst gas outlet.
Further, level-one steam-generating bank, dual evaporation tube bank and economizer are installed from bottom to top in third flue.
Further, the uniform accumulation of heat flower pore wall b of flue gas is equipped between first order gas reversal chamber and the first flue.
Further, incinerator adiabatic furnace, insulated combustion chamber, the first flue, the second flue and third flue, the first order
Gas reversal chamber, second level gas reversal chamber, third level gas reversal chamber and exhaust gas entrance chamber are by insulating refractory
Furnace wall, metal sealing plate and steelframe enclose, and boiler drum is set to the upper steel top of the trellis for enclosing third flue.
Further, incinerator adiabatic furnace installs steady burning burner.
Further, heat-exchanging tube bundle is that screwed pipe is restrained or bellows tube is restrained.
Flue gas moves towards：Coal hydrogen manufacturing decarburization resolution gas enters machine heat economizer from decarburization resolution gas import, and gas is through low temperature
Incinerator adiabatic furnace is entered after section, middle-temperature section, high temperature section preheating, then is ignited by natural gas and generates high-temperature flue gas, high temperature
Then flue gas enters exhaust gas entrance by insulated combustion chamber, the first flue, the second flue, third flue by outer connecting pipe road
Chamber is finally discharged from the exhanst gas outlet of low-temperature zone preheater.Relatively low temperature of the low-temperature zone preheater after residual heat boiler for exchanging heat
Degree flue gas tentatively heats coal hydrogen manufacturing decarburization resolution gas, while further decreasing the temperature of discharge flue gas to reach energy-saving effect, coal
Hydrogen manufacturing decarburization parsing is made leave with rage in heat-exchanging tube bundle, and flue gas is walked outside heat-exchanging tube bundle.Middle-temperature section preheater, high temperature section preheater utilize organic
Exhaust gas direct combustion burns the heat generated and carries out heating coal hydrogen manufacturing decarburization resolution gas, and coal hydrogen manufacturing decarburization resolution gas is made to reach higher temperatures
Degree, may be used a small amount of auxiliary fuel and can reach the poor coal hydrogen manufacturing decarburization resolution gas high temperature of fuel gas and burn.The
High-temperature flue gas in one flue and the second flue persistently can give organic exhaust gas preheater to provide heat, save a large amount of energy.
Advantageous effect of the present invention：
1, VOCs is utilized（Volatile organic waste gas）And the heat that a small amount of combustion of natural gas generates is to VOCs（Volatility organic waste
Gas）Carry out preheating reach a high temperature after ignited by a small amount of natural gas can reach thoroughly destroy by fire, after-flame, reached RTO accumulation of heats and burnt
The pre- thermal incineration burnt is to reduce burning disposal VOCs（Volatile organic waste gas）The advantage of the natural gas consumption needed, eliminates
The hidden danger of valve leaks is burned in RTO accumulation of heats and the disadvantage that environmental protection is difficult up to standard is burned in RTO accumulation of heats, and present apparatus direct combustion firing efficiency can
It is almost the same with RTO accumulation of heat incineration temperatures up to 99.9%, and 850-900 DEG C of incineration temperature, at this temperature in flue gas NOx generation
Amount fully meets national environmental standard requirement, that is, the flue gas discharged requires no denitration process, it is ensured that the fume environment protection of discharge reaches
Mark.
2, by VOCs（Volatile organic waste gas）The waste heat of generation is recycled by waste heat boiler, the steam of generation
It can be used for industrial production, it is energy saving to realize.
3, the high-temperature flue gas generated to organic exhaust gas burning using the uniform accumulation of heat flower pore wall of flue gas is uniformly mixed, it is ensured that
The organic exhaust gas of escape is sufficiently mixed and burns with high-temperature flue gas under the action of flower pore wall.And flower pore wall absorbs burning and generates
High temperature heat to being heated by the exhaust gas of flower pore wall, reach a high temperature and destroy the purpose of organic exhaust gas by fire.
4, waste heat boiler, incinerator and preheater are arranged using vertical, modular structure, greatly save floor space, and subtract
Few field erected workload, simple in structure, easy to operation and maintenance.
Description of the drawings
Fig. 1 is the structural schematic diagram of the present invention；
Fig. 2 is side view of the present invention；
Fig. 3 is the vertical view of the present invention；
Fig. 4 is that flue gas uniform accumulation of heat flower pore wall is staggered in arrangement tracery wall schematic diagram；
Fig. 5 is the in-line arrangement tracery wall schematic diagram of the uniform accumulation of heat flower pore wall of flue gas.
As shown in the figure：1, incinerator adiabatic furnace, 2, insulated combustion chamber, the 3, first flue, the 4, second flue, 5, third cigarette
Road, 6, low-temperature zone preheater, 7, middle-temperature section preheater, 8, high temperature section preheater, 9, first order gas reversal chamber, 10, the second level
Gas reversal chamber, 11, third level gas reversal chamber, 12, exhaust gas entrance chamber, 13, outer connecting pipe road, 14, exhanst gas outlet, 15,
Decarburization resolution gas import, 16, flue gas uniform accumulation of heat flower pore wall a, 17, flue gas uniform accumulation of heat flower pore wall b, 18, level-one steam-generating bank,
19, dual evaporation is restrained, 20, economizer, 21, boiler drum, 22, steady burning burner, 23, upper perforated plate, 24, intermediate bulkhead, 25,
Heat-exchanging tube bundle, 26, lower perforated plate.
Specific implementation mode
Embodiment
Below in conjunction with the accompanying drawings to the present invention to further illustrating；A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device, packet
Include incinerator, waste heat boiler and organic exhaust gas preheater, single unit system uses vertical layout, waste heat boiler above incinerator,
Organic exhaust gas preheater is mounted in waste heat boiler.Incinerator includes incinerator adiabatic furnace（1）And insulated combustion chamber（2）, burn
Burn stove adiabatic furnace（1）Steady burning burner is installed（22）；Waste heat boiler includes level-one steam-generating bank（18）, dual evaporation tube bank
（19）, economizer（21）And boiler drum（22）；Organic exhaust gas preheater is by heat-exchanging tube bundle（25）, upper plate pipe（23）, lower perforated plate
（26）And intermediate bulkhead（24）It forms and is divided into low-temperature zone preheater（6）, middle-temperature section preheater（7）, high temperature section preheater（8）,
Heat-exchanging tube bundle（25）For screwed pipe tube bank or bellows tube tube bank.Incinerator adiabatic furnace（1）And insulated combustion chamber（2）Connection, absolutely
Hot chamber（2）Pass through first order gas reversal chamber（9）With the first flue（3）Connection, the first flue（3）Pass through second level flue gas
Reversal chamber（10）With the second flue（4）Connection, the second flue（4）Pass through third level gas reversal chamber（11）With third flue（5）
Connection, third flue（5）End also pass through outer connecting pipe road（13）With exhaust gas entrance chamber（12）Connection, exhaust gas entrance chamber
（12）With the second flue（4）Top is connected to.Exhaust gas entrance chamber（12）Equipped with decarburization resolution gas import（15）, low-temperature zone preheater
（6）Positioned at exhaust gas entrance chamber（12）It is interior, middle-temperature section preheater（7）Positioned at the second flue（4）It is interior, high temperature section preheater（8）Position
In the first flue（3）It is interior, high temperature section preheater（8）With incinerator adiabatic furnace（1）Connection, low-temperature zone preheater（6）It is additionally provided with
Exhanst gas outlet（14）.Third flue（5）Level-one steam-generating bank is inside installed from bottom to top（18）, dual evaporation tube bank（19）And it saves
Coal device（20）.Incinerator adiabatic furnace（1）And insulated combustion chamber（2）Between be equipped with the uniform accumulation of heat flower pore wall a of flue gas（16）, first
Grade gas reversal chamber（9）With the first flue（3）Between be equipped with the uniform accumulation of heat flower pore wall b of flue gas（17）.Hole is spent in the uniform accumulation of heat of flue gas
Wall a（16）With the uniform accumulation of heat flower pore wall b of flue gas（17）Using thermal storage ceramic in-line arrangement tracery wall or it is staggered in arrangement tracery wall.Incinerator
Adiabatic furnace（1）, insulated combustion chamber（2）, the first flue（3）, the second flue（4）And third flue（5）, first order flue gas turn to
Room（9, second level gas reversal chamber（10）And third level gas reversal chamber（11）And exhaust gas entrance chamber（12）By thermal insulation
Refractory material furnace wall, metal sealing plate and steelframe enclose, boiler drum（21）It is set to and encloses third flue（5）Top
At the top of steelframe.First flue（3）With the second flue（4）It is to force flue gas flow direction according to organic in order to which organic heat economizer is arranged
Heat economizer heat coal hydrogen manufacturing decarburization resolution gas need and be arranged, third flue（5）It is remaining in order to pass through waste heat
Heat boiler absorption forces flue gas flow direction to be arranged according to waste heat boiler structure needs.
Claims (6)
1. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device, including incinerator, waste heat boiler and organic exhaust gas preheater, burn
It includes incinerator adiabatic furnace to burn stove（1）, insulated combustion chamber（2）, waste heat boiler includes level-one steam-generating bank（18）, dual evaporation
Tube bank（19）, economizer（20）And boiler drum（21）, organic exhaust gas preheater is by heat-exchanging tube bundle（25）, upper plate pipe（23）, under
Tube sheet（26）And intermediate bulkhead（24）It forms and is divided into low-temperature zone preheater（6）, middle-temperature section preheater（7）, high temperature section preheater
（8）, which is characterized in that single unit system uses vertical layout, and above incinerator, organic exhaust gas preheater is mounted on waste heat boiler
In waste heat boiler, incinerator adiabatic furnace（1）And insulated combustion chamber（2）Between pass through the uniform accumulation of heat flower pore wall a of flue gas（16）Even
It is logical, insulated combustion chamber（2）Pass through first order gas reversal chamber（9）With the first flue（3）Connection, the first flue（3）Pass through second
Grade gas reversal chamber（10）With the second flue（4）Connection, the second flue（4）Pass through third level gas reversal chamber（11）With third cigarette
Road（5）Connection, third flue（5）End also pass through outer connecting pipe road（13）With exhaust gas entrance chamber（12）Connection, exhaust gas enter
Oral chamber（12）With the second flue（4）Top is connected to, exhaust gas entrance chamber（12）Equipped with decarburization resolution gas import（15）, low-temperature zone
Preheater（6）Positioned at exhaust gas entrance chamber（12）It is interior, middle-temperature section preheater（7）Positioned at the second flue（4）It is interior, high temperature section preheater
（8）Positioned at the first flue（3）It is interior, high temperature section preheater（8）With incinerator adiabatic furnace（1）Connection, low-temperature zone preheater（6）Also
Equipped with exhanst gas outlet（14）.
2. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device according to claim 1, which is characterized in that described
Three flues（5）Level-one steam-generating bank is inside installed from bottom to top（18）, dual evaporation tube bank（19）And economizer（20）.
3. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device according to claim 1, which is characterized in that first order cigarette
Gas reversal chamber（9）With the first flue（3）Between be equipped with the uniform accumulation of heat flower pore wall b of flue gas（15）.
4. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device according to claim 1, which is characterized in that described burns
Burn stove adiabatic furnace（1）, insulated combustion chamber（2）, the first flue（3）, the second flue（4）And third flue（5）, first order flue gas
Reversal chamber（9, second level gas reversal chamber（10）, third level gas reversal chamber（11）And exhaust gas entrance chamber（12）By exhausted
Hot refractory material furnace wall, metal sealing plate and steelframe enclose, boiler drum（21）It is set to and encloses third flue（5）It is upper
At the top of portion's steelframe.
5. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device according to claim 1, which is characterized in that described burns
Burn stove adiabatic furnace（1）Steady burning burner is installed（22）.
6. a kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device according to claim 1, which is characterized in that described changes
Heat pipe bundle（25）For screwed pipe tube bank or bellows tube tube bank.
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| CN201810458843.4A CN108644789A (en) | 2018-05-15 | 2018-05-15 | A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device |
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| CN201810458843.4A CN108644789A (en) | 2018-05-15 | 2018-05-15 | A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device |
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| CN203082896U (en) * | 2013-01-29 | 2013-07-24 | 郑州锅炉股份有限公司 | Calcium carbide furnace tail gas treatment device |
| CN203671619U (en) * | 2013-09-27 | 2014-06-25 | 宁波江宁化工有限公司 | Waste gas preheater |
| CN104121591A (en) * | 2014-07-10 | 2014-10-29 | 广德龙泰电子科技有限公司 | Energy-saving efficient incinerator |
| CN204421021U (en) * | 2015-01-27 | 2015-06-24 | 北京华电光大装备技术有限公司 | A kind of being used for contains N 2the Ω shape thermal oxidation device of O waste gas |
| CN106247347A (en) * | 2016-08-30 | 2016-12-21 | 江苏太湖锅炉股份有限公司 | Refuse incineration exhaust-heating boiler |
| CN106885253A (en) * | 2017-02-21 | 2017-06-23 | 安徽海纳森环境科技有限公司 | A kind of burned waste gas processing unit |
| CN107166977A (en) * | 2017-06-23 | 2017-09-15 | 江苏省冶金设计院有限公司 | A kind of closed vessel furnace furnace gas is reclaimed and cleaning treatment system |
| CN107497291A (en) * | 2017-09-04 | 2017-12-22 | 合肥天翔环境工程有限公司 | A kind of combustion-type VOC processing units |
| CN208365549U (en) * | 2018-05-15 | 2019-01-11 | 大连航化能源装备有限公司 | A kind of coal hydrogen manufacturing decarburization resolution gas incinerating and treating device |
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Application publication date: 20181012 |