CN109140427A - A kind of combustion gas fission device - Google Patents
A kind of combustion gas fission device Download PDFInfo
- Publication number
- CN109140427A CN109140427A CN201811156044.8A CN201811156044A CN109140427A CN 109140427 A CN109140427 A CN 109140427A CN 201811156044 A CN201811156044 A CN 201811156044A CN 109140427 A CN109140427 A CN 109140427A
- Authority
- CN
- China
- Prior art keywords
- pipe
- heat conducting
- air inlet
- heating room
- combustion gas
- 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.)
- Pending
Links
- 239000000567 combustion gas Substances 0.000 title claims abstract description 34
- 230000004992 fission Effects 0.000 title abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 44
- 239000002737 fuel gas Substances 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims abstract description 22
- 239000003054 catalyst Substances 0.000 claims abstract description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 7
- 239000003546 flue gas Substances 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000002912 waste gas Substances 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims 2
- 230000008901 benefit Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004321 preservation Methods 0.000 abstract description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 14
- 239000003345 natural gas Substances 0.000 description 5
- 238000005336 cracking Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000009089 cytolysis Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C5/00—Disposition of burners with respect to the combustion chamber or to one another; Mounting of burners in combustion apparatus
- F23C5/08—Disposition of burners
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/04—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material using washing fluids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/002—Gaseous fuel
- F23K5/007—Details
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2400/00—Pretreatment and supply of gaseous fuel
- F23K2400/10—Pretreatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2900/00—Special features of, or arrangements for fuel supplies
- F23K2900/01041—Heating by using exhaust gas heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K2900/00—Special features of, or arrangements for fuel supplies
- F23K2900/05081—Treating the fuel with catalyst to enhance combustion
Abstract
The present invention relates to fission device technical fields, especially a kind of combustion gas fission device, including heating room, the heating is indoor to be equipped with heat conducting pipe, one end of the heat conducting pipe is equipped with air inlet, air inlet pipe is connected on air inlet, high-temperature fuel gas pipe is equipped in the heat conducting pipe, catalyst is stained on the inner wall of the high-temperature fuel gas pipe, one end of the high-temperature fuel gas pipe and the end of air inlet pipe connect, the other end of the high-temperature fuel gas pipe is connected to the inside of heat conducting pipe, filter core is equipped in the heat conducting pipe and at one end far from air inlet pipe, the high-temperature fuel gas pipe passes through filter core and extends to its right side, the heat contained in the exhaust gas that the present invention rationally utilizes burner to discharge, so as to effectively save the energy, by the way that heat preservation and filter structure layer by layer is arranged, achieve the efficient advantage of clean and environmental protection.
Description
Technical field
The present invention relates to fission device technical field more particularly to a kind of combustion gas fission devices.
Background technique
In order to improve the efficiency and in-furnace temperature of boiler-burner, it is desirable that there is portion of natural gas to crack to be formed to fill in combustion gas
Point calorific value is decomposed, in addition natural gas pyrolysis makes in fuel gas containing a small amount of hydrogen, and hydrogen maximum temperature of burning in air is
2040 DEG C, higher than methane, methane is 1870 DEG C, this is advantageous for improving temperature in boiler furnace.It is general in the prior art to use
Natural gas is preheating to 1000 DEG C or so in advance by regenerative furnace, mixes with air burning again after cracking portion of natural gas to reach
Effect is stated, but due to on-catalytic cracking to be used, accumulation of heat furnace volume is big, land occupation is more, benefit is low, often lower in preheating temperature
When, smelting time is spun out, so that final obtain shutdown maintenance and influence to produce, to improve natural gas pyrolysis efficiency, it is thus proposed that
Use nickel nitrate as the combustion gas fission process of catalyst, but this mode is unfavorable for there is still a need for more energy is consumed
Energy conservation and environmental protection.
Summary of the invention
The purpose of the present invention is to solve a kind of combustion gas fissions for existing in the prior art not energy-efficient disadvantage, and proposing
Device.
To achieve the goals above, present invention employs following technical solutions:
A kind of combustion gas fission device, including heating room are designed, the heating is indoor to be equipped with heat conducting pipe, one end of the heat conducting pipe
Equipped with air inlet, be connected with air inlet pipe on air inlet, be equipped with high-temperature fuel gas pipe in the heat conducting pipe, the high-temperature fuel gas pipe it is interior
Be stained with catalyst on wall, one end of the high-temperature fuel gas pipe and the end of air inlet pipe connect, the high-temperature fuel gas pipe it is another
End is connected to the inside of heat conducting pipe, and filter core, the high-temperature fuel gas pipe are equipped in the heat conducting pipe and at one end far from air inlet pipe
Its right side is extended to across filter core, is connected with combustion gas inlet pipe on the heat conducting pipe side wall on the left of the filter core, the combustion gas inlet pipe is worn
The fuel gas inlet for crossing heating room and burner connects, and the Waste gas outlet of the burner is connected with flue gas leading, the flue gas leading
It is connected to the left end of heating room, the right end of the heating room is connected with exhaust pipe.
Preferably, the heating room is in horizontally disposed cylindrical shape, and the outside of the heating room is equipped with cylindric shell,
The shell and heating room are coaxial, and the inner wall of the shell is equipped with insulating layer, and the insulating layer is insulating sponge layer.
Preferably, it is surrounded with electrothermal tube on the outer wall of the heating room, the heating room is made of stainless steel.
Preferably, it is equidistantly equipped with the second thermally conductive sheet on the inner wall of the heating room, is equidistantly set on the outer wall of the heat conducting pipe
There is the first thermally conductive sheet, first thermally conductive sheet and the second thermally conductive sheet are circular sheet metal, first thermally conductive sheet and second
Thermally conductive sheet is interlaced.
Preferably, first thermally conductive sheet and the second thermally conductive sheet are aluminium flake or copper sheet.
Preferably, the other end of the air inlet pipe by three-way connection connection there are two branched pipe, on the branched pipe
Equipped with control valve and flowmeter, the control valve is solenoid valve, and the flow is calculated as electronic flowmeter, one of them described branch
Pipe is connect with air and nitrogen pipeline, another described branched pipe is connect with gas pipeline.
Preferably, the inside of one end of the heat conducting pipe and heating room, which inserts, connects, in the air inlet pipe and heat conducting pipe
It is connected between air inlet by quick coupling, the other end of the heat conducting pipe passes through the connector that heating room end opens up and resists
The inner wall of end cap, the end cap are connect with the connector edge-wise threads that heating room end opens up.
Preferably, the high-temperature fuel gas pipe be quartz glass tube, the high-temperature fuel gas pipe inside heat conducting pipe twist
Coiling.
Preferably, the other end of the exhaust pipe is connected with exhaust gas processing pool, is equipped with absorbing liquid in the exhaust gas processing pool,
The end of the exhaust pipe enters in exhaust gas processing pool from the side of exhaust gas processing pool and extends to its bottom.
A kind of combustion gas fission device proposed by the present invention, beneficial effect are: it is useless that the present invention rationally utilizes burner to discharge
The heat contained in gas, by the way that heat preservation and filter structure layer by layer is arranged, has clean and environmental protection so as to effectively save the energy
Efficient advantage.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of combustion gas fission device proposed by the present invention.
In figure: shell 1, the first thermally conductive sheet 2, heating room 3, heat conducting pipe 4, exhaust gas processing pool 5, exhaust pipe 6, high-temperature fuel gas pipe
7, end cap 8, filter core 9, combustion gas inlet pipe 10, burner 11, flue gas leading 12, control valve 13, flowmeter 14, branched pipe 15, air inlet pipe
16, the second thermally conductive sheet 17, electrothermal tube 18.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.
Referring to Fig.1, a kind of combustion gas fission device, including heating room 3, heating are equipped with heat conducting pipe 4, one end of heat conducting pipe 4 in room 3
Equipped with air inlet, it is connected with air inlet pipe 16 on air inlet, high-temperature fuel gas pipe 7 is equipped in heat conducting pipe 4, high-temperature fuel gas pipe 7 is quartz
Glass tube, high-temperature fuel gas pipe 7 twist coil inside heat conducting pipe 4.Heat conducting pipe 4 plays the work for absorbing high temperature in heating room 3
With combustion gas is influenced to crack by high-temperature fuel gas pipe 7 by high temperature.
Catalyst is stained on the inner wall of high-temperature fuel gas pipe 7, one end of high-temperature fuel gas pipe 7 and the end of air inlet pipe 16 connect
It connects, the other end of high-temperature fuel gas pipe 7 is connected to the inside of heat conducting pipe 4, is equipped in heat conducting pipe 4 and at one end far from air inlet pipe 16
Filter core 9, high-temperature fuel gas pipe 7 pass through filter core 9 and extend to its right side, are connected with combustion gas inlet pipe on 4 side wall of heat conducting pipe in 9 left side of filter core
10, combustion gas inlet pipe 10 passes through heating room 3 and connect with the fuel gas inlet of burner 11, and the Waste gas outlet of burner 11 is connected with useless
Tracheae 12, flue gas leading 12 are connected to the left end of heating room 3, and the right end of heating room 3 is connected with exhaust pipe 6.It is improved using catalyst
Combustion gas lysis efficiency.Filtering of the combustion gas through filtration core 9 after cracking enters in burner 11 from combustion gas inlet pipe 10 burns, and fires
It burns the exhaust gas generated to enter in heating room 3 from flue gas leading 12 to provide heat, then passes through the discharge of exhaust pipe 6.
Heating room 3 is in horizontally disposed cylindrical shape, and the outside of heating room 3 is equipped with cylindric shell 1, shell 1 and heating
Room 3 is coaxial, and the inner wall of shell 1 is equipped with insulating layer, and insulating layer is insulating sponge layer.It heats and is surrounded with electrothermal tube on the outer wall of room 3
18, heating room 3 is made of stainless steel.Electrothermal tube 18 is for improving high temperature to help combustion gas to crack.
It heats and is equidistantly equipped with the second thermally conductive sheet 17 on the inner wall of room 3, be equidistantly equipped with the first thermally conductive sheet on the outer wall of heat conducting pipe 4
2, the first thermally conductive sheet 2 and the second thermally conductive sheet 17 are circular sheet metal, and the first thermally conductive sheet 2 and the second thermally conductive sheet 17 are mutually handed over
It is wrong.First thermally conductive sheet 2 and the second thermally conductive sheet 17 are aluminium flake or copper sheet.First thermally conductive sheet 7 and the second thermally conductive sheet 17 play increase
Heat-conducting area improves heat exchanger effectiveness, and extends residence time of the exhaust gas in heating room 3, to increase endothermic effect.
The other end of air inlet pipe 16 there are two branched pipe 15, is equipped with control valve on branched pipe 15 by three-way connection connection
13 and flowmeter 14, control valve 13 is solenoid valve, and flowmeter 14 is electronic flowmeter, one of branched pipe 15 and air and nitrogen
Feed channel connection, another branched pipe 15 are connect with gas pipeline.
One end of heat conducting pipe 4 and the inside of heating room 3 insert and connect, between the air inlet in air inlet pipe 16 and heat conducting pipe 4
It being connected by quick coupling, the other end of heat conducting pipe 4 passes through the connector that heating 3 end of room opens up and the inner wall for resisting end cap 8,
End cap 8 is connect with the connector edge-wise threads that heating 3 end of room opens up.It can be facilitated by opening end cap 8 to the progress of heat conducting pipe 4
Maintenance.
The other end of exhaust pipe 6 is connected with exhaust gas processing pool 5, is equipped with absorbing liquid, the end of exhaust pipe 6 in exhaust gas processing pool 5
Portion enters in exhaust gas processing pool 5 from the side of exhaust gas processing pool 5 and extends to its bottom.By exhaust gas processing pool 5 to exhaust gas into
Row absorption processing, avoids pollution environment.
Working principle: it when reaction, after heat conducting pipe 4 is heated to certain temperature, is passed through combustion gas and is cracked, after a period of time
Combustion gas is deactivated, purges a period of time with nitrogen later, is further continued for carrying out cracking reaction.
The foregoing is only a preferred embodiment of the present invention, but scope of protection of the present invention is not limited thereto,
Anyone skilled in the art in the technical scope disclosed by the present invention, according to the technique and scheme of the present invention and its
Inventive concept is subject to equivalent substitution or change, should be covered by the protection scope of the present invention.
Claims (9)
- The device 1. a kind of combustion gas is fissioned, including heating room (3), it is characterised in that: be equipped with heat conducting pipe (4) in the heating room (3), institute The one end for stating heat conducting pipe (4) is equipped with air inlet, is connected with air inlet pipe (16) on air inlet, high temperature is equipped in the heat conducting pipe (4) Fuel gas conduit (7) is stained with catalyst, one end of the high-temperature fuel gas pipe (7) and air inlet on the inner wall of the high-temperature fuel gas pipe (7) The end connection of (16) is managed, the other end of the high-temperature fuel gas pipe (7) is connected to the inside of heat conducting pipe (4), the heat conducting pipe (4) Filter core (9) are equipped at interior and one end far from air inlet pipe (16), the high-temperature fuel gas pipe (7) passes through filter core (9) and extends to its right side Side is connected with combustion gas inlet pipe (10) on heat conducting pipe (4) side wall on the left of the filter core (9), the combustion gas inlet pipe (10) pass through plus Hot cell (3) is connect with the fuel gas inlet of burner (11), and the Waste gas outlet of the burner (11) is connected with flue gas leading (12), The flue gas leading (12) is connected to the left end of heating room (3), and the right end of heating room (3) is connected with exhaust pipe (6).
- The device 2. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: the heating room (3) is in horizontally disposed Cylindrical shape, the outside of heating room (3) are equipped with cylindric shell (1), and the shell (1) and heating room (3) are coaxially, described The inner wall of shell (1) is equipped with insulating layer, and the insulating layer is insulating sponge layer.
- The device 3. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: surround on the outer wall of heating room (3) Have electrothermal tube (18), the heating room (3) is made of stainless steel.
- The device 4. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: equidistant on the inner wall of heating room (3) Equipped with the second thermally conductive sheet (17), the first thermally conductive sheet (2) equidistantly are equipped on the outer wall of the heat conducting pipe (4), first thermally conductive sheet (2) and the second thermally conductive sheet (17) is circular sheet metal, and first thermally conductive sheet (2) and the second thermally conductive sheet (17) are mutually handed over It is wrong.
- The device 5. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: first thermally conductive sheet (2) and second is led Backing (17) is aluminium flake or copper sheet.
- The device 6. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: the other end of the air inlet pipe (16) passes through There are two three-way connection connections branched pipe (15), is equipped with control valve (13) and flowmeter (14), institute on the branched pipe (15) Stating control valve (13) is solenoid valve, and the flowmeter (14) is electronic flowmeter, one of them described branched pipe (15) and air And nitrogen pipeline connection, another described branched pipe (15) connect with gas pipeline.
- The device 7. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: one end of the heat conducting pipe (4) and heating The inside of room (3) inserts connection, is connect between the air inlet pipe (16) and the air inlet on heat conducting pipe (4) by quick coupling, The other end of the heat conducting pipe (4) passes through the connector that heating room (3) end opens up and the inner wall for resisting end cap (8), the end Lid (8) is connect with the connector edge-wise threads that room (3) end opens up are heated.
- The device 8. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: the high-temperature fuel gas pipe (7) is quartzy glass Glass pipe, the high-temperature fuel gas pipe (7) are twist coiled inside heat conducting pipe (4).
- The device 9. a kind of combustion gas according to claim 1 is fissioned, it is characterised in that: the other end of the exhaust pipe (6) connects Have exhaust gas processing pool (5), be equipped with absorbing liquid in the exhaust gas processing pool (5), the end of the exhaust pipe (6) is from exhaust gas processing pool (5) side enters in exhaust gas processing pool (5) and extends to its bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811156044.8A CN109140427A (en) | 2018-09-30 | 2018-09-30 | A kind of combustion gas fission device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811156044.8A CN109140427A (en) | 2018-09-30 | 2018-09-30 | A kind of combustion gas fission device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109140427A true CN109140427A (en) | 2019-01-04 |
Family
ID=64814080
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811156044.8A Pending CN109140427A (en) | 2018-09-30 | 2018-09-30 | A kind of combustion gas fission device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109140427A (en) |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1710329A (en) * | 2005-06-20 | 2005-12-21 | 李志轩 | Bituminous coal combustion boiler and method for removing its black smoke |
| CN201321451Y (en) * | 2008-12-30 | 2009-10-07 | 河南省科学院能源研究所有限公司 | Device for preparing and synthesizing gas for alcohol ether by using biomasses |
| CN101776262A (en) * | 2009-12-30 | 2010-07-14 | 伍镜清 | Energy-saving method and device for gas combustion |
| CN102095200A (en) * | 2011-03-17 | 2011-06-15 | 北京沃克能源科技有限公司 | Double heat accumulation type high-temperature oxygen-deficient combustor with oxygen-enriched air supply |
| CN102220150A (en) * | 2011-05-16 | 2011-10-19 | 山东省科学院能源研究所 | Method for preparing high-quality gas by biomass pyrolysis desulphurization and decarbonization |
| CN102459065A (en) * | 2009-06-24 | 2012-05-16 | 蒂森克虏伯伍德有限公司 | Primary reformer having variable smoke gas flow |
| CN102767404A (en) * | 2011-05-06 | 2012-11-07 | 中国科学院工程热物理研究所 | System and method of gas turbine for utilizing low-concentration gas |
| CN102964883A (en) * | 2012-12-13 | 2013-03-13 | 新疆雅克拉炭黑有限责任公司 | Hot-cracking-method carbon black production process assisted by hydrogen-enriched gas |
| CN103017148A (en) * | 2012-11-29 | 2013-04-03 | 郭丰亮 | Heat preservation double-hearth cracker |
| CN103074093A (en) * | 2013-01-30 | 2013-05-01 | 南京工业大学 | Integral process and system for directly drying and pyrolyzing lignite |
| CN103256600A (en) * | 2013-06-08 | 2013-08-21 | 天津高德恒立科技有限公司 | Preheating method and device of gas burner |
| CN103363811A (en) * | 2012-03-30 | 2013-10-23 | 鞍钢股份有限公司 | Combustion method of high-temperature oxygen-mixed flue gas |
| CN103788972A (en) * | 2014-02-25 | 2014-05-14 | 合肥工业大学 | Internal-combustion heating rotary vane type biomass gasification furnace |
| CN105953409A (en) * | 2016-06-27 | 2016-09-21 | 河南中托力合化学有限公司 | Vertical energy saving device for fuel gas heating medium furnace |
| CN207622248U (en) * | 2017-12-15 | 2018-07-17 | 湛江市广南农业科技有限公司 | A kind of high efficiency burnt gas heater with heat recovery function |
| CN209399354U (en) * | 2018-09-30 | 2019-09-17 | 廊坊市顶天轻工机械有限公司 | A kind of combustion gas fission device |
-
2018
- 2018-09-30 CN CN201811156044.8A patent/CN109140427A/en active Pending
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1710329A (en) * | 2005-06-20 | 2005-12-21 | 李志轩 | Bituminous coal combustion boiler and method for removing its black smoke |
| CN201321451Y (en) * | 2008-12-30 | 2009-10-07 | 河南省科学院能源研究所有限公司 | Device for preparing and synthesizing gas for alcohol ether by using biomasses |
| CN102459065A (en) * | 2009-06-24 | 2012-05-16 | 蒂森克虏伯伍德有限公司 | Primary reformer having variable smoke gas flow |
| CN101776262A (en) * | 2009-12-30 | 2010-07-14 | 伍镜清 | Energy-saving method and device for gas combustion |
| CN102095200A (en) * | 2011-03-17 | 2011-06-15 | 北京沃克能源科技有限公司 | Double heat accumulation type high-temperature oxygen-deficient combustor with oxygen-enriched air supply |
| CN102767404A (en) * | 2011-05-06 | 2012-11-07 | 中国科学院工程热物理研究所 | System and method of gas turbine for utilizing low-concentration gas |
| CN102220150A (en) * | 2011-05-16 | 2011-10-19 | 山东省科学院能源研究所 | Method for preparing high-quality gas by biomass pyrolysis desulphurization and decarbonization |
| CN103363811A (en) * | 2012-03-30 | 2013-10-23 | 鞍钢股份有限公司 | Combustion method of high-temperature oxygen-mixed flue gas |
| CN103017148A (en) * | 2012-11-29 | 2013-04-03 | 郭丰亮 | Heat preservation double-hearth cracker |
| CN102964883A (en) * | 2012-12-13 | 2013-03-13 | 新疆雅克拉炭黑有限责任公司 | Hot-cracking-method carbon black production process assisted by hydrogen-enriched gas |
| CN103074093A (en) * | 2013-01-30 | 2013-05-01 | 南京工业大学 | Integral process and system for directly drying and pyrolyzing lignite |
| CN103256600A (en) * | 2013-06-08 | 2013-08-21 | 天津高德恒立科技有限公司 | Preheating method and device of gas burner |
| CN103788972A (en) * | 2014-02-25 | 2014-05-14 | 合肥工业大学 | Internal-combustion heating rotary vane type biomass gasification furnace |
| CN105953409A (en) * | 2016-06-27 | 2016-09-21 | 河南中托力合化学有限公司 | Vertical energy saving device for fuel gas heating medium furnace |
| CN207622248U (en) * | 2017-12-15 | 2018-07-17 | 湛江市广南农业科技有限公司 | A kind of high efficiency burnt gas heater with heat recovery function |
| CN209399354U (en) * | 2018-09-30 | 2019-09-17 | 廊坊市顶天轻工机械有限公司 | A kind of combustion gas fission device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104501413A (en) | High-efficient flue gas condensation waste heat recovery device and have this recovery unit's gas module stove | |
| CN201954596U (en) | Oil and gas dual-purpose full-automatic civil kitchen range | |
| CN105570956A (en) | Boiler flue gas waste heat circulating heat-supply system | |
| CN209399354U (en) | A kind of combustion gas fission device | |
| CN205245139U (en) | Highly -effective steam generator | |
| CN208579526U (en) | A kind of vertically heat boiler | |
| CN102095194B (en) | Hydrogen energy boiler | |
| CN109140427A (en) | A kind of combustion gas fission device | |
| CN102155785A (en) | Novel direct-exchanging reinforced-discharging type water jacket furnace | |
| CN203396100U (en) | Inversely-arranged stainless steel condensing type gas water heater | |
| CN203203013U (en) | Biomass steam generator | |
| CN108317720B (en) | Fuel oil boiler | |
| CN205783749U (en) | A kind of three backhaul water heaters in terms of hot-water boiler | |
| CN207661975U (en) | A kind of efficient hot water boiler | |
| CN202057033U (en) | Energy-saving steam water boiler | |
| CN205783764U (en) | A kind of water heater in terms of boiler for domestic | |
| CN201463235U (en) | High-efficiency vacuum phase-change hot water boiler | |
| CN205065766U (en) | Heating furnace economizer | |
| CN2733242Y (en) | Heating furnace | |
| CN101162108A (en) | Compound gas superconductive heater | |
| CN2921698Y (en) | Integrated condensation boiler | |
| CN103836649A (en) | Heating stove capable of conducting auxiliary heating on water heater | |
| CN201740229U (en) | Submerged combustion type water jacket furnace | |
| CN201331183Y (en) | Compound gas superconducting heater | |
| CN204678398U (en) | A kind of stove formula water heater |
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 | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20190613 Address after: 065000 Xikou, Wudi Village, Beiwang Township, Guangyang District, Langfang City, Hebei Province Applicant after: Langfang Dingtian Light Industry Machinery Co. Address before: 710400 Hengyi Pioneer Base, Zhenxing Road, Jixian Industrial Park, Zhouzhi County, Xi'an City, Shaanxi Province Applicant before: Xi'an Xindingtian Equipment Intelligent Technology Co., Ltd. |