CN105823040B - Pintsch process burner with external cracking tube - Google Patents
Pintsch process burner with external cracking tube Download PDFInfo
- Publication number
- CN105823040B CN105823040B CN201610342951.6A CN201610342951A CN105823040B CN 105823040 B CN105823040 B CN 105823040B CN 201610342951 A CN201610342951 A CN 201610342951A CN 105823040 B CN105823040 B CN 105823040B
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- Prior art keywords
- tube
- cracking tube
- extension
- pintsch process
- expects pipe
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/36—Details, e.g. burner cooling means, noise reduction means
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
The invention discloses the Pintsch process burners with external cracking tube, it includes mainly combustion barrel, ignition electrode and nozzle, combustion barrel is made of bottom plate, pipe sleeve, the expects pipe that is located in pipe sleeve, nozzle is located at the intermediate position of combustion barrel by bottom plate, nozzle is nearby equipped with ignition electrode, its structural feature is, expects pipe is divided into inner tube and outer tube, outer tube peripheral hardware having heaters, the outlet of inner tube is connected with extension cracking tube, extension cracking tube is located at the outside of combustion barrel inner wall, and the outlet of extension cracking tube is connect by connecting tube with the nozzle in combustion barrel;The Pintsch process burner that the present invention is easy to process, cost is relatively low and lytic effect is more fully novel.
Description
Technical field
The present invention relates to ethanol combustors, and in particular to a kind of improvement of the structure of ethanol combustor.
Background technology
Methanol fuel is set to clean energy resource by country and encourages to promote in automobile and burning industry, first on existing market
Alcohol cooking range table application behind restaurant, hotel as fuel also has and is applied on boiler.Methanol application technology in burning industry has
Two kinds, one is spray burning, another kind is vaporization combustion.Spray burning is exactly that methanol is constantly allowed methanol stream with a conduit
A very long reddish yellow flame is blown out with wind turbine after being lighted at bocca, belongs to particle burning.Vaporization combustion is exactly first handle
Methanol becomes gas reburning burning, and it is methanol is flowed into burner point to use wind turbine to blow to have a kind of burner in the market, there is one on burner
A bocca is cylinder iron to cast, centre be it is empty allow methanol to be flowed through from this, bocca cast iron just will produce high temperature for a moment for burning
Burning again after the methanol gasifying flowed through from this(64 ° of methanol can vaporize), the length of flame that vaporization combustion sprays is than atomization
It is short, flame temperature is also higher than atomization, therefore is also saved with fuel.Either atomization or vaporization combustion, due to first
Alcohol easily occurs wash rice carbon at 400-600 °, so often there is blocking sprayer phenomenon;In addition, atomization and vaporization combustion all be unable to do without wind
Machine aided fires, and blowing fan delivery increases when needing firepower, and wind speed raising can cause part methanol to have little time burning to be discharged in air,
Here it is the peppery eyes of always love that cooks often say, and calorific value is relatively low.
The steam of first alcohol and water is in 2.2mpa and by dedicated catalyst conversion to occur under the conditions of higher than 260 DEG C anti-
It answers, generates the hydrogen and carbon dioxide of chemical ratios, chemical equation CH4O+H20 → CO2+H2.Due to combustion of hydrogen calorific value
High and abundant, if methanol decomposition can be allowed to go out hydrogen and applied in reality, that will be significantly energy saving and very environmentally friendly.It can be due to
Price, use condition and the service life of catalyst for preparing hydrogen determine that it can only can be applied in a large amount of purifying hydrogen of hydrogen, so restricting
It and is applied on automobile and burning industry.
But it is exactly that can equally be cracked into hydrogen and carbon dioxide in 800 DEG C of high temperature or more that methanol, which also has another property,
That is methanol gas, which is placed on the place more than 800 DEG C, can crack out the gaseous mixture of a large amount of hydrogen, such gaseous mixture
Blazing up can increase substantially than the combustion heat value of methanol gas, and what is be discharged is vapor and carbon dioxide, super ring
It protects.
Based on this, Patent No. 201320685066.X discloses a kind of Pintsch process burner, mainly include bottom plate,
Pipe sleeve, cracking tube, heater, ignition electrode, temperature sensor, nozzle and controller, bottom plate constitute combustion barrel, feature with pipe sleeve
It is:Combustion barrel inner circumferential is equipped with two layers of spiral pipes, and internal layer is cracking tube, and outer layer is generating tube, is equipped with and adds between two layers of spiral pipes
The outlet of hot device, helix tube is connected by connecting tube with the nozzle in combustion barrel, and nozzle is nearby equipped with ignition electrode;Its it is opposite with
Atomization on existing market is compared with gasified methanol burner, and advantage is that methanol decomposition is gone out hydrogen partial modifying combustion to improve
Calorific value, it is energy saving, and exhaust gas component only has carbon dioxide and vapor, clean environment firendly.But defect is:Since heater is placed in two layers
Between helix tube, therefore processing program is cumbersome, and production efficiency is relatively low, and production cost is relatively high.
Invention content
The present invention aiming at above-mentioned technical problem, provide it is a kind of it is easy to process, cost is relatively low and lytic effect is more abundant
The Pintsch process burner with external cracking tube.
To achieve the above object, the present invention adopts the following technical scheme that, the invention mainly comprises combustion barrel, ignition electrode and sprays
Head, combustion barrel are made of bottom plate, pipe sleeve, the expects pipe that is located in pipe sleeve, and nozzle is located at the intermediate position of combustion barrel by bottom plate, spray
Head is nearby equipped with ignition electrode, and structural feature is that expects pipe is divided into inner tube and outer tube, outer tube peripheral hardware having heaters, internal layer
The outlet of pipe is connected with extension cracking tube, and extension cracking tube is located at the outside of combustion barrel inner wall, and the outlet of extension cracking tube passes through
Connecting tube is connect with the nozzle in combustion barrel.
It is further improved, outer tube is cast together with heater molten metal, preferably uses molten aluminum or copper liquid or aluminium alloy casting
Together.
It is further improved, expects pipe is divided into internal layer helix tube and outer layer helix tube, and the outlet of internal layer helix tube is connected with extension
Cracking tube.
It is further improved, expects pipe is divided into internal layer corrugated pipes and outer layer corrugated pipes, and the outlet of internal layer corrugated pipes is connected with extension
Cracking tube.
It is further improved, expects pipe is to be bent pipe in the arc-shaped by an expects pipe, and the outlet of expects pipe is connected with extension cracking tube.
It is further improved, expects pipe is to be bent waviness pipe by an expects pipe, and the outlet of expects pipe is connected with extension cracking tube.
Preferably, the cross sectional shape of extension cracking tube is that spiral gradient plane or cone gradual change plane or spiral tubbiness are flat
Face.
Preferably, extension cracking tube is entwined by corrugated pipes.
It is further improved, extension cracking tube is located at the outside of combustion barrel inner wall and the upper area of combustion barrel simultaneously.
Beneficial effects of the present invention:
1, easy to process:Since heating tube is located at outside outer tube, rather than among inner tube and outer tube, so processing hand
Continuous simplicity, production efficiency can also improve, and cost can also reduce;
2, energy saving and efficient:Due to being additionally arranged extension cracking tube, that is, it being additionally arranged cracking zone, outer tube is preheated for vaporizing,
Inner tube is Pintsch process area for vaporization and fraction cracked gas, extension cracking tube, keeps the reaction of its internal cleavage more abundant,
Calorific value is greatly improved, temperature can reach 1550 DEG C, so energy saving and efficient;
3, emission reduction environmental protection:There are most of hydrogen components when burning, so burning is more abundant, the ingredient after burning is single to be exactly
Water and carbon dioxide, super environmental protection, uncontaminated gases discharge.
Description of the drawings
Fig. 1 is the structural diagram of the present invention;
Wherein, 1- ignition electrodes, 2- nozzles, 3- bottom plates, 4- pipe sleeves, 5- expects pipes, 6- heaters, 7- extension cracking tubes, 8- connect
It takes over, 9- inner tubes, 10- outer tubes.
Specific implementation mode
The present invention is described in further details below in conjunction with attached drawing, but the not limitation present invention.
As shown in Figure 1, invention includes mainly combustion barrel, ignition electrode 1 and nozzle 2, combustion barrel is by bottom plate 3, pipe
Set 4, the expects pipe 5 being located in pipe sleeve 4 form, and nozzle 2 is located at the intermediate position of combustion barrel by bottom plate 3, and nozzle 2 is nearby equipped with a little
Fiery needle 1, expects pipe 5 are divided for internal layer helix tube and outer layer helix tube, and outer layer helix tube peripheral hardware having heaters 6, internal layer helix tube goes out
Mouth is connected with extension cracking tube 7, and extension cracking tube 7 is located at the outside of combustion barrel inner wall, and the outlet of extension cracking tube 7 passes through connection
Pipe 8 is connect with the nozzle 2 in combustion barrel, the cross sectional shape of extension cracking tube 7 be spiral gradient plane or cone gradual change plane,
Or spiral tubbiness plane, outer tube 10 are cast together with the molten metal of heater 6, and molten aluminum or copper liquid or aluminium alloy casting can be used one
It rises.
Another embodiment, the expects pipe 5 are divided for internal layer corrugated pipes and outer layer corrugated pipes, the outlet connection of internal layer corrugated pipes
There is extension cracking tube 7;Its effect is relative to two layers of screwed pipe difference, because vaporization contact area is relatively small.
Another embodiment, the expects pipe 5 are to be bent pipe in the arc-shaped by an expects pipe 5, and effect is relative to two layers of spiral shell
Line pipe and two layers of corrugated pipes are all poorer, because vaporization contact area can be relatively small.
Another embodiment, the expects pipe 5 are to be bent waviness pipe by an expects pipe 5, and effect is relative to two layers of spiral shell
Line pipe, two layers of corrugated pipes are all poorer, but quite a lot of relative to an arc-shaped pipe effect.
Another embodiment, extension cracking tube 7 are located at the outside of combustion barrel inner wall and the upper area of combustion barrel simultaneously.
Although in use, 10 having heaters 6 of outer tube, it is mainly used for liquid vaporization preheating;Inner tube 9 is mainly used for
Liquid vaporizes and part cracking reaction;Extension cracking tube 7 belongs to Pintsch process area, and cracking is very abundant, and hydrogen content is substantially
It improves, the flame temperature of ejection can reach 1550 DEG C.
The specific implementation mode of the present invention is write according to progressive mode, and each embodiment is highlighted
Difference, similar portion can be with cross-reference.
Embodiments of the present invention are elaborated above in conjunction with attached drawing, but the present invention is not limited to above-mentioned implementations
Mode within the knowledge of a person skilled in the art can also be without departing from the purpose of the present invention
Various changes can be made.
Claims (9)
1. the Pintsch process burner with external cracking tube includes mainly combustion barrel, ignition electrode(1)And nozzle(2), combustion barrel
By bottom plate(3), pipe sleeve(4), be located at pipe sleeve(4)Interior expects pipe(5)Composition, nozzle(2)Pass through bottom plate(3)It is located in combustion barrel
Between position, nozzle( 2 )Nearby it is equipped with ignition electrode(1), it is characterised in that:Expects pipe(5)It is divided into inner tube(9)And outer tube
(10), outer tube(10)Peripheral hardware having heaters(6), inner tube(9)Outlet be connected with extension cracking tube(7), extension cracking tube
(7)It is located at the outside of combustion barrel inner wall, extension cracking tube(7)Outlet pass through connecting tube(8)With the nozzle in combustion barrel(2)Even
It connects;The outer tube(10)It vaporizes and preheats for liquid, inner tube(9)For liquid vaporization and part cracking reaction, extension
Cracking tube(7)Belong to Pintsch process area;The outer tube(10)With heater(6)Together with molten metal casting.
2. the Pintsch process burner according to claim 1 with external cracking tube, it is characterised in that:The expects pipe
(5)It is divided into internal layer helix tube and outer layer helix tube, the outlet of internal layer helix tube is connected with extension cracking tube(7).
3. the Pintsch process burner according to claim 1 with external cracking tube, it is characterised in that:The expects pipe
(5)It is divided into internal layer corrugated pipes and outer layer corrugated pipes, the outlet of internal layer corrugated pipes is connected with extension cracking tube(7).
4. the Pintsch process burner according to claim 1 with external cracking tube, it is characterised in that:The expects pipe
(5)To be bent pipe in the arc-shaped, expects pipe by an expects pipe(5)Outlet be connected with extension cracking tube(7).
5. the Pintsch process burner according to claim 1 with external cracking tube, it is characterised in that:The expects pipe
(5)To be bent waviness pipe, expects pipe by an expects pipe(5)Outlet be connected with extension cracking tube(7).
6. according to any Pintsch process burners with external cracking tube of claim 1-5, it is characterised in that:Extension
Cracking tube(7)Cross sectional shape be spiral gradient plane or cone gradual change plane or spiral tubbiness plane.
7. according to any Pintsch process burners with external cracking tube of claim 1-5, it is characterised in that:Extension
Cracking tube is entwined by corrugated pipes.
8. according to any Pintsch process burners with external cracking tube of claim 1-5, it is characterised in that:Extension
Cracking tube(7)It is located at the outside of combustion barrel inner wall and the upper area of combustion barrel simultaneously.
9. the Pintsch process burner according to claim 1 with external cracking tube, it is characterised in that:Outer tube(10)
With heater(6)Together with molten aluminum or copper liquid or aluminium alloy casting.
Priority Applications (1)
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CN201610342951.6A CN105823040B (en) | 2016-05-23 | 2016-05-23 | Pintsch process burner with external cracking tube |
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CN201610342951.6A CN105823040B (en) | 2016-05-23 | 2016-05-23 | Pintsch process burner with external cracking tube |
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CN105823040A CN105823040A (en) | 2016-08-03 |
CN105823040B true CN105823040B (en) | 2018-11-06 |
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CN109724075B (en) * | 2019-01-30 | 2024-03-19 | 何建国 | Mixed atomizing pyrolysis combustor |
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Publication number | Priority date | Publication date | Assignee | Title |
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DE3626933A1 (en) * | 1986-08-08 | 1988-02-18 | Kernforschungsanlage Juelich | METHOD AND DEVICE FOR PRODUCING A COMBUSTIBLE GAS MIXTURE FROM LIQUID FUEL, WATER VAPOR AND COMBUSTION AIR |
CN2129892Y (en) * | 1992-08-25 | 1993-04-14 | 王东其 | Synthetic fuel burner device |
CN202074518U (en) * | 2011-05-25 | 2011-12-14 | 重庆市大为石化有限公司 | Liquid fuel gasification combustor and combustion furnace employing same |
CN203298294U (en) * | 2012-12-18 | 2013-11-20 | 刘闽龙 | Electric heating gasification furnace head burning methanol liquid fuel and molded by aluminum casting |
CN203431861U (en) * | 2013-06-21 | 2014-02-12 | 彭伟钦 | Electrothermal gasification combustor combusting alcohol base liquid fuel |
CN203595120U (en) * | 2013-10-31 | 2014-05-14 | 葛士群 | High-temperature pyrolyzing combustor |
CN205664369U (en) * | 2016-05-23 | 2016-10-26 | 葛士群 | Pyrolysis combustor with external schizolysis pipe |
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Effective date of registration: 20170502 Address after: 114200, No. 39, building 3, 13-18, Guangming Road, Haicheng, Liaoning, Anshan, 6 Applicant after: Ge Shiqun Applicant after: Cui Yongxin Address before: 114200, No. 39, building 3, 13-18, Guangming Road, Haicheng, Liaoning, Anshan, 6 Applicant before: Ge Shiqun |
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