CN207276563U - Biomass steam decomposes hydrogen producer - Google Patents
Biomass steam decomposes hydrogen producer Download PDFInfo
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- CN207276563U CN207276563U CN201721049581.3U CN201721049581U CN207276563U CN 207276563 U CN207276563 U CN 207276563U CN 201721049581 U CN201721049581 U CN 201721049581U CN 207276563 U CN207276563 U CN 207276563U
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- furnace body
- steam
- tripe
- biomass
- stove
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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 21
- 239000001257 hydrogen Substances 0.000 title claims abstract description 21
- 239000002028 Biomass Substances 0.000 title claims abstract description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000007789 gas Substances 0.000 claims abstract description 22
- 238000002309 gasification Methods 0.000 claims abstract description 20
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 5
- 241001149930 Protura <class> Species 0.000 claims abstract description 4
- 238000009826 distribution Methods 0.000 claims abstract description 3
- 230000005855 radiation Effects 0.000 claims description 25
- 239000003795 chemical substances by application Substances 0.000 claims description 10
- 239000000919 ceramic Substances 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000002956 ash Substances 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 238000000889 atomisation Methods 0.000 claims description 3
- 235000002918 Fraxinus excelsior Nutrition 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 6
- 230000004048 modification Effects 0.000 abstract description 4
- 238000012986 modification Methods 0.000 abstract description 4
- 150000002431 hydrogen Chemical class 0.000 abstract description 3
- 238000002955 isolation Methods 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 208000012839 conversion disease Diseases 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 208000021760 high fever Diseases 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002916 wood waste Substances 0.000 description 1
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
A kind of biomass steam decomposes hydrogen producer, it accommodates stove tripe using the furnace body 1 that infrared ray occurring source and water source material are formed, setting one on the top of stove tripe has the cartridge type steam of compatible second gasification device from dry device 3, the upper middle part of stove tripe sets the separator 26 of a gasification gas, the bottom of stove tripe sets mesh tray 17 of the centre equipped with convex conehead, the middle upper portion of mesh tray 17 sets a mesh burning column 11, the outside of the lower volume 1 of stove tripe sets a vapor distributor 22, the gasification gas that this biomass steam decomposition hydrogen producer can contain gasification of biomass in tar separates, secondary oxidation gasifies again.Steam can be made to decompose modification, rotten conversion generation hydrogen, the purpose improved so as to fulfill efficiency from the generation gas hybrid reaction of the distribution of dry purification ＆ isolation and biomass.
Description
Technical field
The utility model is that a kind of biomass steam decomposes hydrogen producer, and particularly one kind utilizes wood waste and farming
The discarded object of thing does raw material generation gas, and mixed vapour decomposes modification metamorphic reaction conversion hydrogen, and self-sufficiency conversion energy supply makes
With supporting Multifunctional heating, heat supply, gasification of biomass, vapor decompose hydrogen producer on demand with transfer split, classification.
Background technology
With the development and progress of production and living, energy-consuming heat aspect increase, the dirt brought with energy consumption
Dye problem is presented increasingly, progressively increases the overall development for restricting human society, and the mankind strengthen pollution administration dynamics in recent years, and
The energy is modified, unremitting ongoing effort always in terms of seeking free of contamination renewable and clean energy resource, wherein final conclusion is to change
Become future society energy resource structure, realize environment zero load is Hydrogen Energy, in many Hydrogen Energies produce scheme, by the use of plant as
Hydrogen source, since plant is by fixed carbon dioxide growth, expectation is just enjoyed with its hydrogen making from the restriction of carbon dioxide
One of production of renewable energy resources.Bio-coal gas producer or straw are known as using " heat chemistry evaporating method " in existing technology
Stalk gasification furnace, since evaporation source material can be the discarded object of crops, there is facility advantage easily available and without cost, so
So far many decades are adopted by people adopt always for exploitation.But the primary stage in low side operation is thrown away in technical elements, although
There is the improvement project of many, and thoroughly realized that effective, efficient, high-end embody produced comprehensive reason of Hydrogen Energy again without finding
The method thought, still remains following deficiency：As tar cannot convert gasification for a full due；Containing water vapor cannot be had
Decomposition and inversion is imitated into hydrogen, auto-thermal gasification energy loss is big, and the efficiency for the gas that gasifies is low, and waste heat cannot obtain effective profit
With the furnace body of particularly gasification furnace is easily subject to chemically react corrosion and damage, causes waste and the use cost of material resources
Increase.For this it is an object of the invention to thoroughly overcome these deficiencies existing in the prior art, redesign is made new
Technical solution, can thoroughly realize that perhydrogenating, service life of equipment length, simple and convenient low cost, high efficiency, zero dirt are decomposed in reaction
Dye, global function and can biomass gasified gas environment and meanwhile increase mixing water vapor reaction decomposed metamorphic, modification generation
Combustible gas；Than the gasification gas of biomass generation, the technology that more vapor are converted into Hydrogen Energy dedicates human society to.
The content of the invention
To achieve the above object, the technical solution of the utility model is, using a lower part be equipped with water source inlet and outlet,
Upper top is equipped with the full double wall furnace body for holding water heat absorption aerogenesis of steam outlet, and the inner face whole body of furnace body, which forms one, interval
The lattice-shaped comb in space, lattice-shaped comb be connected with furnace body hold water, be connected hold water grid water comb and furnace body inner wall it
Between carry over and set one layer of infrared radiation net, set the cartridge type of a double wall to steam among the upper end of furnace body tripe internal upper part linking furnace body
Gas is equipped with steam outlet from dry device, skeleton symbol steam from the upper top of dry device, and lower part is equipped with steam inlet port and surplus water is discharged
Mouthful, cartridge type is nested with one layer of cylinder infrared radiation net from the cylinder inner circumferential circle of dry device, and lower part centre sets one layer of infrared ray to fire in cylinder
Burn radiation network.Middle part inner cavity in cylinder be second gasification device, is equipped with gas discharge in cylinder among the upper top of second gasification device
Mouthful, bottom sets a centre to be equipped with the ceramic alternate mesh tray of convex conehead in furnace body tripe, on the middle convex cone of mesh tray
Side sets a pipe column for leading to Rong Shui with furnace body grid, is enclosed in pipe column and is nested with the alternate dictyosome burning column of a ceramics.This
Sample biomass enters burning column, and gasifying agent air lower part into column concentrates injection enhancing volatilization burning to form one together with dictyosome is rubescent
The dilatation radiation source of group's flame compatibility infrared ray, live charcoal is scattered in the mesh tray circle burning of convex cone seat leftover bits and pieces and middle fire is rolled into a ball
And holding the infrared radiation net of radiation furnace body, the infrared ray of generation reflects again to be correspondingly formed in fire with the dictyosome infrared ray on burning column
The radiation in length and breadth of light, forms the guarantor of whole stove tripe and the strong energy radiation source of high temperature vigorous fire, in this way, gasifying agent steam in fire, light
It is that stove tripe lower part intermediate injection is involved in the rolling rising of heat wave whirlpool by charcoal fire center, it is same facilitating components of biomass to be gasified totally
When also possess the infrared ray decomposition condition of water, realize the decomposed metamorphic modification reaction generation of steam mixing gasifying gas based on hydrogen
Want the mixed combustible gas body of component, meanwhile, and introduce a gas into again, cylindrical steam from the cylinder of dry device lower part it is infrared
Line burning radiation net, the infrared radiation net second gasification in burning contacts cylinder, increases steam modification and decomposes conversion energy again
Component and tar thoroughly gasify, improve generation hydrogen purity and gasification whole efficiency.
Above-mentioned technical solution can not also set the burning column in furnace body tripe, easy to the not refined woollen discarded object of application and
The use of rubbish alveolar substance thing, widens material resources, more preferably reduces production cost.The grid water of furnace body inner face can not also be set at the same time
The device of comb and infrared radiation net, the gasification system in stove is contained by single appearance water double wall furnace body, realizes biogas
The easy mode of change, the selection used for different occasions so as to it is each to the greatest extent needed for, although so reducing steam decomposes the energy changed
Amount, but Industrial Engineering difficulty is small, low cost, so as to make up missing, improves efficiency, boosts all-round development.
The special advantage of the utility model compared with the prior art is：Furnace body uses infrared ray occurring source and water material structure
Into since the material of infrared ray occurring source is dry, high fever, it can only not only produce infrared ray, ultraviolet and luminous energy and electromagnetism
The energy of energy expands, moreover it is possible to plays thermal balance, interlayer, dry-run protection furnace body and corrodes from chemical reaction, keep from heat unbalance damage
Bad furnace body, prevents the multiple action of heat loss, and the intervention of water and its grid layout for holding water, and furnace body balance can be made to be extended by consumption
Service life, especially original simple gasification furnace, it is both gasification furnace to change over and the multipurpose of steam water heater is set
It is standby, in terms of industry is with heat, steam hot water can be directly used, can also directly use internal heat or combustion gas split heat supply.Such as
Fruit configuration family uses, and has fuel gas supply kitchen range fiery, has the demand of steam hot water supply cooking and daily life, reach
One supplies how thorough effect, script cheap and simple is easily equipped, and becomes to double simply, inexpensively.Conveniently serve mankind society
Meeting.
Brief description of the drawings
Further indicate below in conjunction with the accompanying drawings
Attached drawing is one embodiment structure diagram of the utility model
One optimal embodiment of the utility model is referring to attached drawing
Embodiment
One lower part is imported and exported equipped with water source, and upper top is equipped with the full double wall stove for holding water heat absorption aerogenesis of steam outlet
Body 1, the inner face whole body of furnace body 1 form a lattice-shaped comb 2 for being equipped with clearance space, and lattice-shaped comb 2 is connected appearance with furnace body 1
Water, carries between be connected the grid water comb 2 and the inner wall of furnace body 1 that hold water and sets one layer of infrared radiation net 24, the tripe of furnace body 1
The cartridge type steam of a double wall is set from dry device 3, top of the cartridge type steam from dry device 3 among the upper end of internal upper part linking furnace body 1
Top surface is equipped with steam outlet, and lower part is equipped with steam inlet port and surplus water outlet, and cartridge type is nested with one from the cylinder inner circumferential circle of dry device 3
A cylinder infrared radiation net 6, the lower part in cylinder set one layer of gas-fired infrared radiation network 5, and the middle part inner cavity in cylinder is secondary
Gasifier, gas discharge outlet 4 is equipped with cylinder among the upper top of second gasification device, bottom sets one to make pottery in the tripe of furnace body 1
The alternate mesh tray 17 of porcelain, the centre of mesh tray 17 are equipped with convex conehead 19, and the lower section of middle convex cone 19 of mesh tray 17 is equipped with gas
The introducing pipe 18 of agent, the middle convex cone face of mesh tray 17 set a lighter 21, the middle convex cone top of mesh tray 17
The lattice-shaped comb 2 of setting one and furnace body 1 leads to the pipe column 13 of Rong Shui, and the inner side on pipe column 13 is nested with an alternate net of ceramics
Eye burning column 11, the top of furnace body 1 are equipped with vapor outlet port connecting line 7 into the lower part from dry device 3, and steam is from dry device 3
Heating atomization separation, have surplus underwater heavy, enters the lower part of furnace body 1 with the appearance water in furnace body 1 simultaneously by lower part outlet connecting line 23
Hold, steam is separating, improving the steam of degree of atomization from dry device 3, passes through stove tripe by upper outlet connecting line 9；Under stove tripe
The tail end that the outside of portion through furnace wall stretching furnace body 1 is connected to stretching sets a vapor distributor 22.Into distributor 22
Steam, respectively as the distribution of gasifying agent and direct decomposition gas；A part is turned round into stove tripe to top by connecting line 10
Gas-fired infrared radiation network 5 is risen in secondary gasifier, and it is upward that a part by connecting line 14 introduces the lower part in stove tripe
Spread in tripe.Among the upper top of furnace body 1 and the engaging portion of the steam from the upper top of dry device 3 on stove tripe top, stove tripe
The gas discharge outlet of connecting line 27 is equipped with above space, the lower end of gas discharge outlet connecting line 27 is equipped with separator 26, point
Lower end from device 26 is equipped with tar and ashes separates the pipe 25 that drops, and the side of separator 26 is equipped with the drop-leg 8 of purifying, point
One end of flow tube 8 ascends into the bottom of the gas-fired infrared radiation network 5 on top.The bottom of gas-fired infrared radiation network 5 and stove
Gasifying agent introduction pipeline 20, bottom extrapersonal space of the gasifying agent by pipeline 20 from furnace body 1 are equipped between the bottom extrapersonal space of body 1
Suction, is ascended into the secondary gasifier of radiation network 5 and top by pipeline 20 in the heating of stove tripe.The lower center ovens of furnace body 1
The top on wall side against burning column 11 in stove tripe is equipped with biomass inlet port 12, and the lower part of furnace body 1 is equipped with water source inlet and outlet 15,
The bottom of furnace body 1 is equipped with ash hole 16.
Claims (4)
1. a kind of biomass steam decomposes hydrogen producer, a lower part is imported and exported equipped with water source, and upper top is arranged equipped with steam
The full double wall furnace body (1) for holding water heat absorption aerogenesis of outlet, the inner face whole body of furnace body (1) form a grid for being equipped with clearance space
Shape comb (2), lattice-shaped comb (2) is connected with furnace body (1) holds water, and the connected grid water comb (2) for holding water is interior with furnace body (1)
Carried between wall and set one layer of infrared radiation net (24), set among the upper end of the tripe internal upper part linking furnace body (1) of furnace body (1)
The cartridge type steam of one double wall is equipped with steam outlet from dry device (3), cartridge type steam from the upper top of dry device (3), and lower part is set
There are steam inlet port and surplus water outlet, cartridge type is nested with a cylinder infrared radiation net (6) from the cylinder inner circumferential circle of dry device (3),
Lower part in cylinder sets one layer of gas-fired infrared radiation network (5), and the middle part inner cavity in cylinder is second gasification device, second gasification in cylinder
Gas discharge outlet (4) is equipped among the upper top of device, bottom sets the alternate mesh tray of a ceramics in the tripe of furnace body (1)
(17), the centre of mesh tray (17) is equipped with convex conehead (19), and gasifying agent is equipped with below the middle convex cone (19) of mesh tray (17)
Introducing pipe (18), mesh tray (17) middle convex cone face set a lighter (21), the middle convex cone of mesh tray (17)
The lattice-shaped comb (2) of top setting one and furnace body (1) leads to the pipe column (13) of Rong Shui, and pipe column is nested with one on the inside of (13)
Alternate mesh burning column (11) of ceramics, the top of furnace body (1) are equipped with vapor outlet port connecting line (7) and enter from dry device (3)
Lower part, steam is atomized in the heating from dry device (3) to be separated, has to remain and sink under water, enters furnace body by lower part outlet connecting line (23)
(1) lower part and the appearance water in furnace body (1) simultaneously hold, steam from dry device (3) separation, improve the steam of degree of atomization, gone out by top
Mouth connecting line (9) passes through stove tripe；The tail end for being connected to stretching on the outside of furnace wall stretching furnace body (1) is passed through to set in the lower part of stove tripe
Put a vapor distributor (22), the upper top of furnace body (1) and knot of the steam on stove tripe top from the upper top of dry device (3)
The gas discharge outlet of connecting line (27) is equipped among conjunction portion, above the space of stove tripe, gas discharge outlet connecting line (27)
Lower end is equipped with separator (26), and the lower end of separator (26) is equipped with tar and ashes separates the pipe (25) that drops, separator (26)
Side is equipped with the drop-leg (8) of purifying, and one end of isocon (8) ascends into the gas-fired infrared radiation network (5) on top
Bottom.
2. biomass steam according to claim 1 decomposes hydrogen producer, it is characterised in that gas-fired infrared radiation network
(5) be equipped with gasifying agent introduction pipeline (20) between bottom and the bottom extrapersonal space of furnace body (1), gasifying agent by pipeline (20) from
The bottom extrapersonal space suction of furnace body (1), ascends into radiation network (5) in the heating of stove tripe by pipeline (20) and top is secondary
In gasifier.
3. biomass steam according to claim 1 decomposes hydrogen producer, it is characterised in that vapor distributor (22)
Effect, steam enter distribution of the distributor (22) respectively as gasifying agent and direct decomposition gas；A part is by connecting line (10)
The gas-fired infrared radiation network (5) on revolution into stove tripe to top is risen in secondary gasifier, and a part is by connecting line
(14) lower part introduced in stove tripe is diffused up in tripe.
4. biomass steam according to claim 1 decomposes hydrogen producer, it is characterised in that the lower center ovens of furnace body (1)
Wall side is equipped with biomass inlet port (12) against the top of column (11) of burning in stove tripe, the lower part of furnace body (1) equipped with water source into
Export (15), the bottom of furnace body (1) is equipped with ash hole (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721049581.3U CN207276563U (en) | 2017-08-14 | 2017-08-14 | Biomass steam decomposes hydrogen producer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721049581.3U CN207276563U (en) | 2017-08-14 | 2017-08-14 | Biomass steam decomposes hydrogen producer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207276563U true CN207276563U (en) | 2018-04-27 |
Family
ID=61984627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721049581.3U Active CN207276563U (en) | 2017-08-14 | 2017-08-14 | Biomass steam decomposes hydrogen producer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207276563U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107460006A (en) * | 2017-08-14 | 2017-12-12 | 张达积 | Biomass steam decomposes hydrogen producer |
-
2017
- 2017-08-14 CN CN201721049581.3U patent/CN207276563U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107460006A (en) * | 2017-08-14 | 2017-12-12 | 张达积 | Biomass steam decomposes hydrogen producer |
| CN107460006B (en) * | 2017-08-14 | 2024-05-31 | 张达积 | Hydrogen gas producer by decomposing biomass steam |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: Room 201, Unit 1, Building 11, Xiangshan Garden, Shangyangtou, Pingnan County, Ningde City, Fujian Province, 352300 Patentee after: Zhang Daji Address before: Room 402, Building D, Hefeng Commercial City, Jiaocheng District, Ningde City, Fujian Province Patentee before: Zhang Daji |
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| CP03 | Change of name, title or address |