CN110496587A - A kind of hydrogen production reaction furnace - Google Patents
A kind of hydrogen production reaction furnace Download PDFInfo
- Publication number
- CN110496587A CN110496587A CN201910786585.7A CN201910786585A CN110496587A CN 110496587 A CN110496587 A CN 110496587A CN 201910786585 A CN201910786585 A CN 201910786585A CN 110496587 A CN110496587 A CN 110496587A
- Authority
- CN
- China
- Prior art keywords
- reaction kettle
- hydrogen production
- tank body
- spray waterpipe
- reaction furnace
- 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
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 33
- 239000001257 hydrogen Substances 0.000 title claims abstract description 33
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000007921 spray Substances 0.000 claims abstract description 29
- 239000006185 dispersion Substances 0.000 claims abstract description 19
- 239000000498 cooling water Substances 0.000 claims abstract description 15
- 238000005192 partition Methods 0.000 claims abstract description 6
- 125000004122 cyclic group Chemical group 0.000 claims description 5
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 2
- 239000000463 material Substances 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
The invention discloses a kind of hydrogen production reaction furnaces, including tank body, the upper end of the tank body is equipped with feed inlet, the lower end of the tank body is equipped with blanking pipe, is equipped with reaction kettle and cooling water tank in the tank body, separates between the reaction kettle and cooling water tank equipped with partition, the reaction kettle is equipped with spray waterpipe, the external water feed apparatus of spray waterpipe, the lower section of the spray waterpipe are equipped with dispersion impeller, are additionally provided with hydrogen outlet on the reaction kettle.The invention can make hydrogen production efficiency higher.
Description
Technical field
The present invention relates to device for producing hydrogen technical field, in particular to a kind of hydrogen production reaction furnace.
Background technique
Hydrogen is minimum the lightest element in known element, while the content in universe is also most abundant.The burning of hydrogen is raw
Cheng Shui, product is not only pollution-free but also can release huge energy.Hydrogen Energy is considered as 21 century most development potentiality
Clean energy resource.
Existing device for producing hydrogen influences the popularization and use of hydrogen producer since hydrogen production efficiency is low and cannot achieve continuity,
Especially when charging, material cannot preferably be reacted with water material.
Summary of the invention
In order to overcome the drawbacks described above of the prior art, the present invention provides a kind of hydrogen production reaction furnace, which can make
Hydrogen production efficiency is higher.
The present invention solves technical solution used by the problems of the prior art are as follows: a kind of hydrogen production reaction furnace, including tank body,
The upper end of the tank body is equipped with feed inlet, and the lower end of the tank body is equipped with blanking pipe, and the tank body is interior equipped with reaction kettle and cold
But water tank separates between the reaction kettle and cooling water tank equipped with partition, and the reaction kettle is equipped with spray waterpipe, the shower water
External water feed apparatus is managed, the lower section of the spray waterpipe is equipped with dispersion impeller, is additionally provided with hydrogen outlet on the reaction kettle.
As a preferred solution of the present invention, the spray waterpipe is cyclic structure, and the spray waterpipe is set and reaction kettle
On inner wall.
As a preferred solution of the present invention, the spray waterpipe two sides are equipped with several water jets.
As a preferred solution of the present invention, the dispersion impeller is funnel-shaped, and the dispersion impeller is connected to by L-type connector
In inner tank wall.
As a preferred solution of the present invention, the bore of the dispersion impeller is less than the internal diameter of tank body.
As a preferred solution of the present invention, the blanking pipe connects blanking connecting tube, and the blanking connecting tube is located at cold
But in water tank, the blanking connecting tube is connected to reaction kettle.
As a preferred solution of the present invention, the cooling water tank is equipped with inlet and outlet.
Compared with prior art, the present invention has following technical effect that
A kind of hydrogen production reaction furnace of the present invention, by the way that funnelform dispersion impeller and cyclic annular shower water are arranged in the reaction vessel
Pipe, material pass through after feed inlet, can be dispersed disk and disperse along surrounding, while the water of spray waterpipe is fallen along side wall, midway
Understand and fall into bottom after material reaction, such response area is bigger, and it is more abundant to will lead to reaction.
Detailed description of the invention
Fig. 1 is a kind of device for producing hydrogen structure chart of the present invention；
Fig. 2 is the structure chart of dispersion impeller in a kind of device for producing hydrogen of the present invention；
Fig. 3 is the structure chart of spray waterpipe in a kind of device for producing hydrogen of the present invention.
Figure label: 1- tank body；2- feed inlet；3- blanking pipe；4- reaction kettle；5- cooling water tank；6- partition；7- spray
Water pipe；8- dispersion impeller；9- hydrogen outlet；10-L type connector；11- connecting tube；12- sprays water inlet；13- water inlet；14- goes out
The mouth of a river；15- water jet.
Specific embodiment
Specific embodiments of the present invention will be further explained with reference to the accompanying drawing.It should be noted that for
The explanation of these embodiments is used to help understand the present invention, but and does not constitute a limitation of the invention.In addition, disclosed below
Embodiment of the present invention involved in technical characteristic can be combined with each other as long as they do not conflict with each other.
A kind of hydrogen production reaction furnace, including cylindrical tank 1, the upper end of the tank body 1 are equipped with feed inlet 2, the feed inlet 2 with
External feeding device connection, material are fallen into tank body 1 through feed inlet 2；The lower end of the tank body 1 is equipped with blanking pipe 3, material
Remaining material is reacted in tank body 1 to discharge through blanking pipe 3.
Further, it is equipped with reaction kettle 4 and cooling water tank 5 in the tank body 1, between the reaction kettle 4 and cooling water tank 5
It is separated equipped with partition 6, material is fed in reaction kettle 4 through feed inlet 2, can generate a large amount of heat, institute after reaction in reaction kettle 4
Stating cooling water tank 5 can cool down to reaction kettle 4.
The reaction kettle 4 is equipped with spray waterpipe 7, and the lower section of the spray waterpipe 7 is equipped with dispersion impeller 8.
After further material is fallen into reaction kettle 4, it can fall as on dispersion impeller 8, divide under the effect of dispersion impeller 8 along surrounding
It scatters, the water sprayed with spray waterpipe 7 is fallen along side wall simultaneously, is reacted halfway.
Further, the hydrogen that the reaction of reaction kettle 4 generates is discharged by setting hydrogen outlet 9 on the reaction kettle 4.
The spray waterpipe 7 is cyclic structure, and the spray waterpipe 7 passes through spray water inlet 1312 and external water feed apparatus
Connection, the spray waterpipe 7 are set on the inner wall of reaction kettle 4, and 7 two sides of spray waterpipe are equipped with several water jets 15.
Further, spray waterpipe 7 can be sprayed sufficiently into reaction kettle 4 by several water jets 15 of setting, allow water
Contact with material is more abundant.
The dispersion impeller 8 is funnel-shaped, and the dispersion impeller 8 is connected on 1 inner wall of tank body by L-type connector 10, the leakage
Bucket-shaped structure, but it can scatter around along inclination cambered surface when material falls into dispersion impeller 8.
The bore of the dispersion impeller 8 is less than the internal diameter of tank body 1, and material can be allowed to continue to fall into reaction kettle 4.
The blanking pipe 3 connects blanking connecting tube 11, and the blanking connecting tube 11 is located in cooling water tank 5, under described
Material connecting tube 11 is connected to reaction kettle 4.
Further, the material that material reacts after the reaction of midway with water falls into bottom, finally deposits on partition 6, under
Material connecting tube 11 drops at blanking pipe 3.
Cooling water tank 5 is equipped with water inlet 13 and water outlet 14, and water passes through 14 row of water outlet after the heating of cooling water tank 5
Out.
Compared with prior art, the present invention has following technical effect that
A kind of hydrogen production reaction furnace of the present invention, by the way that funnelform dispersion impeller 8 and cyclic annular spray are arranged in the reaction vessel
Water pipe 7, material pass through after feed inlet 2, can be dispersed disk 8 and disperse along surrounding, while the water of spray waterpipe 7 is fallen along side wall
Under, halfway can with bottom is fallen into after material reaction, such response area is bigger, will lead to reaction it is more abundant.
Finally, it should be noted that the foregoing is only a preferred embodiment of the present invention, it is not intended to restrict the invention,
Although the present invention is described in detail referring to the foregoing embodiments, for those skilled in the art, still may be used
To modify the technical solutions described in the foregoing embodiments or equivalent replacement of some of the technical features.
All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in of the invention
Within protection scope.
Claims (7)
1. a kind of hydrogen production reaction furnace, including tank body, it is characterised in that: the upper end of the tank body is equipped with feed inlet, the tank body
Lower end is equipped with blanking pipe, is equipped with reaction kettle and cooling water tank in the tank body, is equipped between the reaction kettle and cooling water tank
Partition separates, and the reaction kettle is equipped with spray waterpipe, and the lower section of the spray waterpipe is equipped with dispersion impeller, also sets on the reaction kettle
There is hydrogen outlet.
2. a kind of hydrogen production reaction furnace according to claim 1, it is characterised in that: the spray waterpipe is cyclic structure, institute
It states spray waterpipe to set on the inner wall with reaction kettle, the external water feed apparatus of spray waterpipe.
3. a kind of hydrogen production reaction furnace according to claim 1, it is characterised in that: if the tube wall of the spray waterpipe is equipped with
Dry water jet.
4. a kind of hydrogen production reaction furnace according to claim 1, it is characterised in that: the dispersion impeller is funnel-shaped, and described point
Disk is dissipated to be connected in inner tank wall by L-type connector.
5. a kind of hydrogen production reaction furnace according to claim 4, it is characterised in that: the bore of the dispersion impeller is less than tank body
Internal diameter.
6. a kind of hydrogen production reaction furnace according to claim 1, it is characterised in that: the blanking pipe is connected with blanking connection
Pipe, the blanking connecting tube are located in cooling water tank, and the blanking connecting tube is connected to reaction kettle.
7. a kind of hydrogen production reaction furnace according to claim 1, it is characterised in that: the cooling water tank be equipped with water inlet and
Water outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910786585.7A CN110496587A (en) | 2019-08-23 | 2019-08-23 | A kind of hydrogen production reaction furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910786585.7A CN110496587A (en) | 2019-08-23 | 2019-08-23 | A kind of hydrogen production reaction furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110496587A true CN110496587A (en) | 2019-11-26 |
Family
ID=68589349
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910786585.7A Pending CN110496587A (en) | 2019-08-23 | 2019-08-23 | A kind of hydrogen production reaction furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110496587A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110496586A (en) * | 2019-08-23 | 2019-11-26 | 东莞市宏湖智能装备有限公司 | A kind of hydrogen fuel cell device for producing hydrogen |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032325A (en) * | 2015-08-12 | 2015-11-11 | 范昕昀 | Reaction still |
| CN205216839U (en) * | 2015-12-02 | 2016-05-11 | 宿州学院 | Reation kettle for chemistry experiments |
| CN207385429U (en) * | 2017-08-30 | 2018-05-22 | 成都化润药业有限公司 | Organic synthesis kettle with deodorization functions |
| CN208302775U (en) * | 2018-04-30 | 2019-01-01 | 佛山市顺德区简得建材有限公司 | High-molecular water paint reaction kettle |
| WO2019128903A1 (en) * | 2017-12-25 | 2019-07-04 | 正泰集团股份有限公司 | Automatic continuous hydrogen generation device |
-
2019
- 2019-08-23 CN CN201910786585.7A patent/CN110496587A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032325A (en) * | 2015-08-12 | 2015-11-11 | 范昕昀 | Reaction still |
| CN205216839U (en) * | 2015-12-02 | 2016-05-11 | 宿州学院 | Reation kettle for chemistry experiments |
| CN207385429U (en) * | 2017-08-30 | 2018-05-22 | 成都化润药业有限公司 | Organic synthesis kettle with deodorization functions |
| WO2019128903A1 (en) * | 2017-12-25 | 2019-07-04 | 正泰集团股份有限公司 | Automatic continuous hydrogen generation device |
| CN208302775U (en) * | 2018-04-30 | 2019-01-01 | 佛山市顺德区简得建材有限公司 | High-molecular water paint reaction kettle |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110496586A (en) * | 2019-08-23 | 2019-11-26 | 东莞市宏湖智能装备有限公司 | A kind of hydrogen fuel cell device for producing hydrogen |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201404861Y (en) | Floatation column special for circulating fluidized bed boiler fly ash | |
| CN105623861B (en) | A kind of glycerine esterification reaction unit | |
| CN204051632U (en) | A kind of Venturi tube-type spreader gas-liquid allotter of high-efficient atomizing | |
| CN110496587A (en) | A kind of hydrogen production reaction furnace | |
| WO2022082622A1 (en) | Hydrogenation micro-interface system | |
| CN203075924U (en) | Overflow-jet nozzle type gas-liquid distributor | |
| CN202865188U (en) | Dry power gasification device | |
| CN204294211U (en) | Hexanediamine reactor | |
| CN207243476U (en) | Electronic-grade polycrystalline silicon reduction furnace | |
| CN201399385Y (en) | Dedicated flotation column for fly ash | |
| CN105749850B (en) | A kind of special purpose reactor of controlled syntheses parachlorotoluene | |
| CN202246104U (en) | Fluidized bed reactor for preparing trichlorosilane | |
| CN205550245U (en) | Production surface -activeagent's ethoxylation ware | |
| CN214261820U (en) | Fluidized bed reactor for efficiently producing hydrophobic white carbon black | |
| CN201071305Y (en) | Silicon dioxide producing device | |
| CN106745086A (en) | One kind Ca (OH)2And SO2Multi-stage countercurrent continuously reduces Na2SO4Generation Na2SO3Reaction tower | |
| CN210736210U (en) | Energy-saving continuous sulfur melting kettle | |
| CN208466226U (en) | A kind of new type nozzle | |
| CN210065673U (en) | Ultraviolet light catalytic reaction system for chlorinated paraffin production | |
| CN110496586A (en) | A kind of hydrogen fuel cell device for producing hydrogen | |
| CN106185805B (en) | A kind of solar biomass energy Hydrogen Energy combined power generation device | |
| CN205164701U (en) | A reation kettle for producing silane have a separator | |
| CN101608872B (en) | Device for washing and cooling chlorine | |
| CN215312404U (en) | Reactor suitable for producing fumed silica | |
| CN206343071U (en) | A kind of multi-stage countercurrent reaction tower |
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 |