CN107352508A - A kind of aluminium alkali reacts device for producing hydrogen - Google Patents
A kind of aluminium alkali reacts device for producing hydrogen Download PDFInfo
- Publication number
- CN107352508A CN107352508A CN201710748412.7A CN201710748412A CN107352508A CN 107352508 A CN107352508 A CN 107352508A CN 201710748412 A CN201710748412 A CN 201710748412A CN 107352508 A CN107352508 A CN 107352508A
- Authority
- CN
- China
- Prior art keywords
- reactor
- hydrogen
- collection
- aluminium
- producing hydrogen
- 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
Classifications
-
- 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
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/10—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with metals
- C01B3/105—Cyclic methods
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Fuel Cell (AREA)
Abstract
The present invention relates to a kind of aluminium alkali to react device for producing hydrogen.The invention belongs to technical field of hydrogen preparation.A kind of aluminium alkali reacts device for producing hydrogen, including solid storage tank, reactor and collection of products tank, is characterized in:Solid storage tank store solids alumina particles, the outlet of solid storage tank are connected to drive mechanism, drive mechanism connection reactor top;Reactor gas outlet is connected by pipeline with drive mechanism;Reactor bottom is connected by pipeline with collection of products tank, and collection of products tank top is by liquid delivery pump with being connected in the middle part of reactor;Gas-liquid separation baffle plate, reactor bottom installation heating mantle are installed in the middle part of reactor.The present invention have it is simple in construction, can continuous hydrogen production, reaction controllability is good, and production hydrogen cost is low, and output pressure is high, low power consumption and other advantages, can be widely applied to fuel cell car hydrogenation stations construction field.
Description
Technical field
The invention belongs to technical field of hydrogen preparation, reacts device for producing hydrogen more particularly to a kind of aluminium alkali.
Background technology
Hydrogen is widely used in industries such as many of modern industry purposes, such as metallurgical, chemical industry, food, laboratory apparatus
Hydrogen.On the preparation of hydrogen, mainly there is biomass conversion at present;The fossil resources such as natural gas, oil, coal it is reforming;
The methods of electrolysis water, these technologies there is no method to meet scale of the hydrogen economy development to hydrogen due to the problem of such or such be present
Change demand, especially in hydrogen cell automobile application field.
In order to develop the hydrogen producing technology of suitable hydrogen cell automobile hydrogenation stations, to meet answering for fuel cell car field
With demand, recent years develops with sodium borohydride (NaBH in the world4) be representative new hydrogen production material, this kind of material can be with
Water occurs chemical reaction and produces hydrogen.Control the condition of reaction, caused hydrogen can be supplied directly to fuel cell or
It is other to need hydrogen storage equipment.As Millennium Cell companies of the U.S. cooperate with Daimler-Kreisler Corp, successfully develop with
Boron hydride hydrogen storage fuel is the automobile fuel battery hydrogen-feeding system of medium, and the continual mileage that once feeds is up to 480 kilometers.Though
So there are many advantages come hydrogen-preparing hydrogen-storing using novel light system/hydrogen storage material, also achieve many progress, but further research
Show the problem of this kind of new chemical hydrogen-preparing hydrogen-storing fuel system all has this or that.To study more NaBH at present4Body
Exemplified by system, problems with is there is in actual use:1) cost of raw material is expensive;2) precious metal catalysts such as palladium, ruthenium into
This height, immobilized rear catalyst service life are short (because hydrolysis is to occur to react in the very exothermic of catalyst surface);3)
Reaction product kodalk (NaBO2) easy blocking pipeline;4) recycling utilization of byproduct of reaction is difficult;5) hydrogen storage fuel solution
Stability it is poor because NaBH4A metastable state is in strong alkaline aqueous solution, it is easy to which hydrogen is released in spontaneous generation hydrolysis
Gas, very big potential safety hazard be present, while be also unfavorable for storing for a long time.These defects cause the extensive use of this method by
To a definite limitation.
Metallic aluminium is widely used material in daily life, from basic chemical reaction 1 gram of metallic aluminium of knowledge and water
Reaction can produce 1.24 standards and rise hydrogen.Aluminium rich reserves in the earth's crust, and metallic aluminium can regenerate with water reaction product
Recycle, therefore scale, inexpensive hydrogen can be obtained come hydrogen making using metallic aluminium especially waste aluminium and water reaction
Source.Hydrogenation stations construction of the popularization and application based on aluminium hydrolysis hydrogen producing technology, can greatly promote fuel cell car infrastructure
Build.Because aluminium surface generally has oxide-film, hydrogen production reaction usually requires to carry out under the conditions of sodium hydroxide catalyst is existing,
Control the condition of reaction, caused hydrogen can be supplied directly to fuel cell or other need hydrogen storage equipment.But in actual behaviour
In work, aluminum hydrogen reaction system be there are problems that a lot, and for example course of reaction is difficult to control, and can not realize that continuous hydrogen production etc. is asked
Topic.
The content of the invention
The present invention is solution problems of the prior art, there is provided a kind of aluminium alkali reacts device for producing hydrogen.
It is an object of the invention to provide one kind have it is simple in construction, can continuous hydrogen production, reaction controllability it is good, produce hydrogen cost
It is low, the aluminium alkali reaction device for producing hydrogen for the features such as output pressure is high, and energy consumption is low.
Under the conditions of existing for base catalyst, metallic aluminium can react with water produces hydrogen, is urged with sodium hydroxide (NaOH)
Exemplified by agent:
2Al+2NaOH+6H2O→2Na[Al(OH)4]+3H2↑
The present invention is adopted the technical scheme that to solve technical problem present in known technology:
A kind of aluminium alkali reacts device for producing hydrogen, including solid storage tank, reactor and collection of products tank, is characterized in:Solid
Storage tank store solids alumina particles, the outlet of solid storage tank are connected to drive mechanism, drive mechanism connection reactor top;Reactor
Gas outlet is connected by pipeline with drive mechanism;Reactor bottom is connected by pipeline with collection of products tank, on collection of products tank
Portion is by liquid delivery pump with being connected in the middle part of reactor;Gas-liquid separation baffle plate, reactor bottom installation are installed in the middle part of reactor
Heating mantle.
Aluminium alkali reaction device for producing hydrogen of the present invention can also adopt the following technical scheme that:
Described aluminium alkali reaction device for producing hydrogen, it is characterized in that:Solid alumina particles are to suppress balling-up, outside cladding by aluminium powder
The particle of aluminium foil.
Described aluminium alkali reaction device for producing hydrogen, it is characterized in that:Drive mechanism is cylinder piston.
Described aluminium alkali reaction device for producing hydrogen, it is characterized in that:Collection of products tank top passes through liquid delivery pump and reactor
Middle part connects.
Described aluminium alkali reaction device for producing hydrogen, it is characterized in that:Gas-liquid separation baffle plate is installed in the middle part of reactor.
Described aluminium alkali reaction device for producing hydrogen, it is characterized in that:Reactor bottom installs heating mantle.
The present invention has the advantages and positive effects of:
Aluminium alkali reacts device for producing hydrogen as a result of technical scheme, therefore with simple in construction, can continuously make
Hydrogen, reaction controllability is good, and production hydrogen cost is low, and output pressure is high, low power consumption and other advantages.
Brief description of the drawings
Fig. 1 is aluminium alkali reaction device for producing hydrogen structural representation of the present invention;
In figure, 1- storage tanks;2- solid alumina particles;3- reactors;4- aqueous slkalis;5- drive mechanisms;6- liquid delivery pumps;
7- gas-liquid baffle plates;8- heating mantles;9- valves;10- collection of products tanks;11- aqueous slkalis;12- byproducts of reaction;13- valves;14-
Valve;15- valves.
Embodiment
In order to further understand the content, features and effects of the present invention, hereby enumerating following examples, and coordinate accompanying drawing
Describe in detail as follows:
Embodiment 1
Refering to accompanying drawing 1.
A kind of aluminium alkali reacts device for producing hydrogen, and by storage tank 1, reactor 3, and collection of products tank 10 form, and are characterized in:Gu
The store solids alumina particles 2 of body storage tank 1, the outlet of solid storage tank 1 are connected to drive mechanism 5, and drive mechanism 5 is connected on reactor 3
Portion;The gas outlet of reactor 3 is connected by pipeline with drive mechanism 5;The bottom of reactor 3 is connected by pipeline and collection of products tank 10
Connect, the top of collection of products tank 10 is connected by liquid delivery pump 6 with the middle part of reactor 3;The middle part of reactor 3 is provided with gas-liquid separation
Baffle plate 7, the bottom of reactor 3 installation heating mantle 8.The sodium hydroxide solution being stored in collection of products tank 10 passes through liquid delivery pump
6 are transported in reactor 3, and solid alumina particles 2 are pushed into reactor 3 by drive mechanism 5, and solid alumina particles 2 occur instead with alkali lye 4
Answer hydrogen making.
Embodiment 2
A kind of aluminium alkali reacts device for producing hydrogen, and by storage tank 1, reactor 3, and collection of products tank 10 form.Solid storage tank 1
Store solids alumina particles 2, solid aluminium particle diameter are 5cm.The outlet of solid storage tank 1 is connected to cylinder piston 5, cylinder piston connection
The top of reactor 3;The gas outlet of reactor 3 is connected by pipeline with drive mechanism 5;Received by pipeline and product the bottom of reactor 3
Collection tank 10 is connected, and the top of collection of products tank 10 is connected by liquid delivery pump 6 with the middle part of reactor 3;The middle part of reactor 3 is provided with
Gas-liquid separation baffle plate 7, the bottom of reactor 3 installation heating mantle 8.The sodium hydroxide solution being stored in collection of products tank 10 passes through liquid
Body delivery pump 6 is transported in reactor 3, starts cylinder piston 5 and solid alumina particles 2 are pushed into reactor 3, solid alumina particles 2
Reacted hydrogen making with alkali lye 4.Reaction product is discharged into collection of products tank 10 by valve 9, and product is in collection of products tank
Realize that crystallisation by cooling separates.Alkali lye is transported to reactor by liquid delivery pump again, and alkali lye is heated to specify temperature by heating mantle 8
Degree, cylinder piston, which starts, is pushed into solid alumina particles in reactor, and solid alumina particles and alkali lye react hydrogen making, with
Reaction is carried out, and Hydrogen Vapor Pressure is stepped up in reactor, obtains high pressure hydrogen output.Iterative cycles above procedure realizes continuous system
Hydrogen simultaneously realizes that High Pressure Hydrogen exports.
Claims (6)
1. a kind of aluminium alkali reacts device for producing hydrogen, including solid storage tank, reactor and collection of products tank, it is characterized in that:Solid stores up
Batch can store solids alumina particles, the outlet of solid storage tank are connected to drive mechanism, drive mechanism connection reactor top;Reactor goes out
Gas port is connected by pipeline with drive mechanism;Reactor bottom is connected by pipeline with collection of products tank, collection of products tank top
By liquid delivery pump with being connected in the middle part of reactor;Gas-liquid separation baffle plate is installed, reactor bottom installation adds in the middle part of reactor
Hot jacket.
2. aluminium alkali according to claim 1 reacts device for producing hydrogen, it is characterized in that:Solid alumina particles are to be pressed into by aluminium powder
Ball, the particle of outside cladding aluminium foil.
3. aluminium alkali according to claim 1 reacts device for producing hydrogen, it is characterized in that:Drive mechanism is cylinder piston.
4. aluminium alkali according to claim 1 reacts device for producing hydrogen, it is characterized in that:Collection of products tank top is conveyed by liquid
Pump in the middle part of reactor with being connected.
5. aluminium alkali according to claim 1 reacts device for producing hydrogen, it is characterized in that:Gas-liquid separation gear is installed in the middle part of reactor
Plate.
6. aluminium alkali according to claim 1 reacts device for producing hydrogen, it is characterized in that:Reactor bottom installs heating mantle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710748412.7A CN107352508A (en) | 2017-08-25 | 2017-08-25 | A kind of aluminium alkali reacts device for producing hydrogen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710748412.7A CN107352508A (en) | 2017-08-25 | 2017-08-25 | A kind of aluminium alkali reacts device for producing hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107352508A true CN107352508A (en) | 2017-11-17 |
Family
ID=60288546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710748412.7A Pending CN107352508A (en) | 2017-08-25 | 2017-08-25 | A kind of aluminium alkali reacts device for producing hydrogen |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107352508A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110028040A (en) * | 2019-04-24 | 2019-07-19 | 杭州氢源科技有限公司 | A kind of production technology and its device of aluminium-sodium hydroxide reaction hydrogen manufacturing |
CN111678034A (en) * | 2020-07-01 | 2020-09-18 | 杭州氢源科技有限公司 | High-pressure hydrogen replenishing device and method |
US20210276865A1 (en) * | 2020-03-03 | 2021-09-09 | Massachusetts Institute Of Technology | Hydrogen reactor |
CN113371678A (en) * | 2021-07-19 | 2021-09-10 | 北京理工大学 | Portable controllable continuous hydrogen production device of high-activity aluminum at normal temperature |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1384044A (en) * | 2002-03-04 | 2002-12-11 | 孙元明 | Hydrogen preparing method and device |
CN101671003A (en) * | 2009-10-12 | 2010-03-17 | 中国计量学院 | Aluminum hydrolization hydrogen production device and controlling method thereof |
CN101786603A (en) * | 2010-02-24 | 2010-07-28 | 天津海蓝德能源技术发展有限公司 | Device for preparing hydrogen through hydrolysis |
CN105366639A (en) * | 2015-12-10 | 2016-03-02 | 湖北工业大学 | Portable hydrogen production equipment by automatic control of aluminum-water reaction |
CN106276791A (en) * | 2016-10-10 | 2017-01-04 | 杭州氢源科技有限公司 | A kind of portable aluminium alkali reaction device for producing hydrogen and control method thereof |
-
2017
- 2017-08-25 CN CN201710748412.7A patent/CN107352508A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1384044A (en) * | 2002-03-04 | 2002-12-11 | 孙元明 | Hydrogen preparing method and device |
CN101671003A (en) * | 2009-10-12 | 2010-03-17 | 中国计量学院 | Aluminum hydrolization hydrogen production device and controlling method thereof |
CN101786603A (en) * | 2010-02-24 | 2010-07-28 | 天津海蓝德能源技术发展有限公司 | Device for preparing hydrogen through hydrolysis |
CN105366639A (en) * | 2015-12-10 | 2016-03-02 | 湖北工业大学 | Portable hydrogen production equipment by automatic control of aluminum-water reaction |
CN106276791A (en) * | 2016-10-10 | 2017-01-04 | 杭州氢源科技有限公司 | A kind of portable aluminium alkali reaction device for producing hydrogen and control method thereof |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110028040A (en) * | 2019-04-24 | 2019-07-19 | 杭州氢源科技有限公司 | A kind of production technology and its device of aluminium-sodium hydroxide reaction hydrogen manufacturing |
US20210276865A1 (en) * | 2020-03-03 | 2021-09-09 | Massachusetts Institute Of Technology | Hydrogen reactor |
CN111678034A (en) * | 2020-07-01 | 2020-09-18 | 杭州氢源科技有限公司 | High-pressure hydrogen replenishing device and method |
CN113371678A (en) * | 2021-07-19 | 2021-09-10 | 北京理工大学 | Portable controllable continuous hydrogen production device of high-activity aluminum at normal temperature |
CN113371678B (en) * | 2021-07-19 | 2022-08-23 | 北京理工大学 | Portable controllable continuous hydrogen production device of high-activity aluminum at normal temperature |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107352508A (en) | A kind of aluminium alkali reacts device for producing hydrogen | |
CN103579652B (en) | A kind of fuel cell generation of magnesium hydride hydrolyzation hydrogen supplying | |
CN111039258B (en) | Methanol-water reforming hydrogen production system based on solar fuel | |
CN1162320C (en) | Hydrogen preparing method and device | |
CN212315530U (en) | Hydrogen production device by hydrolysis of sodium borohydride of kilowatt-level fuel cell | |
CN101671003B (en) | Aluminum hydrolization hydrogen production device and controlling method thereof | |
CN101049907B (en) | Instant self-controlled hydrogen supplying method and device from hydrogen chemic produced by hydrolyzing borohydride | |
CN102533384A (en) | Method for electrolysis, reduction and desulfurization of coal water slurry | |
CN212425434U (en) | Integrated kilowatt-level fuel cell sodium borohydride hydrolysis hydrogen production device | |
CN102076603A (en) | Hydrogen-generating colloidal suspension | |
CN201842638U (en) | Automatic-control gas generating device | |
CN201777878U (en) | Micro-chemical hydrogen production device | |
CN101786603A (en) | Device for preparing hydrogen through hydrolysis | |
US20050069486A1 (en) | Method and apparatus for generating hydrogen gas | |
CN201381220Y (en) | Instantaneous self-control hydrogen generation device | |
CN201154897Y (en) | Simple portable hydrogen generator | |
CN103879959B (en) | The aluminum-based composite hydrogen manufacturing material of a kind of high unit hydrogen output and Synthesis and applications thereof | |
CN112429702B (en) | Continuous hydrogen production system and solid fuel | |
CN113264502B (en) | Sodium borohydride hydrolysis hydrogen production device for kilowatt-level fuel cell | |
CN114939436A (en) | Preparation method of Pd nano-particle porous composite material and application of Pd nano-particle porous composite material in low-temperature and normal-temperature hydrogen storage | |
CN103303864A (en) | Method and device for preparing hydrogen by hydrolysis of hydroboron, and application | |
CN111807321A (en) | Seawater hydrogen production reactor and method | |
CN1193927C (en) | Hydrogen generating and storing system and method with sodium-cooled fast reactor as heat source for catalytic pyrolysis of methane | |
CN201217635Y (en) | Hydrogen production plant with hydroboron and instantly automatically controlled hydrogen supply | |
CN107470611A (en) | A kind of hydrogen manufacturing alumina particles and preparation method thereof |
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 | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20171117 |