CN201071300Y - Hydrogen producer - Google Patents
Hydrogen producer Download PDFInfo
- Publication number
- CN201071300Y CN201071300Y CNU2007202007778U CN200720200777U CN201071300Y CN 201071300 Y CN201071300 Y CN 201071300Y CN U2007202007778 U CNU2007202007778 U CN U2007202007778U CN 200720200777 U CN200720200777 U CN 200720200777U CN 201071300 Y CN201071300 Y CN 201071300Y
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- Prior art keywords
- fuel
- hydrogen
- catalyticreactor
- hydrogen generator
- reaction chamber
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- 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.)
- Expired - Fee Related
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- 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
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Abstract
The utility model relates to a hydrogen generator, in particular to a simple self-control pressure hydrogen generator, which comprises a fuel tank (1) provided with a fuel inlet and outlet (2), and a catalytic reactor (6) fixed on the fuel tank (1). An inner housing (3) arranged in the fuel tank divides the fuel tank into an inner chamber, i.e. a fuel reaction chamber (5), and an outer chamber, i.e. a fuel storage chamber (4); a clearance is retained between the lower end of the inner housing (3) and the bottom of the fuel tank (1); the catalytic reactor (6) is arranged in the fuel reaction chamber (4) and can be detached and replaced conveniently. The hydrogen generator of the utility model has the advantages of simple structure, convenient usage, stable performance, self-control pressure and high safety, and belongs to the field of hydrogen generator for providing hydrogen for fuel cell.
Description
Technical field
The utility model relates to a kind of hydrogen generator, relates to a kind of simple type specifically from the governor pressure hydrogen generator.
Background technology
Along with the day of fossil energy is becoming tight and the becoming more and more important of environment protection, cleaning, efficiently is that (Fuel Cell, FC) technology becomes the emerging energy of following Sustainable development, and is subjected to the attention of countries in the world government day by day for the fuel cell of fuel with hydrogen.
Proton Exchange Membrane Fuel Cells (Proton Exchange Membrane Fuel Cell, PEMFC) be as after alkaline fuel cell (AFC), phosphoric acid fuel cell (PAFC), molten carbonate fuel cell (MCFC) and Solid Oxide Fuel Cell (SOFC), grow up the 5th generation fuel cell.Owing to adopted the solid state electrolyte polymeric membrane as ionogen, therefore have characteristics such as the startup of energy conversion rate high and low temperature, no electrolyte leakage, also therefore be acknowledged as the first-selected ideal source that promises to be space flight, military affairs, transportation and portable standby power supply most.
Fuel cell technology has developed into higher level in the world, realize the commercialization of fuel cell, and subject matter solves the hydrogen source problem exactly and reduces cost, and hydrogen source technology has become the business-like technical bottleneck of Proton Exchange Membrane Fuel Cells.At present, main following several for the mode of fuel cell hydrogen-feeding: gas cylinder storage hydrogen, low temperature liquid storage hydrogen, methyl alcohol or gas renormalizing hydrogen manufacturing and hydride (such as lithium borohydride, sodium borohydride, POTASSIUM BOROHYDRIDE or its mixture) hydrolytic hydrogen production etc.Wherein preceding two kinds of hydrogen supply modes exist all that energy consumption is big, cost is high and shortcoming such as poor stability, though the reformation hydrogen production mode can solve transportation, security problems, and the reforming temperature height, transformation efficiency is low, also is not suitable for portable fuel battery.
Hydride (such as sodium borohydride) hydrolytic hydrogen production mode has following advantage: (1) hydrogen production process is pollution-free; (2) storage hydrogen efficiency height; (3) convenient transportation, safe in utilization; (4) hydrogen purity is high.Therefore this hydrogen manufacturing mode has very high stability and very strong practicality, is particularly suitable for the hydrogen supply device of the portable portable power source of fuel cell.
At present, still there is following shortcoming in hydride hydrolytic hydrogen production technology: (1) hydrogenated liquid thing contacts back generation chemical reaction with catalyzer speed is difficult to control; (2) pressure of apparatus system is regulated needs to increase extra equipment, and makes system structure of device complicated, is awkward.
Publication number is that the application for a patent for invention of CN1774390A discloses a kind of self-adjustable hydrogen generator, its catalyticreactor is equipped with and can interrupts catalyzer and contact closed portion to stop hydrogen to generate with liquid fuel, controlled by an elastic device, the lifting situation of fuel container internal pressure when this elastic device can generate according to hydrogen, promote catalyzer and move, to regulate the generation of hydrogen to closed portion or opening portion.But this hydrogen generator complex structure, and its catalyticreactor placed in the fuel container by integral body, and the replacing of catalyzer is very difficult, and a denier elastic device fails, and reaction is difficult in time be stopped, and security is relatively poor.
Therefore need a kind of simple in structure, easy to use, stable performance, pressure automatic control, the safe hydrogen generator that can be used for fuel cell.
The utility model content
The technical problems to be solved in the utility model provides a kind of simple in structure, easy to use, stable performance, pressure automatic control, the safe hydrogen generator that can be used for fuel cell.
For solving the problems of the technologies described above, the utility model hydrogen generator comprises fuel container that is provided with the fuel import and export and the catalyticreactor that is fixed on the fuel container, and concrete structure is as follows:
Being located at inner casing in the fuel container, fuel container is divided into inner room is that fuel reaction chamber and mistress are fuel storage cell two portions; Leave the space between inner casing lower end and the fuel tank bottom; It is indoor that catalyticreactor is located at fuel reaction.
Catalyticreactor is made by polycarbonate, and wall is provided with the hole, and the shape in hole can be geometricdrawing such as circular, square, trilateral, star, and it is standard that the upper limit of pore size can not spill with catalyzer, and it is standard that lower limit enters easily with fuel solution.The ratio that institute's foraminous surface-area accounts for total surface area on the catalyticreactor is preferably 50 ~ 70%.
The bottom of catalyticreactor preferably is higher than the inner casing lower end.
Catalyticreactor is preferably the plug formula and fixes for being removably fixed on the fuel container.
The upper end double as hydrogen outlet of catalyticreactor, and be provided with valve.
Fuel container has fixed measure, can hold a certain amount of liquid fuel, but the size of concrete fuel container can change with the difference of its purposes.Fuel container is to be made by alkaline-resisting pressure-resistant material, is preferably stainless steel or synthetic glass.
The fuel container of the hydrogen generator that the utility model provides is divided into inside and outside two Room by inner casing, i.e. fuel reaction chamber and fuel storage cell, and the bottom is communicated with between two Room.Catalyticreactor is fixed on the fuel container, and the part that is filled with catalyzer is inserted in the fuel reaction chamber.Be that the basic solution of sodium borohydride is imported and exported from fuel and is injected into the fuel container with liquid fuel, the catalyzer in the catalyticreactor touches fuel solution, and the generation hydrogen that reacts with it is immediately opened the hydrogen valve, can think fuel cell hydrogen-feeding.Carrying out along with reaction, hydrogen produces the consumption hydrogen speed of speed greater than fuel cell, the indoor hydrogen accumulation volume of fuel reaction increases gradually, pressure increases thereupon, internal pressure can force the indoor liquid level of fuel reaction to move down, the liquid level of fuel storage cell rises simultaneously, and fuel and catalyzer contact area reduce, and the hydrogen generating rate slows down; Continuous increase along with the fuel cell hydrogen-consuming volume, the indoor hydrogen accumulation volume of fuel reaction reduces gradually, pressure descends thereupon gradually, the indoor liquid level of fuel reaction can go up gradually, the contact area of catalyzer and fuel solution increases gradually, and hydrogen-producing speed increases thereupon, whole process circulation vibration, the same gas spring of principle, thus reach the automatic control of hydrogen pressure.Another beneficial features of the present utility model is to regulate the generating rate and the product hydrogen time of hydrogen by adjusting the volume ratio of fuel reaction chamber and fuel storage cell.Under the certain prerequisite of cumulative volume, the volume of fuel reaction chamber is big more, and the liquid fuel that participates in reaction is many more, and the generating rate of hydrogen is just fast more, and corresponding fuel storage cell volume reduces, and the aerogenesis time shortens; The volume of fuel reaction chamber is more little, and the liquid fuel that participates in reaction is also few more, and the generating rate of hydrogen slows down, and therefore the aerogenesis time lengthening can recently satisfy the actual needs of different fuel battery by the volume of fuel metering reaction chamber and fuel storage cell.Catalyticreactor of the present utility model and hydrogen outlet are integrated, and adopt plug formula method, and this had both helped the cleaning of catalyticreactor passage, help the convenient regeneration of catalyzer again.The utility model hydrogen generator can stop the generation of hydrogen in any stage of reaction, promptly close the valve at hydrogen outlet place, the indoor elevated pressure gradually of fuel reaction forces fuel solution and catalyzer to break away from, and reaction is stopped, and has therefore improved the safety performance of hydrogen generator greatly.Can find out obviously that thus the utility model provides that a kind of it is simple in structure easily from the governor pressure hydrogen generator, production cost is compared traditional hydrogen generator and is greatly reduced with running cost; Can realize effective automatic control of hydrogen pressure, need not additional complicated pressure regulating device, the volume of device is reduced, simplify the operation, be easy to carry; Hydrogen-producing speed and product hydrogen time are adjustable, can satisfy the needs of the pluralities of fuel battery of different purposes, applying flexible; The replacing regeneration of catalyzer is convenient and swift; Can stop the generation of hydrogen at any time, improve safety performance greatly.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Sectional view when Fig. 1 is the utility model work.
Fig. 2 is the sectional view of the utility model when quitting work.
Fig. 3 is the sectional view of another embodiment of the utility model.
Embodiment
A kind of hydrogen generator, as shown in Figure 1, the utility model hydrogen generator comprises that being provided with fuel imports and exports 2 fuel container 1 and the catalyticreactor 6 that is fixed on the fuel container 1, concrete structure is as follows:
It is that fuel reaction chamber 5 and mistress are fuel storage cell 4 two portions that the inner casing 3 that is located at 1 li of fuel container is divided into inner room with fuel container 1; Leave the space between inner casing 3 lower ends and the fuel tank bottom; Catalyticreactor 6 is located in the fuel reaction chamber 5.
Catalyticreactor 6 is made by polycarbonate, and wall is provided with hole 7, and the shape in hole 7 can be geometricdrawing such as circular, square, trilateral, star, and it is standard that the upper limit of pore size can not spill with catalyzer, and it is standard that lower limit enters easily with fuel solution.On the catalyticreactor 6 porose 7 the surface-area ratio that accounts for total surface area be preferably 50 ~ 70%.
Catalyticreactor 6 bottoms preferably are higher than inner casing 3 lower ends.
Catalyticreactor 6 is preferably the plug formula and fixes for being removably fixed on the fuel container 1.
The upper end double as hydrogen outlet of catalyticreactor 6, and be provided with valve 8.
Fuel container 1 has fixed measure, can hold a certain amount of liquid fuel, but the size of concrete fuel container can change with the difference of its purposes.Fuel container 1 is to be made by alkaline-resisting pressure-resistant material, is preferably stainless steel or synthetic glass.
The utility model hydrogen generator is that the fuel cell hydrogen-feeding process is as follows:
The basic solution of sodium borohydride is imported and exported 2 from fuel to be injected into the fuel container 1, the liquid level of fuel storage cell 4 and fuel reaction chamber 5 all rises, catalyzer in the catalyticreactor 6 touches the sodium borohydride basic solution, catalyzed reaction takes place at once generate hydrogen, the hydrogen that Open valve 8 produces can the battery operated use of fueling.
Carrying out along with reaction, if hydrogen produces the consumption hydrogen speed of speed greater than fuel cell, hydrogen accumulation volume in the fuel reaction chamber 5 increases gradually, pressure increases thereupon, internal pressure can force the liquid level in the fuel reaction chamber 5 to move down, the liquid level of fuel storage cell 4 rises simultaneously, and fuel and catalyzer contact area reduce, and the hydrogen generating rate slows down; Continuous increase along with the fuel cell hydrogen-consuming volume, hydrogen accumulation volume in the fuel reaction chamber 5 reduces gradually, pressure descends thereupon gradually, liquid level in the fuel reaction chamber 4 can go up gradually, the contact area of catalyzer and sodium borohydride basic solution increases gradually, hydrogen-producing speed increases thereupon, whole process circulation vibration, and final hydrogen-producing speed is tending towards being complementary with fuel cell consumption hydrogen speed.
As shown in Figure 2, stopping hydrogen supply only needing hydrogen valve 8 is closed, and along with proceeding of reaction, the hydrogen pressure in the fuel reaction chamber 5 raises gradually, forces the liquid level in the fuel reaction chamber 5 to descend gradually, and until breaking away from catalyzer, reaction stops.
When sodium borohydride is consumed to can't satisfy the fuel cell works better time, the utility model hydrogen generator can be imported and exported 2 from fuel and discharge depleted solution, then new sodium borohydride basic solution is imported and exported 2 from fuel and refill, thus the hydrogen supply of a beginning new round.
Catalyzer in the catalyticreactor 6 needs more catalyst changeout this moment through repeatedly using the back inactivation.Earlier catalyticreactor 6 is pulled up from fuel container 1, taken out the catalyzer of inactivation, put into fresh catalyzer, then catalyticreactor 6 is inserted on the fuel container 1, new catalyzer can make reaction proceed.
Hydrogen generator as shown in Figure 3, its catalyticreactor 6 bottoms are lower than inner casing 3 lower ends, and catalyticreactor 6 increases with the contact area of fuel solution, and hydrogen-producing speed increases, and is applicable to continuously hydrogen supply.
The composition of above-mentioned sodium borohydride basic solution: NaBH
4The quality percentage composition be 15 ~ 30%, the quality percentage composition of NaOH is 10 ~ 20%, all the other are water.
Above-mentioned catalyzer of the present utility model is Pt-Ru/C (40%), and is Powdered,, is encased in the porous catalyticreactor attached on foam copper nickel or the nickel foam by sintering.
The utility model also can be used for the hydrogen production reaction of fuel solution for filling metal in acid, the catalyticreactor, and using method is same as above.
Claims (5)
1. hydrogen generator, comprise that being provided with fuel imports and exports the fuel container (1) of (2) and be fixed in catalyticreactor (6) on the fuel container (1), it is characterized in that: be provided with the inner casing (3) that the fuel container internal space is divided into fuel reaction chamber (5) and fuel storage cell (4) in the described fuel container (1), leave the space between inner casing (3) lower end and fuel container (1) bottom; Catalyticreactor (6) is located in the fuel reaction chamber (4).
2. hydrogen generator according to claim 1 is characterized in that being that described catalyticreactor (6) wall is provided with hole (7).
3. hydrogen generator according to claim 1 is characterized in that being that described catalyticreactor (6) bottom is higher than inner casing (3) lower end.
4. hydrogen generator according to claim 1 is characterized in that being that described catalyticreactor (6) is for being removably fixed on the fuel container.
5. hydrogen generator according to claim 4 is characterized in that described catalyticreactor (6) upper end is provided with valve (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007202007778U CN201071300Y (en) | 2007-08-03 | 2007-08-03 | Hydrogen producer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007202007778U CN201071300Y (en) | 2007-08-03 | 2007-08-03 | Hydrogen producer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201071300Y true CN201071300Y (en) | 2008-06-11 |
Family
ID=39549861
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007202007778U Expired - Fee Related CN201071300Y (en) | 2007-08-03 | 2007-08-03 | Hydrogen producer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201071300Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109081306A (en) * | 2018-10-15 | 2018-12-25 | 中国船舶重工集团公司第七0五研究所 | A kind of hydrogen generator of slow-release hydrogen manufacturing |
-
2007
- 2007-08-03 CN CNU2007202007778U patent/CN201071300Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109081306A (en) * | 2018-10-15 | 2018-12-25 | 中国船舶重工集团公司第七0五研究所 | A kind of hydrogen generator of slow-release hydrogen manufacturing |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HANERGY NEW ENERGY RESEARCH + DEVELOPMENT CENTER C Free format text: FORMER OWNER: HANERGY TECHNOLOGY CO., LTD. Effective date: 20110921 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 102209 CHANGPING, BEIJING TO: 065201 LANGFANG, HEBEI PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110921 Address after: 065201 Hebei Province, Sanhe Yanjiao Development Zone Yingbin Road, east of the northeast corner of the island. Patentee after: Chinese new energy R & D Center Co. Ltd. Address before: 102209 Beijing city Changping District town Beiqijia Hongfu Pioneer Park No. 15 hospital Patentee before: Hanergy Technology Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080611 Termination date: 20150803 |
|
| EXPY | Termination of patent right or utility model |