CN1958438B - Device and method for producing hydrogen - Google Patents
Device and method for producing hydrogen Download PDFInfo
- Publication number
- CN1958438B CN1958438B CN2005100309092A CN200510030909A CN1958438B CN 1958438 B CN1958438 B CN 1958438B CN 2005100309092 A CN2005100309092 A CN 2005100309092A CN 200510030909 A CN200510030909 A CN 200510030909A CN 1958438 B CN1958438 B CN 1958438B
- Authority
- CN
- China
- Prior art keywords
- alternative
- hydrogen
- water
- aqueous vapor
- fuel container
- 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.)
- Active
Links
- 229910052739 hydrogen Inorganic materials 0.000 title claims description 74
- 239000001257 hydrogen Substances 0.000 title claims description 74
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims description 60
- 238000004519 manufacturing process Methods 0.000 title description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 78
- 239000000446 fuel Substances 0.000 claims abstract description 36
- 239000000203 mixture Substances 0.000 claims abstract description 35
- 238000000034 method Methods 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 150000004678 hydrides Chemical class 0.000 claims abstract description 22
- 239000003054 catalyst Substances 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 36
- 239000007789 gas Substances 0.000 claims description 25
- 239000012528 membrane Substances 0.000 claims description 23
- 150000002431 hydrogen Chemical class 0.000 claims description 13
- 239000012466 permeate Substances 0.000 claims description 12
- 229940058401 polytetrafluoroethylene Drugs 0.000 claims description 11
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 11
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 11
- -1 poly tetrafluoroethylene Polymers 0.000 claims description 5
- 239000000843 powder Substances 0.000 claims description 5
- 229910010082 LiAlH Inorganic materials 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 229920013662 Zylonite Polymers 0.000 claims description 2
- SMEGJBVQLJJKKX-HOTMZDKISA-N [(2R,3S,4S,5R,6R)-5-acetyloxy-3,4,6-trihydroxyoxan-2-yl]methyl acetate Chemical compound CC(=O)OC[C@@H]1[C@H]([C@@H]([C@H]([C@@H](O1)O)OC(=O)C)O)O SMEGJBVQLJJKKX-HOTMZDKISA-N 0.000 claims description 2
- 230000001276 controlling effect Effects 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- UQSQSQZYBQSBJZ-UHFFFAOYSA-N fluorosulfonic acid Chemical compound OS(F)(=O)=O UQSQSQZYBQSBJZ-UHFFFAOYSA-N 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 5
- 238000003860 storage Methods 0.000 abstract description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical group OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000000243 solution Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 239000000126 substance Substances 0.000 description 6
- 229920000557 Nafion® Polymers 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000000376 reactant Substances 0.000 description 5
- 239000011358 absorbing material Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000010248 power generation Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- NVIFVTYDZMXWGX-UHFFFAOYSA-N sodium metaborate Chemical compound [Na+].[O-]B=O NVIFVTYDZMXWGX-UHFFFAOYSA-N 0.000 description 1
- 150000003460 sulfonic acids Chemical class 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
Images
Classifications
-
- 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
- Fuel Cell (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
This invention relates to apparatus and method for generating H2. Generation of H2 in this invention is realized by contact reaction between water vapor and a dry mixture of hydride and catalyst. The dry mixture is stored in a fuel container selectively permeable for water vapor, and the permeation rate of water vapor from the water source is adjustable. The fuel container is selectively permeable for water vapor, while liquid-state water, H2, O2, N2 and CO2 are impermeable. After generated in the fuel container, H2 is collected and filtered, and then transported through a gas exit on the fuel container to fuel cells or H2-storage containers. Compared with present techniques, this invention has such advantages as simple structure, high energy efficiency, safe operation and easy control.
Description
Technical field
The present invention relates to a kind of device and method that produces hydrogen, relate in particular to a kind of hydrogen formation apparatus and hydrogen production process that fuel hydrogen can be provided for fuel cell.
Background technology
A kind of hydrogen storage scheme of safe, reliable, efficient rate is very important for the commercialization of fuel cell.Hydride is a very potential method to the demand of portable power source, has a variety of methods to be studied exploitation at present, produces hydrogen by reacting with hydride and pure water, and this is NaBH wherein
4Reaction can be represented with following chemical equation: NaBH
4+ 2H
2O=4H
2+ NaBO
4
Other hydride has: LiH, LiAlH
4, LiBH
4, NaH, NaAlH
4, MgH
2, KH, KBH
4, CaH
2, NaBH
4
These reactions are quite violent, and we need accurately control could produce the hydrogen of requirement and prevent blast.The U.S. has a company to adopt NaBH
4Solution is with NaBH
4Solution contacts with catalyzer, adjusts the speed that hydrogen produces by the rotating speed of adjusting pump, and this method is very practical concerning high-power fuel cell.Yet for the battery less than 20W, because reaction is violent, there is certain difficulty in difficult control when practical application.
Some technology in the past adopt the gas-selectively film to divide dried up and hydride, and water directly is penetrated into hydride one side from the water side.Owing to exist water partial pressure, when water and hydride produce hydrogen at a touch, yet this porous film all has permeability for water and hydrogen, and reactant just needs to seal the seepage that prevents hydrogen like this.And the water of reaction usefulness, must just be packaged in process of production in the hydrogen generator, so just reduce energy efficiency in transit.
Have a United States Patent (USP) to introduce a system, this system is made up of two parts, and a part is a chemical hydride, and another part is a methanol aqueous solution.Methanol aqueous solution can be diffused into hydride side and the hydride generation hydrogen that reacts by barrier film.A hydrogen outlet is installed on the reaction vessel, still, must have good sealing to deal with the toxicity and the high diffusibility of methyl alcohol.
Another United States Patent (USP) has been introduced the hydrogen formation apparatus that a kind of water selective membrane divides water proof and hydride.This film does not allow H
2, N
2Pass through Deng gas, so just make hydrogen collect the easy of change.Unfortunately, there is sizable defective in this system in the practice utilization, at first owing to do not have catalyzer or acidic substance inside, water and NaBH
4Between chemical reaction become quite slow, and be not enough to supply with needs; Secondly this reaction process will make anti-strained be difficult to control when the water permselective membrane directly contacts with liquid water, because a large amount of water can directly arrive the hydride side by film.
Summary of the invention
Purpose of the present invention be exactly provide in order to overcome the defective that above-mentioned prior art exists a kind of simple in structure, energy efficiency is high, the device and method of operational safety, the generation hydrogen that is easy to control.Apparatus of the present invention are with after fuel cell is connected, because its light characteristic that is easy to carry about with one can be applied in a lot of fields.
Purpose of the present invention can be achieved through the following technical solutions:
A kind of device that produces hydrogen is characterized in that, this device comprises:
A) alternative fuel container by aqueous vapor,
B) this fuel container contains a kind of mixture, and this mixture is made up of a kind of hydride and at least a catalyzer at least,
C) on fuel container, have a hydrogen delivery port at least,
D) have a gas filter at least,
E) this fuel container has at least a face to be made up of following material: the material of the alternative permeate water of one deck and the alternative material that sees through gas of one deck at least at least,
F) water source.
Described hydride is selected from NaBH
4, LiAlH
4, LiBH
4, NaAlH
4, MgH
2, KBH
4In one or more.
Described catalyzer is selected from C
O, Ni, Pt, Ru or their compound comprise C
OCL
2In one or more.
Described mixture is drying solid powder or particle, and this mixture has been filled 20%～95% volume of fuel container.
The material of described alternative permeate water only allows aqueous vapor to pass through significantly, does not allow to comprise H
2, O
2, N
2, CO
2Gas pass through.
The material of described alternative permeate water is a kind of perfluorinated sulfonic acid (Nafion) film or zylonite (Cellulose) film.
The material that described alternative sees through gas only allows gas to pass through significantly, does not allow liquid water to pass through, and comprises porous polytetrafluoroethylene (PTFE) film.
Described water source is the moisture in the outside air.
Described water source comprises moisture sponge for one deck at least contains the porous material of water.
A kind of method that produces hydrogen is characterized in that, this method comprises:
A) at least a hydride of preparation and at least a catalyst fines or granular mixture,
B) utilize the alternative face that sees through aqueous vapor that said mixture and water source are isolated,
C) allow aqueous vapor be penetrated into this side of hydride by the face that alternative sees through aqueous vapor, produce chemical reaction from the water source side,
D) from fuel container, collect hydrogen,
E) the wherein alternative face that sees through aqueous vapor by the material of the alternative permeate water of one deck at least and at least the alternative material of one deck through gas form.
Described method has also comprised the generation speed of controlling hydrogen by the rate of permeation of control aqueous vapor, and wherein the control of the rate of permeation of aqueous vapor is to be realized with alternative thickness and the porosity that sees through the material of gas by the thickness of the material of regulating alternative permeate water.
The material of alternative permeate water only allows aqueous vapor to pass through significantly in the described method, does not allow to comprise H
2, O
2, N
2, CO
2Gas pass through.
The alternative material that sees through gas only allows gas to pass through significantly in the described method, does not allow liquid water to pass through, and comprises porous polytetrafluoroethylene (PTFE) film.
Described method has also further comprised by the sealed fuel container makes device stop to produce hydrogen.
Compared with prior art, the present invention have simple in structure, energy efficiency is high, operational safety, be easy to advantages such as control.
Description of drawings
Fig. 1 is the structural representation of one embodiment of the invention;
Fig. 2 is the structural representation of another embodiment of the present invention;
Fig. 3 is the structural representation of another embodiment of the present invention.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings and the specific embodiments.
The hydrogen generator of high-energy-density of the present invention adopts multiple factor and technical scheme, and purpose is to improve energy efficiency, and the realization of this purpose is by reducing the amount of carrying of water; Another purpose is hydrogen and the controllable hydrogen generation speed that obtains capacity by hydride.
Dry powdered hydrogenation image LiH, LiAlH
4, LiBH
4, NaH, NaAlH
4, MgH
2, KH, KBH
4, CaH
2, NaBH
4Very high energy density is all arranged, NaBH
4As preferred hydride is because the character of its high-energy-density and the generation of reacting the back unharmful substance, solid NaBH
4Can from environment, absorb aqueous vapor and react, particularly in the higher environment of wetness.If there be not catalyzer to resemble C
OCL
2, Ni, Pt or be in the sour environment, this reaction is suitable slowly so that be not enough to the fuel supplying battery under most of occasions.By experiment, we can see at NaBH
4With add catalyzer such as C in the reaction of water
OCL
2After, speed of response is obviously accelerated.Why we select C
OCL
2Be because its low price and catalysis characteristics efficiently.
The first-selected exsiccant powder of mixture is the contact area for augmenting response.The making method of powder is at first with C
OCL
2Be dissolved in the Virahol, then with NaBH
4Powder is put in the solution.NaBH
4Can be from Morton, these companies of Eagle-Picher or Bayer have bought.These materials can vacuum-drying under the state of 60 ℃ of centigradetemperatures.
These NaBH
4And C
OCL
2Mixture can put into a fuel container that has one deck aqueous vapor selective membrane at least, and this film allows aqueous vapor to enter into the chemical substance side from the water source side to the full extent, hydrogen promptly produces in container, and discharges from being connected the outlet that container is equipped with strainer.NaBH
4With the reaction product sodium metaborate of water can be at NaBH
4Particle surface forms one deck duricrust, and simultaneously, the volume of chemical substance can increase in reaction in the container, so can not fill up reactant fully in the container, must reserve 5%～80% space, also helps to make aqueous vapor fully contact NaBH
4And C
OCL
2Mixture and the discharging of hydrogen.
The aqueous vapor permselective membrane is made up of two-layer at least, one deck is the material of water selective permeation and the material of one deck gas selective permeation, the Nafion film of our first-selected E.I.Du Pont Company of water selectivity permeable material, the Cellulose film also can use, the first-selected porous PTFE film of gas selective material.As shown in Figure 1: 1 is the production well of hydrogen among the figure, and production well can outwards connect accumulator unit or power generation assembly by pipe.Among the figure 4 the expression by NaBH
4With the mixture of catalyzer composition, the 5th, container receives by NaBH for preventing
4The mixture of forming with catalyzer absorbs that aqueous vapor expands and the space reserved, and the 6th, prevent by NaBH
4The mixture of forming with catalyzer produces inflow such as waste residue or cake mass or blocks the strainer of filtrations such as air outlet in reaction process, by NaBH
4The mixture of forming with catalyzer absorbs the aqueous vapor in the surrounding environment, and the water permselective membrane 2 gentle permselective membranes 3 by representing among the figure enter aqueous vapor NaBH is housed
4React in the material fuel container of forming with catalyzer, the hydrogen that reaction produces, 1 outlet flows among fuel cell or the hydrogen storage vessel from figure.
We observe in experiment, if we directly contact the Nafion film with water, the diffusing capacity of water is very big, the NaBH in the container
4Can form solution with water, what chemical reaction will become like this is quite violent and uncontrollable, therefore will avoid the Nafion film directly to contact and control reaction with liquid water, so just need outside the Nafion film, put one deck gas selective material, porous PTFE film is first-selected, and another benefit be can be by adjusting the PTFE film thickness and the aperture diffusivity of adjusting aqueous vapor.When container is placed in the bigger environment of humidity, control the generation speed of hydrogen with regard to the diffusibleness that helps adjusting aqueous vapor, also having a benefit is exactly this gas selective permeation material, can filter the water of low-purity, very useful under this situation that pure water is difficult for seeking out of doors.
In the inboard of water permselective membrane, we can add one deck gas selective permeation film again, as sandwich, form one deck duricrust to avoid resultant of reaction on water permselective membrane surface.
The water source of aqueous vapor can be to be added in outer liquid water of container or the water in the ambient atmosphere environment, and the outside that the porous water wetted material can be placed on fuel container fixes liquid water, by supplying with moisture with tight contact of container.The benefit of doing like this is at first to react water not need to exist in advance in the hydrogen generator, and weight and volume can significantly reduce when transporting like this; Next is the needed water of this hydrogen generator, much smaller than adopting NaBH
4Solution is done the needed water of hydrogen generator of reactant.Use NaBH with previous classics
4The hydrogen generator of solution can only carry about NaBH of 20% to 30% of its reactant weight
4, and the purpose of our first-selection is to make NaBH
4Reach more than 50% of reactant weight.Simultaneously, the water in the surrounding environment also can be utilized, and 5 times of energy densities are to the hydrogen generator that adopts the solution form.If as the water source, the fuel container surface just can contact by direct with indivisible liquid water in the time of at the beginning with the water of surrounding environment, make the hydrogen of its rapid generation aequum.
The hydrogen fueling battery that produces from hydrogen production bioreactor or be collected in the hydrogen storage vessel can obtain highly purified hydrogen through the bed filtration device, and porous PTFE can be preferred.
Fuel container need seal when storing and make it airtight, does not so just have aqueous vapor to enter in the container, in case do not have aqueous vapor to enter in the container after the sealing, reaction will stop.
As shown in Figure 1, a kind of device that produces hydrogen, in Fig. 1: the 1st, the hydrogen production well, this production well can outwards connect hydrogen-storing device or fuel cell power generating system by pipe; 4 the expression by NaBH
4Mixture with the catalyzer composition; The 5th, container receives by NaBH for preventing
4The mixture of forming with catalyzer absorbs that aqueous vapor expands and the space reserved; The 6th, prevent by NaBH
4The mixture of forming with catalyzer produces inflow such as waste residue or cake mass or blocks filtration strainer such as production well in reaction process; By NaBH
4The mixture of forming with catalyzer absorbs the aqueous vapor in the surrounding environment, and the water permselective membrane 2 gentle permselective membranes 3 by representing among Fig. 1 enter aqueous vapor NaBH is housed
4React in the material fuel container of forming with catalyzer, the hydrogen that reaction produces, the production well from Fig. 1 flows in fuel cell or the hydrogen-storing device.Hydrogen production well 1 among Fig. 1, water permselective membrane 2 gentle permselective membranes 3 constitute the fuel container 7 of this device.
As shown in Figure 2, a kind of device that produces hydrogen, the structure of this device be adopt plastics as materials such as (ABS, PVC) as shell 8, built-in water-absorbing material 10 is as sponge etc., add water by water-in 11, moisture water-absorbing material 10 assurance aqueous vapors can enter by water permselective membrane 2 gentle permselective membranes 3 NaBH is housed
4Among the container of catalyzer composition mixture.Among Fig. 2: the 1st, the hydrogen production well, this production well can outwards connect by pipe; 4 the expression be by NaBH
4Mixture with the catalyzer composition; The 5th, container receives by NaBH for preventing
4The mixture of forming with catalyzer absorbs that aqueous vapor expands and the space reserved; The 9th, the skeleton that a kind of silicon rubber, soft rubber or plastic working form, work to support water permselective membrane 2 gentle permselective membranes 3, when the gentle permselective membrane of water permselective membrane 23 by glue on water-absorbing material, prop up by this skeleton again, make the firm inboard that is fixed on water-absorbing material of water permselective membrane 2 gentle permselective membranes 3 energy; 6 are made up of poly tetrafluoroethylene among the figure, are to prevent by NaBH
4The mixture of forming with catalyzer inflow such as waste residue and cake mass or block the strainer of filtrations such as air outlet in reaction process can be effectively by NaBH
4The mixture of forming with catalyzer absorbs the aqueous vapor that adds; Water permselective membrane 2 gentle permselective membranes 3 by representing among the figure enter aqueous vapor NaBH are housed
4The mixture of forming with catalyzer reacts in fuel container, the hydrogen that reaction produces, and production well flows in power generation assembly or the hydrogen-storing device from figure.
As shown in Figure 3, a kind of built-up type produces the device of hydrogen, present embodiment is together in parallel the hydrogen formation apparatus of two groups, four groups, six groups even more embodiment 1 or embodiment 2, hydrogen is finally flowed out by a total air outlet 12, increase the flow of air feed like this, make this hydrogen formation apparatus can supply bigger usefulness device of air and power generation assembly.Among Fig. 3: the 12nd, total air outlet of hydrogen couples together the hydrogen production well 1 of several groups of hydrogen formation apparatus by several group interfaces, is summarized in a house steward, makes hydrogen can put together outflow, improves gas supply capacity and speed.
After the description of the present invention by specification sheets is disclosed out, it will be understood by the professional person in this field, same principle and the object that is not written in the specification sheets can be manufactured comes out, in addition, under the prerequisite of not leaving the principle of the invention, have the variation that many modifications come condition of compatibility and material; Therefore, the product of specification sheets explanation at present of the present invention is just a kind of as expected, and present invention includes any under this principle various forms of devices and directly with the method for this device production hydrogen.
Claims (10)
1. a device that produces hydrogen is characterized in that, this device comprises:
A) alternative fuel container by aqueous vapor,
B) this fuel container contains a kind of mixture, and this mixture is made up of a kind of hydride and at least a catalyzer at least,
C) on fuel container, have a hydrogen delivery port at least,
D) have a gas filter at least,
E) this fuel container has at least a face to be made up of following material: the material of the alternative permeate water of one deck and the alternative material that sees through gas of one deck at least at least,
F) water source;
Described hydride is selected from NaBH
4, LiAlH
4, LiBH
4, NaAlH
4, MgH
2, KBH
4In one or more;
Described catalyzer is selected from C
OCl
2
Described water source comprises moisture sponge.
2. a kind of device that produces hydrogen according to claim 1 is characterized in that described mixture is drying solid powder or particle, and this mixture has been filled 20%～95% volume of fuel container.
3. a kind of device that produces hydrogen according to claim 1 is characterized in that, the material of described alternative permeate water only allows aqueous vapor to pass through significantly, does not allow to comprise H
2, O
2, N
2, CO
2Gas pass through.
4. according to claim 1 or 3 described a kind of devices that produce hydrogen, it is characterized in that the material of described alternative permeate water is a kind of perfluoro sulfonic acid membrane or zylonite film.
5. a kind of device that produces hydrogen according to claim 1 is characterized in that, the material that described alternative sees through gas comprises the porous poly tetrafluoroethylene.
6. method of utilizing the described device of claim 1 to produce hydrogen is characterized in that this method comprises:
A) at least a hydride of preparation and at least a catalyst fines or granular mixture,
B) utilize the alternative face that sees through aqueous vapor that said mixture and water source are isolated,
C) allow aqueous vapor be penetrated into this side of hydride by the face that alternative sees through aqueous vapor, produce chemical reaction from the water source side,
D) from fuel container, collect hydrogen,
E) the wherein alternative face that sees through aqueous vapor by the material of the alternative permeate water of one deck at least and at least the alternative material of one deck through gas form.
7. a kind of method that produces hydrogen according to claim 6, it is characterized in that, described method has also comprised the generation speed of controlling hydrogen by the rate of permeation of control aqueous vapor, and wherein the control of the rate of permeation of aqueous vapor is to be realized with alternative thickness and the porosity that sees through the material of gas by the thickness of the material of regulating alternative permeate water.
8. a kind of method that produces hydrogen according to claim 6 is characterized in that, the material of alternative permeate water only allows aqueous vapor to pass through significantly in the described method, does not allow to comprise H
2, O
2, N
2, CO
2Gas pass through.
9. a kind of method that produces hydrogen according to claim 6 is characterized in that, the alternative material that sees through gas comprises the porous poly tetrafluoroethylene in the described method.
10. a kind of method that produces hydrogen according to claim 6 is characterized in that, described method has also further comprised by the sealed fuel container makes device stop to produce hydrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2005100309092A CN1958438B (en) | 2005-10-31 | 2005-10-31 | Device and method for producing hydrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2005100309092A CN1958438B (en) | 2005-10-31 | 2005-10-31 | Device and method for producing hydrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1958438A CN1958438A (en) | 2007-05-09 |
| CN1958438B true CN1958438B (en) | 2011-01-12 |
Family
ID=38070310
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2005100309092A Active CN1958438B (en) | 2005-10-31 | 2005-10-31 | Device and method for producing hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1958438B (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101565165B (en) * | 2008-04-24 | 2012-06-27 | 汉能科技有限公司 | Safe hydrogen preparing and purifying method for hydrogen generator |
| KR20150016492A (en) * | 2012-03-23 | 2015-02-12 | 인텔리전트 에너지, 인크. | Hydrogen producing fuel cartridge |
| EP2827977A4 (en) | 2012-03-23 | 2015-11-25 | Intelligent Energy Ltd | Hydrogen producing fuel cartridge and methods for producing hydrogen |
| EP3623808A1 (en) * | 2018-09-17 | 2020-03-18 | Seitz, Peter | Electrochemical sensor for the measurement of water content |
| CN109292946A (en) * | 2018-09-20 | 2019-02-01 | 中国人民解放军第二军医大学第二附属医院 | A kind of reverse osmosis membrane bag for helping to discharge hydrogen |
| CN110642223A (en) * | 2019-09-29 | 2020-01-03 | 武汉市能智达科技有限公司 | Compound hydrogen storage material composition and hydrogen production reactor composed of same |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4155712A (en) * | 1976-04-12 | 1979-05-22 | Taschek Walter G | Miniature hydrogen generator |
| US6645651B2 (en) * | 2001-06-01 | 2003-11-11 | Robert G. Hockaday | Fuel generator with diffusion ampoules for fuel cells |
| CN2890023Y (en) * | 2005-10-31 | 2007-04-18 | 上海清能燃料电池技术有限公司 | Hydrogen generating device |
-
2005
- 2005-10-31 CN CN2005100309092A patent/CN1958438B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4155712A (en) * | 1976-04-12 | 1979-05-22 | Taschek Walter G | Miniature hydrogen generator |
| US6645651B2 (en) * | 2001-06-01 | 2003-11-11 | Robert G. Hockaday | Fuel generator with diffusion ampoules for fuel cells |
| CN2890023Y (en) * | 2005-10-31 | 2007-04-18 | 上海清能燃料电池技术有限公司 | Hydrogen generating device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1958438A (en) | 2007-05-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US6645651B2 (en) | Fuel generator with diffusion ampoules for fuel cells | |
| US7393369B2 (en) | Apparatus, system, and method for generating hydrogen | |
| CN1958438B (en) | Device and method for producing hydrogen | |
| US8408246B2 (en) | Fuel cartridge for fuel cells | |
| CA2740591C (en) | Hydrogen-generating fuel cell cartridges | |
| KR101330058B1 (en) | Hydrogen generating fuel cell cartridges | |
| US7323148B2 (en) | Hydrogen generator | |
| JP5781940B2 (en) | Hydrogen generator with airgel catalyst | |
| BRPI0607603B1 (en) | gas generator apparatus, hydrogen generator system fuel, method for generating gas | |
| CN109708002A (en) | A kind of temperature compensation type alloy hydrogen storage hydrogen-feeding system | |
| CN2890023Y (en) | Hydrogen generating device | |
| CN101148249B (en) | On-site hydrogen producing method and on-site hydrogen producing device | |
| JP2008528438A (en) | Hydrogen generation system and method | |
| JP4371746B2 (en) | Hydrogen generation method and apparatus | |
| US20080274384A1 (en) | Self-regulating hydrogen generator for use with a fuel cell | |
| CN103552982B (en) | Sodium borohydride hydrolysis/alcoholysis hydrogen production reactor | |
| JP2005298302A (en) | Hydrogen cartridge and equipment | |
| CN101417787A (en) | Borohydride hydrogen making system | |
| CN113921855A (en) | Fuel cell power system and fuel cell electric ship | |
| CA2733865C (en) | Catalytic hydrogel | |
| CN201154896Y (en) | Hydrogen making system from borohydride | |
| CN101628709A (en) | Method and device for enabling gas generator to have universality | |
| MX2007010172A (en) | Hydrogen generating fuel cell cartridges |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HORIZON FUEL CELL TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: QINGNENG FUEL CELLS TECH CO., LTD., SHANGHAI Effective date: 20110512 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 200030 ROOM 705, NO. 1671, KAIXUAN ROAD, CHANGNING DISTRICT, SHANGHAI TO: ROOM 23, 4/F, BAIYANGGONG BUILDING, NO. 51, KEXUEYUAN ROAD, 2ND SCIENCE PARK, SINGAPORE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110512 Address after: Room 4, building 23, Aries palace, 51 science Road, Singapore Second Science Park Patentee after: Horizon Fuel Cell Technology Co., Ltd. Address before: 200030, room 1671, 705 triumph Road, Shanghai, Changning District Patentee before: Qingneng Fuel Cell Technology Co., Ltd., Shanghai |
|
| ASS | Succession or assignment of patent right |
Owner name: JIANGSU QINGNENG NEW ENERGY TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: HORIZON FUEL CELL TECHNOLOGIES CO., LTD. Effective date: 20110920 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; TO: 215600 SUZHOU, JIANGSU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110920 Address after: 3, building 215600, building C, 9 Guangdong Road, Zhangjiagang Free Trade Zone, Zhangjiagang, Jiangsu, Suzhou, China Patentee after: Jiangsu Qingneng New Energy Technology Co., Ltd. Address before: Room 4, building 23, Aries palace, 51 science Road, Singapore Second Science Park Patentee before: Horizon Fuel Cell Technology Co., Ltd. |
|
| CP03 | Change of name, title or address |
Address after: 215600 Jiangsu, Jiangsu, Suzhou Province, Zhangjiagang city free trade zone, new industry incubator, building 3, 302-309, room A, Jiangsu new energy technology Limited by Share Ltd Patentee after: Jiangsu qingneng new energy technology Limited by Share Ltd Address before: 215600 3 building, No. 9 Guangdong Road, Zhangjiagang Free Trade Zone, Zhangjiagang, Suzhou, Jiangsu, Zhangjiagang, China Patentee before: Jiangsu Qingneng New Energy Technology Co., Ltd. |
|
| CP03 | Change of name, title or address | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210402 Address after: Room 302-309, 3 / F, building a, emerging industry development center, Zhangjiagang Free Trade Zone, Suzhou City, Jiangsu Province Patentee after: JIANGSU HORIZON NEW ENERGY TECHNOLOGIES Co.,Ltd. Patentee after: Haisheng hydrogen Automobile Co.,Ltd. Address before: 215600 Jiangsu, Jiangsu, Suzhou Province, Zhangjiagang city free trade zone, new industry incubator, building 3, 302-309, room A, Jiangsu new energy technology Limited by Share Ltd Patentee before: JIANGSU HORIZON NEW ENERGY TECHNOLOGIES Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210901 Address after: 2 / F, building 2, No. 999, Shanlian Road, Baoshan District, Shanghai Patentee after: Shanghai qingneng horiz New Energy Technology Co., Ltd Patentee after: Haisheng hydrogen Automobile Co.,Ltd. Address before: Room 302-309, 3 / F, building a, emerging industry development center, Zhangjiagang Free Trade Zone, Suzhou City, Jiangsu Province Patentee before: JIANGSU HORIZON NEW ENERGY TECHNOLOGIES Co.,Ltd. Patentee before: Haisheng hydrogen Automobile Co.,Ltd. |
|
| TR01 | Transfer of patent right |