CN202575967U - Hydrogen-manufacturing device - Google Patents
Hydrogen-manufacturing device Download PDFInfo
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- CN202575967U CN202575967U CN 201220160857 CN201220160857U CN202575967U CN 202575967 U CN202575967 U CN 202575967U CN 201220160857 CN201220160857 CN 201220160857 CN 201220160857 U CN201220160857 U CN 201220160857U CN 202575967 U CN202575967 U CN 202575967U
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Abstract
The utility model discloses a hydrogen-manufacturing device, which comprises a liquid-storage container, a main hydrogen-manufacturing device, and one or a plurality of hydrogen-manufacturing sub-devices, wherein the hydrogen-manufacturing sub-devices are used as heating units of the main hydrogen-manufacturing device; hydrogen or/and residual gas manufactured by the hydrogen-manufacturing sub-devices is or are used as initial startup energy for the main hydrogen-manufacturing device; when the hydrogen or/and the residual gas manufactured by the hydrogen-manufacturing sub-devices reaches or reach the preset amount, the main hydrogen-manufacturing device is started up; and subsequently, hydrogen or/and residual gas manufactured by the main hydrogen-manufacturing device keeps or keep the main hydrogen-manufacturing device running. According to the hydrogen-manufacturing device provided by the utility model, the hydrogen-manufacturing sub-devices are additionally arranged to manufacture a certain amount of hydrogen, and the hydrogen is burnt to be used as a startup heating source for the main hydrogen-manufacturing device; the hydrogen manufactured by the main hydrogen-manufacturing device is used as a running heating source for the main hydrogen-manufacturing device; and therefore, the hydrogen-manufacturing device provided by the utility model can be started up and run normally simply with a low-power motor, so as to guarantee the miniaturization and the mobility of the device.
Description
Technical field
The utility model belongs to technical field of hydrogen preparation, relates to a kind of hydrogen producer, relates in particular to a kind of hydrogen producer that needs low-power machine; Simultaneously, the utility model also relates to the hydrogen production process of above-mentioned hydrogen producer.
Background technology
In numerous new forms of energy, Hydrogen Energy will become the optimal energy of 21 century.This be because, under the situation of coal, gasoline and hydrogen of burning identical weight, the most energy that hydrogen produces, and its incendiary product is water, do not have lime-ash and waste gas, do not pollute the environment; And coal and oil combustion generate is carbonic acid gas and sulfurous gas, can produce Greenhouse effect and acid rain respectively.Coal and reserves are limited, and hydrogen mainly is stored in the water, and the unique product in burning back also is a water, can produce hydrogen continuously, uses up never.
Hydrogen is a kind of colourless gas.Burning one gram Hydrogen Energy discharges your heat of 142 kilojoules, is 3 times of gasoline thermal value.The weight of hydrogen is light especially, and it has all gently been howed than gasoline, Sweet natural gas, kerosene, thereby carries, transports conveniently, is the only fuel of the high-speed flight vehicles such as space flight, aviation.Hydrogen can burn in oxygen, and the temperature of hydrogen flame can be up to 2500 ℃, thereby people's hydrogen cutting commonly used or weldsteel iron material.
In the Nature, the distribution of hydrogen is very extensive.Water is exactly big " warehouse " of hydrogen, wherein contains 11% hydrogen.There is 1.5% hydrogen the earth Rio; All contain hydrogen in the oil, coal, Sweet natural gas, animal and plant body etc.The main body of hydrogen is that the form with compound water exists, and earth surface about 70% is covered by water, and moisture storage capacity is very big, therefore we can say that hydrogen is the energy of " inexhaustible, nexhaustible ".If can from water, produce hydrogen with suitable method, hydrogen also will be the quite cheap energy of a kind of price so.
Having many uses of hydrogen, suitability is strong.It can not only be used as fuel, and metal hydride has the function that chemical energy, heat energy and mechanical energy are changed each other.For example, hydrogen storage metal has inhales hydrogen heat release and the ability of absorbing heat and putting hydrogen, can heat be stored, and uses as heating and air-conditioning in the room.
Hydrogen at first is used on the automobile as geseous fuel.In May, 1976, the U.S. develops a kind of automobile of making fuel with hydrogen; Afterwards, Japan also to succeed in developing a kind of be the automobile of fuel with the liquid hydrogen; In the latter stage seventies, the Mercedes of preceding Germany tests hydrogen, and they have only used five kg of hydrogen, has just made running car 110 kilometers.
, not only clean with hydrogen as automobile fuel, start easily at low temperatures, and little the corrosive nature of mover, can prolong the work-ing life of mover.Because hydrogen and air can uniform mixing, can save vaporizer used on the general automobile fully, thereby can simplify the structure that has automobile now.More interesting is to need only the hydrogen of adding 4% in gasoline.Use it as motor car engine fuel, but just fuel-economizing 40%, and need not petrol engine is done great improvement.
Hydrogen is easy to become liquid under certain pressure and temperature, thereby it is all very convenient with iron flask car, on-highway tractor or ship transportation.Liquid hydrogen both can be used as the fuel of automobile, aircraft, also can be used as the fuel of rocket, guided missile.The fly to Apollo Personnel investigation Program of the moon of the U.S. " Long March launch vehicle that number spaceship and China launch a man-made satellite., all make fuel with liquid hydrogen.
In addition, use hydrogen-hydrogen fuel cell directly to change into electric energy to Hydrogen Energy, make utilizing of Hydrogen Energy more convenient.At present, this fuel cell has obtained using on spaceship and undersea boat, and effect is pretty good.Certainly, because cost is higher, also be difficult to generally use for the moment.
The YO of hydrogen is about 3,600 ten thousand tons in the world now, and wherein the overwhelming majority is produced from oil, coal and Sweet natural gas, and this must consume original just mineral fuel very in short supply; The hydrogen that other has 4% is to produce with the method for brine electrolysis, but the electric energy that consumes is too many, does not calculate very much, and therefore, people are trying to explore to study the hydrogen manufacturing novel method.And can reduce the energy consumption in the Chemical Manufacture and reduce cost with methyl alcohol, water reformation hydrogen production, be expected to substitute the technology of " water electrolysis hydrogen production " that be called as electricity-eating tiger, utilize advanced methanol vapor to reform---pressure swing adsorption is produced pure hydrogen and is rich in CO
2Mixed gas, through further aftertreatment, can obtain hydrogen and carbon dioxide gas simultaneously.
Methyl alcohol and water vapour pass through catalyzer under certain temperature, pressure condition; Under the effect of catalyzer; The transformationreation of methanol decomposition reaction and carbon monoxide takes place, generate hydrogen and carbonic acid gas, this is the gas solid catalytic reaction system of component more than, many reactions.Reactional equation is following:
CH
3OH→CO+2H
2 (1)
H
2O+CO→CO
2+H
2 (2)
CH
3OH+H
2O→CO
2+3H
2 (3)
The H that reforming reaction generates
2And CO
2, pass through pressure swing adsorption process (PSA) or palladium membrane sepn again with H
2And CO
2Separate, obtain high-purity hydrogen.The power consumption of pressure swing adsorption process is high, equipment is big, and is not suitable for small-scale Preparation of Hydrogen.
In addition, existing hydrogen producing apparatus needs powerful motor in order to let device start, and more than 3000KW (as shown in Figure 1) usually, only motor just need take a large amount of spaces, and the equipment that makes can't miniaturized, and movability is also very poor.
The utility model content
The utility model technical problem to be solved is: a kind of hydrogen producer is provided, only needs low-power machine can guarantee the normal operation of equipment.
In addition, the utility model also provides the hydrogen production process of above-mentioned hydrogen producer, only needs low-power machine can guarantee the normal operation of equipment.
For solving the problems of the technologies described above, the utility model adopts following technical scheme:
A kind of hydrogen producer, said hydrogen producer comprise liquid container, main hydrogen producer, sub-hydrogen producer;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is passed through the initial start heating source of burning as main hydrogen producer; The hydrogen partial that main hydrogen producer makes is or/and residual air is kept main hydrogen producer operation through burning;
Said sub-hydrogen producer comprises: low-power machine, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber; Said liquid container, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber connect through pipeline successively;
Said low-power machine is in order to satisfy the environmental parameter of sub-vaporizer, sub-reformer chamber, sub-separate chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling, sub-separate chamber separates; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat;
Said main hydrogen producer comprises: interchanger, vaporizer, reformer chamber, separate chamber; Said liquid container, interchanger, vaporizer, reformer chamber, separate chamber connect through pipeline successively;
First alcohol and water in the said liquid container is delivered to the interchanger heat exchange through e Foerderanlage, and interchanger is connected through pipeline with vaporizer; Vaporizer is connected through pipeline with reformer chamber, and reformer chamber is provided with catalyzer;
Transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber;
Be provided with membrane separation apparatus in the said separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
A kind of hydrogen producer, said hydrogen producer comprise liquid container, main hydrogen producer, one or more sub-hydrogen producer; Said sub-hydrogen producer is as the heating unit of main hydrogen producer;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is connected to main hydrogen producer through pipeline, as the initial start energy of main hydrogen producer; The hydrogen partial that main hydrogen producer makes is kept main hydrogen producer operation or/and residual air is connected to main hydrogen producer through pipeline.
As a kind of preferred version of the utility model, said hydrogen producer comprises the plurality of sub hydrogen producer, comprise the first sub-hydrogen producer, the second sub-hydrogen producer, the 3rd sub-hydrogen producer ..., the sub-hydrogen producer of N, each sub-hydrogen producer is connected successively; The hydrogen manufacturing amount of each sub-hydrogen producer unit time becomes big successively;
The first sub-hydrogen producer is as the heating unit of the second sub-hydrogen producer, and the sub-hydrogen producer of i is as the heating unit of i+1 hydrogen producer, and the sub-hydrogen producer of N is as the heating unit of main hydrogen producer; Wherein, i is an integer, 1 <i < N.
As a kind of preferred version of the utility model, said hydrogen producer comprises the plurality of sub hydrogen producer, and the parallel connection of parton hydrogen producer is provided with.
As a kind of preferred version of the utility model, said sub-hydrogen producer comprises low-power machine, sub-reformer chamber, and said sub-reformer chamber is the small-scale reformer chamber, and the hydrogen manufacturing amount of sub-hydrogen producer unit time is less than the hydrogen manufacturing amount of main hydrogen producer time;
Said low-power machine is in order to satisfy the environmental parameter of sub-reformer chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat.
As a kind of preferred version of the utility model, said sub-hydrogen producer comprises: low-power machine, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber; Said liquid container, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber connect through pipeline successively;
Said low-power machine is in order to satisfy the environmental parameter of sub-vaporizer, sub-reformer chamber, sub-separate chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling, sub-separate chamber separates; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat.
As a kind of preferred version of the utility model, said main hydrogen producer comprises: interchanger, vaporizer, reformer chamber, separate chamber; Said liquid container, interchanger, vaporizer, reformer chamber, separate chamber connect through pipeline successively;
First alcohol and water in the said liquid container is delivered to the interchanger heat exchange through e Foerderanlage, and interchanger is connected through pipeline with vaporizer; Vaporizer is connected through pipeline with reformer chamber, and reformer chamber is provided with catalyzer;
Transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber;
Be provided with membrane separation apparatus in the separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
As a kind of preferred version of the utility model, said main hydrogen producer comprises the energy utilization unit,, supplies main hydrogen producer to start or keeps operation or/and the residual air generate energy in order to utilize hydrogen that sub-hydrogen producer, main hydrogen producer make;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is connected to said energy utilization unit through pipeline, as the initial start energy of main hydrogen producer; The hydrogen partial that main hydrogen producer makes is kept main hydrogen producer operation or/and residual air is connected to the energy utilization unit through pipeline.
The beneficial effect of the utility model is: hydrogen producer and hydrogen production process thereof that the utility model proposes prepare certain hydrogen through increasing sub-hydrogen producer, with the startup heating source of this hydrogen partial (can also comprise residual air) burning as main hydrogen producer; The hydrogen that then makes through main hydrogen producer (can also comprise residual air) is as the operation heating source of main hydrogen producer.Therefore, the utility model hydrogen producer only needs low-power machine (like 30W) can guarantee the normal startup and the operation of equipment, thereby can guarantee the miniaturized and the movability of equipment.
Description of drawings
Fig. 1 forms synoptic diagram for the part of existing hydrogen producer.
Fig. 2 is that the part of the utility model hydrogen producer is formed synoptic diagram.
Fig. 3 is the startup schematic diagram of the utility model hydrogen producer.
Fig. 4 is the startup schematic diagram of the utility model hydrogen producer among the embodiment two.
Fig. 5 is the startup schematic diagram of the utility model hydrogen producer among the embodiment three.
Embodiment
Specify the preferred embodiment of the utility model below in conjunction with accompanying drawing.
Embodiment one
See also Fig. 2, the utility model has disclosed a kind of hydrogen producer, and said hydrogen producer comprises liquid container 10, main hydrogen producer 30, sub-hydrogen producer 20.
The hydrogen that said sub-hydrogen producer 20 makes or/and residual air through burning as the initial start heating source of main hydrogen producer 30, the hydrogen that group hydrogen producer 20 makes is or/and residual air when satisfying set amount, starts main hydrogen producer 30; After this, the hydrogen that makes of main hydrogen producer 30 is or/and residual air is kept main hydrogen producer operation through burning.
Said main hydrogen producer 30 can comprise the energy utilization unit,, supplies main hydrogen producer 30 to start or keeps operation or/and the residual air generate energy in order to utilize hydrogen that sub-hydrogen producer 20, main hydrogen producer 30 make.The hydrogen that said sub-hydrogen producer 20 makes is or/and residual air is connected to said energy utilization unit through pipeline, as the initial start energy of main hydrogen producer 30; The hydrogen partial that main hydrogen producer 30 makes is kept main hydrogen producer operation or/and residual air is connected to the energy utilization unit through pipeline.
Said sub-hydrogen producer comprises: low-power machine, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber; Said liquid container, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber connect through pipeline successively.Said low-power machine is in order to satisfy the environmental parameter of sub-vaporizer, sub-reformer chamber, sub-separate chamber; As shown in Figure 3, low-power machine only needs 30W to satisfy the demand usually, can be with hydrogen that makes and residual air storage, like storage 5m
3First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation after treatment, sub-separate chamber separates (also can not carry out lock out operation); With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat.
In the present embodiment, said main hydrogen producer comprises: interchanger, vaporizer, reformer chamber, separate chamber; Said liquid container, interchanger, vaporizer, reformer chamber, separate chamber connect successively through pipeline and (are connected through pipeline with vaporizer like interchanger; Vaporizer is connected through pipeline with reformer chamber).First alcohol and water in the said liquid container is delivered to the interchanger heat exchange through e Foerderanlage, gets into the vaporizer gasification after the heat exchange.Methanol vapor after the gasification and water vapour get into reformer chamber, and reformer chamber is provided with catalyzer, and the temperature of reformer chamber is 280 °-409 °.Transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber.Temperature in the said separate chamber is set at 400 °-460 °; Be provided with membrane separation apparatus in the separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
More than introduced the composition of the utility model hydrogen producer, the utility model also discloses a kind of hydrogen production process of above-mentioned hydrogen producer when disclosing aforesaid device.Said method comprises the steps: that the promotor hydrogen producer prepares hydrogen, and the hydrogen that sub-hydrogen producer makes is or/and residual air, as the initial start energy of main hydrogen producer.The hydrogen that the group hydrogen producer makes is or/and residual air when satisfying set amount, starts main hydrogen producer, and main hydrogen producer prepares hydrogen.The hydrogen partial that main hydrogen producer makes is or/and residual air is kept main hydrogen producer operation.
Wherein, the hydrogen manufacturing step of said sub-hydrogen producer comprises:
Step S11: the first alcohol and water is delivered to sub-interchanger heat exchange through e Foerderanlage, gets into sub-vaporizer gasification after the heat exchange;
Step S12: methanol vapor after the gasification and water vapour get into sub-reformer chamber, and sub-reformer chamber is provided with catalyzer, and the temperature of sub-reformer chamber is 280 °-409 °;
Step S13: the transmission passage between sub-reformer chamber and the sub-separate chamber is through a sub-preheating temperature-controlling mechanism, and this sub-preheating temperature-controlling mechanism is in order to the gas of heating from sub-reformer chamber output; Said sub-preheating temperature-controlling mechanism is as the buffering between sub-reformer chamber and the sub-separate chamber, makes from the temperature of the gas of sub-reformer chamber output identical or approaching with the temperature of sub-separate chamber;
Step S14: the temperature in the said sub-separate chamber is set at 400 °-460 °; Be provided with sub-membrane separation apparatus in the sub-separate chamber, obtain hydrogen from the aerogenesis end of sub-membrane separation apparatus.
The hydrogen manufacturing step of said main hydrogen producer comprises the steps:
Step S21: the first alcohol and water is delivered to the interchanger heat exchange through e Foerderanlage, gets into the vaporizer gasification after the heat exchange;
Step S22: methanol vapor after the gasification and water vapour get into reformer chamber, and reformer chamber is provided with catalyzer, and the temperature of reformer chamber is 280 °-409 °;
Step S23: the transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber;
Step S24: the temperature in the said separate chamber is set at 400 °-460 °; Be provided with membrane separation apparatus in the separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
Embodiment two
See also Fig. 4, in the present embodiment, said hydrogen producer comprises the plurality of sub hydrogen producer, comprise the first sub-hydrogen producer, the second sub-hydrogen producer, the 3rd sub-hydrogen producer ..., the sub-hydrogen producer of N, each sub-hydrogen producer is connected successively; The hydrogen manufacturing amount of each sub-hydrogen producer unit time becomes big successively.
The first sub-hydrogen producer is as the heating unit of the second sub-hydrogen producer, and the sub-hydrogen producer of i is as the heating unit of i+1 hydrogen producer, and the sub-hydrogen producer of N is as the heating unit of main hydrogen producer; Wherein, i is an integer, 1 <i < N.
Embodiment three
See also Fig. 5, in the present embodiment, said hydrogen producer comprises the plurality of sub hydrogen producer, and the parallel connection of parton hydrogen producer is provided with.
In sum, hydrogen producer and hydrogen production process thereof that the utility model proposes prepare certain hydrogen through increasing sub-hydrogen producer, with the startup heating source of this hydrogen partial (can also comprise residual air) burning as main hydrogen producer; The hydrogen that then makes through main hydrogen producer (can also comprise residual air) is as the operation heating source of main hydrogen producer.Therefore, the utility model hydrogen producer only needs low-power machine (like 30W) can guarantee the normal startup and the operation of equipment, thereby can guarantee the miniaturized and the movability of equipment.
Here description of the utility model and application is illustrative, is not to want the scope of the utility model is limited in the above-described embodiments.Here the distortion of the embodiment that is disclosed and change are possible, and the replacement of embodiment is known with the various parts of equivalence for those those of ordinary skill in the art.Those skilled in the art are noted that under the situation of spirit that does not break away from the utility model or essential characteristic, and the utility model can be with other form, structure, layout, ratio, and realize with other assembly, material and parts.Under the situation that does not break away from the utility model scope and spirit, can carry out other distortion and change here to the embodiment that is disclosed.
Claims (8)
1. a hydrogen producer is characterized in that, said hydrogen producer comprises liquid container, main hydrogen producer, sub-hydrogen producer;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is passed through the initial start heating source of burning as main hydrogen producer; The hydrogen partial that main hydrogen producer makes is or/and residual air is kept main hydrogen producer operation through burning;
Said sub-hydrogen producer comprises: low-power machine, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber; Said liquid container, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber connect through pipeline successively;
Said low-power machine is in order to satisfy the environmental parameter of sub-vaporizer, sub-reformer chamber, sub-separate chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling, sub-separate chamber separates; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat;
Said main hydrogen producer comprises: interchanger, vaporizer, reformer chamber, separate chamber; Said liquid container, interchanger, vaporizer, reformer chamber, separate chamber connect through pipeline successively;
First alcohol and water in the said liquid container is delivered to the interchanger heat exchange through e Foerderanlage, and interchanger is connected through pipeline with vaporizer; Vaporizer is connected through pipeline with reformer chamber, and reformer chamber is provided with catalyzer;
Transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber;
Be provided with membrane separation apparatus in the said separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
2. a hydrogen producer is characterized in that, said hydrogen producer comprises liquid container, main hydrogen producer, one or more sub-hydrogen producer; Said sub-hydrogen producer is as the heating unit of main hydrogen producer;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is connected to main hydrogen producer through pipeline, as the initial start energy of main hydrogen producer; The hydrogen partial that main hydrogen producer makes is kept main hydrogen producer operation or/and residual air is connected to main hydrogen producer through pipeline.
3. hydrogen producer according to claim 2 is characterized in that:
Said hydrogen producer comprises the plurality of sub hydrogen producer, comprise the first sub-hydrogen producer, the second sub-hydrogen producer, the 3rd sub-hydrogen producer ..., the sub-hydrogen producer of N, each sub-hydrogen producer is connected successively; The hydrogen manufacturing amount of each sub-hydrogen producer unit time becomes big successively;
The first sub-hydrogen producer is as the heating unit of the second sub-hydrogen producer, and the sub-hydrogen producer of i is as the heating unit of i+1 hydrogen producer, and the sub-hydrogen producer of N is as the heating unit of main hydrogen producer; Wherein, i is an integer, 1＜i＜N.
4. according to claim 2 or 3 described hydrogen producers, it is characterized in that:
Said hydrogen producer comprises the plurality of sub hydrogen producer, and the parallel connection of parton hydrogen producer is provided with.
5. hydrogen producer according to claim 2 is characterized in that:
Said sub-hydrogen producer comprises low-power machine, sub-reformer chamber, and said sub-reformer chamber is the small-scale reformer chamber, and the hydrogen manufacturing amount of sub-hydrogen producer unit time is less than the hydrogen manufacturing amount of main hydrogen producer time;
Said low-power machine is in order to satisfy the environmental parameter of sub-reformer chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat.
6. hydrogen producer according to claim 2 is characterized in that:
Said sub-hydrogen producer comprises: low-power machine, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber; Said liquid container, sub-interchanger, sub-vaporizer, sub-reformer chamber, sub-separate chamber connect through pipeline successively;
Said low-power machine is in order to satisfy the environmental parameter of sub-vaporizer, sub-reformer chamber, sub-separate chamber; First alcohol and water in the liquid container is delivered to sub-reformer chamber reformation through handling, sub-separate chamber separates; With hydrogen that makes and residual air burning, be that the element that main hydrogen producer need heat provides heat.
7. hydrogen producer according to claim 2 is characterized in that:
Said main hydrogen producer comprises: interchanger, vaporizer, reformer chamber, separate chamber; Said liquid container, interchanger, vaporizer, reformer chamber, separate chamber connect through pipeline successively;
First alcohol and water in the said liquid container is delivered to the interchanger heat exchange through e Foerderanlage, and interchanger is connected through pipeline with vaporizer; Vaporizer is connected through pipeline with reformer chamber, and reformer chamber is provided with catalyzer;
Transmission passage between reformer chamber and the separate chamber is through a preheating temperature-controlling mechanism, and this preheating temperature-controlling mechanism is in order to the gas of heating from reformer chamber output; Said preheating temperature-controlling mechanism is as the buffering between reformer chamber and the separate chamber, makes from the temperature of the gas of reformer chamber output identical or approaching with the temperature of separate chamber;
Be provided with membrane separation apparatus in the separate chamber, obtain hydrogen from the aerogenesis end of membrane separation apparatus.
8. hydrogen producer according to claim 2 is characterized in that:
Said main hydrogen producer comprises the energy utilization unit,, supplies main hydrogen producer to start or keeps operation or/and the residual air generate energy in order to utilize hydrogen that sub-hydrogen producer, main hydrogen producer make;
The hydrogen that said sub-hydrogen producer makes is or/and residual air is connected to said energy utilization unit through pipeline, as the initial start energy of main hydrogen producer; The hydrogen partial that main hydrogen producer makes is kept main hydrogen producer operation or/and residual air is connected to the energy utilization unit through pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220160857 CN202575967U (en) | 2012-04-16 | 2012-04-16 | Hydrogen-manufacturing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220160857 CN202575967U (en) | 2012-04-16 | 2012-04-16 | Hydrogen-manufacturing device |
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| Publication Number | Publication Date |
|---|---|
| CN202575967U true CN202575967U (en) | 2012-12-05 |
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|---|---|---|---|
| CN 201220160857 Withdrawn - After Issue CN202575967U (en) | 2012-04-16 | 2012-04-16 | Hydrogen-manufacturing device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102849679A (en) * | 2012-04-16 | 2013-01-02 | 洁星环保科技投资（上海）有限公司 | Hydrogen-producing device and hydrogen-producing method thereof |
| CN103058137A (en) * | 2012-12-21 | 2013-04-24 | 上海合既得动氢机器有限公司 | Movable type methanol water hydrogen manufacturing system and method |
| CN108264020A (en) * | 2018-02-06 | 2018-07-10 | 吴波挺 | A kind of water-gas hydrogen producer |
-
2012
- 2012-04-16 CN CN 201220160857 patent/CN202575967U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102849679A (en) * | 2012-04-16 | 2013-01-02 | 洁星环保科技投资（上海）有限公司 | Hydrogen-producing device and hydrogen-producing method thereof |
| CN103058137A (en) * | 2012-12-21 | 2013-04-24 | 上海合既得动氢机器有限公司 | Movable type methanol water hydrogen manufacturing system and method |
| CN103058137B (en) * | 2012-12-21 | 2015-02-25 | 上海合既得动氢机器有限公司 | Movable type methanol water hydrogen manufacturing system and method |
| CN108264020A (en) * | 2018-02-06 | 2018-07-10 | 吴波挺 | A kind of water-gas hydrogen producer |
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