CN101209816A - Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique - Google Patents
Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique Download PDFInfo
- Publication number
- CN101209816A CN101209816A CNA200610135127XA CN200610135127A CN101209816A CN 101209816 A CN101209816 A CN 101209816A CN A200610135127X A CNA200610135127X A CN A200610135127XA CN 200610135127 A CN200610135127 A CN 200610135127A CN 101209816 A CN101209816 A CN 101209816A
- Authority
- CN
- China
- Prior art keywords
- hydrogen
- carbon composite
- arc light
- general fuel
- electrode
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
The invention relates to a manufacturing device for manufacturing hydrogen by an arc hydrogen carbon composite universal fuel and the technique thereof, which includes a rectifier control device, an arc hydrogen carbon composite universal fuel reactor, and an electrode control device, a condensing device, a slag discharge device and a filtering device of the arc hydrogen carbon composite universal fuel reactor; the devices are all arranged in a shell, and a power supply is connected to the two electrodes in the arc hydrogen carbon composite universal fuel reactor through the rectifier control device. The two electrodes of the arc hydrogen carbon composite universal fuel reactor respectively adopt a carbon electrode and a tungsten electrode. The two electrodes are connected with the electrode control device which adjusts the distance of the discharging ends of the two electrodes. A water inlet and a water outlet on the arc hydrogen carbon composite universal fuel reactor are connected with a water inlet tube and a water outlet tube through a pipeline. The air outlet of the arc hydrogen carbon composite universal fuel reactor is connected with the air inlet of the condensing device. The air outlet of the condensing device is connected to a lower pressure storage device after being processed by the filtering device. An air consumption opening for supplying air to the outside is arranged on the lower pressure storage device.
Description
Technical field
The present invention relates to a kind of arc light hydrogen carbon composite general fuel and get hydrogen production equipment and technology, particularly a kind ofly produce out hydrogen H with arc light under water at the nonequilibrium situations plasma reaction
2The equipment of carbon monoxide and carbonic acid gas and technology both were called (ArcH
2C) arc light hydrogen carbon composite general fuel, (ArcH simultaneously
2C) arc light hydrogen carbon composite general fuel is got hydrogen, belongs to the manufacturing field of hydrogen fuel.
Background technology
Growing tension along with existing traditional energy, people intensive recognize the traditional energy that must adopt a kind of new energy substitution to use at present, image-stone oil, Sweet natural gas, coal etc., the hydrogen fuel of countries in the world focus development are to clean, efficiently to reach the abundant and celebrated new forms of energy of reserves.But all there are defective in various degree in hydrogen producer that adopts and hydrogen manufacturing mode at present, filter the method for hydrogen etc. as natural gas hydrogen preparation, coal hydrogen manufacturing or various membrane sepn, the equipment of these methods and employing exists cost height, output little, so the effect of promoting is bad, industrialization degree is not high.
Summary of the invention
Goal of the invention: the invention provides a kind of arc light hydrogen carbon composite general fuel and get hydrogen production equipment and technology, it is little to produce the problem output that the technology of hydrogen occurs, the problem that aspects such as effect is bad, cost height exist.
Technical scheme: the present invention is achieved through the following technical solutions:
A kind of arc light hydrogen carbon composite general fuel is got hydrogen production equipment, it is characterized in that: this producing apparatus comprises that rectifier control device, arc light hydrogen carbon composite general fuel get hydrogen reactor, arc light hydrogen carbon composite general fuel and get electrode control device, condensing works, slag discharging device and the filtration unit that hydrogen reactor, arc light hydrogen carbon composite general fuel are got hydrogen; They all are arranged in the casing, power supply is connected to arc light hydrogen carbon composite general fuel through rectifier control device and gets on two electrodes in the hydrogen reactor, the electrode that arc light hydrogen carbon composite general fuel is got hydrogen reactor adopts carbon dioxide process carbon electrode, another electrode adopts tungsten electrode, and two electrodes are connected with the electrode control device of adjusting their discharge end distances; The entery and delivery port that arc light hydrogen carbon composite general fuel is got on the hydrogen reactor is connected with inlet pipe, drain pipe by pipeline, the air outlet that arc light hydrogen carbon composite general fuel is got hydrogen reactor is connected with the inlet mouth of condensing works, the air outlet of condensing works is connected on the low pressure storing unit after installing processing after filtration, and the low pressure storing unit is provided with the gas port of using of outside supply gas; The slag-drip opening that arc light hydrogen carbon composite general fuel is got hydrogen reactor is connected with slag discharging device.
Described arc light hydrogen carbon composite general fuel is got hydrogen reactor mainly by carbon dioxide process carbon electrode, tungsten electrode or two carbon electricity level work resistor R L
1And RL
2And reactor body constitutes; Carbon dioxide process carbon electrode adopts the carbon electrode that closely contacts with its inner chamber is set in the copper saddle, the discharge end of carbon dioxide process carbon electrode and tungsten electrode is oppositely arranged as producing the electric arc end, the inner container of reactor body for dress water, the arc-over end of two electrodes is arranged in the reactor body, carbon dioxide process carbon electrode is connected with the electric output terminal of rectifier control device, and tungsten electrode is by working resistance device RL in parallel
1And RL
2The other end of exporting with the electricity of rectifier control device is connected.
Described rectifier control device is made of electrical power control cabinet and rectifier, and electrical source of power is connected with rectifier by electrical power control cabinet, and the electric output terminal of rectifier is connected with two electrodes in arc light hydrogen carbon composite general fuel is got the reactor of hydrogen respectively.
Described condensing works is a cooling driers.
Described filtration unit is arranged in the low pressure compressor, and the air outlet of filtration unit is connected with low pressure gasholder as the low pressure storing unit, and low pressure gasholder is provided with the gas port of using from combustion gas to the outside that supply with.
A kind of arc light hydrogen carbon composite general fuel is got hydrogen production technology, it is characterized in that: utilize above-mentioned equipment, prepare general arc light hydrogen carbon composite general fuel by following step and get hydrogen: a, arc light hydrogen carbon composite general fuel in the equipment is got hydrogen reactor elder generation nitrogen injection, after vacuumizing for 3 times then, extract residue nitrogen again out after injecting full box water, two electrodes in it are imbedded reached 0.4～0.6 meter under water, and by two electrode application voltage of rectifier control device, adjust two electrodes by electrode control device simultaneously, make and form 90 degree～45 degree between their corresponding point, the distance to 1 of two electrode discharge ends～3mm, make two electrodes form arc discharge, produce the plasma reaction under the nonequilibrium situations under water;
B, the arc light hydrogen carbon composite general fuel combustion gas bubble that generates when collecting reaction make them deliver to cooling drying removal moisture in the condensing works by transfer line, extract arc light hydrogen carbon composite general fuel;
C, the arc light hydrogen carbon composite general fuel that obtains among the step b installed filtration after filtration after, in the input low pressure storing unit, promptly obtain arc light hydrogen carbon composite general fuel;
It is to leach CO with the carbon molecular film earlier in filtration unit that device after filtration described in d, the above-mentioned steps c filters
2, CO and impurity composition, remaining arc light hydrogen carbon composite general fuel becomes pure hydrogen after with the palladium metal membrane filtration, handles the back through low pressure compressor again and exports.
Advantage and effect: by the enforcement of technical solution of the present invention, produce the effective, easy to operate of hydrogen, cost is low, is the cost 1/10 of making hydrogen at present, ArcH of the present invention
2One interior at two electrodes of reactor that the C arc light hydrogen carbon composite general fuel is got hydrogen adopt carbon dioxide process carbon electrode, and another adopts tungsten electrode, and arc light with water is being the arc light that working medium produces with megahertz level radio-frequency power supply.The plasma decomposition reaction occurs bubble is collected the hydrogen artificial fuel gas, adopt the porpezite film to divide filter, the pure hydrogen of output then.Be the most effective hydrogen mode of producing, be fit to suitability for industrialized production.
The arc light hydrogen carbon composite general fuel ArcH that utilizes present device and technology to make
2It is 1/10th of common traditional hydrogen manufacturing cost that C gets hydrogen, and can provide super large tolerance to use, and has possessed the requirement that following electric power, power, automobile etc. use.Water, carbon are common materials, and reserves are very abundant, and the convenience of drawing materials also has a large amount of raw material supplies.Therefore, the present invention has opened up new hydrogen production equipment and the technology produced.
Description of drawings
Fig. 1 is that the syndeton synoptic diagram is respectively installed in present device inside;
Fig. 2 is the structural representation that arc light hydrogen carbon composite general fuel of the present invention is got hydrogen reactor.
Embodiment
As follows below in conjunction with accompanying drawing to the detailed description of the invention, but not because of following specific embodiment restriction the present invention.
Among the figure: 1, power supply, 2, rectifier control device, 3, arc light hydrogen carbon composite general fuel gets hydrogen reactor, 4, electrode control device, 5, carbon dioxide process carbon electrode, 6, tungsten electrode, 7, condensing works, 8, filtration unit, 9, the low pressure storing unit, 10, casing.21, reactor body, the arc-over end of 22, two electrodes.
Embodiment 1:
As shown in Figure 1, the present invention is a kind of arc light hydrogen carbon composite general fuel ArcH
2C gets hydrogen production equipment and utilizes the technology of this device fabrication universal fuel, and this producing apparatus comprises that rectifier control device 2, arc light hydrogen carbon composite general fuel get electrode control device 4, condensing works 7, slag discharging device and the filtration unit 8 of the reactor 3 that the reactor 3 of hydrogen, arc light hydrogen carbon composite general fuel get hydrogen; They all are arranged in the casing 10, power supply 1 is connected to arc light hydrogen carbon composite general fuel through rectifier control device 2 and gets on two electrodes 5,6 in the hydrogen reactor 3, the electrode 5 that arc light hydrogen carbon composite general fuel is got the reactor 3 of hydrogen adopts carbon dioxide process carbon electrode, another electrode 6 adopts tungsten electrode, and two electrodes 5,6 are connected with the electrode control device 4 of adjusting their discharge end distances; The entery and delivery port that arc light hydrogen carbon composite general fuel is got on the hydrogen reactor 3 is connected with inlet pipe, drain pipe by pipeline, the air outlet that arc light hydrogen carbon composite general fuel is got hydrogen reactor 3 is connected with the inlet mouth of condensing works 7, the air outlet of condensing works 7 is connected to low pressure storing unit 9 after installing 8 processing after filtration, and low pressure storing unit 9 is provided with the gas port of using of outside supply gas; The slag-drip opening that arc light hydrogen carbon composite general fuel is got the reactor 3 of hydrogen is connected with slag discharging device.
As shown in Figure 2, described arc light hydrogen carbon composite general fuel is got the reactor 3 of hydrogen mainly by carbon dioxide process carbon electrode 5, tungsten electrode 6, working resistance device RL
1And RL
2And reactor body 21 constitutes; Carbon dioxide process carbon electrode 5 adopts the carbon electrode that closely contacts with its inner chamber is set in the copper saddle, carbon dioxide process carbon electrode 5 is oppositely arranged as producing electric arc end 22 with the discharge end of tungsten electrode 6, reactor body 21 inner containers for dress water, it is interior under water that the arc-over end of two electrodes is arranged on container, carbon dioxide process carbon electrode is connected with the electric output terminal of rectifier control device 2, and tungsten electrode is by working resistance device RL in parallel
1And RL
2The other end of exporting with the electricity of rectifier control device 2 is connected.
In invention, adopted tungsten as an electrode for the plasma arc length 1mm～3mm that extends, if as equipment two electrodes all adopt carbon dioxide process carbon electrode, produce a kind of shell so between the carbon, and an electrode adopts carbon dioxide process carbon electrode, after another electrode adopts tungsten electrode, can remove sputter and reduce the shell effect.
Tungsten itself is a kind of very hard, color is the refractory metal of Steel Grey to white, physical property is very excellent, especially its fusing point is very high, be the highest in all non-alloyed metals, the modal filament that bulb is arranged, after reaction electrode of the present invention has adopted tungsten electrode, can cause increasing arc length 2mm, increase gas production rate accordingly, because the fusing point of tungsten is 3410 ± 20 degree, vapour pressure is very low, the highest 1650 degree of tensile strength have reduced loss with it as negative pole, like this so need not change basically.
Described rectifier control device 3 is made of electrical power control cabinet and rectifier, and electrical source of power is connected with rectifier by electrical power control cabinet, and the electric output terminal of rectifier is connected with two electrodes in arc light hydrogen carbon composite general fuel is got the reactor of hydrogen respectively.
Described condensing works 7 is a cooling driers.
Described filtration unit 8 is arranged in the low pressure compressor, and the air outlet of filtration unit is connected with low pressure gasholder as low pressure storing unit 9, and low pressure gasholder is provided with the gas port of using from combustion gas to the outside that supply with.
The present invention is to arc light hydrogen carbon composite general fuel ArcH
2C gets hydrogen production technology, utilizes equipment of the present invention, prepares general arc light hydrogen carbon composite general fuel and obtains hydrogen with it by following step:
A, arc light hydrogen carbon composite general fuel in the equipment is got first nitrogen injection in the hydrogen reactor, after vacuumizing for 3 times then, extract residue nitrogen again out after injecting full box water, two electrodes in it are imbedded reached 0.5 meter under water, make by electrode control device and form 90 degree or 45 degree between the corresponding point of two electrodes, connect positive and negative electrode and add electric current, by electrode control device drive carbon dioxide process carbon electrode and tungsten electrode be close to 1mm～3mm apart from the time, make two electrodes form arc discharge, take place to react under the plasma nonequilibrium situations, produce a kind of arc light arc light hydrogen carbon composite general fuel ArcH
2The combustion gas bubble of C, bubble 25 is as shown in Figure 2 surrounded by water, owing to have multiple combustion gas molecule to emerge in the bubble, is compressed in the storage tank by acquisition system withdrawal bubble and with it, and this combustion gas is colourless, tasteless, and intensive blast power is arranged.Be called ArcH
2C also can be called arc light hydrogen carbon composite general fuel ArcH
2C, arc light hydrogen carbon composite general fuel ArcH
2C can be with oxygen and carbon monoxide, carbonic acid gas with being stored in a pressure-pot, and is nonflammable, non-explosive, can store more than 7 years, surpasses the store recording of unprecedented hydrogen;
The b, (ArcH that generates when collecting reaction
2C) arc hydrogen carbon combustion gas bubble makes them deliver to cooling drying removal moisture in the condensing works by transfer line, extracts (ArcH
2C) arc light hydrogen carbon composite general fuel;
C, with (the ArcH that obtains among the step b
2C) arc light hydrogen carbon composite general fuel will expect that thus more pure hydrogen leaches CO with the carbon molecular film earlier
2, CO and other composition, remaining hydrogen become pure hydrogen, hydrogen 55% (H after with the palladium metal membrane filtration
2) obtain a large amount of pure hydrogen, after handling, low pressure compressor is input in the low pressure storing unit again;
Simultaneously also can be with remaining CO, CO
2Get the pure hydrogen that adds a part in addition by transformation absorption (PSA) process, so just obtain 94% pure hydrogen, this method hydrogen manufacturing (H
2) cost is low, program is simple, and is easy to operate, is the minimum hydrogen production process of present cost, only has 1/10th.
The arc light hydrogen carbon composite general fuel ArcH that obtains after testing
2The main component of C is as follows:
Hydrogen H
255.38%
Carbon monoxide CO 31.7%
Ethene Ethylene C
2H
41.875%
Ethane Ethane C
2H
60.004%
Acetylene Acetylene C
2H
20.522%
Methane Methane CH
40.160%
Carbonic acid gas CO
22.42%
Oxygen O 1.767%
Nitrogen N
26.164%
Its calorific value is 1148BTU/CF, is the existing good substitute of conventional fuel.
Embodiment 2:
Tried out 6 months safely after the device fabrication completion of the present invention, basic overview is: per hour use 2.5 of carbon dioxide process carbon electrodes, and not loss of tungsten electrode, 3.5 cubic metres of aerogenesis, electricity consumption 1.19W, producing arc light hydrogen cost only is 4.20 Renminbi.About 40 yuans of every cubic metre of pure hydrogen of existing market, our manufacturing cost is lower than about 10 times of traditional hydrogen production process.
Embodiment 3:
Also can adopt the power supply of 5HP5KW generating set as present device, by calculating as can be known, if generating set adopts gasoline to act as a fuel, 1 gallon gasoline can output 2.5KW heat;
Then 6 hours * 60=360min (minute)
Energy=130000BTU that gasoline is 1 gallon
5 gallons=130000 * 5=650000BTU/min
65000000/360＝1805BTU/min
Can draw operation generating set per minute consumed energy is 1805BTU/min;
Arc light hydrogen carbon composite general fuel (the ArcH that makes with the present invention
2C), the engine that running drives generating set consumed 10 cubic feet fuel in 7 minutes, consumed 8.57 * 10 feet fuel approximately at 60 minutes, and driving generating set needs 85.7 cubic feet of fuel;
Known generators group energy consumption is 1805BTU/min
So 1805 * 60=108300BTU/Hr
Total energy 108300BTU, divided by 85.7 cubic feet of fuel of using up, can get the fuel actual energy is 1263BTU/CF
Adopt the arc light of carbon dioxide process carbon electrode-tungsten electrode to produce out hydrogen H under water in nonequilibrium situations
2And chemical combination carbon monoxide and carbonic acid gas, changed traditional mode and method of producing hydrogen
Equipment of the present invention can be formed by following system constructing:
(1) power system: 2400 amperes interchange converts the commutation system of direct current to, at power wheel drive carbon dioxide process carbon electrode and a large amount of bubble of tungsten electrode output, and hydrogeneous can reaching to more than 55%;
(2) Controlling System: all adopting automatic control systems in pressure, flow and arc current, mainly is the working procedure by computer system control equipment, comprising the speed of feed of pressure, flow, charging, reactor etc.;
(3) condenser system: drying is carried out in the combustion gas of discharging, remove moisture;
(4) dreg removing system: mainly be to purify by the impurity that impeller pump is discharged after with arc light plasma reaction under the nonequilibrium situations;
(5) filtering system: can be with remaining impurities still in the combustion gas, filter the back and make (ArcH
2C) arc light hydrogen carbon composite general fuel reaches quality standards;
(6) reactive system: major parts is (ArcH
2C) arc light hydrogen carbon composite general fuel is got hydrogen reactor, (ArcH
2C) to get the reactor body in the hydrogen reactor be the vacuum reaction case to arc light hydrogen carbon composite general fuel, and first nitrogen injection after vacuumizing for 3 times then, is extracted residue nitrogen out after injecting full box water again, can obtain (ArcH under vacuum state then
2C) arc light hydrogen carbon composite general fuel H
2+ CO;
(7) drive system: make it the carbon dioxide process carbon electrode and the tungsten electrode that consume in the arc light reaction process without interruption;
(8) stocking system, the pressure system that the combustion gas of the plasma reaction under the nonequilibrium situations is passed through self drives, and enters storing state;
(9) automatic charging, the automatically uninterrupted feed of employing magazine-type guarantees that whole system works well, and keeps 24 hours or 8 hours uninterrupted automatic material loadings, mainly provides carbon dioxide process carbon electrode;
(10) fuel closes by compression with hydrogenation in compressed hydrogen system, at first becomes synthetic hydrogen H
2CO, the main component in the combustion gas is a synthetic gas, H
2CO is roughly equal to 83%, is important chemical material;
(11) establish molecular sieve and remove other gas by transformation absorption, or with palladium metal membrane filtration hydrogen,
Equipment of the present invention and preparation technology, simple in structure, the cost of hydrogen manufacturing is low, especially (the ArcH in it
2C) arc light hydrogen carbon composite general fuel is got an electrode employing tungsten electrode of hydrogen reactor, has avoided the stratum nucleare shell phenomenon of conventional carbon electrode, has also avoided needing the problem of frequent feed because the consumption of conventional carbon electrode is fast.
Claims (6)
1. an arc light hydrogen carbon composite general fuel is got hydrogen production equipment, it is characterized in that: this producing apparatus comprises that rectifier control device (2), arc light hydrogen carbon composite general fuel get hydrogen reactor (3), arc light hydrogen carbon composite general fuel and get electrode control device (4), condensing works (7), slag discharging device and the filtration unit (8) that hydrogen reactor (3), arc light hydrogen carbon composite general fuel are got hydrogen; They all are arranged in the casing (10), power supply (1) is connected to arc light hydrogen carbon composite general fuel through rectifier control device (2) and gets on two electrodes (5,6) in the hydrogen reactor (3), the electrode (5) that arc light hydrogen carbon composite general fuel is got hydrogen reactor (3) adopts carbon dioxide process carbon electrode, another electrode (6) adopts tungsten electrode, and two electrodes (5,6) are connected with the electrode control device (4) of adjusting their discharge end distances; The entery and delivery port that arc light hydrogen carbon composite general fuel is got on the hydrogen reactor (3) is connected with inlet pipe, drain pipe by pipeline, the air outlet that arc light hydrogen carbon composite general fuel is got hydrogen reactor (3) is connected with the inlet mouth of condensing works (7), the air outlet of condensing works (7) is installed after filtration and is connected on the low pressure storing unit (9) after handle (8), and low pressure storing unit (9) is provided with the gas port of using of outside supply gas; The slag-drip opening that arc light hydrogen carbon composite general fuel is got hydrogen reactor (3) is connected with slag discharging device.
2. arc light hydrogen carbon composite general fuel according to claim 1 is got hydrogen production equipment, it is characterized in that: described arc light hydrogen carbon composite general fuel is got hydrogen reactor (3) mainly by carbon dioxide process carbon electrode, tungsten electrode or two carbon electricity level work resistor R L
1And RL
2And reactor body constitutes; Carbon dioxide process carbon electrode adopts the carbon electrode that closely contacts with its inner chamber is set in the copper saddle, the discharge end of carbon dioxide process carbon electrode and tungsten electrode is oppositely arranged as producing the electric arc end, the inner container of reactor body (21) for dress water, the arc-over end (22) of two electrodes is arranged in the reactor body (21), carbon dioxide process carbon electrode is connected with the electric output terminal of rectifier control device (2), and tungsten electrode is by working resistance device RL in parallel
1And RL
2The other end of exporting with the electricity of rectifier control device (2) is connected.
3. arc light hydrogen carbon composite general fuel according to claim 1 is got hydrogen production equipment, it is characterized in that: described rectifier control device (3) is made of electrical power control cabinet and rectifier, electrical source of power is connected with rectifier by electrical power control cabinet, and the electric output terminal of rectifier is connected with two electrodes in arc light hydrogen carbon composite general fuel is got the reactor of hydrogen respectively.
4. arc light hydrogen carbon composite general fuel according to claim 1 is got hydrogen production equipment, it is characterized in that: described condensing works (7) is a cooling driers.
5. arc light hydrogen carbon composite general fuel according to claim 1 is got hydrogen production equipment, it is characterized in that: described filtration unit (8) is arranged in the low pressure compressor, the air outlet of filtration unit is connected with low pressure gasholder as low pressure storing unit (9), and low pressure gasholder is provided with the gas port of using from combustion gas to the outside that supply with.
6. an arc light hydrogen carbon composite general fuel is got hydrogen production technology, it is characterized in that: utilize the described equipment of claim 1, prepare general arc light hydrogen carbon composite general fuel by following step and get hydrogen: a, arc light hydrogen carbon composite general fuel in the equipment is got hydrogen reactor elder generation nitrogen injection, after vacuumizing for 3 times then, extract residue nitrogen again out after injecting full box water, two electrodes in it are imbedded reached 0.4～0.6 meter under water, and by two electrode application voltage of rectifier control device, adjust two electrodes by electrode control device simultaneously, make and form 90 degree～45 degree between their corresponding point, the distance to 1 of two electrode discharge ends～3mm, make two electrodes form arc discharge, produce the plasma reaction under the nonequilibrium situations under water;
B, the arc light hydrogen carbon composite general fuel combustion gas bubble that generates when collecting reaction make them deliver to cooling drying removal moisture in the condensing works by transfer line, extract arc light hydrogen carbon composite general fuel;
C, the arc light hydrogen carbon composite general fuel that obtains among the step b installed filtration after filtration after, in the input low pressure storing unit, promptly obtain arc light hydrogen carbon composite general fuel;
It is to leach CO with the carbon molecular film earlier in filtration unit that device after filtration described in d, the above-mentioned steps c filters
2, CO and impurity composition, remaining arc light hydrogen carbon composite general fuel becomes pure hydrogen after with the palladium metal membrane filtration, handles the back through low pressure compressor again and exports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA200610135127XA CN101209816A (en) | 2006-12-27 | 2006-12-27 | Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA200610135127XA CN101209816A (en) | 2006-12-27 | 2006-12-27 | Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101209816A true CN101209816A (en) | 2008-07-02 |
Family
ID=39610098
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA200610135127XA Pending CN101209816A (en) | 2006-12-27 | 2006-12-27 | Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101209816A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102674243A (en) * | 2011-03-09 | 2012-09-19 | 徐州浩通新材料科技股份有限公司 | Device for producing arc gas efficiently by using under-liquid arcs |
| CN105565268A (en) * | 2016-02-01 | 2016-05-11 | 四川中投亿星新能源科技有限公司 | Synthetic hydrogen gas preparation device |
| CN113369627A (en) * | 2021-07-01 | 2021-09-10 | 广东省科学院中乌焊接研究所 | Welding equipment |
-
2006
- 2006-12-27 CN CNA200610135127XA patent/CN101209816A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102674243A (en) * | 2011-03-09 | 2012-09-19 | 徐州浩通新材料科技股份有限公司 | Device for producing arc gas efficiently by using under-liquid arcs |
| CN105565268A (en) * | 2016-02-01 | 2016-05-11 | 四川中投亿星新能源科技有限公司 | Synthetic hydrogen gas preparation device |
| CN113369627A (en) * | 2021-07-01 | 2021-09-10 | 广东省科学院中乌焊接研究所 | Welding equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1239818C (en) | Method for ultilizing gas reserves with low methane concentrations and high inert gas concentrations for fueling gas turbines | |
| CN103861444B (en) | A kind of collecting carbonic anhydride based on hydrate and desalinization combined production device and method | |
| CN102517086A (en) | Method for using carbon dioxide as delivery gas and back flushing gas of coal powder instead of nitrogen in coal gasification methanol preparation process | |
| CN102946974A (en) | Carbon dioxide separation unit and carbon dioxide separation method | |
| CN113247870B (en) | Method and device for preparing high-purity nitrogen trifluoride gas | |
| UA119810C2 (en) | Process for the ammonia production | |
| CN110938480A (en) | Process for producing biomethane from a biogas stream comprising impurity coagulation | |
| CN101209816A (en) | Arc hydrogen carbon composite universal fuel hydrogen extracting manufacture equipment and technique | |
| US20070163256A1 (en) | Apparatus and methods for gas production during pressure letdown in pipelines | |
| CN109972159A (en) | Water power energy-storage system based on solid hydrogen technology | |
| CN115478285A (en) | Process and apparatus for compressing hydrogen in a hybrid compression system | |
| CN208182929U (en) | A kind of system by gasification and electrolysis coupling symphysis production of synthetic gas | |
| CN109929637A (en) | A kind of method and device based on hydrate gas separation principle purifying gas | |
| CN200992484Y (en) | Arc hydrogen-carbon composite general fuel hydrogen preparation manufacturing equipment | |
| CN103525466A (en) | Method and device for indirectly liquefying coal and separating carbon dioxide | |
| CN103395744A (en) | Rapid hydrogen extraction driving method for pressure swing adsorption hydrogen production system | |
| CN103232857A (en) | Coal-based electric power and chemical product coproduction process capable of realizing zero discharge of CO2 | |
| CN101210543A (en) | Wind power generating equipment with arc light hydrogen carbon composite general fuel production device | |
| CN111961509B (en) | Biogas membrane purification system and method | |
| CN209445063U (en) | A kind of continuous output type flush static state hydrogen compressed, storage, filling integral system | |
| CN205773311U (en) | The defective hydrogen of recoverable and the PSA hydrogen generating system of hydrogen more than needed | |
| US20230257260A1 (en) | Optimized hydrogen production from a hydrocarbon | |
| CN111471500A (en) | System and process method for purifying methane by single-stage membrane separation method | |
| CN116514064B (en) | Underground hydrogen production separation and purification system | |
| CN215103595U (en) | Device for preparing high-purity nitrogen trifluoride gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Open date: 20080702 |