CN101418452B - Hydrogen production plant by high speed water splitting - Google Patents
Hydrogen production plant by high speed water splitting Download PDFInfo
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- CN101418452B CN101418452B CN2008100465484A CN200810046548A CN101418452B CN 101418452 B CN101418452 B CN 101418452B CN 2008100465484 A CN2008100465484 A CN 2008100465484A CN 200810046548 A CN200810046548 A CN 200810046548A CN 101418452 B CN101418452 B CN 101418452B
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- hydrogen
- oxygen
- chlorine
- blower fan
- oxygen chlorine
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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Abstract
The invention provides a high-speed water-decomposition hydrogen production device, which comprises a high-frequency DC power source, a decomposition tank and a decomposer positioned in the decomposition tank. The device is characterized in that a plurality of rows of anode rod groups and cathode rod groups which are alternate in anodes and cathodes and parallel in arrangement are arranged in the decomposer; the upper part of each anode rod group is covered with an oxygen-chlorine collection seal cover having an oxygen-chlorine outlet; the upper part of each cathode rod group is covered with a hydrogen collection seal cover having a hydrogen outlet; oxygen-chlorine communicating pipes are communicated with the oxygen-chlorine outlets on the oxygen-chlorine collection seal covers; hydrogen communicating pipes are communicated with the hydrogen outlets on the hydrogen collection seal covers; the anodes and the cathodes in the decomposer are connected with the anode and cathode of the high-frequency DC power source through conductors respectively; and oxygen-chlorine purification equipment and hydrogen purification equipment are communicated with the oxygen-chlorine communicating pipes and the hydrogen communicating pipes respectively. The device has the advantages of fast water decomposition, energy conservation, low cost and capability of decomposing high-purity hydrogen and oxygen.
Description
Technical field:
The present invention is relevant with the device of original gradient water of decomposition, and is special relevant with hydrogen production plant by high speed water splitting.
Background technology:
People are fuel with oil, coal, natural gas etc., but oil, coal, natural gas source must be limited, and working life is not long.Water hydrogen other fuel advantage can't be obtained that acts as a fuel.Hydrogen uses water as raw material and produces.So source is widely arranged; Liberated heat is many during hydrogen burning, and liberated heat is three times of homogenous quantities gasoline; The hydrogen fuel biggest advantage is that the product after the burning is a water, and water is free from environmental pollution.The method speed of existing gradient brine electrolysis is slow, power consumption, cost height.ZL200520035055.2 provides a kind of device of high speed water of decomposition, and the hydrogen that decomposites, oxygen purity are low.
Summary of the invention:
The objective of the invention is to go up not enoughly, provide that a kind of water of decomposition speed is fast, energy-conservation, cost is low, can decomposite the high speed decomposing hydrogen-production device of highly purified hydrogen, oxygen in order to overcome.
The object of the present invention is achieved like this:
Hydrogen production plant by high speed water splitting of the present invention, comprise the high-frequency DC source, decomposing pool, be arranged in the splitter of decomposing pool, just it is characterized in that having in the splitter many rows, the alternate anode bar group that is arranged in parallel of negative pole, the cathode rod group, every group of anode bar group top is covered with the oxygen chlorine collection seal closure of band oxygen chlorine outlet, every group of cathode rod group top is covered with the hydrogen collection seal closure of band hydrogen outlet, oxygen chlorine communicating pipe is communicated with the oxygen chlorine outlet that each oxygen chlorine is collected on the seal closure, hydrogen communicating pipe is communicated with the hydrogen outlet that each hydrogen is collected on the seal closure, in the splitter just, negative pole respectively by lead and high-frequency DC source just, negative pole connects, oxygen chlorine equipment for purifying and hydrogen purification equipment respectively with oxygen chlorine communicating pipe, hydrogen communicating pipe is communicated with.
In the above-mentioned oxygen chlorine equipment for purifying first water pump that is communicated with oxygen chlorine communicating pipe is arranged, first knockout tower that is connected with first exit of pump, first blower fan that is connected with first knockout tower, first washing tower that is connected with first blower fan, second blower fan that is connected with first washing tower, first drying tower that is connected with second blower fan, the 3rd blower fan that is connected with first drying tower, first freezer that is connected with the 3rd blower fan, the four fan device that is connected with first freezer, the Low Pressure Oxygen chlorine storehouse that is connected with four fan device, the hyperbaric oxygen chlorine storehouse that is connected with Low Pressure Oxygen chlorine storehouse, the oxygen chlorine that is connected with hyperbaric oxygen chlorine storehouse separates freezer, second water pump that is communicated with hydrogen communicating pipe is arranged in the hydrogen purification equipment, second knockout tower that is connected with second exit of pump, the tendencies machine that is connected with second knockout tower, second drying tower that is connected with the tendencies machine, the 6th blower fan that is connected with second drying tower, second washing tower that is connected with the 6th blower fan, the 7th blower fan that is connected with second washing tower, second freezer that is connected with the 7th blower fan, the Bafeng machine that is connected with second freezer, the pressure hydrogen storehouse that is connected with the Bafeng machine, the High Pressure Hydrogen storehouse that is connected with the pressure hydrogen storehouse, first, temperature in second freezer can not be higher than 4 ℃, Low Pressure Oxygen chlorine storehouse, pressure in the pressure hydrogen storehouse can not be higher than 0.8MPa hyperbaric oxygen chlorine storehouse, pressure in the High Pressure Hydrogen storehouse is to get final product about 10MPa.
Water out on first, second above-mentioned knockout tower is connected with scatterer respectively, filtering basin that are connected with each scatterer respectively, each filtering basin communicates with decomposing pool by pipeline, and through scatterer, filtering basin return in the decomposing pool after filtering out impurity from the water of the isolated band impurity of knockout tower.
Every group of above-mentioned anode bar group bottom is contained in anode bar by bolt and installs on the compoboard, every group of cathode rod group bottom is contained in cathode rod by bolt and installs on the compoboard, being positioned at each mounting plate bottom in the decomposing pool has supporting rack, and positive and negative electrode is installed compoboard and placed on the supporting rack.
Above-mentioned adjacent positive and negative interpolar is apart from S=30～180mm.
The pipeline of bringing the water hole into is arranged at above-mentioned decomposing pool bottom, pipeline stretches out decomposing pool the impurity elimination heat radiation filtering basin that are attached thereto by water pump outward, in the impurity elimination heat radiation filtering basin return water pipe that is communicated with decomposing pool is arranged, the water of decomposing pool bottom band impurity pumps into impurity elimination heat radiation filtering basin by pipeline and the water pump of bringing the water hole into, returns in the decomposing pool after filtering out impurity.
Above-mentioned anode bar adopts rare-earth ceramic, rare earth, titanium, vanadium to make, and cathode rod adopts graphite carbon to make, and is corrosion-resistant, durable, long service life, and the cross-sectional shape of positive and negative electrode rod can be circle, square or other shape.
Above-mentioned high-frequency DC source comprises rectifying circuit ZL101, the filtering circuit C101 that is connected with rectifying circuit Z101, the LC oscillatory circuit of forming by L101 and C103 that is connected with filtering circuit C101, the Technitron T101 that collector and emitter is connected with the LC oscillatory circuit is with the anastomosing frequency automatic control circuit of the base stage of Technitron T101.
When the present invention works, in decomposing pool, add conducting salt (as sulfuric acid, hydrochloric acid etc.) and water (seawater does not then add conducting salt in this way), energising, splitter is connected in the high-frequency DC source, splitter work, produce oxygen chlorine gas mixture, hydrogen, under the water pump effect, with oxygen chlorine and water and impurity, or hydrogen and water and impurity are sent into first or second knockout tower respectively, isolate or oxygen and chlorine, or hydrogen, again through first or tendencies machine shearing force send into first or second washing tower, oxygen after the washing and chlorine, or hydrogen is sent into first or second freezer through the 3rd or the 7th blower fan shearing force more again air and steam is cooled to water after the second or the 6th blower fan shearing force is sent into first or second drying tower, oxygen and chlorine or pure hydrogen again through the 4th or the Bafeng machine send into Low Pressure Oxygen chlorine storehouse or Low Pressure Oxygen storehouse, enter oxygen chlorine in the oxygen chlorine storehouse and enter oxygen chlorine again and separate the storehouse and separate.
Water of decomposition speed of the present invention is fast, energy-conservation, and cost is low, can decomposite highly purified hydrogen, chlorine oxygen, is used for industry, agricultural medicine, car industry etc.
Description of drawings:
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the splitter and collection seal closure mutual alignment structural representation among Fig. 1.
Fig. 3 is a high-frequency DC source circuit schematic diagram.
Embodiment:
Referring to Fig. 1, Fig. 2, hydrogen production plant by high speed water splitting of the present invention comprises high-frequency DC source 1, and decomposing pool 2 is arranged in the splitter 3 of decomposing pool.The alternate anode bar group 4 that is arranged in parallel of many row's positive and negative electrodes, cathode rod group 5 are arranged in the splitter.Every group of anode bar group top is covered with the oxygen chlorine collection seal closure 7 of band oxygen chlorine outlet 6, every group of cathode rod group top is covered with the hydrogen collection seal closure 9 of band hydrogen outlet 8, oxygen chlorine communicating pipe 10 is communicated with the oxygen chlorine outlet that each oxygen chlorine is collected on the seal closure, and hydrogen communicating pipe 11 is communicated with the hydrogen outlet that each hydrogen is collected on the seal closure.Anode bar adopts rare-earth ceramic (or rare earth or titanium or vanadium make), and cathode rod adopts graphite carbon to make.Every group of anode bar group bottom is contained in anode bar by bolt and installs on the compoboard 12, and every group of cathode rod group bottom is contained in cathode rod by bolt and installs on the compoboard 13.Being positioned at each mounting plate bottom in the decomposing pool has supporting rack 14, and positive and negative electrode is installed compoboard and placed on the supporting rack.Positive and negative electrode in the splitter is connected by the positive and negative electrode of lead with the high-frequency DC source respectively, and oxygen chlorine equipment for purifying 15 and hydrogen purification equipment 16 are communicated with oxygen chlorine communicating pipe, hydrogen communicating pipe respectively.
First water pump 17 that is communicated with oxygen chlorine communicating pipe is arranged in the oxygen chlorine equipment for purifying, be communicated with first exit of pump first knockout tower 18, first blower fan 19 that is connected with first knockout tower, first washing tower 20 that is connected with first blower fan, second blower fan 21 that is connected with first washing tower, first drying tower 22 that is connected with second blower fan, the 3rd blower fan 23 that is connected with first drying tower, first freezer 24 that is connected with the 3rd blower fan, the four fan device 25 that is connected with first freezer, the Low Pressure Oxygen chlorine storehouse 26 that is connected with four fan device, the automatic control compressor 27 that is connected with Low Pressure Oxygen chlorine storehouse, the oxygen chlorine height that is connected with automatic control compressor overstocks 28, the compressor 29 that overstocks and be connected with oxygen chlorine height, the oxygen chlorine that is connected with compressor separates freezer 30, separates the liquid chlorine storehouse 31 that freezer is connected with oxygen chlorine, the 9th blower fan 32, the oxygen storehouse 33 that is connected with the 9th blower fan.Second water pump 34 that is communicated with hydrogen communicating pipe is arranged in the hydrogen purification equipment, second knockout tower 35 that is connected with second exit of pump, the tendencies machine 36 that is connected with second knockout tower, second washing tower 37 that is connected with the tendencies machine, the 6th blower fan 38 that is connected with second washing tower, second drying tower 39 that is connected with the 6th blower fan, the 7th blower fan 40 that is connected with second drying tower, second freezer 41 that is connected with the 7th blower fan, the Bafeng machine 42 that is connected with second freezer, the pressure hydrogen storehouse 43 that is connected with the Bafeng machine.The automatic compressor 44 that is connected with the pressure hydrogen storehouse, the High Pressure Hydrogen storehouse 45 that is connected with automatic compressor.
Water out on first, second knockout tower is connected with scatterer 46 respectively, the filtering basin 47 that are connected with scatterer, and filtering basin communicate with decomposing pool by pipeline.
Adjacent positive and negative interpolar can be regulated between 30～180mm apart from S.
The decomposing pool bottom has the pipeline 48 of bringing the water hole into, pipeline to stretch out decomposing pool outward by water pump 49 and filtering basin 47.
Referring to Fig. 1, liquid chlorine jar 50 is connected with liquid chlorine storehouse 31 by compressor 51.Hyperbaric oxygen storehouse 52 is connected with oxygen storehouse 33 by automatic compressor 53.Adding oxygen compressor 54 is pressed into hyperbaric oxygen in the oxygen canister 55.Hydrogen during hydrogen compressor 56 overstocks the hydrogen height is pressed in the hydrogen jar 57, is provided with explosion-proof apparatus 58 on the connecting tube that hydrogen compressor and hydrogen height overstock.Liquid hydrogen freezer 59 overstocks with the hydrogen height by compressor 60 and is connected, and liquid hydrogen compressor 61 is pressed into liquid hydrogen in the liquid nitrogen container 62 and uses.The hydrogen height overstock with liquid hydrogen compressor connecting tube on explosion-proof apparatus 58 is housed.At each knockout tower oxygen, chlorine separates freezer, and monitor 63 is housed respectively on the liquid hydrogen freezer.
Referring to Fig. 1, the clamper pond 64 of the control decomposing pool median water level that communicates with it, the filtering basin 65 that are connected with the clamper pond are housed, the water pump 66 that is connected with filtering basin in the decomposing pool water inlet.
Control Room 67 is housed in this device.
The high-frequency DC source is by rectifying circuit ZL101, the filtering circuit C101 that is connected with rectifying circuit Z101, the LC oscillatory circuit of forming by L101 and C103 that is connected with filtering circuit C101, the Technitron T101 that collector and emitter is connected with the LC oscillatory circuit is with the anastomosing frequency automatic control circuit of the base stage of Technitron T101.
Referring to Fig. 3, the anti-interference inhibition circuit of two-wire group that the promising input terminus that makes high-frequency isolation is made up of LH101 in the frequency automatic control circuit, the power electric current mutually offsets by the magnetic flux that winding produces, so in-phase signal is played attenuation, difference is touched signal by the C101 bypass, thereby plays anti-interference effect.In master loop, to come T101 saturated when driving pulse, and the electric current of L102 can not suddenly change, and promptly presses index law and rise.Pulsewidth is less than 2-4MS.When T101 by the time, oscillating current charges to C103, when voltage (uc) when rising to maximum value, current i=0, this moment, high-frequency energy changed into electric field energy, then capacitor discharge, when electric current increased to maximum, voltage uc=0 was after a flyback, coil still has energy storage, electric current is to the electric capacity reverse charging, and by efficiency diode D1 effect, energy storage finished in a week, release finishes, and vice versa.
The frequency automatic control circuit mainly is to produce with master loop to keep with adjustable pulse frequently, the adjustability of safeguards system, the secondary differentiating circuit that comprises R408, C403, R404, C402 is arranged, the comparison circuit that comprises P1, L102, the ratio circuit that comprises A1-A4 comprises the driving circuit of P3, P4, T201 and comprises the indicating circuit of SL325.
Amplifier P3, P5 constitute waveform generator, by discharging and recharging of P415, R416 and C407, be sent to the in-phase end of P4, it is a zigzag wave with fixed frequency, and the anti-phase termination B level point of P4, change B point current potential by regulator potentiometer RW1, on the output terminal of R4, obtain the square wave that dutycycle is changing, this ripple switches by paraphase and the T403 level of T404, obtains the step pulse voltage of suitable peak value on R301.T201 is a driving stage, the prime signal is become two road opposite each other signals, be prime when being level, anti-phase output makes the T201 conducting, penetrates a level output T202 conducting, T203 ends, positive charge injects the conducting electric current by R310 to T101, on the contrary T201 end, T204 also ends, positive charge injects base current by R309 to T203, makes the T101 base stage pull to the negative electricity pressure surface rapidly and ends.P1 is a comparer, changes the voltage parameter at hot-wire coil two ends respectively over to, and L102 " a " end is for power supply, through the voltage of rectifying and wave-filtering, be about 10,000 volts, as can be seen from Figure 3, when the T101 collector voltage surpasses 10,000 volts, the P1 output low level drops to 10,000 volts when following, and P1 recovers high level.Circuit utilizes negative pulse to pass through the secondary differentiating circuit of R408, C403 and R404, C402 composition, on the collector electrode of T401, obtain one by D403, D404 shaping and postpone narrow negative pulse, and make P3 in-phase end clamper by the D402 that is connected with it, control C427 discharge, thereby determine next output pulse constantly, in fact finish synchronous tracking, most important to complete machine work, it guarantees that T101 is operated in the low loss switching state, and P1 output is amplified by the homophase of being made up of T405, T406 again simultaneously.By the output of D408 setting pulse, be actually gating circuit, D408 clamper, T403 are transmitted to instead and end partially at ordinary times when P1 output is low, even have bursty interference this moment, this circuit plays sealing process, prevents output.The collector electrode that the mutual end of comparer P2 is received T101 by divider resistance is used for the monitor voltage amplitude, plays overvoltage protection.A1 to A4 forms comparison circuit, changes according to power range and pulsewidth level, and A1 is organized identical amplification.SL325 is 15 luminous display circuits, and A2 is a follower.A3, A4 form respectively and show and current protecting circuit.The T101 magnetic resistance is big when unloaded, and oscillating current is little, and it is then opposite to put load, makes A3 output high level, and SL325 produces no longer clamper.A4 compares the oscillating current that flows through T101 by setting level.Low-voltage power circuit, the B201 low-voltage power supply adopts separate three windings of n1, n2, n3, and n1, n2 form simple filtering circuit, for driving and the anti-electric current that draws.N3 is a control power supply winding, adapts to the fluctuation of power supply, adopts three-terminal voltage-stabilizing device 78m10.On C204, obtain voltage stably.
What existing brine electrolysis used is 50 hertz of direct supplys, and both compare and are lower than 600 to 8000 times, promptly decompose slow 600 to 8000 times of acceleration.Among the contrast experiment, high frequency DC source best results of the present invention.It is fast to break up in the water hydrogen bond rupture speed, fast 600 to 8000 times than existing brine electrolysis.Make water molecules fission speed the best.Set up French simple and clear, quick, direct, the straight line ionizing water.Hydrogen picture emerging like the tempest, to compare cost much lower with gasoline, hydrogen cheap about 20% to 85%.
The foregoing description is that foregoing of the present invention is further described, but this should be interpreted as that the scope of the above-mentioned theme of the present invention only limits to the foregoing description.All technology that realizes based on foregoing all belong to scope of the present invention.
Claims (8)
1. hydrogen production plant by high speed water splitting, comprise the high-frequency DC source, decomposing pool, be arranged in the splitter of decomposing pool, just it is characterized in that having in the splitter many rows, the alternate anode bar group that is arranged in parallel of negative pole, the cathode rod group, every group of anode bar group top is covered with the oxygen chlorine collection seal closure of band oxygen chlorine outlet, every group of cathode rod group top is covered with the hydrogen collection seal closure of band hydrogen outlet, oxygen chlorine communicating pipe is communicated with the oxygen chlorine outlet that each oxygen chlorine is collected on the seal closure, hydrogen communicating pipe is communicated with the hydrogen outlet that each hydrogen is collected on the seal closure, in the splitter just, negative pole respectively by lead and high-frequency DC source just, negative pole connects, oxygen chlorine equipment for purifying and hydrogen purification equipment respectively with oxygen chlorine communicating pipe, hydrogen communicating pipe is communicated with, first water pump that is communicated with oxygen chlorine communicating pipe is arranged in the oxygen chlorine equipment for purifying, first knockout tower that is connected with first exit of pump, first blower fan that is connected with first knockout tower, first washing tower that is connected with first blower fan, second blower fan that is connected with first washing tower, first drying tower that is connected with second blower fan, the 3rd blower fan that is connected with first drying tower, first freezer that is connected with the 3rd blower fan, the four fan device that is connected with first freezer, the Low Pressure Oxygen chlorine storehouse that is connected with four fan device, the hyperbaric oxygen chlorine storehouse that is connected with Low Pressure Oxygen chlorine storehouse, the oxygen chlorine that is connected with hyperbaric oxygen chlorine storehouse separates freezer, second water pump that is communicated with hydrogen communicating pipe is arranged in the hydrogen purification equipment, second knockout tower that is connected with second exit of pump, the tendencies machine that is connected with second knockout tower, second drying tower that is connected with the tendencies machine, the 6th blower fan that is connected with second drying tower, second washing tower that is connected with the 6th blower fan, the 7th blower fan that is connected with second washing tower, second freezer that is connected with the 7th blower fan, the Bafeng machine that is connected with second freezer, the pressure hydrogen storehouse that is connected with the Bafeng machine, the High Pressure Hydrogen storehouse that is connected with the pressure hydrogen storehouse.
2. hydrogen production plant by high speed water splitting as claimed in claim 1 is characterized in that the water out on first, second knockout tower is connected with scatterer respectively, filtering basin that are connected with each scatterer respectively, and each filtering basin communicates with decomposing pool by pipeline.
3. hydrogen production plant by high speed water splitting as claimed in claim 1 or 2, it is characterized in that every group of anode bar group bottom is contained in anode bar by bolt and installs on the compoboard, every group of cathode rod group bottom is contained in cathode rod by bolt and installs on the compoboard, being positioned at each mounting plate bottom in the decomposing pool has supporting rack, and positive and negative electrode is installed compoboard and placed on the supporting rack.
4. hydrogen production plant by high speed water splitting as claimed in claim 1 or 2 is characterized in that adjacent positive and negative interpolar is apart from S=30～180mm.
5. hydrogen production plant by high speed water splitting as claimed in claim 3 is characterized in that adjacent positive and negative interpolar is apart from S=30～180mm.
6. hydrogen production plant by high speed water splitting as claimed in claim 1 or 2 is characterized in that anode bar adopts rare-earth ceramic, rare earth, titanium, vanadium to make, and cathode rod adopts graphite carbon to make.
7. hydrogen production plant by high speed water splitting as claimed in claim 1 or 2, it is characterized in that the pipeline of bringing the water hole into is arranged at the decomposing pool bottom, pipeline stretches out decomposing pool the impurity elimination heat radiation filtering basin that are attached thereto by water pump outward, in the impurity elimination heat radiation filtering basin return water pipe that is communicated with decomposing pool is arranged.
8. hydrogen production plant by high speed water splitting as claimed in claim 1 or 2, it is characterized in that the high-frequency DC source comprises rectifying circuit (ZL101), the filtering circuit (C101) that is connected with rectifying circuit (ZL101), be connected with filtering circuit (C101) by (L101) and the LC oscillatory circuit (C103) formed, the Technitron (T101) that collector and emitter is connected with the LC oscillatory circuit is with the anastomosing frequency automatic control circuit of the base stage of Technitron (T101).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100465484A CN101418452B (en) | 2008-11-13 | 2008-11-13 | Hydrogen production plant by high speed water splitting |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2008100465484A CN101418452B (en) | 2008-11-13 | 2008-11-13 | Hydrogen production plant by high speed water splitting |
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| CN101418452A CN101418452A (en) | 2009-04-29 |
| CN101418452B true CN101418452B (en) | 2010-09-01 |
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| CN2008100465484A Expired - Fee Related CN101418452B (en) | 2008-11-13 | 2008-11-13 | Hydrogen production plant by high speed water splitting |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102874753A (en) * | 2012-11-01 | 2013-01-16 | 江苏中靖新能源科技有限公司 | Double-layer reactor for hydrogen-making agent reaction |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102352513B (en) * | 2011-10-20 | 2013-09-11 | 广州华秦机械设备有限公司 | System and method for preparing pure hydrogen through electrolysis of water |
| CN105089869B (en) * | 2015-06-04 | 2018-12-14 | 武汉大学 | A kind of double telescopic electrode waters make the internal-combustion engine arrangement of fuel |
| CN115261888A (en) * | 2022-08-09 | 2022-11-01 | 王新前 | Quantum electrolyzed water flash hydrogen production device for engine fuel |
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2008
- 2008-11-13 CN CN2008100465484A patent/CN101418452B/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102874753A (en) * | 2012-11-01 | 2013-01-16 | 江苏中靖新能源科技有限公司 | Double-layer reactor for hydrogen-making agent reaction |
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Granted publication date: 20100901 Termination date: 20111113 |