CN1259590A - Hydrogen-oxygen fuel generator, its structure and use - Google Patents
Hydrogen-oxygen fuel generator, its structure and use Download PDFInfo
- Publication number
- CN1259590A CN1259590A CN99126589A CN99126589A CN1259590A CN 1259590 A CN1259590 A CN 1259590A CN 99126589 A CN99126589 A CN 99126589A CN 99126589 A CN99126589 A CN 99126589A CN 1259590 A CN1259590 A CN 1259590A
- Authority
- CN
- China
- Prior art keywords
- gas
- water
- hydrogen
- liquid
- electrolyzer
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The present invention relates to equipment for electrolysis of water, its main equipment electrolytic bath is set with several electrolytic plates which are formed from foamed nickel, these plates form several small electrolytic chambers, a long gas chamber, a passage, a gas outlet, a liquid outlet. Under the control of circuit controller, the power source is switched on, the water pump is used to deliver water from water storage tank to electrolytic bath, where water is electrolyzed, water and produced gas are passed through gas guide pipe and liquid guide pipe and fed into radiator, after cooling, delivered to liquid storage tank and gas liquid separating tank where gas and water are further separated, the gas is passed through gas outlet, via pressure gauge, pressure controller, fire retarder, gas valve to utensil for use.
Description
The present invention relates to a kind of brine electrolysis and produce hydrogen and the device of oxygen and the improvement of structure, particularly relating to this device can provide the free of contamination geseous fuel that is more suitable for doing the pharmaceutical sector use.
Brine electrolysis produces hydrogen and oxygen is well-known, its application is also comparatively general, existing Gas Plant is produced the (China Patent No.: 942228103) be used for the high-purity hydrogen gas generator small sized product of gas look general analysis, all belong to electrolytic water device of manufacturer production such as Hewlett-Packard in the large-scale plant of hydrogen.
China utility model patent ZL94244597X and patent application prospectus 941177831 are same devices, also disclosed a kind of device of brine electrolysis, this device mainly stays tower (water strainer) water cooler, storage filling, retarding chamber etc. to be communicated with and to form with conduit by electrolyzer, essence, structure adopts the single channel circulation style, promptly water is imported in the electrolyzer with water pump, making current, under the battery lead plate effect, produce hydrogen or oxygen gas, to the liquid storage filling, gas is delivered to the combustion equipment interface by the outlet on retarding chamber top through vacuum breaker to gas-liquid behind same conduit input water cooler.From its prospectus and pertinent data as can be known.Battery lead plate in the major equipment electrolyzer is that stainless steel plate is made, and be shaped as dish, and stainless steel plate is poor because of the material activation performance, and electrolytic efficiency is low; And impurity such as ferric oxide are very easily adhered on the surface, and dirt settling increases with the increase of working hour, thereby directly influence electrolytic efficiency decline again; Adopt the disk-shaped electrode plate simultaneously, though between pole plate, kept certain distance, but the edge spacing that the edge of a pole plate and another pole plate protrude only has several millimeters, almost link to each other, in machine run, because of the starting immediate current is bigger, the pole plate gap is accumulated factor affecting such as impurity and often spark phenomenon occurred and burn gasket ring, cause short circuit to pole plate is linked to each other, and can not use; Its structure is contacted each parts by a conduit and is formed, this frame mode, the gas that electrolytic solution and electrolysis are produced all is to circulate from a conduit, because of gas-liquid is striven stream, be subjected to the long-pending restriction of catheter section in addition, promptly gas is stifled the not smooth phenomenon of gas communication often to occur, gas is hurried in the electrolyzer at this moment increases, force water level decline in the electrolyzer, and fluctuation of current or cutout appear, this phenomenon occurs incessantly repeatedly, and the result shows as and gives vent to anger unstable suddenly big or suddenly smallly, causes the machine can not continous-stable work.Owing to exist above-mentioned defective in actual product is used, still can not be widely used.
From security standpoint, its device is equipped with a vent valve above retarding chamber, but when liquid storage was irritated the conduit appearance obstruction of leading to retarding chamber, vent valve had just lost effect, this moment, electrolysis continuation gas constantly increased in closed circuit, the state that causes device to be in being absolutely unsafe.
Purpose of the present invention just provides a kind of efficient height, rational in infrastructure, hydrogen-oxygen fuel generator that security is good.
For realizing purpose of the present invention, in this producer major equipment electrolyzer several battery lead plates are set, battery lead plate is made with foamed nickel material, because of its material reactivity good, and the foaming nickel surface has many apertures, respective area with the area stainless steel plate than being three times of stainless steel electrode plate approximately, thereby electrolytic efficiency height, several little tank rooms have been determined to have formed in the electrolyzer by battery lead plate shape shown in Figure 2, an elongated air chamber is formed at top, a passage is formed at the bottom, correspondingly establishes a production well air guide on the top of electrolyzer one end, and a fluid hole drain is established in the bottom, make the gas-liquid shunting, production well links to each other with two scatterers respectively with catheter by airway with fluid hole, and the gas of electrolytic solution and decomposition is delivered in the liquid storage filling by irritating the conduit that links to each other with liquid storage after the scatterer cooling.Liquid storage is irritated top and is equipped with a pressure release valve, liquid storage is irritated with the gas-liquid separation filling and is communicated up and down, link to each other if a water pump makes its inlet end and liquid storage irritate the bottom, exit end links to each other with the electrolyzer inlet end, has so just constituted the loop line of a gas-liquid shunting two-way circulation.If a circuit control panel is under its control, connect power supply, water pump is irritated water and is delivered to electrolysis in the electrolyzer by liquid storage, during isolated gas stream to gas-liquid separation is irritated, after gas-liquid separation, air outlet valve is delivered to through tensimeter, pressure controller, flame-retardant device in the production well output loop line of gas by gas-liquid separation abhiseca portion, is connected use with apparatus by air outlet valve.Tensimeter is in order to show the operating pressure size; Pressure controller control machine operating pressure is no more than set(ting)value 0.3MPa, and when in a single day flame-retardant device produces tempering in order to stop, flame enters in the loop line.Each conduit tie point is tightly connected with heat-shrink tube.
Because the electrolytic tank electrode plate is provided with multi-disc and adopted foamed nickel material to make, because of its reactivity is good, and correspondingly increased the electrolysis area, and cell construction is also more reasonable, thereby has improved electrolytic efficiency; Adopt gas-liquid shunting two-way circulation structure, guaranteed that gas-liquid flow is clear and coherent smooth, make the running of this function steady and continuous; In the loop line, be provided with pressure release valve and closed circuit outside flame-retardant device, pressure controller are set, removed hidden danger, guaranteed the security of complete machine.
Hydrogen-oxygen fuel generator proposed by the invention can be applicable to the every field that various industries are done flame machining.Be not more suitable for using combustion gas owing to not producing any dusty gas after the burning of hydrogen or oxygen gas that this producer produced, can be applicable to the combustion gas of pharmacy industry injection ampoule embedding stringy in pharmaceutical industries is required.
The present invention is further illustrated below in conjunction with drawings and Examples:
Fig. 1 is the structure principle chart of oxyhydrogen generator of the present invention.
Fig. 2 is the shape figure of battery lead plate of the present invention.
Fig. 3 is a flame-retardant device structure principle chart of the present invention.
Be provided with some battery lead plates (2) in the electrolyzer of producer disclosed by the invention (1), battery lead plate is made with foaming nickel, by battery lead plate (2) shape shown in Figure 2, just make the inner structure of electrolyzer (1) form several little tank rooms (3), top forms an elongated air chamber (4) bottom and forms that a passage (5) is corresponding with air chamber (4) on the top of electrolyzer one end establishes a production well (6) air guide, and a corresponding fluid hole (7) drain of establishing with passage (5) in bottom is shunted gas-liquid.One circuit control panel (17) is set under its control, connects power supply, water pump (20) water electrolysis in the input electrolyzer (1) from liquid storage filling (12), the gas that each little tank room (3) produces rises to air chamber (4), and delivers to scatterer (10) by the production well (6) on top through airway (8); Liquid is delivered to scatterer (11) by fluid hole (7) through catheter (9) from the path (5) of bottom, the liquid (about about 85 ℃ of temperature) of output and oxyhydrogen and the water vapour that decomposites in the electrolyzer (1), water temperature descends when scatterer (10) (11), gas cooling, water vapour becomes water, irritate in (12) and the gas-liquid separation filling (15) through conduit input liquid storage again, liquid storage is irritated (12) top and is provided with a pressure release valve (13), the top is provided with filler cover (14), liquid storage is irritated (12) and is communicated up and down with gas-liquid separation filling (15), gas-liquid is irritated in (15) through separating once more in separation, the production well (16) that knallgas is irritated (15) top by gas-liquid separation is exported the loop line, through tensimeter (18) pressure controller (19), flame-retardant device (22) is delivered to air outlet valve (23) use that links to each other with apparatus.Irritate in (12) at liquid storage and separate cooled liquid, decompose again in water pump is imported electrolyzer (1) once more, so just constituted the loop line of gas-liquid shunting two-way circulation, constantly reciprocal process has produced the gas of uninterrupted use.
Tensimeter (18) shows the operating pressure size, and pressure controller (19) is no more than limit value 0.3MPa in order to control pressure.Pressure controller (19) cuts off electrolysis power automatically when tensimeter (18) shows above 0.3MPa, and when tensimeter (18) showed that 0.1MPa is following, power supply is conducting automatically again, and electrolysis continues, and this action does not influence normal and continuous operation.
Block gas-liquid separation and irritate (15) top production well (16), pressure constantly rises in the loop line, and when reaching 0.6MPa, pressure release valve (13) is backed down automatic vent by pressure, opens obstruction, and when pressure during less than 0.6MPa, pressure valve (13) is closed again automatically.
At work, in case when producing tempering, flame-retardant device (22) stops flame to enter in the inner loop line, plays safe fire retardation.Fig. 3 is the structure and the schematic diagram of flame-retardant device, flame-retardant device is made up of fire-retardant valve, Frpipe, fire-retardant ball, fire resistant fluid and rupture disk, gas is fed the bottom of flame-retardant device through unidirectional fire-retardant valve and Frpipe by inlet, fire-retardant ball is with gas dispersion and see through fire resistant fluid by being exported to air outlet valve, in case when producing tempering, under effects such as fire resistant fluid, fire-retardant valve, the rupture disk drum is split, the vent gas pressure drag ends flame and refluxes.Can continue to use after changing a rupture disk.
The tie point of each conduit (21) adopts heat-shrink tube to be tightly connected.
On pharmaceutical sector uses, must be connected mutually with pharmaceutical sector equipment by a special valve body, the shape of these valve body two end interfaces, diameter, bridging mode all can be according to medical various device appliance requires designs.Be used for experimentizing on the injection ampoule wire drawing filling and sealing machine in several families pharmaceutical factory.Substitute it with special valve body and be fixed on gas transmission junctor on the filling and sealing machine platform, with an end of valve body fixedly the spiral shell button be designed to be complementary with set screw nut, two end interfaces and filling and sealing machine inlet pipe, escape pipe are identical, and be fixed on the platform, after simultaneously interface being connected, light filling and sealing machine, working properly and effect is better than traditional combustion gas.
Claims (8)
1. hydrogen-oxygen fuel generator comprises that mainly electrolyzer, scatterer, water storage are irritated, gas-water separation is irritated and water pump.Be characterized in: multi-disc pole plate (2) is set in the electrolyzer (1) makes with foamed nickel material.The shape of battery lead plate (2) has determined to form in the electrolyzer several little tank rooms (3), top forms an elongated air chamber (4) and a passage (5) is formed at the bottom, corresponding on the top of electrolyzer one end a production well (6) air guide is set with air chamber (4), and it is continuous by the same scatterer of airway (8) (10), a corresponding fluid hole (7) drain that is provided with in its underpart with passage (5), link to each other by the same scatterer of catheter (9) (11), make gas-liquid form shunting.Two scatterers link to each other with the top of liquid storage filling (12) respectively with conduit, and liquid storage is irritated (12) top and is provided with a pressure release valve (13), and a top cover (14) is in order to water filling, and liquid storage is irritated (12) and communicated up and down with gas-water separation filling (15).Under circuit control panel (17) control, connect power supply, water pump (20) is delivered to electrolysis in the electrolyzer through irritating the end that links to each other with liquid storage with water, isolated oxyhydrogen is by airway (8), liquid is imported liquid storage by catheter (9) again through scatterer and is irritated (12), hydrogen and oxygen gas mixture is irritated in (15) after separating in gas-liquid separation, production well (16) output by its top, through tensimeter (18) pressure controller (19), flame-retardant device (22) is delivered to air outlet valve (23), irritate in (12) at liquid storage and separate cooled liquid, in water pump is imported electrolyzer (1) once more, decompose again.This sample producer has just constituted the loop line of a gas-liquid shunting two-way circulation.Each conduit tie point (21) all is tightly connected with heat-shrink tube.
2. hydrogen-oxygen fuel generator according to claim 1 is characterized in that: electrolyzer (1) can be provided with one, two or four.
3. hydrogen-oxygen fuel generator according to claim 1 is characterized in that: the plate top, the garden that is shaped as of battery lead plate cuts an arc area and forms a straight flange, and symmetrical bottom cuts a small half of garden area, forms a little semicircle hole.And battery lead plate is made with foamed nickel material, and it is particularly useful for small-sized electrolytic water device applicable to various electrolytic water devices, and its shape, size, what all can design according to the electrolytic water device needs.
4. hydrogen-oxygen fuel generator according to claim 1 is characterized in that: adopt circuit control panel (17) to control whole actions of this machine.
5. hydrogen-oxygen fuel generator according to claim 1 is characterized in that: liquid storage in the loop line is provided with a pressure release valve on irritating, when internal pressure reaches 0.6MPa, the pressure release valve automatic vent, when pressure during less than 0.6MPa pressure release valve close automatically.
6. hydrogen-oxygen fuel generator according to claim 1 is characterized in that: the tie point of each conduit (21) is to adopt the heat-shrink tube sealing method to connect, and its heat resisting temperature is 90 ℃, and bearing pressure is 0.8MPa, and characteristics are that sealing is tight, simple to operate.
7. hydrogen-oxygen fuel generator according to claim 1, it is characterized in that: flame-retardant device (22) set outside the loop line is made up of fire-retardant valve, Frpipe, fire resistant fluid, fire-retardant ball and rupture disk, its building up principle is: gas is entered the bottom of flame-retardant device through unidirectional fire-retardant valve, Frpipe by inlet, fire-retardant ball is with gas dispersion, see through fire resistant fluid by the air outlet to air outlet valve, in case when producing tempering, under the effect of fire resistant fluid, fire-retardant valve etc., the rupture disk drum is split discharge air pressure, stop flame to reflux.Still can continue to use after changing a rupture disk, play the safeguard protection effect.
8. hydrogen-oxygen fuel generator according to claim 1, it is characterized in that: the hydrogen or oxygen gas burning no any pollution in back that producer produced, its purposes is more suitable for being used for the required various flame machining combustion gas of pharmaceutical sector, can be used for pharmacy industry injection ampoule embedding stringy flame.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99126589A CN1259590A (en) | 1999-12-22 | 1999-12-22 | Hydrogen-oxygen fuel generator, its structure and use |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99126589A CN1259590A (en) | 1999-12-22 | 1999-12-22 | Hydrogen-oxygen fuel generator, its structure and use |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1259590A true CN1259590A (en) | 2000-07-12 |
Family
ID=5284467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99126589A Pending CN1259590A (en) | 1999-12-22 | 1999-12-22 | Hydrogen-oxygen fuel generator, its structure and use |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1259590A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010080018A1 (en) * | 2009-01-06 | 2010-07-15 | Hydrogen Fuelsaver Sdn Bhd | An oxyhydrogen generator |
| CN101550552B (en) * | 2009-05-20 | 2011-01-12 | 王可全 | Hydrogen-oxygen mixed gas generator |
| CN102094214A (en) * | 2010-12-09 | 2011-06-15 | 沈阳威德新能源有限公司 | Hydrogen/oxygen energy generator |
| CN101525753B (en) * | 2008-03-04 | 2012-04-18 | 黄国峰 | Water fuel feeding system |
| CN102978650A (en) * | 2012-12-08 | 2013-03-20 | 哈尔滨德卡尔氢能技术开发有限公司 | Automatic oxyhydrogen machine of dual-connected tanks for removing carbon deposit of engine |
| CN104805464A (en) * | 2014-01-23 | 2015-07-29 | 火传利能科技股份有限公司 | High-pressure oxyhydrogen machine |
| CN105332000A (en) * | 2015-11-10 | 2016-02-17 | 深圳万兴顺投资有限公司 | Oxyhydrogen machine and oxyhydrogen generating method |
| CN109545417A (en) * | 2018-11-19 | 2019-03-29 | 中广核工程有限公司 | The system of nuclear power station removal radioactive emission hydrogen component |
| CN111748823A (en) * | 2020-06-28 | 2020-10-09 | 安徽明天氢能科技股份有限公司 | Dehumidifying constant-temperature oxyhydrogen machine |
-
1999
- 1999-12-22 CN CN99126589A patent/CN1259590A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101525753B (en) * | 2008-03-04 | 2012-04-18 | 黄国峰 | Water fuel feeding system |
| WO2010080018A1 (en) * | 2009-01-06 | 2010-07-15 | Hydrogen Fuelsaver Sdn Bhd | An oxyhydrogen generator |
| CN101550552B (en) * | 2009-05-20 | 2011-01-12 | 王可全 | Hydrogen-oxygen mixed gas generator |
| CN102094214A (en) * | 2010-12-09 | 2011-06-15 | 沈阳威德新能源有限公司 | Hydrogen/oxygen energy generator |
| CN102094214B (en) * | 2010-12-09 | 2012-05-30 | 沈阳威德新能源有限公司 | Hydrogen/oxygen energy generator |
| CN102978650A (en) * | 2012-12-08 | 2013-03-20 | 哈尔滨德卡尔氢能技术开发有限公司 | Automatic oxyhydrogen machine of dual-connected tanks for removing carbon deposit of engine |
| CN102978650B (en) * | 2012-12-08 | 2015-07-15 | 哈尔滨安琦科技开发有限公司 | Automatic oxyhydrogen machine of dual-connected tanks for removing carbon deposit of engine |
| CN104805464A (en) * | 2014-01-23 | 2015-07-29 | 火传利能科技股份有限公司 | High-pressure oxyhydrogen machine |
| CN104805464B (en) * | 2014-01-23 | 2017-11-24 | 火传利能科技股份有限公司 | High voltage hydrogen-oxygen machine |
| CN105332000A (en) * | 2015-11-10 | 2016-02-17 | 深圳万兴顺投资有限公司 | Oxyhydrogen machine and oxyhydrogen generating method |
| CN109545417A (en) * | 2018-11-19 | 2019-03-29 | 中广核工程有限公司 | The system of nuclear power station removal radioactive emission hydrogen component |
| CN111748823A (en) * | 2020-06-28 | 2020-10-09 | 安徽明天氢能科技股份有限公司 | Dehumidifying constant-temperature oxyhydrogen machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101550552B (en) | Hydrogen-oxygen mixed gas generator | |
| CN1259590A (en) | Hydrogen-oxygen fuel generator, its structure and use | |
| CN112349937A (en) | Distributed energy system of methanol hydrogen production coupled fuel cell and operation method | |
| CN103848399B (en) | A kind of light-water produces the method and apparatus of depleted water | |
| CN103820169B (en) | A kind of combined type height temperature rough gas cooling purifying device and method | |
| CN2319846Y (en) | Common anode hydrogen generator with improved pressure controller | |
| CN201824039U (en) | Water-energy steel structure cutting equipment | |
| CN1261051A (en) | Process for preparing stable ClO2 solution based on hydrochloric acid | |
| CN113912008A (en) | Pressure swing adsorption hydrogen production method for coke oven gas | |
| CN2594654Y (en) | Oxygen-hydrogen mixed fuel producer | |
| CN214456853U (en) | Automatic change oxygenerator | |
| CN2253682Y (en) | Hydrogen-oxygen cutting-welding machine | |
| CN2231370Y (en) | Electrolytic water gas burning generator | |
| CN2182704Y (en) | Multifunctional hydrogen-oxygen welding and cutting machine | |
| CN113478052A (en) | Oxyhydrogen continuous casting billet flame cutting system and operation process thereof | |
| CN211120742U (en) | Hot water tank for formaldehyde production | |
| CN212713767U (en) | Gas-water separation and water storage device | |
| CN212293760U (en) | Hydrogen production equipment | |
| CN209276645U (en) | A kind of Integrated Processing Unit of hydro-electrolytic hydrogen production device | |
| CN1216184C (en) | Hydrogen energy generator | |
| CN205154443U (en) | Water tank device of vehicle energy saving maintenance system | |
| CN2297625Y (en) | Hydrocarbon liquified fuel oil storage vaporisation can | |
| CN2186859Y (en) | Precision hydrolyzing gas welder | |
| CN2603088Y (en) | High-efficient environment protective combustible gas generator by underwater electric arc | |
| CN2231955Y (en) | hydrogen energy welding cutting machine |
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 |