CN105154906A - Oxygen-hydrogen generation system - Google Patents
Oxygen-hydrogen generation system Download PDFInfo
- Publication number
- CN105154906A CN105154906A CN201510466216.1A CN201510466216A CN105154906A CN 105154906 A CN105154906 A CN 105154906A CN 201510466216 A CN201510466216 A CN 201510466216A CN 105154906 A CN105154906 A CN 105154906A
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- Prior art keywords
- hydrogen
- water separator
- air water
- gas
- oxygen
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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
Abstract
The invention discloses an oxygen-hydrogen generation system. The oxygen-hydrogen generation system comprises electrolytic baths, temperature adjusting tanks, primary gas-water separators, a gas collecting device and a secondary gas-water separator, wherein the electrolytic baths contain alkaline solutions and are used for generating a hydrogen and oxygen mixed gas in an electrolysis mode; the temperature adjusting tanks are arranged above the electrolytic baths, communicated with the electrolytic baths and used for cooling the hydrogen and oxygen mixed gas discharged after electrolysis of the electrolytic baths; the primary gas-water separators are arranged above the temperature adjusting tanks, communicated with the temperature adjusting tanks and used for conducting primary gas-water separation on the hydrogen and oxygen mixed gas discharged from the temperature adjusting tanks; the gas collecting device is communicated with the primary gas-water separators and used for collecting the hydrogen and oxygen mixed gas separated out from the primary gas-water separators; the secondary gas-water separator is communicated with the gas collecting device and the primary gas-water separators and used for conducting secondary gas-water separation on the hydrogen and oxygen mixed gas discharged from the gas collecting device and preventing the hydrogen and oxygen mixed gas from flowing back again. Hydrogen and oxygen can be prevented from being combined into water molecules again, the purity and quality of the hydrogen and oxygen mixed gas are improved, the structure is simple, and the efficiency is high.
Description
Technical field
The present invention relates to hydrogen-oxygen and field occurs, particularly relate to a kind of hydrogen-oxygen generation systems for aid burning equipment.
Background technology
Current coal combustion equipment due to coal burning insufficient, cause wasting energy and contaminate environment.As the oxyhydrogen generator of the assisted combustion device of combustion equipment, mainly positive and negative conducting electrode is installed in a cell, then connects direct supply respectively and water electrolysis is produced hydrogen and oxygen.Can be used for diesel engine, the vehicles or power generation system that petrol motor, oil engine provide power, can burning efficiency of internal combustion engine be improved, reduce fuel consumption, increase power, reduce exhaust gas emission, reduce oil engine carbon deposit, improve internal-combustion engine life-span.
But the oxyhydrogen generator of prior art comprises electrolyzer, is arranged on the air outlet of electrolyzer upper end and is arranged on the positive and negative electrode of electrolyte bath, wherein, air outlet is directly connected with the air-intake duct of oil engine.But because the thermal value of positive and negative conducting electrode is large, the gas temperature when producing hydrogen and oxygen is high, and atom is more active, poor stability.Now, hydrogen atom and the easy recombine of Sauerstoffatom, form water molecules, make the efficiency of generation hydrogen and oxygen low.
Summary of the invention
In view of this, the invention provides a kind of hydrogen-oxygen generation systems, be mainly used in solving that its hydrogen-oxygen of oxyhydrogen generator of the prior art easily combines, gas is too much in tank, tempering after-explosion damage equipment, threaten the problem of personnel safety.
According to one aspect of the present invention, provide a kind of hydrogen-oxygen generation systems, comprising: electrolyzer, be connected with water supply installation, storage inside has basic solution, produces hydrogen and oxygen gas mixture for electrolysis; Temperature regulating tank, is placed in above described electrolyzer, is communicated with described electrolyzer, for cooling to the hydrogen and oxygen gas mixture of discharging after described electrolytic tank electrolysis; Elementary air water separator, is placed in above described temperature regulating tank, is communicated with described temperature regulating tank, carries out first gas-water separation for the hydrogen and oxygen gas mixture of discharging described temperature regulating tank; Gas collecting device, is communicated with described elementary air water separator, for collecting the isolated hydrogen and oxygen gas mixture of described elementary air water separator; Secondary air water separator, is communicated with elementary air water separator with described gas collecting device, carries out secondary gas-water separation for the hydrogen and oxygen gas mixture of discharging described gas collecting device, and prevents hydrogen and oxygen gas mixture adverse current again.
Preferably, also comprise: three grades of air water separators, being communicated with secondary air water separator with described elementary air water separator, for reducing the water content of the hydrogen and oxygen gas mixture flowed out from described secondary air water separator, preventing described hydrogen and oxygen gas mixture to described secondary air water separator adverse current simultaneously.
Preferably, the number of described electrolyzer is 4, be arranged on side by side on insulating frame, the number of described temperature regulating tank is 4, each described temperature regulating tank is placed in corresponding described upper part of the electrolytic cell, the top of each described electrolyzer is provided with for discharging hydrogen and oxygen gas mixture first air outlet, and each described first air outlet is connected with corresponding described temperature regulating tank by the first air guide channel.
Preferably, the number of described elementary air water separator is 2, each described elementary air water separator is communicated with two described temperature regulating tanks, the upper end of described temperature regulating tank is provided with for discharging cooled hydrogen and oxygen gas mixture second air outlet, and described second air outlet is communicated with corresponding elementary air water separator by the second air guide channel.
Preferably, described elementary air water separator comprises the first elementary air water separator and the second elementary air water separator, described gas collecting device is arranged between two described elementary air water separators and elementary air water separator described with two is communicated with respectively, described elementary air water separator is horizontal elementary air water separator, described gas collecting device is vertical gas gathering device, and the horizontal installation position of described gas collecting device is higher than described elementary air water separator.
Preferably, also comprise: automatically controlled gas boosting safety pump, be placed in gas output channel, the pressure born for reducing anti-back-fire device also makes to form negative pressure in gas collecting device and secondary air water separator, ensures the security in gas course of conveying.
Preferably, the horizontal installation position of described secondary air water separator is higher than described elementary air water separator, and the installation site of described three grades of air water separators is higher than described secondary air water separator.
By technique scheme, the technical scheme that the embodiment of the present invention provides at least has following advantages:
First air outlet of electrolyzer is communicated with temperature regulating tank by the present invention, and can reduce the temperature of brine electrolysis, prevents because water temperature over-high produces a large amount of water vapour.Air water separator can carry out gas-water separation to hydrogen and oxygen gas mixture, thus reduces the humidity of hydrogen and oxygen gas mixture, improves the quality of hydrogen and oxygen gas mixture.
Above-mentioned explanation is only the general introduction of technical solution of the present invention, in order to technique means of the present invention can be better understood, and can be implemented according to the content of specification sheets, and can become apparent, below especially exemplified by the specific embodiment of the present invention to allow above and other objects of the present invention, feature and advantage.
Accompanying drawing explanation
By reading hereafter detailed description of the preferred embodiment, various other advantage and benefit will become cheer and bright for those of ordinary skill in the art.Accompanying drawing only for illustrating the object of preferred implementation, and does not think limitation of the present invention.And in whole accompanying drawing, represent identical parts by identical reference symbol.In the accompanying drawings:
Fig. 1 shows the structural representation of the hydrogen-oxygen generation systems that the embodiment of the present invention provides;
Reference numeral:
1, electrolyzer; 2, the first air outlet; 3, the first air guide channel; 4, temperature regulating tank; 51, the first elementary air water separator; 52, the second elementary air water separator; 6, the second air outlet; 7, the second air guide channel; 8, the 3rd air outlet; 9, gas collecting device; 10, the 3rd air guide channel; 11, secondary air water separator; 12, three grades of air water separators; 13, automatically controlled gas boosting safety pump; 14, hydrogen or oxygen gas output channel; 15, regulation of level tank; 16, regulation of level tank working shaft.
Embodiment
Below with reference to accompanying drawings exemplary embodiment of the present disclosure is described in more detail.Although show exemplary embodiment of the present disclosure in accompanying drawing, however should be appreciated that can realize the disclosure in a variety of manners and not should limit by the embodiment set forth here.On the contrary, provide these embodiments to be in order to more thoroughly the disclosure can be understood, and complete for the scope of the present disclosure can be conveyed to those skilled in the art.
According to an aspect of the embodiment of the present invention, provide a kind of hydrogen-oxygen generation systems, as shown in Figure 1, described system comprises: several electrolyzers 1, and electrolyzer 1 is connected with water supplying unit, and water supplying unit is used for providing brine electrolysis for electrolyzer 1; The cell body outer wall of electrolyzer 1 is provided with positive and negative electrode, and positive and negative electrode is electrically connected with power supply unit, for electrolyzer 1 provides the electric current of electrolysis.The number of the electrolyzer 1 in the present embodiment is 4, it should be noted that the present embodiment does not limit the number of electrolyzer 1, can according to need of production sets itself.
Further, the upper end of each electrolyzer 1 is provided with the first air outlet 2, for discharging the hydrogen and oxygen gas mixture after electrolysis, each first air outlet 2 is connected with corresponding temperature regulating tank 4 by the first air guide channel 3, be understandable that, hydrogen and oxygen are along with the direction of current, flow in temperature regulating tank 4, particularly, temperature regulating tank 4 arranges the first inlet mouth, the first air outlet 2 on each electrolyzer 1 is communicated with the first inlet mouth on temperature regulating tank 4 respectively by the first air guide channel 3 of correspondence, temperature regulating tank 4 is placed in the upper end of electrolyzer 1, for cooling to the hydrogen and oxygen gas mixture of discharging after electrolyzer 1 electrolysis, the temperature of hydrogen and oxygen gas mixture can be reduced when excess temperature regulating tank 4, strengthen the stability of gas.Be understandable that, described temperature regulating tank 4 inside can hold the liquid for cooling such as cold water.
Because when electrolysis, the temperature of brine electrolysis is very high, easily boiling produces a large amount of water vapour, if directly discharged from electrolyzer 1, can contain a large amount of water vapour, cause the production rate of hydrogen and oxygen low in hydrogen and oxygen gas mixture.First air outlet 2 of electrolyzer 1 is communicated with temperature regulating tank 4 by the embodiment of the present invention, temperature regulating tank 4 inside is cold water, from the second air outlet 6 of temperature regulating tank 4, hydrogen and oxygen are discharged, therefore can reduce the temperature of the brine electrolysis of generation, increase the efficiency producing hydrogen and oxygen.
Closer, in the present embodiment, elementary air water separator is connected with between two adjacent temperature regulating tanks 4, particularly, the upper end of each temperature regulating tank 4 is provided with second air outlet 6, for discharging cooled hydrogen and oxygen gas mixture, the bottom of each elementary air water separator is provided with two the second inlet mouths, second air outlet 6 is communicated with the second air guide channel 7, every two the second air guide channels 7 connect with two the second inlet mouths of corresponding elementary air water separator, thus two temperature regulating tanks 4 are communicated with an elementary air water separator, the hydrogen and oxygen gas mixture of discharging due to temperature regulating tank 4 carries moisture content, therefore, elementary air water separator is used for carrying out gas-water separation to hydrogen and oxygen gas mixture, preferably, elementary air water separator 5 inside can arrange for dry hydrogen and oxygen drying material, be provided with stainless steel capillary or funnel type step-down division box etc. and fly structure etc. for separating of air water.
In the present embodiment, the hydrogen and oxygen gas mixture that temperature regulating tank 4 produces is discharged from the second air outlet 6, elementary air water separator is flowed into inner via the second air guide channel 7, by the moisture content that elementary air water separator absorption temperature regulating tank 4 is discharged, reduce the humidity of hydrogen and oxygen gas mixture, and discharged by the 3rd air outlet 8 of elementary air water separator one end, improve the quality of hydrogen and oxygen gas mixture.
In a particular application, gas collecting device 9 is communicated with between two elementary air water separators, particularly, gas collecting device 9 is communicated with between first elementary air water separator 51 and the second elementary air water separator 52, two the 3rd inlet mouths are provided with in the middle of gas collecting device 9 outer wall, the 3rd air outlet 8 be positioned on elementary air water separator is communicated with the 3rd corresponding inlet mouth respectively by the 3rd air guide channel 10, gas collecting device 9 between two elementary air water separators above, for collecting through the isolated hydrogen and oxygen gas mixture of one-level air water separator, gas collecting device 9 is communicated with secondary air water separator 11 with the second elementary air water separator 52, secondary air water separator 11 is for secondary separation air water, improve the quality of hydrogen and oxygen gas mixture, with prevent the oxyhydrogen that flowed out by gas collection device 9 again adverse current in its gas collection device 9.
In the present embodiment, secondary air water separator 11 is communicated with three grades of air water separators 12 by gas output channel, the installation site of three grades of air water separators 12 is higher than described secondary air water separator 11, thus prevent hydrogen and oxygen gas mixture adverse current, three grades of air water separators 12 are for reducing the water content of the hydrogen and oxygen gas mixture flowed out from secondary air water separator 11, simultaneously for storing organic agent, to prevent knallgas to secondary air water separator 11 adverse current, preferably, automatically controlled gas boosting safety pump 13 is also installed, be placed in gas output channel, the pressure born for reducing anti-back-fire device also makes to form negative pressure in gas collecting device and secondary air water separator, ensure the security in gas course of conveying.
For ensureing the security in gas course of conveying; The pneumatic outlet of three grades of air water separators 12 is connected with one end of hydrogen or oxygen gas output channel 14, and the other end of hydrogen or oxygen gas output channel 14 connects nozzle, for spraying oxyhydrogen.
In addition, one end of the first elementary air water separator 51 is communicated with regulation of level tank 15, and the other end of regulation of level tank 15 is connected with regulation of level tank working shaft 16.
It should be noted that, first elementary air water separator 51 and the second elementary air water separator 52 inside hold full water, gas collecting device 9, secondary air water separator 11 and three grades of air water separator 12 inside hold water and contain a small amount of gas, wherein, gas collecting device 9, secondary air water separator 11 and three grades of inner water levels held of air water separator 12 are in same level.
The present embodiment can improve the amount of produced oxyhydrogen and then guarantee the oxyhydrogen generation systems of economy.Be after raw material energising with basic solution, extract hydrogen and oxygen gas mixture, through gas-water separation with after filtering, enter combustion equipment, make fuel be able to Thorough combustion, thus the hydrocarbons content in boiler institute emission is reduced, save energy also substantially improves Air quality.
In the above-described embodiments, the description of each embodiment is all emphasized particularly on different fields, in certain embodiment, there is no the part described in detail, can see the associated description of other embodiments.
Be understandable that, the correlated characteristic in aforesaid method and device can reference mutually.In addition, " first ", " second " in above-described embodiment etc. are for distinguishing each embodiment, and do not represent the quality of each embodiment.
Those skilled in the art can be well understood to, and for convenience and simplicity of description, the system of foregoing description, the specific works process of device and unit, with reference to the corresponding process in preceding method embodiment, can not repeat them here.
Intrinsic not relevant to any certain computer, virtual system or miscellaneous equipment with display at this algorithm provided.Various general-purpose system also can with use based on together with this teaching.According to description above, the structure constructed required by this type systematic is apparent.In addition, the present invention is not also for any certain programmed language.It should be understood that and various programming language can be utilized to realize content of the present invention described here, and the description done language-specific is above to disclose preferred forms of the present invention.
In specification sheets provided herein, describe a large amount of detail.But can understand, embodiments of the invention can be put into practice when not having these details.In some instances, be not shown specifically known method, structure and technology, so that not fuzzy understanding of this description.
Similarly, be to be understood that, in order to simplify the disclosure and to help to understand in each inventive aspect one or more, in the description above to exemplary embodiment of the present invention, each feature of the present invention is grouped together in single embodiment, figure or the description to it sometimes.But, the method for the disclosure should be construed to the following intention of reflection: namely the present invention for required protection requires feature more more than the feature clearly recorded in each claim.Or rather, as claims below reflect, all features of disclosed single embodiment before inventive aspect is to be less than.Therefore, the claims following embodiment are incorporated to this embodiment thus clearly, and wherein each claim itself is as independent embodiment of the present invention.
Those skilled in the art are appreciated that and adaptively can change the module in the equipment in embodiment and they are arranged in one or more equipment different from this embodiment.Module in embodiment or unit or assembly can be combined into a module or unit or assembly, and multiple submodule or subelement or sub-component can be put them in addition.Except at least some in such feature and/or process or unit be mutually repel except, any combination can be adopted to combine all processes of all features disclosed in this specification sheets (comprising adjoint claim, summary and accompanying drawing) and so disclosed any method or equipment or unit.Unless expressly stated otherwise, each feature disclosed in this specification sheets (comprising adjoint claim, summary and accompanying drawing) can by providing identical, alternative features that is equivalent or similar object replaces.
In addition, those skilled in the art can understand, although embodiments more described herein to comprise in other embodiment some included feature instead of further feature, the combination of the feature of different embodiment means and to be within scope of the present invention and to form different embodiments.Such as, in the following claims, the one of any of embodiment required for protection can use with arbitrary array mode.
All parts embodiment of the present invention with hardware implementing, or can realize with the software module run on one or more treater, or realizes with their combination.It will be understood by those of skill in the art that the some or all functions that microprocessor or digital signal processor (DSP) can be used in practice to realize according to the some or all parts in a kind of oil field data Monitoring systems of the embodiment of the present invention and device.The present invention can also be embodied as part or all equipment for performing method as described herein or device program (such as, computer program and computer program).Realizing program of the present invention and can store on a computer-readable medium like this, or the form of one or more signal can be had.Such signal can be downloaded from internet website and obtain, or provides on carrier signal, or provides with any other form.
The present invention will be described instead of limit the invention to it should be noted above-described embodiment, and those skilled in the art can design alternative embodiment when not departing from the scope of claims.In the claims, any reference symbol between bracket should be configured to limitations on claims.Word " comprises " not to be got rid of existence and does not arrange element in the claims or step.Word "a" or "an" before being positioned at element is not got rid of and be there is multiple such element.The present invention can by means of including the hardware of some different elements and realizing by means of the computer of suitably programming.In the unit claim listing some devices, several in these devices can be carry out particular embodiment by same hardware branch.Word first, second and third-class use do not represent any order.Can be title by these word explanations.
Claims (7)
1. a hydrogen-oxygen generation systems, is characterized in that, comprising:
Electrolyzer, is connected with water supply installation, and storage inside has basic solution, produces hydrogen and oxygen gas mixture for electrolysis;
Temperature regulating tank, is placed in above described electrolyzer, is communicated with described electrolyzer, for cooling to the hydrogen and oxygen gas mixture of discharging after described electrolytic tank electrolysis;
Elementary air water separator, is placed in above described temperature regulating tank, is communicated with described temperature regulating tank, carries out first gas-water separation for the hydrogen and oxygen gas mixture of discharging described temperature regulating tank;
Gas collecting device, is communicated with described elementary air water separator, for collecting the isolated hydrogen and oxygen gas mixture of described elementary air water separator;
Secondary air water separator, is communicated with elementary air water separator with described gas collecting device, carries out secondary gas-water separation for the hydrogen and oxygen gas mixture of discharging described gas collecting device, and prevents hydrogen and oxygen gas mixture adverse current again.
2. hydrogen-oxygen generation systems according to claim 1, is characterized in that, also comprise:
Three grades of air water separators, be communicated with secondary air water separator with described elementary air water separator, for reducing the water content of the hydrogen and oxygen gas mixture flowed out from described secondary air water separator, prevent described hydrogen and oxygen gas mixture to described secondary air water separator adverse current simultaneously.
3. hydrogen-oxygen generation systems according to claim 1, it is characterized in that, the number of described electrolyzer is 4, be arranged on side by side on insulating frame, the number of described temperature regulating tank is 4, each described temperature regulating tank is placed in corresponding described upper part of the electrolytic cell, and the top of each described electrolyzer is provided with for discharging hydrogen and oxygen gas mixture first air outlet, and each described first air outlet is connected with corresponding described temperature regulating tank by the first air guide channel.
4. hydrogen-oxygen generation systems according to claim 3, it is characterized in that, the number of described elementary air water separator is 2, each described elementary air water separator is communicated with two described temperature regulating tanks, the upper end of described temperature regulating tank is provided with for discharging cooled hydrogen and oxygen gas mixture second air outlet, and described second air outlet is communicated with corresponding elementary air water separator by the second air guide channel.
5. hydrogen-oxygen generation systems according to claim 4, it is characterized in that, described elementary air water separator comprises the first elementary air water separator and the second elementary air water separator, described gas collecting device is arranged between two described elementary air water separators and elementary air water separator described with two is communicated with respectively, described elementary air water separator is horizontal elementary air water separator, described gas collecting device is vertical gas gathering device, and the horizontal installation position of described gas collecting device is higher than described elementary air water separator.
6. hydrogen-oxygen generation systems according to claim 2, is characterized in that, also comprise:
Automatically controlled gas boosting safety pump, is placed in gas output channel, and the pressure born for reducing anti-back-fire device also makes to form negative pressure in gas collecting device and secondary air water separator, ensures the security in gas course of conveying.
7. hydrogen-oxygen generation systems according to claim 2, is characterized in that, the horizontal installation position of described secondary air water separator is higher than described elementary air water separator, and the installation site of described three grades of air water separators is higher than described secondary air water separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510466216.1A CN105154906A (en) | 2015-07-28 | 2015-07-28 | Oxygen-hydrogen generation system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510466216.1A CN105154906A (en) | 2015-07-28 | 2015-07-28 | Oxygen-hydrogen generation system |
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| CN105154906A true CN105154906A (en) | 2015-12-16 |
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| CN201510466216.1A Pending CN105154906A (en) | 2015-07-28 | 2015-07-28 | Oxygen-hydrogen generation system |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2205273Y (en) * | 1994-06-21 | 1995-08-16 | 杨仁明 | High efficiency safety hydroelectrolytic hydrogen-oxygen welding and cutting machine |
| CN2352544Y (en) * | 1998-05-20 | 1999-12-08 | 王宜清 | Low voltage large current apparatus for producing hydrogen and oxygen |
| JP2010133027A (en) * | 2008-12-05 | 2010-06-17 | Boo-Sung Hwang | Hydrogen-oxygen mixture generating system |
| CN204939625U (en) * | 2015-07-28 | 2016-01-06 | 石祥 | A kind of hydrogen-oxygen generation systems |
-
2015
- 2015-07-28 CN CN201510466216.1A patent/CN105154906A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2205273Y (en) * | 1994-06-21 | 1995-08-16 | 杨仁明 | High efficiency safety hydroelectrolytic hydrogen-oxygen welding and cutting machine |
| CN2352544Y (en) * | 1998-05-20 | 1999-12-08 | 王宜清 | Low voltage large current apparatus for producing hydrogen and oxygen |
| JP2010133027A (en) * | 2008-12-05 | 2010-06-17 | Boo-Sung Hwang | Hydrogen-oxygen mixture generating system |
| CN204939625U (en) * | 2015-07-28 | 2016-01-06 | 石祥 | A kind of hydrogen-oxygen generation systems |
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