CN101498456A - Apparatus for generating electrolytic gas composite fuel, and method for generating this fuel - Google Patents
Apparatus for generating electrolytic gas composite fuel, and method for generating this fuel Download PDFInfo
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- CN101498456A CN101498456A CNA2008101880978A CN200810188097A CN101498456A CN 101498456 A CN101498456 A CN 101498456A CN A2008101880978 A CNA2008101880978 A CN A2008101880978A CN 200810188097 A CN200810188097 A CN 200810188097A CN 101498456 A CN101498456 A CN 101498456A
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Abstract
The present invention provides an apparatus for generating electrolytic gas composite fuel generated by mixing fossil fuels and electrolytic gas generated by electrolyzing water in alkaline electrolyte, and method for generating this fuel. The electrolytic gas composite fuel generation apparatus has a mixing tank, an electrolytic gas supply device, a fossil fuel supply device and an electrolytic gas composite fuel discharge device. The fuel generation apparatus also includes a movable elevating portion and a controller, wherein, the movable elevating portion is provided with a movable structure capable of ascending and descending and a plurality of splitter plates mounted on the structure, the splitter plate is provided with a plurality of micro pores that the bubbles of the electrolytic gas and gaseous fossil fuels are not liable to pass through, state, the splitter plates are provided in the horizontal direction in a state the periphery surface of the splitter plates are close to the inner wall of the mixing tank, so as to be immersed by the liquid filled in the mixing tank; the controller controls stopping or opening, allowance, and specified ingredient proportion of the electrolytic gas and/or gaseous fossil fuels om the mixing tank.
Description
Technical field
The present invention relates to a kind of water electrolytic gas fuel combination generating means and method for generation, the water electrolytic gas that obtains by the water that utilizes in the electrolysis alkaline electrolyte mixes with the gaseous state fossil fuel of liquefied natural gas or liquefied petroleum gas etc. and obtains the water electrolytic gas fuel combination.
Background technology
As everyone knows, in potassium hydroxide (KOH) aqueous solution of alkalescence, hydrone (H
2O) ionization produces hydroxide ion OH
-With hydrogen ion H
+Here, because hydroxide ion OH
-From negative pole (negative electrode) side direction positive pole (anode) side shifting, thus be called as anion, and hydrogen ion H
+Then on the contrary from anodal (anode) side direction negative pole (negative electrode) side shifting, so be called as cation.This hydrogen ion and hydrone H
2O is combined into " hydrogen ion (H
3O
+) ".This just means that there are a lot " hydrogen ion (H with covalent bonds in (inside of electrolytic cell just) under hydrone and hydrogen ion mixed environment
3O
+) ".As anionic hydroxide ion OH
-And hydrogen ion (H
3O
+) can be hydrolysis acquisition by the alkaline electrolyte in the electrolytic cell.
Prior art as mixed combustion under special state with water and fossil fuel, patent document 1 discloses following a kind of slaked lime fuel burner, it makes steam and is vaporific fossil fuel and mixes, and is connected with the pipeline that is used for supplying with fuel combination.On this pipeline, be formed with the steam manifold (manifold) that steam is passed through, have the structure that vaporific kerosene is imported on the path of this steam.In addition, on above-mentioned steam manifold, be formed with the 1st and the 2nd nozzle support column.In the patent document 1 disclosed slaked lime fuel burner, the top of steam manifold is equipped with gas manifold, also is provided with to be used for spraying Blang's gas the 1st nozzle and the 2nd nozzle of (HHO gas comprises 2 parts of hydrogen and 1 part of oxygen).In the disclosed burner of this existing file, in the kerosene of atomizing, sneak into steam, and realize suitable burning by in gas manifold, mixing with Blang's gas.
A kind of combustion method and device of slaked lime fuel mix emulsion are disclosed in the patent document 2.In this patent document, use microwave (ultrashort wave) irradiation slaked lime fuel mix emulsion to make its gasification that heats up.The slaked lime fuel mix gas of the above-mentioned gasification that heated up supplied in the burner it is lighted.The gas of the high heat of high temperature is provided by burning Blang gas in this burner.Preferably in this burner, obtain the gas of high temperature high heat, like this, can obtain the high temperature about 2000 ℃ by burning Blang gas.
A kind of Blang's air burner of the Blang's gas that burns is safely conscientiously disclosed in patent document 3.On this burner, be formed with the burner body that Blang's air flow inlet and gas ejection ports are communicated with, and improve security in the more than one at least back-fire mechanism that prevents of the inner setting of Blang's gas path of burner body.All be to obtain mist in above-mentioned each patent document by the Blang's gas that in fuel, adds steam or obtain by water, make its burning afterwards, just disclosed in each patent document is that the vaporific hybrid fuel that waits is imported in the combustion mechanism such as burner its method of lighting or device.
The following a kind of device and manufacture method thereof of mixing Blang's gas of making disclosed in patent document 4, promptly, in the mixing channel that is loaded with liquid VOC to inside, supply with Blang's gas, in the organic gas that volatility organic solution produces and the device that Blang's gas mixes, mixing channel inside has isolated wall, be formed with the intransitable ventilative micropore of using of Blang's gas bubble on it, this is the further Blang's gas that is supplied to that adsorbs of bubble coalescence body independently, and further enlarge, obtain mixing Blang's gas thus.In this patent document; the gaseous organic compound that liquid VOC gasification in the mixing channel is produced mixes with Blang's gas; simultaneously; the isolated wall that is arranged on mixing channel inside is non-movable structure; and so the unexposed mechanism that stops or open to mixing channel supply Blang gas, flammable organic compound gas etc. is different fully with this part-structure among the present invention.
The open communique spy of [patent document 1] Japanese patent of invention opens 2002-5414
The open communique spy of [patent document 2] Japanese patent of invention opens flat 10-267260
The open communique spy of [patent document 3] Japanese patent of invention opens 2003-207107
The open communique spy of [patent document 4] Japanese patent of invention opens 2005-320416
Summary of the invention
Therefore, the object of the invention is to provide a kind of water electrolytic gas that obtains by the water that utilizes in the electrolysis alkaline electrolyte to mix water electrolytic gas fuel combination generating means and the method for generation that obtains the water electrolytic gas fuel combination with the gaseous state fossil fuel of liquefied natural gas or liquefied petroleum gas etc.After the inventor carries out various researchs by the device to water electrolytic gas and the mixing of gaseous state fossil fuel, developed the device of following generation fuel, utilize this device, can reduce emission amount of carbon dioxide, and can significantly reduce consumption, can continue to obtain to have the fuel of strong firepower simultaneously as the gaseous state fossil fuel of raw material.Technical scheme 1 described invention is a kind of water electrolytic gas fuel combination generating means as shown in Figure 1 and Figure 2, it has mixing channel, water electrolytic gas feed mechanism, fossil fuel feed mechanism, water electrolytic gas fuel combination output mechanism, wherein, be loaded with one or more organic solutions such as alkanes, alcohols, ethers in the mixing channel, in mixing channel inside, the married operation of the water electrolytic gas of the air bubble-shaped that is repeating to be supplied to and gaseous state fossil fuel; The water electrolytic gas that the water electrolytic gas feedway will produce by the water in the electrolysis alkaline electrolyte supplies to mixing channel with the bubble attitude; The fossil fuel feed mechanism supplies to mixing channel with the gaseous state fossil fuel with the bubble attitude; Water electrolytic gas fuel combination output mechanism constantly mixes above-mentioned water electrolytic gas and gaseous state fossil fuel and the water electrolytic gas fuel combination that produces is discharged into the fuel use device.This water electrolytic gas fuel combination generating means also has movable lifting unit and controlling organization, wherein, movable lifting unit has the movable structure that can carry out lifting action, a plurality of demarcation strips are installed on it, offer the micropore that the bubble of a plurality of above-mentioned water electrolytic gas and gaseous state fossil fuel is difficult for passing through on the described demarcation strip, described demarcation strip is provided with the approaching state along continuous straight runs of outer peripheral face and mixing channel inwall, and liquid-immersed by institute's splendid attire in the above-mentioned mixing channel; Supply with in the controlling organization subtend mixing channel above-mentioned water electrolytic gas and/or gaseous state fossil fuel stop or open, quantity delivered, predetermined component ratio control.
In the technical scheme 2 described water electrolytic gas fuel combination generating means, splendid attire can be selected arbitrarily from alkanes, alcohols, ethers in the organic solution of mixing channel inside.
In the technical scheme 3 described water electrolytic gas fuel combination generating means, the gaseous state fossil fuel that above-mentioned fossil fuel feed mechanism is supplied with can be selected arbitrarily from liquefied petroleum gas (LPG), liquefied natural gas (LNG), dry distillation coal gas etc.
In the technical scheme 4 described water electrolytic gas fuel combination generating means, the water electrolytic gas fuel combination that above-mentioned water electrolytic gas fuel combination generating means produces comprises the gas that produces because of the gasification of organic solutions such as above-mentioned alkanes, alcohols, ethers.
In the technical scheme 5 described water electrolytic gas fuel combination generating means, on the movable lifting unit three layers of demarcation strip are installed, the thickness of nethermost demarcation strip is 0.5～2.5mm, preferred 1～2mm, micro-pore diameter is 0.5～3.5mm on it, preferred 1～3mm, and material is stainless steel or resin, the micro-pore diameter of two demarcation strips of its top is 0.2～1.5mm, the network structure body of stainless steel about preferred 0.3～1mm or resinous flat shape.In addition, three demarcation strips all can be resin system, and thickness of slab can be that 10～15mm, micro-pore diameter can be 3～10mm.In addition, the shape that is formed at the micropore on the demarcation strip can be tip taper shape up.
In the technical scheme 6 described water electrolytic gas fuel combination generating means; the bubble of described water electrolytic gas and gaseous state fossil fuel is assembled in a large number in the lower face side of above-mentioned demarcation strip; thereby causing to be moved upward stagnates or is moved upward and cause the movable lifting unit of described demarcation strip to rise or descend; by detecting the shift in position of this movable lifting unit, controlling organization can be controlled and supply with stopping or opening (beginning once more) of water electrolytic gas and gaseous state fossil fuel in mixing channel.
In the technical scheme 7 described water electrolytic gas fuel combination generating means,, supply with stopping or opening (beginning once more) and control of water electrolytic gas and gaseous state fossil fuel in the controlling organization subtend mixing channel by detecting the variation of mixing channel pressure inside.
In the technical scheme 8 described water electrolytic gas fuel combination generating means, when the pressure in detecting mixing channel is identical with the setting pressure that stops supply gaseous state fossil fuel in mixing channel, stop in mixing channel, to supply with water electrolytic gas, when the pressure in detecting mixing channel was lower than this setting pressure, water electrolytic gas was supplied with in beginning (beginning once more) in mixing channel.
In the technical scheme 9 described water electrolytic gas fuel combination generating means, as shown in Figure 3 a kind of, apparatus for generating water electrolytic gas be used to produce electrolysis gas and it is transported to above-mentioned water electrolytic gas feed mechanism, it has electrolytic cell, water electrolytic gas-electrolyte separating tank, electrolyte is forced cooling body and circulate electrolyte mechanism, this electrolytic cell has the electrolyte introducing port, outlet, positive plate, minus plate and electrolyte rotational flow mechanism, wherein, the electrolyte introducing port is arranged on the bottom side of electrolytic cell, outlet is arranged on the top side of electrolytic cell, be used for discharging electrolyte and water electrolytic gas mixture, positive plate is arranged on the bottom side of this electrolytic cell inside, minus plate is arranged on the top side of electrolytic cell inside, electrolyte rotational flow mechanism is not electrically connected with other parts, flows while be used for making alkaline electrolyte to rotate to the direction of minus plate from positive plate; The water electrolytic gas that outlet on electrolytic cell is discharged and the mixture of electrolyte are discharged into water electrolytic gas-electrolyte separating tank, wherein water electrolytic gas and electrolyte is carried out gas-liquid separation, separate the gas that obtains and be discharged to the outside, electrolyte is left in the separating tank; Electrolyte forces cooling body that the electrolyte that remains in the separating tank is forced cooling; Circulate electrolyte mechanism makes the circulate electrolyte in the separating tank arrive electrolytic cell one side.
In the technical scheme 10 described water electrolytic gas fuel combination generating means, as shown in Figure 4, being arranged on interior positive plate of electrolytic cell and the electrolyte rotational flow mechanism between the minus plate is made up of the metallic plate of regulation sheet number, every metallic plate is provided with the flow-through opening of 2～6 symmetries in the position of off-centered outer circumferential side, be configured by the angle that the flow-through opening on the different metal plate is offset successively regulation electrolyte is rotated when mobile.
In the technical scheme 11 described water electrolytic gas fuel combination method for generation, to import in the mixing channel with the bubble state by water electrolytic gas that water obtained in the electrolysis alkaline electrolyte and gaseous state fossil fuel, be loaded with organic solutions such as alkanes, alcohols, ethers in the described mixing channel, in mixing channel inside, repeating the even married operation of the above-mentioned water electrolytic gas that is imported into.Movable lifting unit is for carrying out the movable structure of lifting action, a plurality of demarcation strips are installed on it, offer the micropore that the bubble of a plurality of above-mentioned water electrolytic gas and gaseous state fossil fuel is difficult for passing through on the described demarcation strip, described demarcation strip is provided with the approaching state along continuous straight runs of outer peripheral face and mixing channel inwall, liquid-immersed by institute's splendid attire in the above-mentioned mixing channel.The bubble of above-mentioned water electrolytic gas and gaseous state fossil fuel is assembled in a large number in the lower face side of above-mentioned demarcation strip; thereby being moved upward the movable lifting unit that can cause when stagnation or bubble are moved upward by this micropore above-mentioned demarcation strip is installed rises or descends; by detecting the shift in position of movable lifting unit; control is to stopping of supplying with in mixing channel of above-mentioned water electrolytic gas and/or gaseous state fossil fuel or open, quantity delivered, predetermined component ratio; water electrolytic gas and gaseous state fossil fuel constantly mix, and generate the water electrolytic gas fuel combination.
In the technical scheme 12 described water electrolytic gas fuel combination method for generation, by detecting the variation of mixing channel pressure inside, controlling organization control is supplied with stopping of water electrolytic gas and gaseous state fossil fuel or is opened in described mixing channel.
In the technical scheme 13 described water electrolytic gas fuel combination method for generation, pressure in detecting described mixing channel is identical with the setting pressure that stops in described mixing channel supplying with the gaseous state fossil fuel and when furnishing good supplies to stop condition, stop to supply with water electrolytic gas in described mixing channel; When the pressure in detecting mixing channel was lower than this setting pressure, beginning (beginning once more) was supplied with water electrolytic gas in described mixing channel.
[invention effect]
Adopt the water electrolytic gas fuel combination generating means among the present invention, to import to the bottom of mixing channel by water electrolytic gas that water obtained in the electrolysis alkaline electrolyte and the pressurization of gaseous state fossil fuel, the inside of one or more organic solutions of the alkanes of institute's splendid attire, alcohols, ethers etc. in mixing channel then, the water electrolytic gas that carries out air bubble-shaped repeatedly with as the mixing of the gaseous state fossil fuel of raw material, obtain the water electrolytic gas fuel combination thus.Above-mentioned water electrolytic gas and gaseous state fossil fuel are imported with the bubble attitude in the mixing channel, and these bubble coalescence are mixed, assembled in the lower face side of the demarcation strip with micropore that a large amount of bubbles are difficult for passing through.This demarcation strip is installed on the movable lifting unit with movable structure that can lifting in mixing channel integratedly, and simultaneously, demarcation strip is provided with by along continuous straight runs with the state of its outer peripheral face near the mixing channel inwall, is contained in the liquid-immersed of mixing channel inside.
In the present invention, because demarcation strip is provided with the micropore that the bubble of a large amount of water electrolytic gas and gaseous state fossil fuel is difficult for passing through, so accumulate in the lower face side of demarcation strip in a large number and form aggregation from the above-mentioned bubble of the pressurized importing in bottom of mixing channel, take place to be detained and to cause above-mentioned mixing channel internal pressure to raise in the process that aggregation is moved upward, and then cause being equipped with the movable lifting unit rising of this demarcation strip.After this bubble coalescence body was destroyed, bubble can be moved upward by the micropore on the demarcation strip, is accompanied by above-mentioned action, and movable lifting unit descends.Utilize touch sensor to measure the rising of above-mentioned movable lifting unit or the shift in position of decline, perhaps utilizing pressure sensor to measure the mixing channel pressure inside changes, when movable lifting unit rises or after mixing channel inside becomes high pressure, close the power supply of apparatus for generating water electrolytic gas, stop the supply of water electrolytic gas, close choke valve simultaneously, stop the supply of gaseous state fossil fuel in mixing channel.
Adopt said structure, the water electrolytic gas fuel combination that will produce according to the present invention mixes with existing liquefied natural gas (LNG) or liquefied petroleum gas (LPG) etc., and when warming machine is used the burner internal combustion, about 40% of consumption when obtaining the required LPG consumption of equal heat for simple burning LPG has reduced fuel consumption largely.In addition, owing to can stop the supply of water electrolytic gas under certain condition, can reduce the electric weight that consumes when apparatus for generating water electrolytic gas moves.Like this, the water electrolytic gas fuel combination of discharging from output mechanism can obtain completing combustion basically.
As described above water electrolytic gas is mixed mutually with the gaseous state fossil fuel, can improve efficiency of combustion greatly, reduced significantly simultaneously to obtaining the consumption of the required fossil fuel of regulation heat.In addition, about the water electrolytic gas that water obtained in the above-mentioned electrolysis alkaline electrolyte, the device that the applicant can utilize Japanese patent application laid to be willing to that 2008-277756 invention disclosed name is called in " apparatus for generating water electrolytic gas " obtains water electrolytic gas.Adopt that this apparatus for generating water electrolytic gas continues, the gas that produces electrolysis efficiently, and utilize above-mentioned water electrolytic gas feed mechanism that water electrolytic gas is imported in the mixing channel.In addition, owing to be to utilize the brine electrolysis gas that produces electrolysis basically, so abundant raw material is with low cost.
Like this, by the cheap and abundant like this raw material of water is carried out the water electrolytic gas that electrolysis obtains, can improve the efficiency of combustion of hydrocarbons or other carbonaceous materials of gaseous state.Obtain the water electrolytic gas fuel combination by in the gaseous state fossil fuel, sneaking into water electrolytic gas, have the effect that improves caloric value, have large improvement from this viewpoint tool of effective use of energy sources.
The water electrolytic gas fuel combination that employing obtains according to the present invention can obtain strong combustion reaction as described above.In addition, owing to containing the gas that liquid organic solution gasification such as alkanes because of splendid attire in the above-mentioned mixing channel, alcohols, ethers produces in the water electrolytic gas fuel combination among the present invention, so combustion reaction is become vivaciously acutely.Relevant combustion reaction is not only applicable to burners such as simple heater, warming machine, also be applicable to the burner of broad sense, the hot machine of various use fuel gas such as internal combustion engine, gas turbine, jet engine for example, the water electrolytic gas fuel combination that is obtained according to the present invention can be used as the fuel of above-mentioned various hot machines.
Adopt the present invention, become vivaciously by water electrolytic gas and suitable gaseous state fossil fuel are mixed the burning that makes the gaseous state fossil fuel, thereby obtain stronger firepower.Like this, this existing method of burning with using airborne oxygen is compared, and has reduced by 60% for obtaining the identical gaseous state fossil fuel amount that heat consumed.Therefore, reduce to some extent in the air capacity that burning is consumed the time,, reduced the shared ratio of emission amount of carbon dioxide of its generation so improved heating efficiency for obtaining identical heat.Certainly, when saving, effectively utilizing the limited fossil fuel of reserves, also be beneficial to the minimizing global greenhouse effect.In addition, owing to can significantly reduce oxysulfide (SO
X) and nitrogen oxide (NO
X) discharge capacity, so very effective for reducing environmental pollution.
Description of drawings
(A) expression is the simple profile of the water electrolytic gas fuel combination generating means among the present invention among Fig. 1, (B) profile of the A-A line in Biao Shi edge (A).
What Fig. 2 represented is the schematic diagram of gas with the configuration example of electrolytic cell that produce electrolysis of the apparatus for generating water electrolytic gas among the present invention.
What Fig. 3 represented is the schematic diagram of the basic structure of the employed apparatus for generating water electrolytic gas of water electrolytic gas fuel combination generating means among the present invention.
Fig. 4 represents is the schematic diagram of configuration example of the electrolytic cell of the apparatus for generating water electrolytic gas shown in Fig. 3.
Fig. 5 represents is the schematic diagram of the configuration example of the single piece of sheet metal of employed metallic plate group in the electrolytic cell of the apparatus for generating water electrolytic gas shown in the pie graph 3.
Fig. 6 is the configuration photo of demo plant integral body that the performance of the water electrolytic gas fuel combination that obtains according to the present invention is confirmed.
Fig. 7 is the photo of expression flame status of burner noz(zle) ejection from demo plant, and demo plant wherein is used to confirm the performance of the water electrolytic gas fuel combination of acquisition according to the present invention.
Fig. 8 is the figure according to the configuration photo made of demo plant integral body shown in Figure 6.
Fig. 9 is the figure according to the expression shown in Figure 7 photo made of the flame status of burner noz(zle) ejection from demo plant.
[symbol description]
10: the water electrolytic gas equipment for producing mixed fuel, 11: mixing channel, 12: the water electrolytic gas feed mechanism, 13: the fossil fuel feed mechanism, 14: water electrolytic gas fuel combination output mechanism, 15: movable lifting unit, 16: the outer peripheral face outer frame, 17: the upper surface outer frame, 20: controlling organization, 30: apparatus for generating water electrolytic gas (electrolysis unit), 31: electrolyte introducing port, 32: positive plate (anode), 33: minus plate (negative electrode), 34: electrolyte rotation circulation mechanism's (metallic plate group), 34-1～n: metallic plate, 35: the mixture outlet, 36: electrolyte supply mouth, 37: tubular insulator, 38: in-line filter, 39: the electrolyte outlet, 40: gaseous state fossil fuel feedway (gas bomb), 41: introducing port, 42: electrolyte outlet, 43: cooling electrolyte introducing port, 44: circulating pump, 45: gas discharge outlet, 47: electrolyte is by opening (opening), 51,52,53: demarcation strip, 54: dip portion, 55,56,57: pitman, 58: peristome, 60: the fuel use device, 102,103: non-return valve, 300: the gas that produces electrolysis electrolytic cell (electrolytic cell), 301: water electrolytic gas-electrolyte separating tank (separating tank), 302: electrolyte is forced cooling body, 303: circulate electrolyte mechanism, C: central point, L: liquid, S: gap.
The specific embodiment
Next, with reference to accompanying drawing water electrolytic gas equipment for producing mixed fuel and production method among the present invention are described.(A) is the schematic diagram that is used for illustrating the present invention's water electrolytic gas equipment for producing mixed fuel among Fig. 1, and (B) is the profile along the A-A line in (A) among Fig. 1.Fig. 2 is the water electrolytic gas equipment for producing mixed fuel among the present invention and the schematic diagram of relevant peripheral device.As shown in the figure, water electrolytic gas equipment for producing mixed fuel 10 among the present invention comprises mixing channel 11, water electrolytic gas feed mechanism 12, gaseous state fossil fuel feed mechanism 13 and water electrolytic gas fuel combination output mechanism 14, wherein, be loaded with organic solution L such as alkanes, alcohols, ethers in the mixing channel 11, in mixing channel 11, repeating to carry out the water electrolytic gas of the air bubble-shaped that imports from the bottom and the married operation of gaseous state fossil fuel; Water electrolytic gas feedway 12 will supply to mixing channel 11 by the water electrolytic gas that water obtained in the electrolysis alkaline electrolyte; Fossil fuel feed mechanism 13 supplies to mixing channel 11 with the gaseous state fossil fuel; Water electrolytic gas fuel combination output mechanism 14 is discharged into the water electrolytic gas fuel combination that above-mentioned water electrolytic gas and gaseous state fossil fuel constantly mix generation in the fuel use device 60.
Be provided with movable lifting unit 15 in the inside of mixing channel 11, this movable lifting unit 15 is can be at the movable structure of the inner lifting of mixing channel, on movable lifting unit 15, be provided with dip portion 54, demarcation strip 53, demarcation strip 52 and demarcation strip 51 regularly with its one, wherein, dip portion 54 can be disposed thereon from the mode that outer peripheral face outer frame 16 breaks away from its side face end; By the pitman 57 that four stainless steels are made, demarcation strip 53 interfixes with dip portion 54; By pitman 56, demarcation strip 52 interfixes with demarcation strip 53; By pitman 55, demarcation strip 51 interfixes with demarcation strip 52.In order to make above-mentioned movable lifting unit 15 rise or to descend, be formed with the gap S about 5～10mm between the upper surface of dip portion 54 and the upper surface outer frame 17 along with the variation of mixing channel air pressure inside.
Dip portion 54 forms the circular plate type that central authorities have peristome 58, is used for the water electrolytic gas fuel combination is imported to water electrolytic gas fuel combination output mechanism 14.In addition, because what use in the present embodiment is mixing channel 11 cylindraceous, so, dip portion 54 and demarcation strip 51,52,53 are circular plate type, but the shape of dip portion 54 and demarcation strip is not limited to circular plate type, can be and the corresponding shape of the shape of this mixing channel, for example polygons such as pentagon, hexagon, heptagon.Certainly, the shape of this mixing channel 11 can be various polygons.
Be formed with the micropore that the bubble of a plurality of water electrolytic gas and gaseous state fossil fuel is difficult for passing through on the demarcation strip of installing on the movable lifting unit 15 51,52,53, liquid-immersed in the mixed grooves 11 of demarcation strip 51,52,53, and the equal along continuous straight runs setting of each demarcation strip, the inwall of its outer peripheral face and mixing channel 11 is approaching.The thickness of nethermost demarcation strip 51 is 0.5～2.5mm, preferred 1～2mm, and micro-pore diameter is 0.5～3.5mm on it, preferred 1～3mm, the material of demarcation strip 51 can adopt stainless steel or resin.Micro-pore diameter on the demarcation strip 52,53 of its top is 0.2～1.5mm, the plate shaped network structure body that stainless steel about preferred 0.3～1mm or resin are made.In addition, when demarcation strip 51,52,53 was formed from a resin, its thickness of slab can be that 10～15mm, micro-pore diameter can be 3～10mm, and the shape that is formed at the micropore on the demarcation strip can be the taper shape of tip towards the top.
Being provided with the purpose that polylith is formed with the demarcation strip of a plurality of micropores as described above, is for the water electrolytic gas of regulating air bubble-shaped and the holdup time and the pressure of gaseous state fossil fuel, mixes uniformly really to guarantee the two.Though three demarcation strips are installed on the movable lifting unit 15 in the present embodiment, be not limited thereto, can adopt diameter and the corresponding polylith demarcation strip more than of density with the micropore that forms.Though the movable structure of movable in the present embodiment lifting unit is the peripheral end face by dip portion 54 to be arranged on the upper end of periphery outer frame 16 in departing mode and to realize, but be not limited thereto, also can adopt following structure, for example, the pitman 57 that will be used for being connected and fixed dip portion 54 and demarcation strip 53 and the bottom of the connecting portion of demarcation strip 53 are as detent, make the pitman insertion section of demarcation strip make big opening so that its relatively pitman carry out lifting action.
In addition, the structure of movable lifting unit 15 is according to the formation condition of the gaseous state fossil fuel that uses this device with the fuel combination of water electrolytic gas, can do the adaptability adjusting for the spacing between each demarcation strip 51,52,53 that is mounted thereon.This spacing is adjusted as follows: the pitman of cut-and-dried all lengths is processed into the length identical with desired spacing, perhaps, utilizes screw that pitman is connected with each demarcation strip, setting pitman is that specific length is to form expectation at interval by the screw adjustment.According to the kind of liquid such as the alkanes of splendid attire in the mixing channel, alcohols, ethers, viscosity, volume, temperature etc., simultaneously the kind of gaseous state fossil fuel, quantity delivered, the scale of device, generation of water electrolytic gas fuel combination etc. are taken in, come diameter and density to the micropore that forms on the demarcation strip, and the spacing of each demarcation strip, the configuration regulate, in the hope of mixing velocity and the growing amount that reaches regulation.
Splendid attire exceeds uppermost demarcation strip 53 in organic solution L such as the alkanes of mixing channel 11 inside, alcohols, ethers., for example can select gasoline, ethanol, methyl alcohol, dimethyl ether, kerosene etc. herein for use as organic solutions such as alkanes, alcohols, ethers.For example can select liquefied petroleum gas (LPG), liquefied natural gas (LNG), dry distillation coal gas etc. for use by the gaseous state fossil fuel that fossil fuel feed mechanism 13 is supplied with.
In addition, can contain the gas that produces because of the gasification of organic solutions such as the alkanes in the mixing channel, alcohols, ethers in the water electrolytic gas fuel combination that produces utilizing device of the present invention, this gas can be used as the combustion adjuvant of water electrolytic gas fuel combination, can obtain stronger active combustion reaction thus.At this moment, need suitably in mixing channel, to replenish organic solution L.
In order to overcome the hydraulic pressure of organic solutions such as alkanes in the mixing channel, alcohols, ethers, need apply certain pressure could be imported in the mixing channel by water electrolytic gas and the gaseous state fossil fuel that water electrolytic gas feed mechanism 12 and fossil fuel feed mechanism 13 are supplied with, institute's applied pressure is 0.05～0.2MPa, about preferred 0.08～0.15MPa.In addition, water electrolytic gas feed mechanism 12 and fossil fuel feed mechanism 13 are provided with non-return valve 102,103, this non-return valve be used for preventing being injected into liquid in the above-mentioned mixing channel from the mixing channel adverse current to apparatus for generating water electrolytic gas 30 or gaseous state fossil fuel feedway such as gas bomb 40 in, particularly when the generation that can reliably prevent adverse current in the mixing channel during for high pressure.
Device among the present invention is provided with controlling organization 20 (with reference to Fig. 2), be used for controlling to mixing channel supply with water electrolytic gas with and/or the gaseous state fossil fuel stop or open, the ratio of quantity delivered, predetermined component etc.The bubble of water electrolytic gas and gaseous state fossil fuel accumulates in the demarcation strip lower face side in a large number and forms the bubble coalescence body, this bubble coalescence body is moved upward to be stagnated and causes being equipped with and rise on the position of movable lifting unit 15 of demarcation strip, by this shift in position of detection such as touch sensors, controlling organization 20 control apparatus for generating water electrolytic gas 30 and gaseous state fossil fuel feedway 40 stop to supply with water electrolytic gas and gaseous state fossil fuel in mixing channel.On the other hand, the bubble coalescence body is destroyed, bubble is moved upward the movable lifting unit 15 that causes by this micropore and descends, and by detecting this shift in position, controlling organization 20 controls begin or begin once more (opening) again and supply with water electrolytic gas and gaseous state fossil fuel to mixing channel.
In addition; detect stagnation that is moved upward because of above-mentioned bubble or the variation that is moved upward the pressure inside of the mixing channel that causes by pressure sensor, above-mentioned controlling organization 20 is supplied with stopping of water electrolytic gas and gaseous state fossil fuel in can the subtend mixing channel or is opened (beginning once more) and control.When the pressure inside of mixing channel is identical with the setting pressure that stops to supply with the gaseous state fossil fuel in mixing channel, above-mentioned controlling organization 20 controls stop to supply with water electrolytic gas in mixing channel, when the pressure inside of mixing channel was lower than this setting pressure, water electrolytic gas was supplied with in above-mentioned controlling organization 20 control beginnings (beginning once more) in mixing channel.
Above-mentioned stop/open (the beginning once more) of supplying with water electrolytic gas in mixing channel moves, be to utilize the ON/OFF switching controls of the startup power supply of the apparatus for generating water electrolytic gas that the back will narrate to realize, that supplies with the gaseous state fossil fuel in mixing channel stops/opens (beginning once more) action, is that the choke valve that is arranged on by open and close controlling on the gas bomb 40 such as liquefied petroleum gas is realized.In addition, though the control device that the action of above-mentioned each composed component integral body is controlled can also be set, owing to be prior art well-known to those skilled in the art, and belong to better simply structure, its detailed description of Therefore, omited.
What Fig. 3 represented is the schematic diagram of the basic structure of the employed apparatus for generating water electrolytic gas of water electrolytic gas fuel combination generating means among the present invention, and what Fig. 4 represented is the schematic diagram of gas with the configuration example of electrolytic cell that produce electrolysis.Employed apparatus for generating water electrolytic gas 30 comprises produce electrolysis gas electrolytic cell 300, water electrolytic gas-electrolyte separating tank 301, electrolyte forced cooling device 302 and electrolyte circulation means 303 among the present invention.Also preferably on electrolyte circulation means 303, in illustrated position or copy the configuration example of other devices of the same race that in-line filter 38 and electrolyte outlet 39 etc. are set in position, wherein, in-line filter 38 is used for impurity screening, and electrolyte outlet 39 is used for the electrolyte in the removal system.
In the bottom of above-mentioned electrolytic cell 300 electrolyte introducing port 31 is set.Bottom side at electrolytic cell 300 is provided with positive plate 32, and side is provided with minus plate 33 at an upper portion thereof, and the metallic plate 34-1～34-n that is arranged at intervals with regulation sheet number to stipulate between two electrodes is as electrolyte rotational flow mechanism.Positive plate 32 and minus plate 33 can be made by stainless steel 304 or stainless steel 316 (Japanese specification).Will narrate as the back, above-mentioned each metallic plate group 34 is by various plastics system tubular insulator 37 fixed bearings, do not form with two battery lead plates 32,33 or other positions to be electrically connected.In addition, though be not electrically connected between each metallic plate, but has different current potentials on each metallic plate, this is owing to be full of electrolyte layer between positive plate 32 and the minus plate 33, so must form electric potential gradient and produce potential difference from the anode side cathode side, the current potential that has on each metallic plate is corresponding with the potential difference that this electric potential gradient produces, and metallic plate group 34 has played and guaranteed that rotating flow crosses the effect of homogeneity of the electrolyte in metallic plate zone.
In the present invention, force circulate electrolyte by utilizing electrolyte circulation means, and utilize metallic plate group 34 to make the electrolyte rotational flow as electrolyte rotational flow mechanism, can suppress the rising of temperature in the electrolytic cell 300, thereby can fix supporting metal sheets group 34 with plastic outer frameworks such as vinyl chloride.Like this, can reduce the manufacturing cost of electrolytic cell significantly.In addition, can be by the generation of avoiding with the outside of insulator encirclement electrolytic cell leaking electricity.Can be that 1.8V sets the interval between metallic plate 34-1～34-n for example according to making the potential difference between adjacent metal sheets.Like this, electrolyte from anode through metallic plate group 34 rotational flows of regulation sheet number to the process of negative electrode water by electrolysis.Thereby can produce electrolysis gas.Therefore,, both can quicken the generation of the water electrolytic gas in the electrolytic cell, can increase the growing amount of water electrolytic gas again by configuration multi-disc metallic plate.The mixture of water electrolytic gas and electrolyte is discharged by the outlet 35 from the top.
Fig. 5 represents to constitute the embodiment of the single metal plate of metallic plate group 34, wherein, metallic plate group 34 gas that produces electrolysis forms with the arranged spaced of stipulating with the metallic plate of the sheet number that will stipulate between anode in the electrolytic cell 300 and the negative electrode (for example from about 10 to more than 100).In addition, though in Fig. 5 this metallic plate be shaped as circle, also can be that pentagon, hexagon, heptagon etc. are various polygon-shaped.At metallic plate is in the embodiment of circle, offers 47,4 electrolyte circulation openings of 4 electrolyte circulation openings, 47 relative central point C on the every metallic plate and is centrosymmetric.In addition, because what adopt in the present embodiment is circular metallic plate, so, the outer framework of these metallic plate groups of fixed bearing also is cylindric, but the shape of the outer framework of fixed bearing metallic plate group is not limited to cylindric, when metallic plate was the such polygon of pentagon, hexagon, heptagon, outer framework can be the polygon cylindrical body corresponding with the shape of this metallic plate.
The purpose that electrolyte circulation opening 47 is set on above-mentioned single piece of sheet metal is to make water electrolytic gas and electrolyte flow to cathode side from anode-side.Assemble the fixedly circular metal plate of institute's chip select number according to following mode: the opening 47 on each sheet metallic plate is offset the angle (for example being offset 15 ° successively shown in (1)～(6) among Fig. 5) of regulation successively.Like this, opening on the metallic plate 34-1 of the most close relative anode one side, opening with the metallic plate 34-2 of predetermined distance side disposed thereon for example has been offset 15 ° in the counterclockwise direction, the opening of the metallic plate 34-3 of metallic plate 34-2 upside further has been offset for example 15 ° along same direction, by that analogy, the opening of each metallic plate is offset suitable angle successively, simultaneously, the suitable quantity of the sheet number of metallic plate for selecting from tens of to 100 tens of, the metallic plate of these quantity is by tubular insulator fixed bearing.In addition, the deviation angle of opening is not limited to 15 °.
The DC voltage that applies between positive plate and the minus plate is according to being arranged on the sheet number of the metallic plate group between positive plate and the minus plate and deciding, and preferably can make potential difference between adjacent metal sheets be roughly the DC voltage of 1.8V.In addition, the opening 47 on each metallic plate is offset for example 15 ° of the angles of regulation successively from the anode-side to the cathode side, like this, the electrolyte that flows through is fitly arranged, and shape passes through opening in the shape of a spiral.The electrolyte that flows to the direction of negative electrode through above-mentioned metallic plate group (be about to each metallic plate and be offset the metallic plate group that the angle of regulation is configured successively) from anode according to opening, along the glide path that sheet number and deviation angle are determined that is provided with, form the upwelling that is accompanied by rotational flow by the metallic plate group.Like this, electrolyte has been subjected to well-regulated stirring in process of flowing, has therefore promoted cell reaction, thereby can improve the production rate of water electrolytic gas.
In addition, because the opening of metallic plate has the effect that can promote that the water electrolytic gas that produces in the cell reaction rises as constituted above, so 4～6 openings can be set on every metallic plate.In addition, the electrolyte supply mouth 36 that the band valve is set in the upper end of above-mentioned electrolytic cell 300 replenishes new electrolyte.This electrolyte supply mouth 36 also can be installed in other positions, for example can with pipeline that the electrolyte introducing port 31 of lower end is connected on flow divider is installed, carry out the supply of electrolyte by this flow divider.
The water electrolytic gas of discharging from electrolytic cell 300 and the mixture of electrolyte import from the introducing port 41 of the bottom side of separating tank 301.At this moment, the mixture of water electrolytic gas and electrolyte is in squit hole is discharged into separating tank 301, and wherein, squit hole is outstanding in groove from the bottom of separating tank 301, a plurality of micropores is set on it, or is formed by porous mass.The resistance that the water electrolytic gas component is subjected to by by the squit hole that micropore is set or formed by porous mass time the and electrolyte by the time resistance that is subjected to different, promoted the dispersion of gas component thus, promoted gas-liquid separation preferably.The gas component of the water electrolytic gas that is obtained by gas-liquid separation derives from the gas discharge outlet 45 that is arranged on separating tank 301 upper ends via pipeline like this, by water electrolytic gas feed mechanism 12 pressurized importing in the mixing channel 11.
Through after the above-mentioned gas-liquid separation, the electrolyte that remains in the separating tank is discharged from the electrolyte outlet 42 that is arranged on the separating tank bottom, a part is transported in the electrolyte forced cooling device 302 and after being cooled to preference temperature, the cooling electrolyte introducing port 43 of the bottom through being arranged on separating tank turns back in the separating tank.At this moment, though the temperature of the electrolyte in the electrolytic cell 300 is different because of the difference of ambient temperature or generation gas collecting amount, preferably be roughly 18 ℃～25 ℃.For reaction temperature, cross and lowly then to cause the cell reaction instability, the too high cell reaction inefficiency that then causes, thus preferably with the temperature maintenance of the electrolyte in the electrolytic cell 300 in above-mentioned scope.
Be not transported to the remaining electrolyte of electrolyte forced cooling device 302, be circulated to electrolytic cell 300 through electrolyte circulation means 303 and in-line filter 38.This moment is as for ratio how to choose the electrolyte that is transported to forced cooling device 302, and how to determine to be recycled directly to electrolyte content in the electrolytic cell 300, can solve by adding control device, promptly, temperature according to operating environment, the for example temperature of ambient temperature, electrolyte self, and running time utilizes this control device that the numerical value of these two is carried out the best increase and decrease.Said structure is applicable to the device with following structure, that is, be provided with an electrolyte outlet as shown in Figure 3 in separating tank bottom, electrolyte be split into two parts midway at conduit, a part is transported to electrolyte forced cooling device 302, and a part is recycled to electrolytic cell 300.
In addition, also can the electrolyte outlet be set in addition in the separating tank bottom, be used for carrying out other one road circulation of supplying with the electrolyte of electrolytic cell, make and be recycled to electrolytic cell from this electrolyte outlet by electrolyte circulation means (for example pump) after remaining in the interior electrolyte of separating tank is cooled to proper temperature, on the other hand, the electrolyte of discharging from another outlet is recycled in the separating tank through cooling electrolyte introducing port by being arranged on the circulating pump 44 on the electrolyte forced cooling device 302 independently.
Produce water electrolytic gas by the apparatus for generating water electrolytic gas with said structure, the water electrolytic gas of generation is discharged from the gas discharge outlet 45 of the upper end that is arranged on separating tank, in water electrolytic gas feed mechanism 12 pressurized importing mixing channels 11 high-efficiency continuously.Supplied to mixing channel from the water electrolytic gas and the gaseous state fossil fuel of apparatus for generating water electrolytic gas 30 and gas bomb 40 pressurized importings with the bubble state, above-mentioned bubble gathers the lower face side of nethermost demarcation strip 51 at first in a large number, forms the bubble coalescence body and also mixes constantly.Through certain hour, the destroyed formation micro-bubble of this bubble coalescence body, micro-bubble mixes once more by being formed at the lower face side that gathers demarcation strip 52 behind the micropore on the demarcation strip 51.Afterwards, this bubble coalescence body is broken to micro-bubble, similarly by being formed at the lower face side that gathers demarcation strip 53 behind the micropore on the demarcation strip 52, mixes constantly.Be fed into fuel use device 60 by carrying out the water electrolytic gas fuel combination that gathering as described above and mixing produce repeatedly through water electrolytic gas fuel combination output mechanism 14.
[embodiment 1]
Fig. 6 is the configuration photo of demo plant integral body that the performance of the water electrolytic gas fuel combination that obtains according to the present invention is confirmed, and Fig. 7 is the photo of the flame status of the burner noz(zle) ejection of expression from demo plant.Fig. 8 and Fig. 9 are respectively the figure according to the photo made of Fig. 6 and Fig. 7.In Fig. 8 and Fig. 9, be followed successively by the generating means 10, apparatus for generating water electrolytic gas 30 and the control device 20 that blow out flame burning nozzle 60, water electrolytic gas fuel combination from left to right.In addition, the LPG gas bomb 40 as the fossil fuel feedway is set at outdoor.
The structure of the generation device of the water electrolytic gas fuel combination in the above-mentioned experimental provision is, be perfused with gasoline in mixing channel inside, in this mixing channel, dispose movable lifting unit with movable structure, be installed with dip portion and three demarcation strips by stainless steel pitman on this movable lifting unit, nethermost demarcation strip is that thickness is the corrosion resistant plate about 1.5mm, be formed with diameter on it and be the micropore about 1.5mm, the demarcation strip of its top is stainless network structure body, is formed with diameter and is the micropore about 0.5mm.
Water electrolytic gas and LPG supply with from the bottom of the mixing channel of experimental provision with said structure, and wherein, water electrolytic gas is produced by apparatus for generating water electrolytic gas, and LPG is supplied with by the LPG gas bomb that pressure is set at 0.1MPa.At this moment, in apparatus for generating water electrolytic gas, utilize the alkaline potassium hydroxide electrolyte gas that produces electrolysis, needle-valve also is set the water electrolytic gas that imports to mixing channel and the amount of LPG are finely tuned respectively.In addition, as the attachment device of burning water electrolytic gas air mixture, can be the large-scale warming machine LPG burner noz(zle) of Off Le エ Application ネ Star Co., Ltd. production model of using such as commercial heater unit as ELGU150.The LPG rated consumption of this burner noz(zle) is 2.4m
3/ h.
Experiment is carried out in a laboratory building of area, the Northeast (outstanding Yu Xian), and the careat of this laboratory building is 180m
2, the roof is stamped galvanized steel plain sheet, the about 5m of ceiling average height, and the experimental provision as constituted above that turns round, temperature is set at 20 ℃, tests several times respectively in one hour.Start experimental provision, though when about 15 minutes of beginning after mixing channel is supplied with water electrolytic gas and LPG, stopped the running of apparatus for generating water electrolytic gas, and stopped the importing of water electrolytic gas and LPG, but the fired state that does not observe the water electrolytic gas air mixture changes.Again through 15 minutes, start apparatus for generating water electrolytic gas once more afterwards, beginning imports water electrolytic gas and LPG (beginning once more) in mixing channel.In this experiment, carry out above-mentioned stop, open (beginning once more) off and on repeatedly and move.
Test 1:2008 January 18, weather: the moon, 3.2 ℃ of outdoor temperatures, room temperature is 2.5 ℃ before the beginning
Experiment 2:2008 January 19, weather: fine, 0.5 ℃ of outdoor temperature, room temperature-0.2 ℃ before the beginning
Temperature with warming machine ejection is 45 ℃, and room temperature is set at 20 ℃ and is as the criterion and makes device running one hour respectively.The measured value of comprehensive twice test, the average consumption of LPG are 0.71m
3/ h can make room temperature reach more than 18.5～20 ℃.
This moment, the average consumption of LPG was 0.71m
3/ h, only be burner the LPG rated consumption about 40%.In addition, through liquid level instrumentation amount, the gasoline during experiment in the mixing channel has only reduced amount seldom.In addition,, compare with the consumption of the fossil fuel that reduces though need consume several years electricity and the some water of supply when carrying out with the synchronous brine electrolysis of experiment, or inappreciable.
In addition, concentration of carbon dioxide is 10.7% in the burning A heavy oil institute exhaust gas discharged, concentration of carbon dioxide is 11.63% in the burning LPG institute exhaust gas discharged, compares carbon dioxide (CO in the fuel institute exhaust gas discharged that burning obtains according to the present invention with the two
2) concentration be 5.4%, the carbon dioxide (CO that the latter produces
2) obviously minimizing of amount.Nitrogen oxide (NO in the burning A heavy oil institute exhaust gas discharged
X) concentration be 79ppm, compare with it, the concentration of the nitrogen oxide in the fuel institute exhaust gas discharged that burning obtains according to the present invention is 39ppm, the concentration of the nitrogen oxide that the latter produces is obviously lower.740 ℃ the ignition temperature that obtains during with burning A heavy oil is compared, and its ignition temperature is for deserving to be called 1,010 ℃ of high temperature during fuel that burning the present invention obtains.
[industrial application]
The generating means of the water electrolytic gas fuel combination among the present invention is by detecting movable lifting unit Rising and the variation of the internal pressure in the shift in position of decline or the mixing channel, control In mixing channel, supply with stopping of water electrolytic gas and gaseous state fossil fuel, so, with the present invention The middle water electrolytic gas fuel combination that produces supplies to the heating burners such as existing burning LPG Make its mixed combustion, for the amount that obtains the LPG that the regulation heat consumes when only burning LPG 40% of the LPG that consumes, in addition, under certain condition, by stopping to supply with water electrolytic gas The electric weight that consumes in the time of can reducing apparatus for generating water electrolytic gas work.
The water electrolytic gas fuel combination that utilizes the apparatus for generating water electrolytic gas among the present invention to produce can To obtain than the more caloric value of the existing fossil fuel of simple burning, simultaneously several when burning Can not produce impurity. Therefore, owing to significantly improved efficiency of combustion, can reduce fossil The consumption of fuel, the discharge capacity of the carbon dioxide that also significantly having reduced simultaneously burns produces. Like this, owing to be to utilize brine electrolysis to obtain mist, throw so remove the equipment at initial stage Enter fund, the electric weight that main cost consumes when being brine electrolysis is so the cost increase has Limit.
In addition, the water electrolytic gas of the generation of the apparatus for generating water electrolytic gas among the present invention is not only applicable to The device that directly burns at open space that common burner is such also is applicable to airtight Make internal combustion mechanism that liquid fuel or gaseous fuel burn explosively, engine etc. in the space, And other large-sized boilers such as use that liquid, gas, solid-fuelled generating are used, by will Water electrolytic gas adds in the fuel or is ejected in the combustion chamber, can obtain than adopting existing skill The heat energy that art is bigger. In other words, utilize the fuel than prior art much less just can obtain Stronger heat output, thus efficiency of combustion improved significantly. Therefore, not only obtained The energy-saving effect of fuel saving, and can reduce largely the discharge capacity of carbon dioxide, Has positive effect aspect the greenhouse effects that reduce the earth. In addition, in the earth The fossil fuel that reserve is limited can prolong it by effective utilization and utilize the time.
Claims (13)
1. water electrolytic gas fuel combination generating means, it has mixing channel, water electrolytic gas feed mechanism, fossil fuel feed mechanism, water electrolytic gas fuel combination output mechanism, wherein, be loaded with one or more organic solutions such as alkanes, alcohols, ethers in the described mixing channel, in described mixing channel inside, the married operation of the water electrolytic gas of the air bubble-shaped that is repeating to be supplied to and gaseous state fossil fuel; The water electrolytic gas that described water electrolytic gas feedway will produce by the water in the electrolysis alkaline electrolyte supplies to described mixing channel with air bubble-shaped; Described fossil fuel feed mechanism supplies to described mixing channel with the gaseous state fossil fuel with air bubble-shaped; Described water electrolytic gas fuel combination output mechanism constantly mixes above-mentioned water electrolytic gas and gaseous state fossil fuel and the water electrolytic gas fuel combination that produces is discharged into the fuel use device, it is characterized in that having:
Movable lifting unit, described movable lifting unit has the movable structure that can carry out lifting action, a plurality of demarcation strips are installed on it, offer the micropore that the bubble of a plurality of above-mentioned water electrolytic gas and gaseous state fossil fuel is difficult for passing through on the described demarcation strip, described demarcation strip is provided with the approaching state along continuous straight runs of outer peripheral face and described mixing channel inwall, liquid-immersed by institute's splendid attire in the described mixing channel;
Controlling organization, supply with in the described mixing channel of described controlling organization subtend above-mentioned water electrolytic gas and/or gaseous state fossil fuel stop or open, quantity delivered, predetermined component ratio control.
2. water electrolytic gas fuel combination generating means as claimed in claim 1 is characterized in that: splendid attire can be selected arbitrarily from alkanes, alcohols, ethers organic solution in the organic solution of described mixing channel inside.
3. water electrolytic gas fuel combination generating means as claimed in claim 1 or 2 is characterized in that: the gaseous state fossil fuel that described fossil fuel feed mechanism is supplied with can be selected arbitrarily from liquefied petroleum gas LPG, liquefied natural gas LNG, dry distillation coal gas etc.
4. as each described water electrolytic gas fuel combination generating means in the claim 1 to 3, it is characterized in that: the water electrolytic gas fuel combination that described water electrolytic gas fuel combination generating means produces comprises the gas that produces because of the gasification of organic solutions such as above-mentioned alkanes, alcohols, ethers.
5. as each described water electrolytic gas fuel combination generating means in the claim 1 to 4, it is characterized in that: three layers of demarcation strip are installed on the described movable lifting unit, the thickness of nethermost stainless steel demarcation strip is 0.5～2.5mm, micro-pore diameter is 0.5～3.5mm on it, and two demarcation strips of its top are that micro-pore diameter is the plate shaped network structure body of 0.2～1.5mm.
6. as each described water electrolytic gas fuel combination generating means in the claim 1 to 5; it is characterized in that: the bubble of described water electrolytic gas and gaseous state fossil fuel is assembled in a large number in the lower face side of described demarcation strip; thereby being moved upward the movable lifting unit that causes described demarcation strip when stagnating or being moved upward rises or descends; by detecting the shift in position of this movable lifting unit, described controlling organization can be controlled and supply with stopping or opening of water electrolytic gas and gaseous state fossil fuel in described mixing channel.
7. as each described water electrolytic gas fuel combination generating means in the claim 1 to 5; it is characterized in that: by detecting the variation of described mixing channel pressure inside, supply with stopping or driving row control into of water electrolytic gas and gaseous state fossil fuel in the described mixing channel of described controlling organization subtend.
8. as each described water electrolytic gas fuel combination generating means in the claim 1 to 5, it is characterized in that: when the pressure in detecting described mixing channel is identical with the setting pressure that stops supply gaseous state fossil fuel in described mixing channel, stop in described mixing channel, supplying with water electrolytic gas; When the pressure in detecting described mixing channel was lower than this setting pressure, beginning was supplied with water electrolytic gas in described mixing channel.
9. as each described water electrolytic gas fuel combination generating means in the claim 1 to 8, it is characterized in that: apparatus for generating water electrolytic gas be used to produce electrolysis gas and it is transported to described water electrolytic gas feed mechanism, it has electrolytic cell, water electrolytic gas-electrolyte separating tank, electrolyte is forced cooling body and circulate electrolyte mechanism, described electrolytic cell has the electrolyte introducing port, outlet, positive plate, minus plate and electrolyte rotational flow mechanism, wherein, described electrolyte introducing port is arranged on the bottom side of described electrolytic cell, described outlet is arranged on the top side of described electrolytic cell, be used for discharging electrolyte and water electrolytic gas mixture, described positive plate is arranged on the bottom side of described electrolytic cell inside, described minus plate is arranged on the top side of described electrolytic cell inside, described electrolyte rotational flow mechanism is not electrically connected with other parts, flows while be used for making alkaline electrolyte to rotate to the direction of described minus plate from described positive plate; The water electrolytic gas that outlet on described electrolytic cell is discharged and the mixture of electrolyte are discharged into described water electrolytic gas-electrolyte separating tank, wherein water electrolytic gas and electrolyte is carried out gas-liquid separation, separate the gas that obtains and be discharged to the outside, electrolyte is left in the described separating tank; Described electrolyte forces cooling body that the electrolyte that remains in the described separating tank is forced cooling; Described circulate electrolyte mechanism makes circulate electrolyte in the described separating tank to described electrolytic cell one side.
10. the water electrolytic gas fuel combination generating means described in claim 9, it is characterized in that: be arranged on interior positive plate of described electrolytic cell and the electrolyte rotational flow mechanism between the minus plate and form by the metallic plate of regulation sheet number, every metallic plate is provided with the flow-through opening of 2～6 symmetries in the position of off-centered outer circumferential side, be configured by the angle that the flow-through opening on the different metal plate is offset successively regulation electrolyte is rotated when mobile.
11. the production method of a water electrolytic gas fuel combination, it is by mixing the gas fuel combination that produces electrolysis with water electrolytic gas repeatedly with the gaseous state fossil fuel, be characterised in that: will import in the mixing channel with the bubble state by water electrolytic gas that water obtained in the electrolysis alkaline electrolyte and gaseous state fossil fuel, be loaded with alkanes in the described mixing channel, alcohols, one or more organic solutions such as ethers, in described mixing channel inside, repeating the mixed uniformly operation of the above-mentioned water electrolytic gas that is imported into
On movable lifting unit, a plurality of demarcation strips are installed, described movable lifting unit is for carrying out the movable structure of lifting action, offer the micropore that the bubble of a plurality of above-mentioned water electrolytic gas and gaseous state fossil fuel is difficult for passing through on the described demarcation strip, this demarcation strip is with outer peripheral face and the approaching state along continuous straight runs setting of mixing channel inwall, liquid-immersed by institute's splendid attire in the above-mentioned mixing channel
The bubble of described water electrolytic gas and gaseous state fossil fuel is assembled in a large number in the lower face side of described demarcation strip; thereby being moved upward the movable lifting unit that can cause when stagnation or bubble are moved upward by this micropore described demarcation strip is installed rises or descends; by detecting the shift in position of described movable lifting unit; control in described mixing channel, supply with stopping of water electrolytic gas and/or gaseous state fossil fuel or open, quantity delivered, predetermined component ratio
Above-mentioned water electrolytic gas and gaseous state fossil fuel constantly mix, and generate the water electrolytic gas fuel combination.
12. the production method of the water electrolytic gas fuel combination described in claim 11; it is characterized in that: by detecting the variation of described mixing channel pressure inside, described controlling organization control is supplied with stopping of water electrolytic gas and gaseous state fossil fuel or is opened in described mixing channel.
13. the production method of the water electrolytic gas fuel combination described in claim 11, it is characterized in that: the pressure in detecting described mixing channel is identical with the setting pressure that stops in described mixing channel supplying with the gaseous state fossil fuel and when furnishing good supplies to stop condition, stop to supply with water electrolytic gas in described mixing channel; When the pressure in detecting described mixing channel was lower than this setting pressure, beginning was supplied with water electrolytic gas in described mixing channel.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008022592 | 2008-02-01 | ||
| JP2008022592 | 2008-02-01 | ||
| JP2008290940 | 2008-11-13 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101498456A true CN101498456A (en) | 2009-08-05 |
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ID=40945648
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|---|---|---|---|
| CNA2008101880978A Pending CN101498456A (en) | 2008-02-01 | 2008-12-30 | Apparatus for generating electrolytic gas composite fuel, and method for generating this fuel |
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| JP (1) | JP3171237U (en) |
| CN (1) | CN101498456A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104312648A (en) * | 2014-09-04 | 2015-01-28 | 朱光华 | Fuel gas with high calorific value, preparation method thereof and equipment for carrying out the preparation method |
| CN107586576A (en) * | 2016-07-06 | 2018-01-16 | 徐建镛 | A kind of water ion activity combustion gas and its preparation method and application |
| CN109913888A (en) * | 2016-12-08 | 2019-06-21 | 张羽瑶 | The preparation method and device of a kind of active water ion-gas and active water ion-gas |
| CN111059463A (en) * | 2019-12-24 | 2020-04-24 | 兰州空间技术物理研究所 | Micro-flow air supply system and device |
| CN114483407A (en) * | 2022-01-25 | 2022-05-13 | 浙江吉利控股集团有限公司 | Engine start control method, vehicle, and computer-readable storage medium |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117165343A (en) * | 2023-03-13 | 2023-12-05 | 江苏与奏实业有限公司 | Fuel mixed by water electrolysis gas and catalyst and turbine prime motor power generation system |
-
2008
- 2008-12-30 CN CNA2008101880978A patent/CN101498456A/en active Pending
-
2011
- 2011-08-09 JP JP2011004667U patent/JP3171237U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104312648A (en) * | 2014-09-04 | 2015-01-28 | 朱光华 | Fuel gas with high calorific value, preparation method thereof and equipment for carrying out the preparation method |
| CN104312648B (en) * | 2014-09-04 | 2016-08-31 | 北京洁能创新能源科技有限公司 | A kind of high heating value combustion gas and preparation method thereof and facilities and equipments |
| CN107586576A (en) * | 2016-07-06 | 2018-01-16 | 徐建镛 | A kind of water ion activity combustion gas and its preparation method and application |
| CN109913888A (en) * | 2016-12-08 | 2019-06-21 | 张羽瑶 | The preparation method and device of a kind of active water ion-gas and active water ion-gas |
| CN111059463A (en) * | 2019-12-24 | 2020-04-24 | 兰州空间技术物理研究所 | Micro-flow air supply system and device |
| CN114483407A (en) * | 2022-01-25 | 2022-05-13 | 浙江吉利控股集团有限公司 | Engine start control method, vehicle, and computer-readable storage medium |
| CN114483407B (en) * | 2022-01-25 | 2024-03-19 | 浙江吉利控股集团有限公司 | Control method of methanol engine, vehicle and computer readable storage medium |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3171237U (en) | 2011-10-20 |
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