CN1081752A - Active ion fuel and its manufacturing installation and combustion system thereof - Google Patents
Active ion fuel and its manufacturing installation and combustion system thereof Download PDFInfo
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- CN1081752A CN1081752A CN93109341A CN93109341A CN1081752A CN 1081752 A CN1081752 A CN 1081752A CN 93109341 A CN93109341 A CN 93109341A CN 93109341 A CN93109341 A CN 93109341A CN 1081752 A CN1081752 A CN 1081752A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D11/00—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
- F23D11/10—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
- F23D11/16—Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour in which an emulsion of water and fuel is sprayed
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
- F23K5/08—Preparation of fuel
- F23K5/10—Mixing with other fluids
- F23K5/12—Preparing emulsions
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Abstract
With extremely simple structure, the manufacturing and the burning of the active ion fuel that nitrogen oxide reduces have been realized making.Liquid fuel injection valve 25 and bilge injection valve 30 are together to mixing teeter chamber's 31 injecting LPG in liquefied condition and water.Corresponding, injected liquid fuel and water mix in mixing teeter chamber 31 mutually, thereby, carry out milkiness liquefaction and active ionization.Because carried out milkiness liquefaction and active ionization, thus burning easily, thus the nitrogen oxide in the exhaust is tailed off.
Description
The present invention relates to the active ion fuel of water and liquid fuel mixing, for making active ion fuel production apparatus and this active ion fuel combustion system of this active ion fuel.Relate in more detail with special method liquid fuel and water mixing stirring, for the active ion fuel production apparatus of making active ion fuel be the high combustion system of low public hazards, efficiency of combustion of the burning of the active ion fuel of realizing manufacturing thus.
Mechanical fuel can be used in combination separately or with the combustion chamber, still, as most important function, need make the fuel completing combustion of being supplied with.That is to say that possible limit combustion rate is preferably near 100%.For this reason, the size of the flame during burning, shape need be suitable for various conditions, and in addition, specific combustion intensity is necessary for suitable numerical value.According to circumstances different, require the Temperature Distribution of flame to be homogeneous or desirable distribution.
In addition, in recent years, social strong request reduces the generation of atmosphere pollution of nitrogen oxide, flue dust, carbon monoxide etc. and the generation of noise as far as possible.For example, use in the fuel, use B, C heavy oil at boiler and kiln.But recently, oxysulfide (SOx) and nitrogen oxide (NOx) in the discharging gas are becoming problem, for this reason, also use crude oil, light oil, kerosene etc. sometimes.The amount of the SOx of discharging in the gas, relevant with the content of sulphur in the fuel.
Thereby, along with reinforcement to the SOx restriction in the discharging gas, thereby, the low fuel of sulfur content used.In order to adapt to this situation, implemented the use sweet crude, the oil desulfurization device has been set, flue gas desulfurization equipment has been set, measure such as fuel conversion.But the low sulfuration of crude oil has almost reached the limit.In addition, the NOx in the discharging gas is mainly generated by burning, and organic compound in the fuel and the nitrogen in the ammonia change into NOx.This conversion ratio is generally 30～60% in industrial burner.
On the other hand, the airborne nitrogen by supplying with in order to burn also can generate NOx.Combustion machine generally is made of the fuel supply system air supply system of unifying.The major part of fuel feed system is that fuel sprays machinery, and with suitable amount of exercise burner oil, the occasion of liquid fuel within makes its dispersion after the micronize.The major part of air supply system is a blast regulator, and combustion air is mixed in the fuel that is sprayed effectively, in order to make flame stabilizationization in air-flow, controls combustion characteristics simultaneously, the function that it has restriction and adjusts air stream.That is to say, deliver air to hot spots with needing positive and optimal dose.
Make the burner of liquid fuel combustion, generally be called oil burner, be divided into aerosol type and evaporation type.Aerosol type is for the surface area of the per unit volume that increases fuel as far as possible specific area just, be to make fuel fog change into the method that the little a large amount of oil droplet groups of diameter are burnt, burning load can not be too high, still, even the fuel of heavy system also can make its burning.In contrast, evaporation type is to utilize the high temp objects surface to make the mode of fuel vaporization.
, in recent years, because the care of earth environment is strengthened, thereby strengthened people suddenly to reducing the requirement of nitrogen oxide.The method that nitrogen oxide is reduced, various schemes have been proposed, wherein for example, in the clear 61-91407 communique of Japan's patent disclosure, disclosed following method, be about to water and mix, again its part or all with hydrocarbon based fuel is mixed, supply to the emulsion fuel feeding method of the adding oxygen in the combustion apparatus then with the air or the pure oxygen that contain high concentration oxygen.
This system need supply with pure oxygen or contain the air of high concentration oxygen.In addition, in the occasion of using air, because the influence of airborne nitrogen, nitrogen oxide increases, and system also needs to assemble complicated loop.Only water or vapor mixing to the method in the fuel a lot of schemes (the clear 52-25807 of Japan's patent disclosure number, the clear 63-148012 of Japan's patent disclosure number etc. many patents) have been proposed also.In addition, also have many waters and oil make the method for emulsion motion (for example, United States Patent (USP) the 4th, 416,610, United States Patent (USP) the 3rd, 648,714).With the emulsion of these emulsion manufacturing installation manufacturings, neither Ionized fuel as described below and device is also complicated.
The present inventor has proposed with the agitator that embeds magnet the motion (PCT/JP91/00776) of making the device of emulsion.But, this emulsion manufacturing installation, owing to use the rotation wing, magnet, employed energy can not transform effectively to fuel, that is to say the problem of off-energy in the time of can not ignoring fuel making.The present invention, with extremely simple structure realized with above-mentioned patent in the identical substantially active ion fuel of emulsion of the emulsion manufacturing installation manufacturing of being suggested plans.
The objective of the invention is to, provide structure extremely simple, for making the manufacturing installation and the combustion system thereof of the active ion fuel that nitrogen oxide reduces.
Active ion fuel of the present invention is a kind of fuel as described below.
It is water and hydrocarbon system liquid fuel or solid-fuelled emulsion, and it is by fine aforesaid liquid fuel or solid fuel particle and excites water to be constituted.Wherein, the cluster of above-mentioned water forms micelle around aforesaid liquid fuel or above-mentioned solid-fuelled particle, thereby becomes lyophilic colloid, and the above-mentioned water that excites is to make above-mentioned water excite the water of back generation as the bearing-type motion of spinning motion.
This active ion fuel is by following manufacturing installation manufacturing.This active ion fuel production apparatus is made of following part: the liquid-fuel tank that is used for the storage solution fluid fuel, with the liquid fuel feed pump that is used for the pressurization of aforesaid liquid fuel, with the water pot that is used to preserve water, with the water pump that is used for above-mentioned water pressurization, with supply with aforesaid liquid fuel and above-mentioned water by aforesaid liquid liquid-fuel tank and above-mentioned water pot, and be divided interval mixing teeter chamber, be arranged on an end of above-mentioned mixing teeter chamber, above-mentioned pressurized water is injected into vaporific bilge injection valve and chews corresponding with above-mentioned water injection, be arranged on the other end of above-mentioned mixing chamber, be used for the liquid fuel injection valve that above-mentioned pressurized liquid fuel is sprayed.
Burn in the above-mentioned active ion fuel combustion system below.
This combustion system is made of the lower face branch; they are respectively to be used for active ion petrolift that active ion fuel is pressurizeed; this active ion fuel is to use the aforesaid liquid fuel that taken out by above-mentioned mixing teeter chamber and above-mentioned water manufacturing; with the above-mentioned active ion fuel particlesization that is used for sending here, the burner that then sprays with by above-mentioned active ion petrolift.
Preferably by forming in order to make the fuel that comes from the above-mentioned burner plural slit of burning, and the fuel tank that has the space in inside constitutes.
In addition, above-mentioned burn pot also can be to have diameter of Spherical Volume in inside, and, have two layers of inside and outside wall.
Effect of the present invention is to make active ion fuel with extremely simple structure.
Other effect of the present invention is, when the active ion fuel with active ion fuel production apparatus of the present invention manufacturing burns, because air supply energetically, so can realize the burning gases that NOx is few.
Another other effect of the present invention is, base use combustion system of the present invention, when making this active ion fuel combustion, owing to steam in burning gases is many, so its thermal conductivity height.
Liquid fuel injection valve, bilge injection valve are together to mixing chamber injecting LPG in liquefied condition and water.Liquid fuel and water that subtend is sprayed mix in mixing chamber mutually, carry out active ionizations.Pump is delivered to burner by mixing the active ion fuel that the teeter chamber attracts milkiness liquefaction and active ionization after the pressurization, burner atomizes in the internal combustion boiler and sends.Because the preheating in advance of internal combustion boiler, so make the burning beginning by this preheating.In this burning, need not carry out the air air-supply energetically.So-called two kinds of liquid milkiness liquefaction and active ionization are carried out Ionized energy owing to this fuel has, exactly so when making its burning, become the state of easy burning.
Fig. 1 is the functional block diagram of the summary of expression combustion system of the present invention.
Fig. 2 is the profile at the main position of mixing and blending machine structure.
Fig. 3 is the outside drawing of internal combustion boiler.
Fig. 4 is the exploded view of internal combustion boiler.
Fig. 5 among Fig. 3 with the V-V profile of line when deciding what is right and what is wrong of deciding what is right and what is wrong.
Fig. 6 is for making internal combustion boiler sphere other embodiment of double walled combustion chamber.
The overview of combustion system
Below, according to figure embodiments of the invention are described.Fig. 1 is the calcspar of the overview of expression combustion system.The 1st liquid-fuel tank 1 be used for storage in preheating described below in the jar of employed liquid fuel during fuel boiler 16.This liquid fuel is to be transported in the active ion petrolift (not shown) in the burner 15 by valve 18a, the active ion petrolift with this liquid fuel pressurization after, be transported to Fuelinjection nozzle 18.
In the 2nd liquid-fuel tank 2, the liquid fuel of the usefulness of burning in store.Water pot 3 is to be used for preserving with following method and jar by the water of the liquid fuel mixing stirring of the 2nd liquid-fuel tank 2.Liquid fuel in the liquid-fuel tank 2 supplies to mixing and blending machine structure 7 by pipeline by liquid fuel feed pump 4, flow control valve 5, flowmeter 6.
Liquid fuel feed pump 4 is used for liquid fuel is pressurizeed.Flow control valve 5, the amount that is used for regulating the liquid fuel that is transported to fuel mix rabbling mechanism 7.Flowmeter 6 is used for the metering liquid flow fuel.Water in the water pot 3 is put meter 10 by pipeline by water pump 8, flow control valve 9, stream and is supplied in the mixing and blending machine 7.
Water pump 8 is to be used for the water of water pot 3 is pressurizeed.Flow control valve 9 is the valves that are used for regulating the flow of the water that is transported to fuel mix rabbling mechanism 7.Flowmeter 10 is the flows that are used to measure water.Supply to the liquid of the 2nd liquid-fuel tank 2 of fuel mix rabbling mechanism 7 and the water in the water pot 3, adopt means as described below to mix stirring, thereby make its milkiness liquefaction and active ionization.Water after emulsified liquefaction and the active ionization and liquid fuel after being attracted by fuel mix rabbling mechanism 7 by valve 11 usefulness pumps 12, carry out forced feed to burner 15, are ejected in the combustion chamber 17 with Fuelinjection nozzle 19.
Pressure gauge 13 is the defeated pressure of row that is used to measure, monitor active ion petrolift 12, so that make it keep certain measuring instrument.Flowmeter 14 is what to be used to measure by active ion petrolift 12 to the flow fuel of being liquefied by milkiness of being supplied of burner 15 and active ionization.Burner 15, the pressure of having installed by fuel makes liquid fuel spray at a high speed from orifice plate, carries out micronized Fuelinjection nozzle 18,19 and air blast.
The structure of burner 15 is well-known, so at this in detail its structure is not described in detail.In the present embodiment, 19 two valves of Fuelinjection nozzle of the preheating Fuelinjection nozzle of using 18 and the usefulness of burning have been installed.Fuelinjection nozzle that preheating is used and air blast only use when preheating internal combustion boiler 16., burnt in the internal combustion boiler by micronized active ion fuel by Fuelinjection nozzle 19, thus heating exterior combustion chamber 17.
Fuel mix rabbling mechanism 7
Fig. 2 is the profile of fuel mix rabbling mechanism 7.Fuel mix rabbling mechanism 7, its body 20 is the garden barrel shape, the diameter of this garden tube is identical substantially with length.End at body 20 is screwed into plug screw 21 in the body 20.In the rear end of plug screw 21, be screwed into pipe joint 23.On the end face of the flange 22 of plug screw 21 and body 22, installing O-ring seals 24 is so that will seal between plug screw 21 and the body 22.Front end at plug screw 21 is screwed into Fuelinjection nozzle.
Equally, in the other end of body 20, plug screw 26 is screwed in the body 20.In the rear end of plug screw 26, be screwed into pipe joint 28.On the end face of the flange 27 of plug screw 26 and body 20, installing O-ring seals 29 is so that will seal between plug screw 26 and the body 20.Front end at plug screw 26 is screwed into bilge injection valve 30.
The space that Fuelinjection nozzle 25 in body 20 and bilge injection valve 30 are surrounded, zoning go out the mixing chamber 31 of garden tubular.On the location about of the centre of body 20, be provided for arranging defeated at radial direction by row's outlet 32 of the active ion fuel of active ionization.On row's outlet 32, be connected with pipe joint 33.Liquid fuel injection valve 25, bilge injection valve 30 are together to mixing teeter chamber injecting LPG in liquefied condition and water simultaneously.
In addition, body 20, plug screw 21,26, Fuelinjection nozzle 25, bilge injection valve 30 and and joint 23,28 etc. can use the magnetic material manufacturing, but wish preferably nonmagnetic substances such as pottery, stainless steel.The jet angle θ of liquid fuel injection valve 25, bilge injection valve 30 is preferably about 30 °～60 ° of types.In addition, the moulding pressure when it sprays is preferably 5～10 kilograms per centimeter
2Scope.
In addition, if on the next door of the pipe joint 28 of supplying with water magneto is set, then the manufacturing efficient of active ion fuel will be higher.
The active ion fuel of using the fuel supplied with by fuel mix rabbling mechanism 7 and water to make attracts and pressurizes with active ion petrolift 12, then supplies in the Fuelinjection nozzle 19 of burner 15.Burner 15, the active ion fuel atomization nebulized to be blown in the internal combustion boiler 16.Fig. 3 is the figure of the outward appearance of expression internal combustion boiler 16.Fig. 4 is the exploded view of internal combustion boiler 16.Fig. 5 among Fig. 3 with the V-V profile of line when deciding what is right and what is wrong of deciding what is right and what is wrong.Internal combustion boiler 16, the structure of the double storied boiler of fuel boiler 40 and inboard burning boiler 41 outside having.
The outside boiler 40 and inboard boiler 41 are made the shape of tubular, have offered several slits 42 in its periphery respectively along the garden side face.Because the internal diameter of outside burning boiler 40 is bigger than the external diameter of inboard burning boiler 41, so between has just formed space 42.Active ion fuel promptly burns in the exterior combustion chamber 17 as burning boiler in the outside of this space 42 and outside burning boiler 40.
Operation
Aforesaid active ion fuel production apparatus and active ion fuel combustion system use by following operation.At first, by valve 18a liquid fuel is fed to built-in pump (not shown) in the burner 15 by liquid-fuel tank 1.In the present embodiment, this fuel uses commercially available kerosene.Built-in pump in the burner 15 will be transported in the Fuelinjection nozzle 18 after the liquid fuel pressurization.This Fuelinjection nozzle 18 is transported to internal combustion boiler 16 behind the liquid fuel atomization with forced feed.The liquid fuel of the atomizing in the internal combustion boiler 16 carries out ignition by the ignition means (not shown).
Liquid fuel relies on the air that is transported by air blast to take fire, and by this combustion heat, makes burning boiler 16 preheating fully.After making burning boiler 16 heating by this preheating, then valve 18a closes, and is stopped by the supply of the liquid fuel of liquid-fuel tank 1.Then, pump 5,8 startings before valve 18a closes.Liquid fuel injection valve 25, bilge injection valve 30 be while injecting LPG in liquefied condition and water in mixing teeter chamber 31 together.Adapt therewith, injected liquid fuel and water mix in mixing teeter chamber 31 mutually, thereby carry out milkiness liquefaction and ionization.
After valve 18a closed, valve 11 was opened, and active ion petrolift 12 attracts by being liquefied by milkiness and the water of active ionization and the active ion fuel of fuel manufacturing, and pressurizeed and (be about in the present embodiment, 8 kilograms per centimeter
2) be transported to burner 15.Be transported to the active ion fuel of burner 15, be transported to after being atomized in the inboard burning boiler 41 of internal combustion boiler 16.Because the 16 quilt preheatings in advance of internal combustion boiler, so, be easy to beginning by this preheated burning.In this burning, do not need to carry air energetically by air blast, can adopt gravity-flow ventilation.
So-called two kinds of liquid also be can be described as owing to having the ionization energy, so making it is the state that burns easily in burning by active ionization.In addition, this active ion fuel, because the molecule of water and oil disperses the emulsion form that forms as colloidal particle or than its little particle, so, become the state of easy completing combustion.Thereby, even air supply in burning boiler 16 energetically not utilizes the gravity-flow ventilation also can continuous burning.
The theory of combustion
This continuous burning principle is inferred as described as follows.
H
2O(water) such as everyone knows, be dipole (dipole), be that the center is to the e-(electronics with the oxygen atom to the length of each electric charge) be 0.99 dust, to nuclear proton (proton) also be 0.99 dust both keep balance.
(Chemical formula 1)
As everyone knows, oxygen element (O) and hydrogen atom (H) carry out covalent bonds, and the formed angle of two hydrogen atoms (H) of carrying out covalent bonds be 105 ° 3 '.
Cluster (cluster) is called that a part of particle part is in relevant state in multiparticle system.The dynamic molecular bloc framework of water (being one of cluster) is with 10
-12The speed of second is repeatedly being carried out discrete and forming process.The dynamic molecular bloc framework of feedwater is with electric charge, in case improve the electric charge of the oxonium ion (oxygen atom) of divalence, then proton (proton) just can attract the e-(electronics), thus make the angle of two electronics recited above become greater than 105 ° 3 '.
(Chemical formula 2)
Proton (proton) is subjected to the e-(electronics) the quantity of electric charge about, constantly carry out restoring after the small vibration.That is to say that feedwater applies external force, because electric charge improves, so the dipole energy rate improves, water is excited (excitation), and dynamic molecular bloc framework (cluster) is divided into least unit, becomes high density, and formation is discrete, and speed is faster than 10
-12Second, present Brownian movement (Brownian movement).
This be excited
(chemical formula 3)
Be unsaturated hydrocarbons (oil) with small mixing (microblend) of physics with (chain) alkene (hydrocarbon) be that above-mentioned fuel mix rabbling mechanism 7 mixes, just carry out
(chemical formula 4)
Reaction.This reaction has promptly added that the reaction of the compound of ozone is identical with (chain) alkene unsaturated hydrocarbons (oil) such as (hydrocarbon) and ozonide on two key parts of the compound with ethylenic linkage, carbon and oxygen carry out the ionic bond combination, this RCH
2OCH
2R is that to have with oxygen be the structure of the hydrocarbon at center.
This be excited
(chemical formula 3),
With 1/32nd power of hydrocarbon by proton attractive.That is to say that around oil molecule, the dipole of water is according to the positive polarity of rule, become fine cluster (dynamic molecular bloc framework), become the gyration that is produced by above-mentioned fuel mix rabbling mechanism 7, i.e. the state of the said bearing-type of this specification motion promptly becomes and excites water.
The cluster of this water that is excited, vibration around oil molecule, thus form minimum micelle (micelle).That is to say, this micelle, the little molecule of most (generally by several to dozens of) combines generation lyophilic colloid particle by intermolecular power, becomes the active ion fuel of following chemical constitution.
(chemical formula 5)
Surround the rotary speed of the dipole that excites water of oil molecule, be about 10
-6Second order of magnitude, the part that only is attracted is slower than the cluster rotary speed of outermost shell.Keep the cluster of the water of the positive directionality of rule in its outside, become hub equally.Its rotary speed is about 10
-9Second.In addition, produce same situation near its foreign steamer, the hydrone that excites that this is not influenced by proton fully carries out Brownian movement outside micelle, promptly because hot caused irregular movement.
(chemical formula 6)
(chain) alkene (hydrocarbon) unsaturated hydrocarbons (oil) of this center be excited
(chemical formula 3)
Combine, generate 1 mole of organic matter with following reaction.
(chemical formula 7) this organic matter that generates burns by following reaction.
(reaction equation 8)
On the one hand, what shell carried out bearing-type motion excites water (Bea ring movement of Active-water cluster) when being positioned at the oil firing of center, cause water vapour outburst (Detonation of setam), thereby the cluster of the water of miniaturization resolves into hydrogen and oxygen, make unburned oily completing combustion, so, a thirtieth (see below and state) when even the quantity delivered of the air in when burning reduces to common burning, also can burn, and, nitrogen oxide (NOx) in the discharging gas reduces to below a thirtieth, and sulfur oxide (SOx) reduces to below 1/3rd.
By adding this active ion fuel of 55% water, keep efficiency of combustion (saving essence efficient) 40%.Do not do the original emulsion of bearing-type motion, as use microscopic examination, then water becomes 5～50 microns water droplet in oil, only forms colloid at emulsification point.In addition, the size of the water droplet steam bubble of the emulsion in past when burning is 60～600 microns, and the heat of evaporation loss is with respect to the addition 1% of water, and heat loss is 0.08%, as adds 5% water, and the combustion heat loss of emulsion is exactly 0.4%.Therefore, it is unfavorable that the emulsion in past, the addition of water surpass 5%.In addition, the emulsion in past had not both had the bearing-type motion, do not combine with two keys of butylene yet, owing to added 55% water, thereby can not burn.
As above detailed description the in detail, the active ion fuel of novelty of the present invention, according to the diverse Theory of Combustion of the emulsion in past, even added aforesaid 55% water, the temperature in the stove also rises 40%, is epoch-making combustion method.
In addition, as the means that water is excited, in the present embodiment, adopted above-mentioned active ion fuel production apparatus, still, other means also can.For example, when making water be subjected to the vibration of the hyperacoustic materiality of 60～90Hz, owing to inject the e-(electronics to water with electric field, magnetic field, discharge, electro-optical package, electron gun etc.), excite the dipole energy rate thereby strengthen, make it become activated state, become ionized water.In addition, the foregoing description is the example that makes liquid fuel combustion, still, so long as solid fuels such as hydrocarbon system coal also can.At this moment, several microns unit preferably uses the small material of the particle that is ground into below 5 microns.With the external force of this ionized water by physics, for example ultrasonic wave, pressure, ダ-(trade (brand) name) of ミ Network ロ レ Application mix with (chain) alkene (hydrocarbon).
Under solid-fuelled situation, also can make in the same way with above-mentioned active ion fuel production apparatus.Being that solid fuel is distributed in the water in this case, that is to say, is to use after being made for suspension.Can be better if mix suitable stabilizing agent in this case.
Experimental data
Use kerosene and carry out Actual combustion, then, measure the nitrogen oxide (NOx) and the oxysulfide (SOx) that discharge in the gas with the active ion fuel of system of the present invention manufacturing.Below, its experimental data is shown.
Burning boiler (to call combustion chamber in the following text) the 16th, the garden tubular of 270 millimeters of external diameters, 550 millimeters of length.Material use chrome-molybdenum steel (Japanese Industrial Standards, SCM415).Combustion chamber (to call in the following text in the stove) is high 1000 millimeters, 950 millimeters of depth, wide 1100 millimeters.The outer wall of stove carries out thermal insulation with refractory brick.
(table 1)
In combustion experiment, the conduit of airtight air inlet port is installed earlier, measure the air mass flow in this conduit of flowing through then.Its result is that when 1. kerosene burnt, air capacity was 2.2 meters
3/ minute, 2. when the active ion fuel combustion, air capacity is 0.07 meter
3/ minute.
Thereby, combustion air amount at hypothesis kerosene is under 100% the situation, then employed air capacity only is 3.3% when the active ion fuel combustion, according to the value shown in the above-mentioned table 1, nitrogen oxide (NOx), oxysulfide (SOx) in the discharging gas, when using active ion fuel, during than use kerosene, in fact reduced to a thirtieth.
In addition, this numerical value is to be calculated with the capacity in the discharging gas by the measurement result of table 1, comprises error.
The embodiment 2 of burning boiler
Fig. 6 does glomeration with burning boiler 80, and is the example of the combustion chamber of double walled.About 300 mm dias of inwall 81 and outer wall 82(are set), a plurality of flame radiation mouths 85 are set respectively on outer circumference surface separately.The supply of active ion fuel by the periphery of inwall 81, is undertaken by the nozzle 84 with 60 jet angles of spending.To the supply of the active ion fuel of nozzle 84, undertaken by petroleum pipeline 83.In addition, the eject position and the angle of the nozzle 84 of this moment are preferably sprayed with big as far as possible angle and to the center of inwall 81.
[changing 1]
[changing 2]
Claims (5)
1, a kind of active ion fuel, it is water and hydrocarbon system liquid fuel or solid-fuelled emulsion, it is by fine aforesaid liquid fuel or solid fuel particle and excites water to be constituted.Wherein, the cluster of above-mentioned water is around aforesaid liquid fuel or above-mentioned solid fuel particle, form micelle, thereby become lyophilic colloid (lyophilic colloid), the above-mentioned water that excites is to make above-mentioned water excite the water of back generation as the bearing-type motion of spinning motion.
2, a kind of active ion fuel production apparatus, it is made of following several parts: the fuel tank that is used for storage solution fluid fuel or solid fuel suspension fuel, with the petrolift that is used for above-mentioned fuel pressurization, with the water pot that is used to preserve water, be used for water pump with above-mentioned water pressurization, with supply with above-mentioned fuel and above-mentioned water by above-mentioned fuel tank and above-mentioned water pot, and has a mixing teeter chamber that has been divided the space, be injected into above-mentioned pressurized water vaporific with being used for, be installed in above-mentioned mixing teeter chamber an end bilge injection valve and be used to spray pressurized above-mentioned fuel, be installed in the above-mentioned Fuelinjection nozzle that mixes the other end of teeter chamber accordingly with above-mentioned bilge injection valve.
3, the combustion system of claim 1 or 2 described active ion fuel; it is characterized in that: it is by being used for the active ion petrolift of above-mentioned active ion fuel pressurization and will being made of the nozzle that the above-mentioned active ion fuel particlesization that above-mentioned active ion petrolift is supplied with is then sprayed.
4, the combustion system of the described active ion fuel of claim 3 is characterized in that: it makes the slit of being burnt by last nozzle ejection fuel by forming, and the burning boiler that has the space in interior constitutes.
5, the combustion system of the described active ion fuel of claim 5 is characterized in that: above-mentioned boiler has diameter of Spherical Volume at inner, and, have double-deck inside and outside wall.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4219696A JPH0642734A (en) | 1992-07-27 | 1992-07-27 | Ionization emulsion manufacturing device its combustion system |
| JP219696/92 | 1992-07-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1081752A true CN1081752A (en) | 1994-02-09 |
Family
ID=16739535
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN93109341A Pending CN1081752A (en) | 1992-07-27 | 1993-07-27 | Active ion fuel and its manufacturing installation and combustion system thereof |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0581230A2 (en) |
| JP (1) | JPH0642734A (en) |
| KR (1) | KR940002542A (en) |
| CN (1) | CN1081752A (en) |
| TW (1) | TW221457B (en) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5992354A (en) | 1993-07-02 | 1999-11-30 | Massachusetts Institute Of Technology | Combustion of nanopartitioned fuel |
| CA2207339A1 (en) * | 1996-06-12 | 1997-12-12 | Goro Ishida | Emulsion fuel production method and apparatus, emulsion fuel combustion apparatus, and emulsion fuel production supply apparatus |
| JP2008019359A (en) * | 2006-07-13 | 2008-01-31 | Shinkawa Yoshiro | Manufacturing method of emulsion composition and apparatus for emulsification |
| JP4790066B2 (en) | 2007-07-23 | 2011-10-12 | やまと総合環境株式会社 | Water emulsion production equipment |
| ITVT20080003A1 (en) * | 2008-02-18 | 2009-08-19 | Salvatore Mario Pandolfo | SYSTEM FOR ADDITIVATION IN HYDROCARBONS, LIQUIDS OR GASEOUSES, WATER OR STEAM, DERIVED FROM ELECTROCHEMICAL TREATMENT |
| CN102187079B (en) * | 2008-10-24 | 2014-03-05 | 深井利春 | Method for producing emulsion fuel, and method for handling emulsion fuel |
| US8640677B2 (en) | 2009-04-01 | 2014-02-04 | James Gonzales | Electrostatic air charging system for an internal combustion engine |
| US8739685B2 (en) * | 2009-12-28 | 2014-06-03 | Takai Tofu & Soymilk Equipment Co. | Tofu coagulant producing apparatus and soymilk coagulation machine comprising the same |
| WO2013054451A1 (en) * | 2011-10-12 | 2013-04-18 | Hattori Mitsuharu | Method for producing compatible transparent water-containing oil |
| JP2013095884A (en) * | 2011-11-03 | 2013-05-20 | Hiroshi Yamashita | Apparatus and method for generating emulsion fuel |
| JP5711186B2 (en) * | 2012-05-25 | 2015-04-30 | 株式会社ワールドビジネス | Mixed fuel generating apparatus and method |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2604610C3 (en) * | 1976-02-06 | 1978-07-13 | Hans 7209 Aldingen Messner | Device for generating a directly combustible, emulsifying oil-water mixture |
| DE2839064A1 (en) * | 1977-09-07 | 1979-03-15 | Cleanodan As | Emulsifier for water injection into fuel oil - having opposed jets for water and oil in closed box which leads to storage before cavitation pump |
| FR2461515A1 (en) * | 1979-07-24 | 1981-02-06 | Robert Guerin | Emulsification of mutually insol. liquids - by pumping mixt. through passage of narrowing section with wide slowing and diverting sections to give ultra-colloidal emulsion |
| US4432771A (en) * | 1981-05-15 | 1984-02-21 | International Telephone And Telegraph Corporation | Combustible coal/water mixtures for fuels and methods of preparing the same |
| US5249957A (en) * | 1990-06-14 | 1993-10-05 | Kiichi Hirata | Emulsion producing apparatus and its combustion system |
-
1992
- 1992-07-27 JP JP4219696A patent/JPH0642734A/en active Pending
-
1993
- 1993-02-12 TW TW082100994A patent/TW221457B/zh active
- 1993-07-26 KR KR1019930014201A patent/KR940002542A/en not_active Application Discontinuation
- 1993-07-26 EP EP93111937A patent/EP0581230A2/en not_active Withdrawn
- 1993-07-27 CN CN93109341A patent/CN1081752A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| EP0581230A2 (en) | 1994-02-02 |
| TW221457B (en) | 1994-03-01 |
| JPH0642734A (en) | 1994-02-18 |
| EP0581230A3 (en) | 1994-02-23 |
| KR940002542A (en) | 1994-02-17 |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |