CN102187079A - Apparatus for producing emulsion fuel, method for producing emulsion fuel, method for handling emulsion fuel, and emulsion fuel - Google Patents
Apparatus for producing emulsion fuel, method for producing emulsion fuel, method for handling emulsion fuel, and emulsion fuel Download PDFInfo
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- CN102187079A CN102187079A CN200980142528XA CN200980142528A CN102187079A CN 102187079 A CN102187079 A CN 102187079A CN 200980142528X A CN200980142528X A CN 200980142528XA CN 200980142528 A CN200980142528 A CN 200980142528A CN 102187079 A CN102187079 A CN 102187079A
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- fuel
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- mixing chamber
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- 239000000446 fuel Substances 0.000 title claims abstract description 648
- 239000000839 emulsion Substances 0.000 title claims abstract description 245
- 238000000034 method Methods 0.000 title claims abstract description 127
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 69
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 549
- 239000007788 liquid Substances 0.000 claims abstract description 138
- 238000002485 combustion reaction Methods 0.000 claims abstract description 64
- 239000002828 fuel tank Substances 0.000 claims abstract description 59
- 239000000203 mixture Substances 0.000 claims abstract description 23
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 60
- 239000011435 rock Substances 0.000 claims description 60
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 38
- 239000008158 vegetable oil Substances 0.000 claims description 38
- 238000009434 installation Methods 0.000 claims description 36
- 239000000377 silicon dioxide Substances 0.000 claims description 30
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 20
- 239000003456 ion exchange resin Substances 0.000 claims description 20
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 20
- 239000003921 oil Substances 0.000 claims description 20
- 229940070527 tourmaline Drugs 0.000 claims description 20
- 229910052613 tourmaline Inorganic materials 0.000 claims description 20
- 239000011032 tourmaline Substances 0.000 claims description 20
- 230000008676 import Effects 0.000 claims description 19
- 235000019198 oils Nutrition 0.000 claims description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 235000019774 Rice Bran oil Nutrition 0.000 claims description 9
- 235000019486 Sunflower oil Nutrition 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 239000004359 castor oil Substances 0.000 claims description 9
- 235000019438 castor oil Nutrition 0.000 claims description 9
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 239000001301 oxygen Substances 0.000 claims description 9
- 229910052760 oxygen Inorganic materials 0.000 claims description 9
- 239000010499 rapseed oil Substances 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 239000008165 rice bran oil Substances 0.000 claims description 9
- 239000002600 sunflower oil Substances 0.000 claims description 9
- 239000007921 spray Substances 0.000 claims description 7
- 241000196324 Embryophyta Species 0.000 claims description 6
- 230000037452 priming Effects 0.000 claims description 4
- 238000004945 emulsification Methods 0.000 abstract description 20
- 238000002347 injection Methods 0.000 abstract description 3
- 239000007924 injection Substances 0.000 abstract description 3
- 239000002245 particle Substances 0.000 description 13
- 239000004094 surface-active agent Substances 0.000 description 11
- 238000003756 stirring Methods 0.000 description 9
- 239000003995 emulsifying agent Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000010304 firing Methods 0.000 description 5
- 239000008399 tap water Substances 0.000 description 5
- 235000020679 tap water Nutrition 0.000 description 5
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- -1 from burner Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000005332 obsidian Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B47/00—Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines
- F02B47/02—Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being water or steam
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M25/00—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
- F02M25/022—Adding fuel and water emulsion, water or steam
- F02M25/0221—Details of the water supply system, e.g. pumps or arrangement of valves
- F02M25/0225—Water atomisers or mixers, e.g. using ultrasonic waves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M25/00—Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
- F02M25/022—Adding fuel and water emulsion, water or steam
- F02M25/0228—Adding fuel and water emulsion
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Water Supply & Treatment (AREA)
- Feeding And Controlling Fuel (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Disclosed are: an emulsion fuel; an apparatus capable of producing a necessary amount of an emulsion fuel; a method for producing an emulsion fuel; and a method for handling an emulsion fuel. An apparatus for producing an emulsion fuel comprises a fuel supply pump (24) which is arranged in a fuel supply channel (20) that communicates with a combustion means (23), and a liquid mixing means (10) which is arranged in the upstream of the fuel supply channel (20) and provided with a mixing chamber (30) having one side communicating with a fuel tank (12) via an injection opening (32) and another side communicating with a water tank (16). The negative pressure of the fuel supply pump (24) for supplying a fuel to the combustion means (23) is further applied to the mixing chamber (30), so that the fuel supplied from the fuel tank (12) is injected into the mixing chamber (30) through the injection opening (32) and water supplied from the water tank (16) is introduced into the mixing chamber (30), thereby mixing the fuel and water together in the mixing chamber (30). By mixing the fuel and water together in the mixing chamber (30), there is produced an emulsion fuel, a part of which is emulsified and the other part of which remains in the form of a mixture of the fuel and water. By introducing the emulsion fuel into the fuel supply pump (24), emulsification of the fuel is advanced.
Description
Technical field
The present invention relates to be used for after producing emulsion fuel, making immediately the manufacturing installation of the emulsion fuel of its burning, the manufacture method of emulsion fuel, the method and the emulsion fuel of use emulsion fuel.
Background technique
At present, known widely fuel, water and the emulsifier such as light oil, heavy oil, lam-oil, gasoline of making are made various emulsion fuels.Under the situation of making emulsion fuel, the general known following method that has: in the manufacturing case of emulsion fuel is large-scale mixing box, put into emulsifiers such as fuel, water and surface active agent, utilize large-scale stirring apparatus (by being located at the outer driving element of case and rotating and the mixing blade be located in the case constitutes because of this driving element) to mix the three kinds of liquid (patent documentation 1) in the case.
The mixing box of making emulsion fuel does not directly link with the burner (combustion elements) of burning emulsion fuel, generally speaking, the emulsion fuel that produces is transferred to the container that directly links with burner, where necessary emulsion fuel is supplied to burner from container.Yet, because the emulsion fuel of storing in container generally can separate at short notice, therefore, before using as emulsion fuel, use the emulsion fuel after large-scale stirring apparatus (having driving element and mixing blade) will separate to carry out emulsification again, then, the emulsion fuel after the emulsification again is supplied to burner and makes its burning.
The prior art document
Patent documentation
Patent documentation 1: the Japan Patent spy opens the 2001-323288 communique
Summary of the invention
Invent technical problem to be solved
Under the existing situation of making emulsion fuel, for the manufacturing of emulsion fuel with store and need two kinds of large-scale casees (mixing box and container) respectively.Therefore, existing not only needs to have and two kinds of bigger spaces that Large Box is corresponding, and the higher such shortcoming of the expense of two kinds of Large Box.In addition, in mixing box, must have and be used for these three kinds of liquid of fuel, water and emulsifier are mixed the large-scale stirring apparatuss that stir, and in container, must have the emulsion fuel that is used to make after in container, the separating large-scale stirring apparatus of emulsification again.Therefore, need two kinds of large-scale stirring apparatuss, thereby exist manufacture cost to uprise such shortcoming.In addition,, also there is following unfavorable condition: owing to use surface active agent (chemical product),, and can produce dioxin because of the burning of this surface active agent so cost is higher in order to make emulsion fuel.
At present, be built-in with burner (combustion elements), fuel feed pump and fuel supply path in the burner device that uses in boiler etc., wherein, above-mentioned fuel feed pump is delivered to this burner with fuel; Above-mentioned fuel supply path arrives burner via above-mentioned fuel feed pump halfway.In burner device, the work of burn-out device, fuel feed pump along with stopping of boiler.Under the situation of using emulsion fuel to act as a fuel, from burner, fuel feed pump stop to start working to next time during, the emulsion fuel that is full of in fuel feed pump and fuel supply path is separated into fuel and water.Exist because of this isolated water and make fuel feed pump (can be used in fuel but can not be used in the pump of water) the such unfavorable condition of fault.In addition, at cold area, the water after exist separating freezes and makes the unfavorable condition of fuel feed pump, the breakage of fuel supply path.Because therefore these unfavorable conditions, have hindered popularizing of emulsion fuel.
The object of the present invention is to provide the manufacturing installation that can after producing emulsion fuel, use the emulsion fuel of emulsion fuel immediately, the manufacture method of emulsion fuel, the method and the emulsion fuel of use emulsion fuel.
The technological scheme that the technical solution problem is adopted
The manufacturing installation of emulsion fuel involved in the present invention is applicable to the situation from the fuel supply path that has fuel feed pump halfway towards the combustion elements fueling, it is characterized in that, comprising: fuel tank, and this fuel tank is used for fuel is accommodated; Water tank, this water tank is used for water is accommodated; Liquid hybrid element, this liquid hybrid element have makes mixing chamber that fuel mixes with water and towards the jetburner of above-mentioned mixing chamber burner oil, and above-mentioned mixing chamber is communicated with the upstream side of above-mentioned fuel supply path; Fuel passage, an end of this fuel passage is communicated with above-mentioned fuel tank, and the other end is communicated with the above-mentioned jetburner of aforesaid liquid hybrid element; And water passage, one end of this water passage is communicated with above-mentioned water tank, the other end is communicated with the above-mentioned mixing chamber of aforesaid liquid hybrid element, fuel in the above-mentioned fuel tank is sprayed in above-mentioned mixing chamber via above-mentioned jetburner from above-mentioned fuel passage, and the fuel in the above-mentioned water tank imported in the above-mentioned mixing chamber from above-mentioned water passage, thereby fuel and water are mixed to make emulsion fuel in above-mentioned mixing chamber.Feature of the present invention is, send having of above-mentioned fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the above-mentioned jetburner of above-mentioned liquid hybrid element, send having of above-mentioned water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the above-mentioned mixing chamber of above-mentioned liquid hybrid element.Feature of the present invention is, makes above-mentioned fuel feed pump, above-mentionedly sends with petrolift, above-mentionedly sends that the water priming of pump-stopping action carrying out simultaneously.Feature of the present invention is, has fuel Flow-rate adjustment element midway in above-mentioned fuel passage, this fuel is used for the flow fuel that flows through above-mentioned fuel passage is regulated with the Flow-rate adjustment element, above-mentioned water passage have water Flow-rate adjustment element midway, this water is used for the flow of the water that flows through above-mentioned water passage is regulated with the Flow-rate adjustment element.Feature of the present invention is, above-mentioned water passage have open and close valve midway, this open and close valve is used for above-mentioned water passage opened closes.Feature of the present invention is that above-mentioned fuel tank and above-mentioned water tank are disposed at the position higher than aforesaid liquid hybrid element.Feature of the present invention is, the vegetable oil that is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil is mixed with water in the above-mentioned water tank.Feature of the present invention is, has the second liquid hybrid element, this second liquid hybrid element is adjacent in the downstream side of aforesaid liquid hybrid element, the emulsion fuel that will mix in the above-mentioned mixing chamber of aforesaid liquid hybrid element imports, have second mixing chamber and second jetburner in the inside of the above-mentioned second liquid hybrid element, wherein, above-mentioned second mixing chamber is communicated with the upstream side of above-mentioned fuel supply path, above-mentioned second jetburner will be in the above-mentioned mixing chamber of aforesaid liquid hybrid element mixed fuel and water in above-mentioned second mixing chamber, spray.Feature of the present invention is, the vegetable oil path is set, this vegetable oil path is communicated with above-mentioned second mixing chamber of the above-mentioned second liquid hybrid element, and this vegetable oil path is communicated with the plant fuel tank that vegetable oil is accommodated that is disposed at the position higher than the position of the above-mentioned second liquid hybrid element.Feature of the present invention is that above-mentioned vegetable oil is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil.Feature of the present invention is, is under the situation of general water at above-mentioned water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.Feature of the present invention is that the water that is contained in the above-mentioned water tank is used bunch process water of handling lessly.Feature of the present invention is that the water that is contained in the above-mentioned water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.Feature of the present invention is, is contained in water in the above-mentioned water tank and is by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock to cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.Feature of the present invention is that above-mentioned process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.Feature of the present invention is, is under the situation of process water at water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
The feature of the manufacture method of emulsion fuel involved in the present invention is, having of the fuel supply path that is communicated with combustion elements midway towards the fuel feed pump of above-mentioned combustion elements fueling, has the liquid hybrid element, this liquid hybrid element has and is used to make mixing chamber that fuel mixes with water and towards the jetburner of above-mentioned mixing chamber burner oil, and be communicated with above-mentioned fuel supply path, by fuel passage the fuel tank that fuel is accommodated is communicated with the above-mentioned jetburner of aforesaid liquid hybrid element, by water passage the water tank that water is accommodated is communicated with above-mentioned mixing chamber, work by above-mentioned fuel feed pump makes the negative pressure of above-mentioned fuel feed pump feed through to above-mentioned mixing chamber via above-mentioned fuel supply path, utilize above-mentioned negative pressure that the water in the above-mentioned water passage is imported above-mentioned mixing chamber and the fuel in the above-mentioned fuel passage is sprayed towards above-mentioned mixing chamber via above-mentioned jetburner, in above-mentioned mixing chamber, to form emulsion fuel, above-mentioned emulsion fuel is supplied with towards above-mentioned combustion elements from above-mentioned fuel feed pump.Feature of the present invention is, send having of above-mentioned fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the above-mentioned jetburner of above-mentioned liquid hybrid element, send having of above-mentioned water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the above-mentioned mixing chamber of above-mentioned liquid hybrid element.Feature of the present invention is, makes above-mentioned fuel feed pump, above-mentionedly sends with petrolift, above-mentionedly sends that the water priming of pump-stopping action carrying out simultaneously.Feature of the present invention is, has fuel Flow-rate adjustment element midway in above-mentioned fuel passage, this fuel is used for the flow fuel that flows through above-mentioned fuel passage is regulated with the Flow-rate adjustment element, above-mentioned water passage have water Flow-rate adjustment element midway, this water is used for the flow of the water that flows through above-mentioned water passage is regulated with the Flow-rate adjustment element.Feature of the present invention is, above-mentioned water passage have open and close valve midway, this open and close valve is used for above-mentioned water passage opened closes.Feature of the present invention is that above-mentioned fuel tank and above-mentioned water tank are disposed at the position higher than aforesaid liquid hybrid element.Feature of the present invention is, the vegetable oil that is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil is mixed with water in the above-mentioned water tank.Feature of the present invention is, has the second liquid hybrid element, this second liquid hybrid element is adjacent in the downstream side of aforesaid liquid hybrid element, the emulsion fuel that will mix in the above-mentioned mixing chamber of aforesaid liquid hybrid element imports, have second mixing chamber and second jetburner in the inside of the above-mentioned second liquid hybrid element, wherein, above-mentioned second mixing chamber is communicated with the upstream side of above-mentioned fuel supply path, and fuel and water that above-mentioned second jetburner will mix in the above-mentioned mixing chamber of aforesaid liquid hybrid element spray in above-mentioned second mixing chamber.Feature of the present invention is, the vegetable oil path is set, this vegetable oil path is communicated with above-mentioned second mixing chamber of the above-mentioned second liquid hybrid element, and this vegetable oil path is communicated with the plant fuel tank that vegetable oil is accommodated that is disposed at the position higher than the position of the above-mentioned second liquid hybrid element.Feature of the present invention is that above-mentioned vegetable oil is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil.Feature of the present invention is, is under the situation of general water at above-mentioned water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.Feature of the present invention is that the water that is contained in the above-mentioned water tank is used bunch process water of handling lessly.Feature of the present invention is that the water that is contained in the above-mentioned water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.Feature of the present invention is, is contained in water in the above-mentioned water tank and is by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock to cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.Feature of the present invention is that above-mentioned process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.Feature of the present invention is, is under the situation of process water at water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
The feature of the method for use emulsion fuel involved in the present invention is, having of the fuel supply path that is communicated with combustion elements midway towards the fuel feed pump of above-mentioned combustion elements fueling, has the liquid hybrid element, this liquid hybrid element has and is used to make mixing chamber that fuel mixes with water and the jetburner of burner oil in the above-mentioned mixing chamber, and be communicated with above-mentioned fuel supply path, by above-mentioned jetburner and fuel passage the fuel tank that fuel is accommodated is communicated with above-mentioned mixing chamber, by water passage the water tank that water is accommodated is communicated with above-mentioned mixing chamber, being provided with of above-mentioned water passage above-mentioned water passage is opened the open and close valve of closing midway, work by above-mentioned fuel feed pump makes the negative pressure of above-mentioned fuel feed pump feed through to above-mentioned mixing chamber, utilize above-mentioned negative pressure to make the fuel in the above-mentioned fuel passage import above-mentioned mixing chamber via above-mentioned jetburner and make the water of above-mentioned water passage import above-mentioned mixing chamber, thereby fuel and water are mixed to produce incomplete emulsion fuel in above-mentioned mixing chamber, before above-mentioned fuel feed pump is stopped, utilize above-mentioned open and close valve to close above-mentioned water passage, above-mentioned fuel feed pump is worked on, and fill up above-mentioned fuel supply path by fuel in and after in the emulsion in the above-mentioned fuel feed pump, stop above-mentioned fuel feed pump.Feature of the present invention is, send having of above-mentioned fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the above-mentioned jetburner of above-mentioned liquid hybrid element, send having of above-mentioned water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the above-mentioned mixing chamber of above-mentioned liquid hybrid element.Feature of the present invention is, is under the situation of general water at above-mentioned water, and the mixing in the V/V 100% of mixed fuel and water in above-mentioned mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.Feature of the present invention is that the water that is contained in the above-mentioned water tank is used bunch process water of handling lessly.Feature of the present invention is that the water that is contained in the above-mentioned water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.Feature of the present invention is, is contained in water in the above-mentioned water tank and is by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock to cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.Feature of the present invention is that above-mentioned process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.Feature of the present invention is, is under the situation of process water at water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
Emulsion fuel involved in the present invention only is made of fuel and water, it is characterized in that, makes the emulsion fuel that is formed by fuel and water and milkization of V/V more than 80% be in the state that mixes with not emulsified fuel and water below 20%.Feature of the present invention is, is under the situation of general water at above-mentioned water, and the mixing in the V/V 100% of mixed fuel and water in above-mentioned mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.Feature of the present invention is that the water that is contained in the above-mentioned water tank is used bunch process water of handling lessly.Feature of the present invention is that the water that is contained in the above-mentioned water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.Feature of the present invention is, is contained in water in the above-mentioned water tank and is by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock to cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.Feature of the present invention is that above-mentioned process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.Feature of the present invention is, is under the situation of process water at water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
The invention effect
According to emulsion fuel manufacturing installation and manufacture method thereof involved in the present invention, need not to be used to the mixing box that fuel is mixed with water, the container that is used to store the emulsion fuel that produces.So, need not the space of two kinds of at present required large-scale casees.In addition, owing to need not to be used for fuel, water and emulsifier are made emulsion fuel and the emulsion fuel large-scale stirring apparatus of emulsification again that makes after separating, therefore, can make the emulsion fuel manufacturing installation with low-down price.In the present invention, the fuel feed pump that to establish the emulsification driving element with water that acts as a fuel only, and utilize the attraction force of the fuel feed pump of having established to make fuel collide to mix with water and make emulsion fuel, therefore, this emulsification method is very simple, and can reduce the cost as device significantly.
In the present invention, find in addition that even comprise the not emulsion fuel of the fuel of emulsification and water (below, as " incomplete emulsion fuel ") of a part, after the manufacturing at once under the situation of burning, it also can burning reliably in combustion elements.Because incomplete emulsion fuel also can burn after manufacturing at once, therefore, use is included in establishes fuel feed pump in the burner device, the attraction force of utilizing this fuel feed pump to produce in the mixing chamber of liquid hybrid element, produce incomplete emulsion fuel (emulsion fuel more than 80% and remaining below 20% fuel and the material of the admixture of water).So, need not at present required being used for and make the dedicated pump of fuel and water mixing and emulsifying, thereby can produce the more cheap emulsion fuel manufacturing installation of price by the mode that extrudes.In addition, by utilizing fuel feed pump that incomplete emulsion fuel is mixed, water in the incomplete emulsion fuel becomes thinner particle, and these particles are dispersed in emulsion fuel and the not emulsified fuel widely, thereby can make the burning reliably in fuel element of this incomplete fuel.
Send in the setting midway of fuel passage and to use petrolift, send in the setting midway of water passage and use water pump.Utilize above-mentioned sending in the liquid hybrid element, to generate the required suitable pressure of emulsion fuel fuel, water to be delivered to the liquid hybrid element by fuel and water with sending with water pump with petrolift.In addition, owing to have to send and use water pump with sending with petrolift, thereby the pressure of the emulsion fuel that can supply with towards the fuel supply path in the downstream side of liquid hybrid element becomes appropriate pressure, and then can keep longlyer in the life-span of the fuel feed pump that is provided with of fuel supply path midway.In addition, make the fuel feed pump of using towards the combustion elements fueling operating switch, fuel passage be provided with midway send with the step switch of petrolift and the sending of setting midway of water passage and connect-disconnect action simultaneously with the step switch of water pump.By this, the open and close valve that is provided with of water passage can be omitted in midway, thereby the manufacture cost of device can be reduced.
In the method for use emulsion fuel involved in the present invention, before the work of burn-out element, fuel feed pump, utilize open and close valve will supply with the closing of water passage of water midway towards the mixing chamber of the liquid hybrid element that fuel is mixed with water.By this, before the work of burn-out element, fuel feed pump, fuel feed pump, fuel supply path only import the fuel from fuel tank, thereby form the state that fuel feed pump, fuel supply path are filled up by fuel.After fuel feed pump, fuel supply path are filled up by fuel, the work of burn-out element, fuel feed pump.When combustion elements, when fuel feed pump stops, in fuel feed pump, fuel supply path, only be full of fuel, thereby incomplete emulsion fuel is not existed.Consequently, emulsion fuel is separated and the water that produces does not exist, thereby can prevent the generation of the fault of the fuel feed pump that the existence because of water causes, the generation of the fault of the fuel feed pump that freezes to cause, the fuel supply path of water when cold.In addition, when unlatching utilized the burning of fuel element once more, owing to only have fuel at first in fuel feed pump, fuel supply path, therefore, combustion elements became well to the ignitability of fuel, thereby can light a fire reliably.
Emulsion fuel involved in the present invention, even if be supplied to the emulsion fuel of fuel element and be incomplete emulsion fuel (V/V of emulsion fuel more than 80% and the V/V of not emulsified fuel and water at the mixture below 20%), after producing, immediately under the situation of burning (water that preferably is contained in the incomplete emulsion fuel is blended in state in emulsion fuel, the fuel widely with smaller particles), also can make the burning reliably in combustion elements of this incomplete emulsion fuel.Therefore, do not use the emulsifiers such as surface active agent of present use, and only use burning and water to make emulsion fuel.Emulsion fuel involved in the present invention be incomplete emulsion fuel (emulsion fuel more than 80% and remaining below 20% not emulsified fuel and the material of the admixture of water), even if so incomplete emulsion fuel, if be contained in inner water is dispersed in emulsion fuel, the not emulsified fuel with becoming smaller particles and approximate equality, the water that then becomes smaller particles can not hinder burning, even if incomplete emulsion fuel also can burn fully.Then, the fuel feed pump rotation that the manufactured incomplete emulsion fuel that goes out has been established in apparatus for combining liquids is stirred, thereby make the water in the incomplete emulsion fuel become littler particle and be in flowing state, therefore, even if do not use surface active agent, also can utilize combustion elements that this incomplete emulsion fuel is burnt reliably.Because emulsion fuel of the present invention does not use emulsifiers such as surface active agent, therefore, can cut down the manufacture cost of emulsion fuel significantly, and can not produce dioxin, thereby can use as the fuel that does not injure environment.
The water that uses in emulsion fuel involved in the present invention used by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock cross the process water that forms, cross the process water that forms and make any process water circular flow in above-mentioned two kinds of process water cross any process water in the process water of the rock that contains a large amount of silica in the igneous rock by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.Mix at the liquid hybrid element with fuel by making above any process water, even if incomplete emulsion fuel, also can produce roughly the emulsion fuel of 90% V/V, compare, can when burning, discharge higher burning energy with the incomplete emulsion fuel that uses general water.
Description of drawings
Fig. 1 is an embodiment the structural drawing of the manufacturing installation of expression emulsion fuel of the present invention.
Fig. 2 is the sectional view of the liquid hybrid element that uses in the manufacturing installation of emulsion fuel of Fig. 1.
Fig. 3 is another embodiment's the structural drawing of the manufacturing installation of expression emulsion fuel of the present invention.
Fig. 4 is another embodiment's the structural drawing of the manufacturing installation of expression emulsion fuel of the present invention.
Fig. 5 is another embodiment's the structural drawing of the manufacturing installation of expression emulsion fuel of the present invention.
Symbol description
10 liquid hybrid elements
12 fuel tanks
14 fuel passage
16 water tanks
18 water passages
20 fuel supply paths
22 burner device
23 combustion elements
24 fuel feed pumps
26 blades
30 mixing chambers
32 jetburners
40 fuel flow control valves
44 Water flow adjusting valves
48 open and close valves
50 second liquid hybrid elements
52 vegetable oil paths
54 plant fuel tanks
56 second mixing chambers
58 second jetburners
60 send and use petrolift
62 send and use water pump
Embodiment
The present invention utilizes fuel and water to make the emulsion fuel of necessary amount when using emulsion fuel.
Embodiment 1
Then, the present invention will be described with reference to the accompanying drawings.Fig. 1 is an embodiment the structural drawing of expression emulsion fuel manufacturing installation of the present invention, and Fig. 2 is the sectional view of the liquid hybrid element that uses among Fig. 1.Emulsion fuel manufacturing installation of the present invention comprises: the liquid hybrid element 10 that fuel is mixed with water; The fuel tank 12 that fuel is accommodated; The fuel passage 14 that liquid hybrid element 10 is communicated with fuel tank 12; The water tank 16 that water is accommodated; And the water passage 18 that liquid hybrid element 10 is communicated with water tank 16.Fuel tank 12 and water tank 16 are set to: its be disposed at liquid hybrid element 10 near, and be disposed at the position higher than liquid hybrid element 10, import liquid hybrid element 10 thereby make because of gravity from the fuel of fuel tank 12 with from the water of water tank 16.The fuel that is contained in the fuel tank 12 uses various fuel such as heavy oil, light oil, lam-oil, gasoline, ethanol (also comprising bio-ethanol), waste oil.The water that is contained in the water tank 16 uses general water (or process water described later) such as tap water.Yet, in the present invention, do not use surface active agent as chemical product.
As shown in Figure 2, liquid hybrid element 10 has shell 28a, 28b, has mixing chamber 30 in the inside of these shells 28a, 28b and towards the jetburner 32 of mixing chamber opening.In addition, also be formed with first introducing port 34, second introducing port 36 and exhaust port 38 in apparatus for combining liquids 10, wherein, above-mentioned first introducing port 34 is communicated with an end with fuel passage 14, and the other end is communicated with jetburner 32; Above-mentioned second introducing port 36 is communicated with an end with water passage 18, and the other end is communicated with mixing chamber 30; Above-mentioned exhaust port 38 is communicated with an end with mixing chamber 30, and the other end is communicated with fuel supply path 20.The cross section of jetburner 32 is set to be compared less with the cross section of fuel passage 14, the cross section of water passage 18, the cross section of mixing chamber 30, the cross section of exhaust port 38.Liquid hybrid element 10 is used for two kinds of liquid are mixed, and for example, can be two-fluid spray nozzle.In the liquid hybrid element 10 of above structure, 30 spray from jetburner 32 towards mixing chamber from the fuel of fuel tank 12, be imported into mixing chamber 30 from the water of water tank 16, thereby being collided in mixing chamber 30 with water, mixes fuel.It is that 2～3cm, length are that the element of the size of 5～6cm is comparatively desirable that liquid hybrid element 10 uses diameter for example.
In the fuel passage 14 that liquid hybrid element 10 is communicated with fuel tank 12 midway, (liquid hybrid element 10 sides) are provided with fuel flow control valve 40 and one-way valve 42 successively towards upstream side (fuel tank 12 sides) from the downstream side.At the water passage 18 that liquid hybrid element 10 is communicated with water tank 16 midway, (liquid hybrid element 10 sides) are provided with open and close valves 48 such as Water flow adjusting valve 44, one-way valve 46 and solenoid valve successively towards upstream side (water tank 16 sides) from the downstream side.Open and close valve 48 is used for stopping water supply towards liquid hybrid element 10 from water passage 18 around the finish time in the burning front and back zero hour, the burning of combustion elements 23.Utilize fuel flow control valve 40 and Water flow adjusting valve 44 that the fuel in the mixing chamber 30 that imports liquid hybrid element 10 and the ratio of mixture of water are regulated.
Regulate fuel flow modulating valve 40 and Water flow adjusting valve 44, for example, when the ratio of the total of fuel that will mix in mixing chamber 30 and water was made as 100%, the ratio that makes fuel was more than 45%, and to make the ratio of water be below 55%.By make ratio of mixture in mixing chamber 30 is that fuel and ratio of mixture more than 45% is that water collision below 55% mixes, and generates the incomplete emulsion fuel of the admixture that is in fuel and water of emulsion fuel more than 80% and remaining not emulsification below 20%.At this, when the ratio of water surpassed 55%, the generation ratio of emulsion fuel can diminish, thereby can not play the effect of emulsion fuel.
Then, the method that the emulsion fuel manufacturing installation that uses Fig. 1 is made emulsion fuel describes.Under the initial situation of using the emulsion fuel manufacturing installation, utilize open and close valve 48 to close water passage 18 in advance, thereby make fuel from fuel tank 12 via fuel passage 14 in liquid hybrid element 10 mixing chamber 30 and fuel supply path 20 in be full of.Then, when utilizing fuel element 23 to take fire and making fuel feed pump 24 work, utilize open and close valve 48 path 18 of fetching boiling water, thereby can import in the mixing chamber 30 of liquid hybrid element 10 from the water of water passage 18.Fuel from fuel passage 14 is configured at any time can both import in the mixing chamber 30 of liquid hybrid element 10.
When fuel feed pump 24 work with from fuel feed pump 24 towards combustion elements during 23 fuelings, can produce attraction force in the fuel supply path 20 of the upstream side of the position of fuel feed pump 24 be negative pressure, and this negative pressure arrives in the mixing chamber 30 of liquid hybrid elements 10 via fuel supply path 20.The negative pressure that arrives in the mixing chamber 30 arrives in the fuel tank 12 from fuel passage 14 via jetburner 32 on the one hand, arrives in the water tank 16 from water passage 18 on the other hand.Be injected in the mixing chamber 30 because of the negative pressure in this mixing chamber 30 make fuel from fuel passage 14 be attracted from jetburner 32, and the water from water passage 18 is attracted in the mixing chamber 30.In mixing chamber 30, because from jetburner 32 high velocity jet fuel that goes out and the water collision that sucks in the mixing chamber 30, therefore, fuel mixes with the water collision, thereby form the not incomplete emulsion fuel of emulsification (volume in 100% volume, more than 80% becomes emulsion fuel, and remaining 20% volume is in fuel and the state that mix not emulsified with water) of a part.In order to generate volume more than 80% and become the incomplete emulsion of emulsion fuel, the attraction force of based on fuel supply pump 24, fuel supply path 20 are set the fuel import volume, water import volume of internal diameter, the fuel supply path 20 of fuel injection orifices 32 etc.
Since the attraction force of fuel feed pump 24 and in mixing chamber 30 the manufactured incomplete emulsion fuel that goes out after this can be imported into fuel feed pump 24 via fuel supply path 24 because of the attraction force of fuel feed pump 24.The incomplete emulsion fuel that is imported into fuel feed pump 24 is for example stirred by blade 26, also is distributed in the emulsion fuel equably thereby make fuel and water become smaller particles, and is in flowing state.Subsequently, incomplete emulsion fuel is transported to combustion elements 23 from fuel feed pump 24, and is burned in combustion elements 23.Incomplete emulsion fuel comprises not emulsified water, is distributed in the emulsion fuel equably but this not emulsified water becomes smaller particles.Because the not emulsified water that comprises in incomplete emulsion fuel is mixed in the emulsion fuel equably as smaller particles, therefore, can not hinder burning by combustion elements 23, consequently, can make incomplete emulsion fuel burning reliably.
As mentioned above, in the present invention, only will be used for being used as unique driving element of making emulsion fuel with fuel and water towards the existing known fuel feed pump 24 of combustion elements 23 fuelings.Promptly, the negative pressure that produces by the work because of fuel feed pump 24 makes fuel collide in the mixing chamber 30 of liquid hybrid element 10 with water to mix, thereby produce incomplete emulsion fuel (more than 80% for emulsion fuel, remaining fuel and the state that mix not emulsified that be in below 20%) with water.Then, by incomplete emulsion fuel is attracted to fuel feed pump 24, and the action that utilizes the blade 26 of this fuel feed pump 24 to stir incomplete emulsion fuel more equably, thereby makes not emulsified water become thinner particle and be distributed in equably in the incomplete emulsion fuel.The V/V of incomplete its emulsion fuel of emulsion fuel after being stirred by the blade 26 of fuel feed pump 24 is identical with manufactured V/V when going out in mixing chamber 30, also is distributed in equably in the incomplete emulsion fuel but water becomes thinner particle.Even the burned incomplete emulsion fuel of fuel in combustion elements 23, it also can perfect combustion, even if thereby compare also about equally with the emulsion fuel of 100% emulsification by the heating energy that burning obtains.
In the present invention, water in being contained in water tank 16 is under the situation of general water such as tap water, when the volume of mixed fuel and water was made as 100% in will the mixing chamber 30 at liquid hybrid element 10, the V/V that makes fuel was more than 45%, and to make the V/V of water be below 55%.In this case, even if do not use surface active agent, fuel is collided in mixing chamber 30 with water to be mixed, when the fuel in will importing mixing chamber 30 and the volume of water are made as 100%, ratio with the V/V more than 80% is made emulsion fuel, and with the ratio of remaining V/V below 20% fuel and water is remained in not emulsified mode.That is, become incomplete emulsion fuel (the not emulsified fuel below the emulsion fuel more than 80% and the 20% and mixture of water).Then, this incomplete emulsion fuel is imported in the fuel feed pump 24 and is stirred, and the fuel below 20% becomes the particle thinner than the emulsion fuel more than 80% with water, and mixes with the state in the whole equal distribution of emulsion fuel.Like this, although incomplete emulsion fuel is not by 100% emulsification, but because the water that exists in this incomplete emulsion fuel becomes thinner particle and is blended in equably in emulsion fuel and the fuel, therefore, this incomplete emulsion fuel is burnt fully in combustion elements 23 as emulsion fuel.
For example, under desire that the running of boiler (not shown) the is stopped situation of (work of combustion elements 23, fuel feed pump 24 is stopped), before stopping this action, utilize open and close valve 48 to close water passage 18, thereby make water can not import the mixing chamber 30 of liquid hybrid element 10 from water passage 18.Not being imported into the work that makes combustion elements 23, fuel feed pump 24 under the state of mixing chamber 30 at water continues for example about 30 seconds, after in fuel feed pump 24, fuel supply path 20 and mixing chamber 30, being in the state that is full of from the fuel of fuel passage 14, the work of burn-out element 23 and fuel feed pump 24.If under the residual situation that emulsion fuel arranged in the inside of fuel feed pump 24 and fuel supply path 20, then before burning by combustion elements 23 once more during, emulsion fuel can be separated into fuel and water, water after this separation becomes the reason of fuel feed pump 24 faults of fuel special use, and becomes the reason that the fuel supply path 20 when freezing breaks.Yet, in the method for use emulsion fuel of the present invention, under the state that the work that makes combustion elements 23, fuel feed pump 24 stops, only residual in the inside of fuel feed pump 24 and fuel supply path 20 have the fuel that is supplied to from fuel passage 14, thereby can prevent the breakage of fuel feed pump 24 and fuel supply path 20.In addition, when the burning of opening once more by fuel element 23, owing to have only fuel supply to combustion elements 23 at first, therefore, the ignitability of 23 pairs of fuel of combustion elements becomes well, thereby can light a fire reliably.When the burning of opening once more by combustion elements 23, the fetch boiling water time point of path 18 of open and close valve 48 gets final product in the front and back of work zero hour of fuel feed pump 24, and for example, making work zero hour of this time point and fuel feed pump 24 is the same time.
As mentioned above, according to emulsion manufacturing installation of the present invention and emulsion manufacture method, because driving element is the attraction force towards the existing known fuel feed pump 24 of combustion elements 23 fuelings, therefore, construction element as the emulsion manufacturing installation, use liquid hybrid element 10, various path (fuel passage 14 and water passage 18) and multiple valve (fuel flow control valve 40, water passage modulating valve 44, open and close valve 48) to get final product, thus cutting down cost significantly.In addition, in the present invention,, therefore, need not to use the large-scale mixing box that is used to make emulsion fuel, the large-scale container that is used to store the emulsion fuel that produces owing to when making emulsion fuel, consume the emulsion fuel that produces.So, need not the space of these casees.
The present application people finds, even burned emulsion fuel is incomplete emulsion fuel (material that emulsion fuel more than 80% and remaining not emulsified fuel below 20% mix with water) in combustion elements 23, if use at once after making, even if incomplete emulsion fuel also can perfect combustion.From this point as can be seen, the emulsion fuel of supplying with towards combustion elements 23 need not to use the emulsion fuel that is under 100% emulsified state.So, in the present invention, only use existing known fuel feed pump 24 as the driving element that fuel is mixed with water and milkization, and, even if do not use surface active agent, also can produce the incomplete emulsion fuel that can in combustion elements 23, burn.In the present invention, as long as use known fuel feed pump 24, thereby reduced price economically significantly as the driving element that fuel is mixed with water and milkization.And therefore the surface active agent owing to not using as chemical agent, can prevent the generation of dioxin.
In the above description, the water that is housed in the water tank 16 uses general water such as tap water, but also can use special process water to replace general water.Can further promote the emulsion fuel of manufacturing in mixing chamber 30 and the emulsification of water by using process water.As the process water of using in the present invention, can use any water in several water.At first, the first, can consider with the water that reduced bunch as process water.Can bunch make glassware for drinking water that surface activity power be arranged by what reduce water.For example, can by water is flow through in the magnetic field that is formed by magnet etc. water is flow through in electromagnetic wave or make ultrasound and the water butt or make ultraviolet irradiation to water or make far-infrared radiation to water reduce water bunch.As reduce water bunch method be not limited to these methods.The second, can be thought of as and contain a large amount of dissolved oxygens (for example, from the nearer value of saturation state (8.4mg/l)) and treated water, treated water for containing a large amount of active hydrogens (for example, from the nearer value of saturation state (absorbance 3.0)).For example, can make water contain a large amount of dissolved oxygens by ozone is contacted with water, but the method that water contains dissolved oxygen is not limited thereto.For example, can contain a large amount of active hydrogens by making water flow through magnetic field, but as the method that water contains a large amount of active hydrogens is not limited thereto.It is comparatively desirable containing a large amount of dissolved oxygens and active hydrogen simultaneously, as long as but comprise at least one side and just can carry out emulsification well.The 3rd, can consider will with the order of the rock that contains a large amount of silica in ion exchange resin, tourmaline, the igneous rock (for example obsidian) by the water that forms or with the order of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline by any water in the water that forms as process water.The 4th, can consider to make in the rock that contains a large amount of silica of any water in igneous rock in the third the water repeatedly water that circular flow crosses as process water.Especially under the situation of use the 3rd, the 4th kind of process water, the fuel in the mixing chamber 30 becomes big with the emulsification of water than regular meeting, and the heat when combustion elements 23 internal combustion emulsion fuels is become greatly.
Process water can promote fuel and the emulsification of water in mixing chamber 30.Under the situation of using process water, if the fuel that will mix and the volume of process water are made as 100%, and to make the volume ratio of fuel be more than 35%, and the V/V that makes process water is below 65%, then in mixing chamber 30, collide when mixing when fuel and water, can form incomplete emulsion fuel.When using process water, incomplete emulsion fuel forms the material of the state that emulsion fuel more than 90% and remaining not emulsified fuel below 10% mixes with water.That is,,, can increase the ratio of the emulsion fuel that produces in the mixing chamber 30 with general water ratio by using process water.Even if use incomplete emulsion fuel, also can in fuel element 23, burn fully, thereby can fully use as emulsion fuel.That is,, then can further reduce the usage ratio of fuel if use process water to replace tap water.
General water or process water such as tap water in also can making vegetable oil and being housed in water tank 16 are mixed.As vegetable oil, use the vegetable oil that constitutes by at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil.This vegetable oil mixes more than 0.1% with the total 100% of water with respect to fuel.Vegetable oil promotes the emulsification of fuel and water, plays the effect identical with surface active agent.Because therefore vegetable oil can, be not excellent for the emulsification that promotes fuel and water because of burning produces dioxin.
In embodiment 1, used a liquid hybrid element 10, used but also can in series dispose a plurality of and liquid hybrid elements liquid hybrid element 10 same structures.As shown in Figure 3, the outlet at the exhaust port 38 of liquid hybrid element 10 links the second liquid hybrid element 50 that has with these liquid hybrid element 10 same structures.The upstream extremity of fuel supply path 20 is connected with the exhaust port 38 (with reference to Fig. 2) of this second liquid hybrid element 50.Under the situation of Fig. 3, an end of vegetable oil path 52 and second introducing port 36 (with reference to Fig. 2) of the second liquid hybrid element 50 are linked, and the other end of plant fuel tank 54 with this vegetable oil path 52 is communicated with.In the second liquid hybrid element 50, be provided with second mixing chamber 56 and second jetburner 58, wherein, above-mentioned second mixing chamber 56 is communicated with vegetable oil path 52, and above-mentioned second jetburner 58 sprays the incomplete emulsion fuel that is produced by liquid hybrid element 10 towards this second mixing chamber 56.In the second liquid hybrid element 50, the vegetable oil that imports from vegetable oil path 52 is collided second mixing chamber 56 in the incomplete emulsion fuel that is produced by liquid hybrid element 10 mix, and can utilize the emulsification of the incomplete emulsion fuel of vegetable oil promotion importing fuel feed pump 24.
In addition, also can link liquid hybrid element with liquid hybrid element 10 (the second liquid hybrid element 50) same structure in the downstream side of the second liquid hybrid element 50 again.In this case, second introducing port 36 (with reference to Fig. 2) of the liquid hybrid element that will newly link in the downstream side is closed.Even make under vegetable oil and the situation that fuel and water mix, the emulsion fuel that is supplied to combustion elements 23 from fuel feed pump 24 also may be by whole emulsifications, even if a part is residual with the not emulsified state of fuel and water, incomplete emulsion fuel also can burn in combustion elements 23 fully, thereby can fully use as emulsion fuel.Under with the situation of water as process water, if the volume ratio of mixture of process water is below 65%, the volume ratio of mixture of fuel is more than 35%, and then emulsion fuel can burn in combustion elements 23 fully, thereby can fully use as emulsion fuel.
Embodiment 3
In embodiment 1, represented that liquid hybrid element 10, fuel tank 12, water tank 16 and combustion elements 23 are disposed at the state of desirable each other position.That is, fuel tank 12 and water tank 16 are in the state that is disposed near the of liquid hybrid element 10 and is disposed at the position higher than liquid hybrid element 10.In addition, liquid hybrid element 10 is near the state that is disposed at firing unit 22.Yet, in existing fuel-burning equipment, there is the fuel tank established, the water tank level configurations of having established situation in height identical or the height lower than the height of combustion elements 23 with the height of combustion elements 23, or the situation that exists the fuel tank of having established, the water tank of having established to dispose in the mode away from combustion elements 23.Embodiment 3 uses the present invention at the situation that disposes the fuel tank of having established, the water tank of having established especially, according to Fig. 4 embodiment 3 is described.But, even under the situation that is not provided with the fuel tank of having established, the water tank of having established, also can use the present invention.In Fig. 4, the symbolic representation same member identical with the member symbol of Fig. 1.
Even in this embodiment 3, also identical with embodiment 1, except the fuel tank of having established, the water tank of having established, also fuel tank 12 and water tank 16 are disposed near the top position the liquid hybrid element 10.Utilize fuel passage 14 that fuel tank 12 is communicated with liquid hybrid element 10 in the same manner with embodiment 1.In this fuel passage 14 midway, sending with petrolift 60 from fuel tank 12 nearer new settings the in position.That is,, have one-way valve 42, fuel flow control valve 40 in the downstream side of petrolift 60 in fuel passage 14 midway.In addition, utilize water passage 18 that water tank 16 is communicated with liquid hybrid element 10 in the same manner with embodiment 1.At this water passage 18 midway, send with water pump 62 dried up case 16 nearer new settings the in position.That is,, have open and close valve 48, one-way valve 46, Water flow adjusting valve 44 at water passage 18 midway in the downstream side of sending with water pump 62.
Promptly established in existing device and to be communicated with an end of establishing fuel passage 66 on the fuel tank 64, the fuel of having established in the fuel tank 64 move via establishing fuel passage 66.Establish having of fuel passage 66 midway at this and established petrolift 68.Be disposed under the situation of height identical or the height lower establishing fuel tank 64 than the height of this combustion elements 23 with the height of combustion elements 23, or be disposed under the situation away from the position of combustion elements 23 establishing fuel tank 64, the other end of having established fuel passage 66 for example is communicated with existing known emulsion manufacturing installation (not shown).On the other hand, promptly established in existing device and to be communicated with an end of establishing water passage 72 on the water tank 70, the water of having established in the water tank 70 move via establishing water passage 72.Establish being provided with of water passage 72 midway at this and established water pump 74.Be disposed under the situation of height identical or the height lower establishing water tank 70 than the height of this combustion elements 23 with the height of combustion elements 23, or be disposed under the situation away from the position of combustion elements 23 establishing water tank 70, the other end of having established water passage 72 for example is communicated with existing known emulsion manufacturing installation (not shown).
Use established fuel tank 64, establish fuel passage 66, establish under the situation of petrolift 68, cut off established fuel passage 66 the other end as free end, with fuelings in can be from the free end of establishing fuel passage 66 towards fuel tank 12.Because it is bigger to have established the flow of petrolift 68, therefore, disconnect with fuel passage 14, the fuel that will come from establishing petrolift 68 conveyings is temporarily put into fuel tank 12.By this, can not make the bigger influence of establishing petrolift 68 of flow feed through to fuel passage 14 and downstream thereof.On the other hand, use established water tank 70, establish water passage 72, establish under the situation of water pump 74, cut off established water passage 72 the other end as free end, in water tank 16, supplying with water from the free end of establishing water passage 72.Because it is bigger to have established the flow of water pump 74, therefore, disconnect with water passage 18, the fuel that will come from establishing water pump 74 conveyings is temporarily put into water tank 16.By this, can not make the bigger influence of establishing water pump 74 of flow feed through to water passage 18 and downstream thereof.
No matter established fuel tank 64, established under the situation of water tank 70 using or do not use, all can be midway in fuel passage 14, send with petrolift 60 being provided with from fuel tank 12 nearer positions.In addition,, send with water pump 62 in dried up case 16 nearer positions settings at water passage 18 midway.Send with petrolift 60 with send compare with the flow of establishing petrolift 68, established water pump 74 with the flow of water pump 62 less, can be so that fuel and water mix well at liquid hybrid element 10 generates the required suitable pressure of emulsion fuel fuel, water are delivered to liquid hybrid element 10.That is, send with petrolift 60 and send with water pump 62 will be delivered to the pressure of the fuel of liquid hybrid element 10, the pressure of water is made as appropriate pressure.In addition, send with petrolift 60 and send and also will be made as appropriate pressure towards the pressure of the emulsion fuel of fuel supply path 20 supplies in the downstream side of liquid hybrid element 10 with water pump 62, consequently, have make the life-span of the fuel feed pump that midway is provided with 24 of fuel supply path 20 keep long effect.
Embodiment 4
Then, with embodiment's 3 (Fig. 4) improvement as embodiment 4 and in Fig. 5, represent.In Fig. 5, the symbolic representation same member identical with the member symbol of Fig. 4.In Fig. 5 (embodiment 4), its main position different with Fig. 1 (embodiment 1) is open and close valve 48 these points that midway are provided with that omitted at water passage 18.In addition, embodiment 4 and embodiment's 3 difference is to make fuel feed pump 24, send with petrolift 60 and send with the connection-disconnection of the switch of water pump 62 and work linkedly.The coupled switch that is used to make the switch of fuel feed pump 24, fuel tank 12 and water tank 16 to work linkedly is existing known technology, therefore, omits the diagram of this coupled switch.In addition, identical with Fig. 4 in Fig. 5 (embodiment 4), represented to establish fuel tank 64, establish fuel passage 66, establish petrolift 68, establish water tank, establish water passage 72, establish water pump 74, but also can omit these members.
Existence will be disposed at the situation that the fuel feed pump 24 in the fuel tank 12 of upstream of position of liquid hybrid element 10 and water tank 16 and the downstream of the position that is disposed at liquid hybrid element 10 disposes close to each otherly.Producing emulsion fuel and using at once under the situation of the emulsion fuel produce, making the fuel feed pump of using towards combustion elements 23 fuelings 24, the sending of below of fuel tank 12 start simultaneously-quit work with the sending of below of petrolift 60 and water tank 16 with water pump 62.Therefore, also can use the operating switch (not shown) that is used to make fuel feed pump 24, send with the operating switch (not shown) of petrolift 60 and send for example coupled switch with operating switch (not shown) connection-disconnection simultaneously of water pump 62.By this, can be omitted in the open and close valve 48 that is provided with of water passage 18 midway.Although used and made fuel feed pump 24, sent with petrolift 60 and send switch,, therefore, can reduce the manufacture cost of device owing to omitted open and close valve 48 with water pump 62 interlocks.
Claims (47)
1. the manufacturing installation of an emulsion fuel is applicable to the situation from the fuel supply path that has fuel feed pump halfway towards the combustion elements fueling, it is characterized in that, comprising:
Fuel tank, this fuel tank is used for fuel is accommodated;
Water tank, this water tank is used for water is accommodated;
Liquid hybrid element, this liquid hybrid element have makes mixing chamber that fuel mixes with water and towards the jetburner of described mixing chamber burner oil, and described mixing chamber is communicated with the upstream side of described fuel supply path;
Fuel passage, an end of this fuel passage is communicated with described fuel tank, and the other end is communicated with the described jetburner of described liquid hybrid element; And
Water passage, an end of this water passage is communicated with described water tank, and the other end is communicated with the described mixing chamber of described liquid hybrid element,
Fuel in the described fuel tank is sprayed in described mixing chamber via described jetburner from described fuel passage, and the fuel in the described water tank imported in the described mixing chamber from described water passage, thereby fuel and water are mixed to make emulsion fuel in described mixing chamber.
2. the manufacturing installation of emulsion fuel as claimed in claim 1 is characterized in that,
Send having of described fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the described jetburner of described liquid hybrid element,
Send having of described water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the described mixing chamber of described liquid hybrid element.
3. the manufacturing installation of emulsion fuel as claimed in claim 2 is characterized in that,
Make described fuel feed pump, describedly send, describedly send water priming of pump-stop action and carry out simultaneously with petrolift.
4. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
Described fuel passage have fuel Flow-rate adjustment element midway, this fuel is used for the flow fuel that flows through described fuel passage is regulated with the Flow-rate adjustment element,
Described water passage have water Flow-rate adjustment element midway, this water is used for the flow of the water that flows through described water passage is regulated with the Flow-rate adjustment element.
5. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
Described water passage have open and close valve midway, this open and close valve is used for described water passage opened closes.
6. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
Described fuel tank and described water tank are disposed at than the high position of described liquid hybrid element.
7. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
The vegetable oil that is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil is mixed with water in the described water tank.
8. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
Have the second liquid hybrid element, this second liquid hybrid element is adjacent in the downstream side of described liquid hybrid element, and the emulsion fuel that will mix in the described mixing chamber of described liquid hybrid element imports,
Have second mixing chamber and second jetburner in the inside of the described second liquid hybrid element, wherein, described second mixing chamber is communicated with the upstream side of described fuel supply path, described second jetburner will be in the described mixing chamber of described liquid hybrid element mixed fuel and water in described second mixing chamber, spray.
9. the manufacturing installation of emulsion fuel as claimed in claim 8 is characterized in that,
The vegetable oil path is set, and this vegetable oil path is communicated with described second mixing chamber of the described second liquid hybrid element,
Described vegetable oil path is communicated with the plant fuel tank that vegetable oil is accommodated that is disposed at the position higher than the position of the described second liquid hybrid element.
10. the manufacturing installation of emulsion fuel as claimed in claim 9 is characterized in that,
Described vegetable oil is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil.
11. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
At described water is under the situation of general water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.
12. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
The water that is contained in the described water tank is used bunch process water of handling lessly.
13. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
The water that is contained in the described water tank is used the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.
14. the manufacturing installation of emulsion fuel as claimed in claim 1 or 2 is characterized in that,
Use by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock and cross the process water that forms and cross any process water in the process water that forms being contained in water in the described water tank by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.
15. the manufacturing installation of emulsion fuel as claimed in claim 14 is characterized in that,
Described process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.
16. the manufacturing installation of emulsion fuel as claimed in claim 14 is characterized in that,
At water is under the situation of process water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
17. the manufacture method of an emulsion fuel is characterized in that,
Having of the fuel supply path that is communicated with combustion elements midway towards the fuel feed pump of described combustion elements fueling,
Have the liquid hybrid element, this liquid hybrid element have be used to make mixing chamber that fuel mixes with water and in the described mixing chamber jetburner of burner oil, and be communicated with described fuel supply path,
By fuel passage the fuel tank that fuel is accommodated is communicated with the described jetburner of described liquid hybrid element,
By water passage the water tank that water is accommodated is communicated with described mixing chamber,
Work by described fuel feed pump makes the negative pressure of described fuel feed pump feed through to described mixing chamber via described fuel supply path,
Import described mixing chamber and the fuel in the described fuel passage is sprayed towards described mixing chamber via described jetburner because of described negative pressure makes the water in the described water passage, in described mixing chamber, forming emulsion fuel,
Described emulsion fuel is supplied with towards described combustion elements from described fuel feed pump.
18. the manufacture method of emulsion fuel as claimed in claim 17 is characterized in that,
Send having of described fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the described jetburner of described liquid hybrid element,
Send having of described water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the described mixing chamber of described liquid hybrid element.
19. the manufacture method of emulsion fuel as claimed in claim 18 is characterized in that,
Make described fuel feed pump, describedly send, describedly send water priming of pump-stop action and carry out simultaneously with petrolift.
20. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
Described fuel passage have fuel Flow-rate adjustment element midway, this fuel is used for the flow fuel that flows through described fuel passage is regulated with the Flow-rate adjustment element,
Described water passage have water Flow-rate adjustment element midway, this water is used for the flow of the water that flows through described water passage is regulated with the Flow-rate adjustment element.
21. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
Described water passage have open and close valve midway, this open and close valve is used for described water passage opened closes.
22. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
Described fuel tank and described water tank are disposed at than the high position of described liquid hybrid element.
23. the manufacture method of emulsion fuel as claimed in claim 22 is characterized in that,
The interior water of vegetable oil that at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil constitutes and described water tank is mixed.
24. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
Have the second liquid hybrid element, this second liquid hybrid element is adjacent in the downstream side of described liquid hybrid element, and the emulsion fuel that will mix in the described mixing chamber of described liquid hybrid element imports,
Have second mixing chamber and second jetburner in the inside of the described second liquid hybrid element, wherein, described second mixing chamber is communicated with the upstream side of described fuel supply path, and fuel and water that described second jetburner will mix in the described mixing chamber of described liquid hybrid element spray in described second mixing chamber.
25. the manufacture method of emulsion fuel as claimed in claim 24 is characterized in that,
The vegetable oil path is set, and this vegetable oil path is communicated with described second mixing chamber of the described second liquid hybrid element,
Described vegetable oil path is communicated with the plant fuel tank that vegetable oil is accommodated that is disposed at the position higher than the position of the described second liquid hybrid element.
26. the manufacture method of emulsion fuel as claimed in claim 25 is characterized in that,
Described vegetable oil is made of at least a oil in castor oil, sunflower oil, rape oil and the rice bran oil.
27. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
At described water is under the situation of general water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.
28. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
The water that is contained in the described water tank is used bunch process water of handling lessly.
29. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
The water that is contained in the described water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.
30. the manufacture method as claim 17 or 18 described emulsion fuels is characterized in that,
Be contained in water in the described water tank and be by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock and cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.
31. the manufacture method of emulsion fuel as claimed in claim 30 is characterized in that,
Described process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.
32. the manufacture method of emulsion fuel as claimed in claim 30 is characterized in that,
At water is under the situation of process water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
33. a method of using emulsion fuel is characterized in that,
Having of the fuel supply path that is communicated with combustion elements midway towards the fuel feed pump of described combustion elements fueling,
Have the liquid hybrid element, this liquid hybrid element have be used to make mixing chamber that fuel mixes with water and in the described mixing chamber jetburner of burner oil, and be communicated with described fuel supply path,
By described jetburner and fuel passage the fuel tank that fuel is accommodated is communicated with described mixing chamber,
By water passage the water tank that water is accommodated is communicated with described mixing chamber,
Being provided with of described water passage described water passage is opened the open and close valve of closing midway,
Work by described fuel feed pump makes the negative pressure of described fuel feed pump feed through to described mixing chamber,
Utilize described negative pressure to make the fuel in the described fuel passage import described mixing chamber via described jetburner and make the water of described water passage import described mixing chamber, thereby fuel and water mixed in described mixing chamber producing incomplete emulsion fuel,
Before described fuel feed pump is stopped, utilize described open and close valve to close described water passage, described fuel feed pump is worked on, and fill up described fuel supply path by fuel in and after in the emulsion in the described fuel feed pump, stop described fuel feed pump.
34. the method for use emulsion fuel as claimed in claim 33 is characterized in that,
Send having of described fuel passage midway and to use petrolift, this is sent with petrolift fuel is sent towards the described jetburner of described liquid hybrid element,
Send having of described water passage midway and to use water pump, this is sent with water pump and is used for sending water towards the described mixing chamber of described liquid hybrid element.
35. the method as claim 33 or 34 described use emulsion fuels is characterized in that,
At described water is under the situation of general water, and the mixing in the V/V 100% of mixed fuel and water in described mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.
36. the method as claim 33 or 34 described use emulsion fuels is characterized in that,
The water that is contained in the described water tank is used bunch process water of handling lessly.
37. the method as claim 33 or 34 described use emulsion fuels is characterized in that,
The water that is contained in the described water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.
38. the method as claim 33 or 34 described use emulsion fuels is characterized in that,
Be contained in water in the described water tank and be by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock and cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.
39. the method for use emulsion fuel as claimed in claim 38 is characterized in that,
Described process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.
40. the method for use emulsion fuel as claimed in claim 38 is characterized in that,
At water is under the situation of process water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
41. an emulsion fuel only is made of fuel and water, it is characterized in that,
Make the emulsion fuel that forms by fuel and water and milkization of V/V more than 80% be in the state that mixes with not emulsified fuel and water below 20%.
42. emulsion fuel as claimed in claim 41 is characterized in that,
At described water is under the situation of general water, and the mixing in the V/V 100% of mixed fuel and water in described mixing chamber, the V/V that makes fuel is more than 45%, and the V/V that makes water is below 55%.
43. emulsion fuel as claimed in claim 41 is characterized in that,
The water that is contained in the described water tank is used bunch process water of handling lessly.
44. emulsion fuel as claimed in claim 41 is characterized in that,
The water that is contained in the described water tank is the process water of handling at least one side of containing in dissolved oxygen and the active hydrogen.
45. emulsion fuel as claimed in claim 41 is characterized in that,
Be contained in water in the described water tank and be by the sequential flow that contains the rock of a large amount of silica in ion exchange resin, tourmaline, the igneous rock and cross the process water that forms and cross any process water in the process water that forms by the sequential flow of the rock that contains a large amount of silica in ion exchange resin, the igneous rock, tourmaline.
46. emulsion fuel as claimed in claim 45 is characterized in that,
Described process water is the water that circular flow is crossed the rock that contains a large amount of silica in the igneous rock.
47. emulsion fuel as claimed in claim 45 is characterized in that,
At water is under the situation of process water, and the mixing in the V/V 100% of mixed fuel and water in mixing chamber, the V/V that makes fuel is more than 35%, and the V/V that makes water is below 65%.
Applications Claiming Priority (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008-274541 | 2008-10-24 | ||
| JP2008274541 | 2008-10-24 | ||
| JP2009-003388 | 2009-01-09 | ||
| JP2009003388 | 2009-01-09 | ||
| JP2009042372 | 2009-02-25 | ||
| JP2009-042372 | 2009-02-25 | ||
| PCT/JP2009/068115 WO2010047343A1 (en) | 2008-10-24 | 2009-10-21 | Apparatus for producing emulsion fuel, method for producing emulsion fuel, method for handling emulsion fuel, and emulsion fuel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102187079A true CN102187079A (en) | 2011-09-14 |
| CN102187079B CN102187079B (en) | 2014-03-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200980142528.XA Expired - Fee Related CN102187079B (en) | 2008-10-24 | 2009-10-21 | Method for producing emulsion fuel, and method for handling emulsion fuel |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JPWO2010047343A1 (en) |
| CN (1) | CN102187079B (en) |
| WO (1) | WO2010047343A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106164589A (en) * | 2014-06-24 | 2016-11-23 | 深井利春 | Emulsion fuel feedway and supply method thereof |
| CN111226034A (en) * | 2017-10-27 | 2020-06-02 | 宝马股份公司 | Method for preventing icing of an injection system of an internal combustion engine |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2017209166A1 (en) * | 2016-05-31 | 2017-12-07 | 深井 利春 | Water supply device, water supply method, and vehicle |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0642734A (en) * | 1992-07-27 | 1994-02-18 | Kiichi Hirata | Ionization emulsion manufacturing device its combustion system |
| DE4341038A1 (en) * | 1993-12-02 | 1995-06-08 | Reinhard Weber | Fuel supply system for diesel engines |
| CN1287222A (en) * | 2000-07-14 | 2001-03-14 | 清华大学 | Clean combustion process with less exhausted nitrogen oxide and carbon black particle for diesel engine |
| CN1338025A (en) * | 1999-01-28 | 2002-02-27 | 斯普利泰克技术公司 | Method and device for producing a fuel mixture for an internal combustion engine |
-
2009
- 2009-10-21 JP JP2010534825A patent/JPWO2010047343A1/en active Pending
- 2009-10-21 CN CN200980142528.XA patent/CN102187079B/en not_active Expired - Fee Related
- 2009-10-21 WO PCT/JP2009/068115 patent/WO2010047343A1/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0642734A (en) * | 1992-07-27 | 1994-02-18 | Kiichi Hirata | Ionization emulsion manufacturing device its combustion system |
| DE4341038A1 (en) * | 1993-12-02 | 1995-06-08 | Reinhard Weber | Fuel supply system for diesel engines |
| CN1338025A (en) * | 1999-01-28 | 2002-02-27 | 斯普利泰克技术公司 | Method and device for producing a fuel mixture for an internal combustion engine |
| CN1287222A (en) * | 2000-07-14 | 2001-03-14 | 清华大学 | Clean combustion process with less exhausted nitrogen oxide and carbon black particle for diesel engine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106164589A (en) * | 2014-06-24 | 2016-11-23 | 深井利春 | Emulsion fuel feedway and supply method thereof |
| CN111226034A (en) * | 2017-10-27 | 2020-06-02 | 宝马股份公司 | Method for preventing icing of an injection system of an internal combustion engine |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2010047343A1 (en) | 2010-04-29 |
| JPWO2010047343A1 (en) | 2012-03-22 |
| CN102187079B (en) | 2014-03-05 |
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