CN101993746A - Fuel manufacturing method - Google Patents
Fuel manufacturing method Download PDFInfo
- Publication number
- CN101993746A CN101993746A CN200910208314XA CN200910208314A CN101993746A CN 101993746 A CN101993746 A CN 101993746A CN 200910208314X A CN200910208314X A CN 200910208314XA CN 200910208314 A CN200910208314 A CN 200910208314A CN 101993746 A CN101993746 A CN 101993746A
- Authority
- CN
- China
- Prior art keywords
- fuel
- water
- distribution channel
- oil fuel
- propellant combination
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
The present invention provides a method for manufacturing micronized emulsion fuel having stable state and capable of solving problems of low universality and complex device. The method is that the emulsion fuel is manufactured by dispersing water into fuel oil, and includes: a first step of flowing the water and the fuel oil through regions applied by magnetic force respectively, wherein molecules of the water and the fule oil are all micronized by the magnetic force; a second step of mixing the water and the fuel oil; and a third step of stirring the mixed fuel of the water and the fuel oil and micronizing molecules of the mixed fuel.
Description
Technical field
The present invention relates to fuel production method, relate in particular to the method for making emulsion fuel.
Background technology
The heat with the combustion fuel gained be delivered in the water and convert water vapour to and the thermal source machines such as boiler of hot water in, as burnt fuel, can utilize and add to water and tensio-active agent in the oil fuel and stir, thereby make the emulsion fuel (Emulsion Fuel) of water-dispersion in the oil fuel.This emulsion fuel can suppress to follow burning and generation that the oxynitride (NOx), oxysulfide (SOx), the particle-like substance (PM (particulate matter)) that generate wait, has the effect that alleviates the carrying capacity of environment that discharge gas brings.Therefore, in recent years, emulsion fuel more and more is concerned by people.
The apparatus for reforming of fuel that is connected on the diesel engine is disclosed in the patent documentation 1.In this apparatus for reforming of fuel, the mixed solution of liquid fuel and water is applied high-frequency vibration, generated micronized emulsion fuel.And, come controlled liq fuel feed and water supply amount by corresponding engine operating status, thereby carry out fuel reforming.
Yet above-mentioned apparatus for reforming of fuel is the vehicle loading type, constitutes with the Controlling System combination of running condition.Therefore, it is low and be difficult to make the problem of micronize and stable emulsion fuel with low cost to have produced versatility.
[patent documentation 1] TOHKEMY 2004-76608 communique
Summary of the invention
Therefore, the objective of the invention is to solve above-mentioned problem, promptly solve the complicated of the low and device of versatility, the method for making micronize and in stable condition fuel is provided.
To achieve these goals, the fuel production method of an embodiment of the invention is to make the method make the emulsion fuel of water-dispersion in the oil fuel, and this method comprises:
Above-mentioned water and above-mentioned oil fuel are flowed through respectively apply the zone of magnetic force, and the molecule of above-mentioned water and the molecule of above-mentioned oil fuel are carried out micronized first operation respectively with this magnetic force;
Second operation of mixing above-mentioned water and above-mentioned oil fuel;
The propellant combination that has mixed above-mentioned water and above-mentioned oil fuel is stirred and the molecule of this propellant combination is carried out micronized the 3rd operation.
In addition, the fuel production apparatus of another embodiment of the present invention is to make the fuel production apparatus make the emulsion fuel of water-dispersion in the oil fuel, and this device adopts following structure:
Above-mentioned fuel production apparatus comprises: the water distribution channel of the above-mentioned water that circulates; The oil fuel distribution channel of the above-mentioned oil fuel of mentioned emulsifier has been added in circulation; The propellant combination distribution channel of circulation propellant combination, this propellant combination is mixed with the above-mentioned oil fuel of above-mentioned oil fuel with distribution channel of flowing through by the above-mentioned water of above-mentioned water with distribution channel of flowing through; And the steel basin (tank) that the above-mentioned propellant combination of flowing through is stirred with the above-mentioned propellant combination of distribution channel;
Around above-mentioned water usefulness distribution channel and above-mentioned oil fuel usefulness distribution channel, dispose the magnet that in this each distribution channel, applies magnetic force respectively.
The present invention passes through structure as mentioned above, can adopt simple device to make versatility height, micronize and in stable condition fuel.
Description of drawings
Fig. 1 is the structure iron of the fuel production apparatus in the expression embodiment 1.
Fig. 2 is the structure iron of the disclosed magnetic force of presentation graphs 1 portion.
Fig. 3 is the synoptic diagram that is used to illustrate the fuel production method that uses the disclosed fuel production apparatus of Fig. 1.
Nomenclature
1 water distribution channel
2 oil fuel distribution channels
3 propellant combination distribution channels
4 magnet
11,21,31 magnetic force portions
20 oil fuel steel basins
32,35 pumps
33 pressure regulator valves
34 steel basins
36 grooves
Embodiment
<embodiment 1 〉
Referring to figs. 1 through Fig. 3 first embodiment of the invention is described.Fig. 1 is the structure iron of expression fuel production apparatus.Fig. 2 is the synoptic diagram of the local structure of this device of expression.Fig. 3 is the synoptic diagram that is used to illustrate the fuel production method that uses fuel production apparatus.
[fuel production apparatus]
At first, with reference to Fig. 1 and Fig. 2 the structure of fuel production apparatus is described.At first, the fuel production apparatus in the present embodiment is a device of making emulsion fuel, and this emulsion fuel is to add water and emulsifying agent and make water-dispersion in oil fuel and form in the such oil fuel of A heavy oil.At this moment, the volume ratio of A heavy oil and water be roughly each 50%, the volume ratio of adding emulsifying agent wherein to is 0.5% of a final emulsion fuel manufacture.And the method for making of emulsion fuel is the water-in-oil method for making (W/O method for making) that wraps into water in oil.But each components in proportions is not limited to above-mentioned value.
In addition, mentioned emulsifier is all tensio-active agents, is the general name that intramolecularly has hydrophilic group and oleophilic group material, has the oil fuel of making and does not separate with water, and make water be evenly dispersed in effect in this oil fuel.In addition, oil fuel is not limited to A heavy oil, also can be other oil fuel such as kerosene, light oil.
And as shown in Figure 1, fuel production apparatus comprises: making the logical pipe arrangement of current is water distribution channel 1; The pipe arrangement that makes the A heavy oil circulation of having added emulsifying agent is an oil fuel distribution channel 2; The pipe arrangement that makes the propellant combination circulation that has mixed water and A heavy oil is a propellant combination distribution channel 3.
Fuel production apparatus comprises that also adding emulsifying agent to also stir in the A heavy oil groove is oil fuel steel basin 20 (oil fuel whipping appts).At first, with dropping into A heavy oil in the steel basin 20, in this A heavy oil add emulsifying agent simultaneously to this oil fuel.Then, the A heavy oil to the state that added mentioned emulsifier stirs.Then, make above-mentioned oil fuel flow into oil fuel distribution channel 2 with the A heavy oil in the steel basin 20.In addition, oil fuel for example is equipped with agitating vane with steel basin 20, stirs A heavy oil and emulsifying agent by rotating this agitating vane.
Also be provided with the magnetic force portion 11 that applies magnetic force to the water of circulation midway with distribution channel 1 at above-mentioned water.As shown in Figure 2, this magnetic force portion 11 disposes magnet 4 at water around with distribution channel 1.In this example, the magnetic force of magnet 4 is 4140 Gausses, and is clipping water with two row of distribution channel 1, and being decided the interval separate configuration with institute has 12 magnet 4.But the magnetic force of magnet 4, allocation position and number etc. are not subjected to above-mentioned restriction.Thus, with in the distribution channel 1, can apply the magnetic force of above-mentioned magnet 4 to this water by the water that water flowed into as shown by arrow F surrounded by magnet 4, thus to water molecules carry out micronize (reunionization, clustered).For example, by using the magnet of above-mentioned magnetic force and number, water molecules can be formed the particulate below the 50 μ m.
Identical with distribution channel 1 with above-mentioned water, the A heavy oil that also has been provided with to the interpolation of circulating emulsifying agent midway with distribution channel 2 at above-mentioned oil fuel applies the magnetic force portion 21 of magnetic force.This magnetic force portion 21 adopts and is arranged on above-mentioned water with (symbol 11) identical structure on the distribution channel 1, as shown in Figure 2, disposes a plurality of magnet 4 at oil fuel on every side with distribution channel 2.In addition, the magnetic force of magnet 4, configuration and number etc. can be same as described above, also can be different.Thus,, can apply the magnetic force of magnet 4 to this A heavy oil, thereby the A heavy oil molecules is carried out micronize (reunionization) with in the distribution channel 2 by the oil fuel that A heavy oil flowed into as shown by arrow F surrounded by magnet 4.For example, by using the magnet of above-mentioned magnetic force and number, can be below molecule micronize to the 50 μ m with A heavy oil.
Then, above-mentioned water connects in the downstream side of above-mentioned each magnetic force portion 11,21 placement with distribution channel 1 and oil fuel distribution channel 2, and leads to propellant combination distribution channel 3.Thus, propellant combination with distribution channel 3 in the propellant combination that mixed by micronized water and A heavy oil by above-mentioned molecule of circulation.At this moment, this water and A heavy oil are respectively by micronize, and owing to be added on the effect of the emulsifying agent in the A heavy oil, the propellant combination uniform mixing that makes water and A heavy oil mix separates together and not.
Identical with above-mentioned water with distribution channel 1, with in the distribution channel 3, also be provided with the magnetic force portion 31 that applies magnetic force to the propellant combination of circulation at propellant combination.This magnetic force portion 31 adopts and is arranged on above-mentioned water with the identical structure of magnetic force portion (symbol 11) in the distribution channel 1, as shown in Figure 2, is provided with a plurality of magnet 4 at propellant combination on every side with distribution channel 3.In addition, the magnetic force of magnet 4, configuration, number etc. can be same as described above, also can be different.Thus,, can apply the magnetic force of magnet 4 to the molecule of this propellant combination, thereby can make the further micronize of propellant combination (reunionization) with in the distribution channel 3 by the propellant combination that propellant combination flowed into as shown by arrow F surrounded by magnet 4.
In the downstream side of propellant combination, also be provided with pump 32, the pressure regulator valve 33 of sending propellant combination with the above-mentioned magnetic force of disposing of distribution channel 3 portion 31.This pressure regulator valve 33 for example can be controlled its action by electronic signal S1, thereby adjusts propellant combination being sent to the pressure in downstream.
And it is steel basin 34 (whipping appts) that propellant combination also is provided with the groove that mixes fuel with distribution channel 3.This steel basin 34 is controlled stirring velocity by electronic signal S2, and for example control mixes the speed of rotation such as agitating vane of fuel.For example, thus can control stirring velocity makes below molecule micronize to the 30 μ m of propellant combination by stirring.
In the downstream side of propellant combination, be provided with the pump 35 of sending propellant combination, the groove 36 of accumulating propellant combination with the above-mentioned steel basin 34 of disposing of distribution channel 3.And the propellant combination that is accumulated in the groove 36 is an emulsion fuel, for example can supply with thermal source machines such as boiler, and burn in this thermal source machine.
[fuel production method]
Then, with reference to Fig. 3,, be manufactured on the method for adding the emulsion fuel of water and emulsifying agent in the oil fuel and describe using the fuel production apparatus of said structure.
At first, add A heavy oil with steel basin 20, add emulsifying agent simultaneously at oil fuel.Then, stir the A heavy oil added emulsifying agent at oil fuel in steel basin 20.Then, make A heavy oil flow into oil fuel distribution channel 2 (arrow Y1).Simultaneously, move the water to flow into water distribution channel 1 (arrow Y2).
Then, be arranged at water, applying magnetic force from magnet 4 to the water of this water of flowing through with distribution channel 1 with in the distribution channel 1 magnetic force portion 11 midway.So, making water molecules micronize (reunionization) with this magnetic force, for example, can make below water micronize to the 50 μ m (arrow Y2) by using the magnet 4 of above-mentioned magnetic force, configuration.Equally, in the magnetic force portion 21 that oil fuel is provided with distribution channel 2 midway, to this oil fuel of flowing through with the interpolation of distribution channel 2 the A heavy oil of emulsifying agent apply magnetic force from magnet 4.Therefore, make A heavy oil molecules micronize (reunionization), for example, can make below A heavy oil micronize to the 50 μ m (arrow Y1) by using the magnet 4 of above-mentioned magnetic force, configuration with this magnetic force.Thus, water and A heavy oil before mixed respectively by magnetic force by micronize (first operation).
Then, the above-mentioned water of flowing through is used in distribution channel 3 interflow with the A heavy oil of distribution channel 2 at propellant combination with the oil fuel of flowing through with the water of distribution channel 1, mixes forming propellant combination mutually, flows to this propellant combination again and uses in the distribution channel 3 (arrow Y3).At this moment, the water at interflow and A heavy oil are respectively by micronize, and because the effect of the emulsifying agent that adds in the A heavy oil separates the propellant combination uniform mixing together and not.Then, be arranged at propellant combination with in the distribution channel 3 magnetic force portion 31 midway, this propellant combination applies magnetic force from magnet 4 with the propellant combination of distribution channel 3 to flowing through.Therefore, make propellant combination micronize (reunionization) (second operation) with magnetic force.
Then, the propellant combination of flowing through flows in the steel basin 34 (arrow Y4) with the propellant combination of distribution channel 3, and stirs (the 3rd operation) in this steel basin.So,, make the further micronize of molecule of propellant combination by this stirring.For example, by the control stirring velocity, make below molecule micronize to the 30 μ m of propellant combination.
Then, the propellant combination after the micronize is accumulated in (arrow Y5) in the groove 36.Then, be that emulsion fuel acts as a fuel and supplies with for example combustion unit such as boiler with being accumulated in propellant combination in the groove 36.
By adopting above operation, can make in stable condition high-quality emulsion fuel, this emulsion fuel is by below abundant micronize to the 30 μ m, and A heavy oil does not separate with water and water evenly spreads in this A heavy oil.Above-mentioned manufacturing installation, manufacture method can use the so simple structure of magnet to realize, and the versatility height, and be therefore very useful.
More than to being illustrated with the situation that distribution channel 3 is provided with magnetic force portion 31 at propellant combination, but can be not this magnetic force portion 31 be set in distribution channel 3 at propellant combination yet.That is to say, can apply magnetic force the propellant combination of water and A heavy oil.
In addition, in the above description with in A heavy oil, add emulsifying agent before water mixes and stir, but can add emulsifying agent at any time, and oil fuel also can be set with steel basin 20.But,, can suppress separating of water and A heavy oil as mentioned above by in A heavy oil, adding emulsifying agent before the mixing water.
<embodiment 2 〉
Then, second embodiment of the present invention is described.Structure to above-mentioned fuel production method and fuel production apparatus in the present embodiment is carried out brief description.
The fuel production method of an embodiment of the invention is to make the method make the emulsion fuel of water-dispersion in the oil fuel, and this method comprises:
Above-mentioned water and above-mentioned oil fuel are flowed through respectively apply the zone of magnetic force, and the molecule of above-mentioned water and the molecule of above-mentioned oil fuel are carried out micronized first operation respectively with this magnetic force;
Second operation of mixing above-mentioned water and above-mentioned oil fuel;
The propellant combination that has mixed above-mentioned water and above-mentioned oil fuel is stirred and the molecule of this propellant combination is carried out micronized the 3rd operation.
And, in the above-mentioned fuel production method, preferably in above-mentioned second operation, above-mentioned propellant combination is flowed through applies the zone of magnetic force, and make the molecule micronize of above-mentioned propellant combination with this magnetic force.
And in the above-mentioned fuel production method, preferably in above-mentioned first operation, after adding emulsifying agent and stir in above-mentioned oil fuel, thereby the zone that this oil fuel is flowed through apply magnetic force makes the molecule micronize of this oil fuel.
And, in the above-mentioned fuel production method, preferably in above-mentioned first operation, distributed magnet around each distribution channel that above-mentioned water and above-mentioned oil fuel are flowed through respectively, above-mentioned water and above-mentioned oil fuel in flowing into this each distribution channel respectively apply magnetic force respectively.Equally, preferably in above-mentioned second operation, distributed magnet around distribution channel that above-mentioned propellant combination is flowed through, the above-mentioned propellant combination in flowing into this distribution channel applies magnetic force.
And, in the above-mentioned fuel production method, preferably in above-mentioned first operation, respectively above-mentioned water and above-mentioned oil fuel are applied the magnetic force of institute's definite value, so that the molecule of above-mentioned water and above-mentioned oil fuel is respectively below micronize to the 50 μ m.And, preferably in above-mentioned the 3rd operation, this propellant combination is stirred so that below molecule micronize to the 30 μ m of above-mentioned propellant combination.
And, be the fuel production apparatus of another embodiment of the present invention of realizing above-mentioned fuel production method, be to make the fuel production apparatus that makes the emulsion fuel of water-dispersion in the oil fuel, this device adopts following structure:
Comprise: the water distribution channel of the above-mentioned water that circulates; The oil fuel distribution channel of the above-mentioned oil fuel of mentioned emulsifier has been added in circulation; The propellant combination distribution channel of circulation propellant combination, this propellant combination have mixed the above-mentioned water of flowing through is used distribution channel with the above-mentioned water of distribution channel and the above-mentioned oil fuel of flowing through above-mentioned oil fuel; And the steel basin that the above-mentioned propellant combination of flowing through is stirred with the above-mentioned propellant combination of distribution channel;
Around above-mentioned water usefulness distribution channel and above-mentioned oil fuel usefulness distribution channel, dispose the magnet that in this each distribution channel, applies magnetic force respectively.
In the above-mentioned fuel production apparatus, the oil fuel whipping appts that the above-mentioned oil fuel that is added with mentioned emulsifier is stirred is set preferably, above-mentioned oil fuel makes the above-mentioned oil fuel circulation of adopting above-mentioned oil fuel to stir with whipping appts with distribution channel.
Utilizability on the industry
The present invention can be used for making the emulsion fuel of the burning such as the thermal source machine of supplying with boiler, has the utilizability on the industry.
Claims (9)
1. a manufacturing makes the fuel production method of the emulsion fuel of water-dispersion in the oil fuel, and this method comprises:
Described water and described oil fuel are flowed through respectively apply the zone of magnetic force, and the molecule of described water and the molecule of described oil fuel are carried out micronized first operation respectively with this magnetic force;
Second operation of mixing described water and described oil fuel;
The propellant combination that has mixed described water and described oil fuel is stirred and the molecule of this propellant combination is carried out micronized the 3rd operation.
2. fuel production method as claimed in claim 1 wherein, in described second operation, is flowed through described propellant combination and is applied the zone of magnetic force, and makes the molecule micronize of described propellant combination with this magnetic force.
3. fuel production method as claimed in claim 1, wherein, in described first operation, after adding emulsifying agent and stir in described oil fuel, thereby the zone that this oil fuel is flowed through apply magnetic force makes the molecule micronize of this oil fuel.
4. fuel production method as claimed in claim 1, wherein, in described first operation, distributed magnet around each distribution channel that described water and described oil fuel are flowed through respectively, described water and described oil fuel in flowing into this each distribution channel respectively apply magnetic force respectively.
5. fuel production method as claimed in claim 2, wherein, in described second operation, distributed magnet around the distribution channel of flowing through at described propellant combination, the described propellant combination in flowing into this distribution channel applies magnetic force.
6. fuel production method as claimed in claim 1 wherein, in described first operation, applies the magnetic force of institute's definite value respectively to described water and described oil fuel, so that the molecule of described water and described oil fuel is respectively below micronize to the 50 μ m.
7. fuel production method as claimed in claim 1 wherein, in described the 3rd operation, stirs so that below molecule micronize to the 30 μ m of described propellant combination this propellant combination.
8. a manufacturing makes the fuel production apparatus of the emulsion fuel of water-dispersion in the oil fuel, and described fuel production apparatus comprises:
The water distribution channel of described water circulates; The oil fuel distribution channel of the described oil fuel of described emulsifying agent has been added in circulation; The propellant combination distribution channel of circulation propellant combination, this propellant combination is mixed with the described oil fuel of described oil fuel with distribution channel of flowing through by the described water of described water with distribution channel of flowing through; And the steel basin that the described propellant combination of flowing through is stirred with the described propellant combination of distribution channel;
Around described water usefulness distribution channel and described oil fuel usefulness distribution channel, dispose the magnet that in this each distribution channel, applies magnetic force respectively.
9. fuel production apparatus as claimed in claim 8, wherein, described fuel production apparatus comprises the oil fuel whipping appts that the described oil fuel that is added with described emulsifying agent is stirred,
Described oil fuel makes the described oil fuel circulation of adopting described oil fuel to stir with whipping appts with distribution channel.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2009187234A JP2011038000A (en) | 2009-08-12 | 2009-08-12 | Fuel manufacturing method |
JP2009-187234 | 2009-08-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101993746A true CN101993746A (en) | 2011-03-30 |
Family
ID=43766091
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN200910208314XA Pending CN101993746A (en) | 2009-08-12 | 2009-10-29 | Fuel manufacturing method |
Country Status (2)
Country | Link |
---|---|
JP (1) | JP2011038000A (en) |
CN (1) | CN101993746A (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5267898B1 (en) * | 2012-05-11 | 2013-08-21 | 株式会社山陽ポンプ工業所 | Method and apparatus for reforming fossil fuel |
KR101328151B1 (en) | 2013-04-11 | 2013-11-13 | 고천일 | Apparatus for manufacturing a reforming fuel and a method for manuracturing the same |
WO2015198231A1 (en) * | 2014-06-25 | 2015-12-30 | Advanced Financial Services S.A. | Device and method for making emulsions of water in heavy fuel oil |
US10751675B2 (en) | 2014-11-10 | 2020-08-25 | Eme Finance Ltd. | Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion |
IT201600132801A1 (en) | 2016-12-30 | 2018-06-30 | Eme International Ltd | Apparatus and process for producing liquid from biomass, biofuel and biomaterial |
US10947469B2 (en) | 2019-05-13 | 2021-03-16 | James Chun Koh | Apparatus and method for manufacturing bio emulsion fuel using vegetable oil |
US11584894B2 (en) | 2021-04-23 | 2023-02-21 | James Chun Koh | Apparatus for bio emulsion fuel manufacturing from waste oils and method using the same |
AU2022374189B1 (en) * | 2021-12-21 | 2023-07-06 | Manuel Barreiro | Fuel conditioning system |
-
2009
- 2009-08-12 JP JP2009187234A patent/JP2011038000A/en not_active Withdrawn
- 2009-10-29 CN CN200910208314XA patent/CN101993746A/en active Pending
Also Published As
Publication number | Publication date |
---|---|
JP2011038000A (en) | 2011-02-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101993746A (en) | Fuel manufacturing method | |
EP1975393A1 (en) | Biodiesel fuel engine system and method of driving biodiesel fuel engine | |
JP2007032937A (en) | Mixed fuel preparation device | |
JP4156191B2 (en) | Emulsion production equipment | |
JPWO2009054377A1 (en) | Emulsion fuel, method for producing the same and apparatus for producing the same | |
KR20110028645A (en) | High shear process for air/fuel mixing | |
US20120279118A1 (en) | Fuel emulsification system | |
JPWO2009014147A1 (en) | Water emulsion production equipment | |
JP4733711B2 (en) | Mixed fuel supply device and mixed fuel supply method | |
CN101574632A (en) | Continuous emulsifying device | |
CN203208992U (en) | Online flotation reagent emulsification device | |
JP2020186360A (en) | Production apparatus and production method of bio-emulsion fuel using vegetable oil | |
JP2006016495A (en) | Method for supplying emulsified fuel and apparatus for the same | |
CN102451624A (en) | Mixing device | |
CN109964063A (en) | Hydraulic formula speed changer | |
CN108927080B (en) | Equipment for preparing lipid microsphere | |
WO2008004450A1 (en) | Emulsion fuel and equipment and process for production of the same | |
US20140223808A1 (en) | Method of Manufacturing a Reforming Fuel by Adding Water to a Fuel Oil and the Manufacturing Apparatus thereof | |
JP2009293819A (en) | Emulsion fuel supply device and emulsion fuel combustor | |
JP2010149089A (en) | Method and apparatus for producing emulsion oil continuously | |
JP2017222730A (en) | Water blended fuel and apparatus for generating water blended fuel | |
KR101389978B1 (en) | Emulsified Fuel Manufacturing Apparatus | |
US11434817B2 (en) | Systems for supplying liquid fuel emulsion to a combustion system of a gas turbine | |
US20150122216A1 (en) | Method and system to improve atomization and combustion of heavy fuel oils | |
WO2016068137A1 (en) | Effluent-mixed fuel generation/supply system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110330 |