CN201906579U - Multi-stage emulsification device for blended fuel - Google Patents
Multi-stage emulsification device for blended fuel Download PDFInfo
- Publication number
- CN201906579U CN201906579U CN2011200003872U CN201120000387U CN201906579U CN 201906579 U CN201906579 U CN 201906579U CN 2011200003872 U CN2011200003872 U CN 2011200003872U CN 201120000387 U CN201120000387 U CN 201120000387U CN 201906579 U CN201906579 U CN 201906579U
- Authority
- CN
- China
- Prior art keywords
- oscillator
- fuel
- emulsifier
- communicated
- open channel
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The utility model discloses multi-stage emulsification device which has a good emulsification effect on blended fuel or oil-water blended fuel, and greatly improves the rate of economizing petrol. The multi-stage emulsification device comprises a water inlet pipe (2) and an oil inlet pipe which are communicated with a premixer (1), wherein the premixer (1) is communicated with a static mixer (4); crucially, the static mixer (4) is communicated with a pressure stabilizer (5); the pressure stabilizer (5) is communicated with an oil pump (6) for driving the blended fuel to flow and then connected with an emulsifier (7); the outlet of the emulsifier (7) is connected with a tee joint (8); one outlet (9) of the tee joint (8) serves as the final outlet for emulsified fuel; another outlet of the tee joint (8) is connected with a return pipe (23) and then communicated with the pressure stabilizer (5); and the oil pump (6) is connected with a driving motor (10). By using the multi-stage emulsification device, the rate of economizing petrol can be increased to more than 10 percent.
Description
Technical field:
The utility model relates to the mixing arrangement of at least two kinds of immiscible liquid, specifically is meant the device that two kinds of immiscible liquid can be reached a kind of multistage emulsification of very high emulsification degree at least.
Background technology:
Along with the progress of society, the use of fossil fuel is more and more big, and by the prediction of International or National how tame mechanism, fossil fuel is only enough human the uses decades of oil particularly, and therefore tapping a new source of energy with energy savings is the important state basic policy of country.The exploitation of new forms of energy relates to a large amount of fund inputs and technical problem, is not can solve by short-term, and traditional oil fuel also will be on the energy in the highest flight, so energy savings just has crucial meaning.Oil-water fuel blend after the emulsification or oil/water or oil/alcohol-blended fuel can be saved the checking that certain energy has obtained technology, and existing some theoretical explanations, but think that at present the rate of economizing gasoline of aqueous fuel generally has only 4～5%, idol has the report rate of economizing gasoline can reach about 10%, but also not having the product report of industrially scalable in the reality, only is the result that the laboratory obtains.Why is the rate of economizing gasoline of profit fuel not high in the reality? can improve again? what is the combustion mechanism of profit fuel on earth? problem is a lot, all explain again and be difficult to, but can say for certain that the quality with the emulsification of profit fuel has direct relation, as setting about from the emulsifying effectiveness of profit fuel, improve rate of economizing gasoline, crucial meaning is then arranged.
Summary of the invention:
Goal of the invention of the present utility model is to disclose a kind of fuel combination or oil-water fuel blend to be had fine emulsifying effectiveness, and the multistage emulsifier unit that rate of economizing gasoline is significantly improved.
Realize that technical solution of the present utility model is as follows: comprise the water inlet pipe and the oil inlet pipe that are communicated with premixer, premixer is communicated with static mixer, key is that static mixer is communicated with voltage-stablizer, after being communicated with, the voltage-stablizer oil pump mobile with driving fuel combination connect an emulsifier again, the emulsifier outlet connects threeway, one outlet of threeway is that the final outlet of emulsion fuel, another outlet of threeway connect return duct and be communicated with voltage-stablizer, and oil pump is connected with drive motors.
Described emulsifier comprises a base, in the through hole of base one end, be provided with nozzle, nozzle has a flat slit-shaped spout, the other end of base be have a strip can be by the open channel of liquid, be provided with the wedge shape oscillator that on three-dimensional, to make micro-displacement in the open channel, the tip of wedge shape oscillator is over against the flat slit-shaped spout of nozzle, and a cover plate is fixed on the surface of open channel.
The sidewall of described oscillator has four blind holes, places above-mentioned blind hole and makes oscillator be positioned at the center of open channel through the end of the screw thread holder of open channel sidewall.
The described emulsion fuel that is back to voltage-stablizer through return duct be oil pump output the fuel combination amount 50～80%, the output pressure of oil pump is 10～25kg/cm
2
The described emulsion fuel that is back to voltage-stablizer through return duct be oil pump output the fuel combination amount 65～72%, and the output pressure of oil pump is 18～22kg/cm
2
Described water inlet pipe is provided with water meter, entering water electromagnetic valve and control valve, is provided with pressure check valve on return duct.
Described voltage-stablizer also is provided with user's return duct, and user's return duct is provided with gas and oil separating plant.
Of the present utility model simple in structure, emulsifying effectiveness to profit fuel is splendid, can carry out emulsification to the aqueous fuel of diesel oil/water, gasoline/water, heavy oil/water or other type, the content of water in oil can reach about 20%, in the situation of not adding any emulsifying agent, fuel after the emulsification uses immediately, and rate of economizing gasoline can generally reach more than 10%, even rate of economizing gasoline reaches near 20%.Not only broken through the index of the rate of economizing gasoline under the existing universal, and can realize industrially scalable, also can use at all types of combustion apparatus, as automobile, big craft, Industrial Stoves, heavy oil boiler etc., all obtained good result of the test, exhaust emission when also reducing burning simultaneously is the very real equipment with fine economic benefit and social benefit.
Description of drawings:
Fig. 1 is the structural representation of an embodiment of the present utility model.
Fig. 2 is the overall structure schematic diagram of the emulsifier in the utility model.
Fig. 3 is the sectional structure schematic diagram of emulsifier.
Fig. 4 is the structural representation of an embodiment of the oscillator that uses in the emulsifier.
The specific embodiment:
See also Fig. 1～Fig. 4, specific embodiment of the utility model is as follows: comprise the water inlet pipe 2 and the oil inlet pipe 3 that are communicated with premixer 1, premixer 1 is communicated with static mixer 4, and premixer 3 has a cavity, tentatively mixes under the effect of hydraulic pressure and oil pressure; Static mixer 4 is the conventional prior art of using, its structure generally is helical duct to be arranged in it or rotatable blade is arranged, profit fuel after the premixed makes the preliminary emulsification of profit fuel at fluid pressure current downflow state complex, static mixer 4 is communicated with voltage-stablizer 5 afterwards, the profit fuel of preliminary emulsification enters voltage-stablizer 5, voltage-stablizer 5 is not only the device in volume of profit fuel, it plays a linking effect to amount of liquid in the system pipeline and pressure, make the fluid pressure in the whole pipeline that one good pressure transition be arranged, guarantee the continuous supply of fuel combination; Voltage-stablizer 5 connects the vibrate emulsifier 7 of emulsification of a pair of fuel combination again with driving after oil pump 6 that fuel combination flows is communicated with, emulsifier 7 outlets connect threeway 8, one liquid outlet 9 of threeway 8 is the final outlet of emulsion fuel, profit fuel after the part emulsification is exported to combustion apparatus through this, another outlet of threeway 8 connects return duct 9 and is communicated with voltage-stablizer 5, mixing profit fuel after the part emulsification is back to voltage-stablizer 5, and the profit fuel with the new preliminary emulsification that replenishes in voltage-stablizer 5 carries out emulsification again; Oil pump 6 is connected with drive motors 10.Through a large amount of tests, the emulsification liquid measure that control is flowed back to voltage-stablizer 5 through return duct 23 be oil pump 6 outputs liquid measure 50～80%, so most of fuel combination passes through twice emulsification of emulsifier 7 at least, partially mixed fuel can be by repeatedly emulsification, promptly emulsification is once in premixer 1, emulsification is once in static mixer 4 again, carry out emulsification again at emulsifier 7 again, after refluxing again, most of fuel combination after the emulsification repeats above-mentioned emulsion process again, then fuel combination is emulsified at least 5～6 times, so be multipole emulsification; The particle diameter of the dispergated particle water in the fuel after above-mentioned multipole emulsification can reach about 10 μ m, and good uniformity.
In the utility model, the emulsification of 7 pairs of fuel combinations of emulsifier is extremely important, described emulsifier 7 comprises a base 11, in the through hole of base 11 1 ends, be provided with nozzle 12, nozzle 12 has a flat slit-shaped spout, the other end of base 11 is the open channel 13 with Tong Guo liquid of a strip, be provided with the wedge shape oscillator 14 that on three-dimensional, to make micro-displacement in the open channel 13, the tip of wedge shape oscillator 14 is over against the flat slit-shaped spout of nozzle 12, one cover plate 15 is screwed the surface in open channel 13, open channel 13 constitutes the emulsification passages, opens cover plate 15 and can safeguard or change the wedge shape oscillators 14 in the open channel 13; Early stage tentatively the liquid of emulsification mixing come out through the flat slit-shaped spout high velocity jet of nozzle 12, enter open channel 13 (being the emulsification passage) over against nozzle 12, the moment that ejects is the mixed once of liquid, but in open channel 13, be provided with the oscillator 14 of the tool wedge shaped tip of a micro-displacement on three-dimensional, the wedge shaped tip part of the positive bump of the mixing material of high-speed motion oscillator 14, when making mixing material further broken oscillator 14 is applied an active force, this active force will make oscillator 14 vibrate on three-dimensional, and form the passage that mixing material flows between two surfaces of oscillator 14 and the open channel 13, the vibration of oscillator 14 applies the particle of multidirectional active force and further broken mixing material again to mixing material, a large amount of minute particles in the mixing material is mixed in the fluid, can thinks that maybe the fuel oil of mixed emulsification shape is that a large amount of water in oil molecules constitutes; Above-mentioned can make the mixed process of mixing material quite complicated on microcosmic at the oscillator 14 that vibrates on the three-dimensional, exist multidirectional active force to be applied on the mobile mixing material, and this multidirectional active force all puts on mixing material in fluid flows through the process of all surface of oscillator 14, so can make mixing material reach very high emulsification degree.
In open channel 13, on three-dimensional, make micro displacement for making above-mentioned oscillator 14, sidewall at oscillator 14 has four blind holes 22, end through the screw thread holder 16 of open channel 13 sidewalls places above-mentioned blind hole 22 and makes oscillator 14 be positioned at the center of open channel 13, between the inner surface of the blind hole 22 of the end of screw thread holder 16 and oscillator 14 sidewalls a minim gap is arranged, the existence in this gap makes oscillator 14 that a micro displacement space all can be arranged on three-dimensional, is equivalent to end intrafascicular approximately that oscillator 14 can be suspended in four holders 16; Remove above-mentioned structure, when oscillator 14 has certain thickness, oscillator 14 has two through holes to run through the two side, through hole through the correspondence of base 11, two fixed axis (not shown)s are fixedlyed connected with base 11 after passing the through hole of oscillator 14, oscillator 14 places the center of open channel 13, and the diameter of fixed axis is slightly less than the diameter of the through hole of base 11, and then oscillator 14 can be at the three-dimensional top offset in the gap that two above-mentioned diameter differences constitute; Above-mentioned gap length can be regulated, and preceding a kind of structure only need be regulated screw thread holder 16 and be got final product, and a kind of structure in back is by the fixed axis of changing different-diameter or the oscillator 14 of changing the through hole of tool different-diameter, the size that just can regulate above-mentioned gap; The difference of gap length, the amplitude difference of oscillator 14 under impact flow then, the size that acts on the reaction force on the fluid-mixing is also different, and then reaches the degree of regulating emulsifying liquid; In the displacement structure of two kinds of above-mentioned oscillators 14, when flow rate of fluid improved, the frequency of oscillation of oscillator 14 improved, the raising of frequency of oscillation, and corresponding emulsification degree also improves.The cross sectional shape of above-mentioned open channel 13 is rectangle or circle, when the cross sectional shape of open channel 13 is rectangle, its structure is the open channel of nozzle 12 over against a rectangle cross section, and open channel is provided with a fixable cover plate 15, and then open channel just constitutes the emulsification passage; The cross sectional shape of above-mentioned open channel 13 is circular, then only needs the passage of nozzle 12 over against a circular cross-section; Aforesaidly the open channel 13 that oscillator 14 is applicable to the rectangle cross section is set, the open channel 13 that oscillator 14 is applicable to circular cross-section is set by fixed axis by screw thread holder 16.
Draw through a large amount of tests, the emulsification degree of mixing material is relevant with the flow regime of mixing material in open channel 13, and the flow regime of fluid is more complicated, and the emulsification degree better.Therefore, one end of described oscillator 14 is a wedge shaped tip, this wedge shaped tip is a flat, tip portion is over against above-mentioned nozzle 12, the other end of oscillator 14 is and above-mentioned wedge shaped tip symmetrical structure, between two wedge shaped tip parts is the tabular linkage section of a square-section, 14 of oscillators form two surfaces, form between the surface of these two surfaces and open channel 13 liquid flow on, lower channel, fluid is by open channel 13 time, at first impinge upon over against the wedge shaped tip part of the oscillator 14 of nozzle 12, mainly be divided into by oscillator 14 then, flowing in two surfaces of following two parts by oscillator 14, converges back outflow oscillator at the afterbody of the other end of oscillator 14.By hydromechanical theory, oscillator 14 is away from the important function that is mixed with of the shape convection cell of an end of nozzle 12, when being symmetrical structure as the wedge shaped tip at the two ends of above-mentioned oscillator 14, fluid mobile more stable can form local turbulent flow at tail end under the situation of laminar flow; Tail end as oscillator 14 is asymmetric wedge shape, and this asymmetric wedge shape is as being shorter than the front end wedge shape of (end over against nozzle 12 is called front end), and then the turbulent flow of tail end is more strong; As tail end is the streamlined curved surface, and then the turbulent flow of tail end relaxes relatively; As tail end is plane, and then the turbulent flow of tail end is the strongest.The front end of above-mentioned oscillator 14 and the structure of tail end wedge shaped tip identical or different can adapt to the emulsification of different mixing materials.
Integrally-built identical or different except above-mentioned oscillator 14 to adapt to the mobile emulsification of different mixing materials, increase the complex flowization of mixing material, help also that fluid is subjected to more active force to increase the fragmentation of liquid particles in flow process in the overall process by oscillator 14 both sides.For reaching above-mentioned purpose, the surface that makes oscillator 14 is a matsurface, and this matsurface is that many small raised lines vertical with oscillator 14 length directions constitute, or is that a plurality of small pits constitute, or is that a plurality of small projectioies constitute; When fluid passed through rough surface, fluid resistance increased, and promptly boundary-layer increases, gradient zones in fluid and oscillator 14 surface formation different in flow rate, increased the interaction force in the fluid, can further increase the degree of crushing of different liquids particle in the fluid, the emulsifiability of mixing material is increased; Above-mentioned oscillator 14 rough surfaces that are made of small raised line or small pit or minute protrusions can be formed by the process technology of routine, or rough surface separately factor constitute or can multifactorly constitute, or can constitute by the other factors outside above-mentioned three kinds of factors, but basic reason all is to increase fluid flow resistance or form a plurality of small turbulent regions to increase the interaction force of mixing material inside on oscillator 14 surfaces, finally increases the emulsification degree of mixing material; Certainly also can form matsurface at the inner surface of open channel 13, also available small raised line of the inner surface of open channel 13 or formations such as groove or pit also can reach the effect of the emulsification degree that increases mixing material; Further, the inner surface of the surface of oscillator 14 and open channel 13 is matsurface simultaneously, can further improve the emulsification degree of mixing material.Because the emulsification degree of mixing material is decided by multiple factor, the multiple factors such as form of the active force that applies of the interaction force between the surface tension of the polarity of the molecule of each liquid or size, liquid, each liquid, the external world that mixing material is subjected to and size thereof, liquid flow for example.In the utility model, mixing material is subjected to behind certain pressure by after spurting into open channel 13 with flat in the nozzle 12, directly clash into the corresponding wedge shaped tip of oscillator 14, oscillator 14 vibrates under the effect of impact, mixing material multi-direction motion back under reaction force is final under the restriction of wedge shaped tip, flow in two surfaces at oscillator 14, the active force of the oscillator 14 that mixing material is vibrated again, also be subjected to the internal action power of the turbulent flow of the frictional force on aforesaid oscillator 14 surfaces and formation, finally further disorderly flowing of the tail end fluid of oscillator 14, a series of fluid flow and multiaction power under, fluid-mixing can reach higher emulsification degree; Be the flow process that promotes above-mentioned fluid and the generation of active force, the length of the wedge shaped tip of the front end of oscillator 14 is 2～4 with the ratio of the thickness of oscillator 14, be preferably 2.5～3.2, when wedge shaped tip above-mentioned length and thickness than scope in the time, fluid-mixing has positive preferably bump to wedge shaped tip, wedge shaped tip has preferable rigidity again and also fluid-mixing is had suitable shunting action, is beneficial to passage or gap that fluid-mixing flows into the both sides of oscillator 15.
The thickness of oscillator 14 is greater than 1.5mm and less than the height of open channel 13 or the full-size of open channel 13, and and form the gap between the inwall of open channel 13, the thickness requirement of oscillator 14 can guarantee that it has certain rigid, weight, simultaneously make fluid-mixing be subjected to the resistance of certain area (being the area of the section of oscillator 14) again, and making the flow velocity on 14 liang of surfaces of oscillator obtain certain raising, the factor of these above-mentioned several respects all helps the emulsification of mixing material.
The front has provided structure and its effect of emulsifier 7 in detail, the effect of emulsifier 7 is extremely important, but multistage (inferior) emulsification and the mobile unobstructed of mixing material of whole device play an important role equally, for guaranteeing the high efficiency flow of above-mentioned mixing material, the output pressure of oil pump 6 is 10～25kg/cm
2For better, oil pump 6 is driven by motor 10, and through the emulsion fuel liquid measure that return duct 23 flows back to voltage-stablizer 5 be oil pump 6 outputs liquid measure 50～80%, under this state, the jet velocity of the liquid in the emulsifier 7 can reach a high value, the frequency of oscillation of oscillator 14 is also higher, emulsified at least device 7 emulsifications of liquid three times; Or oil pump 6 output pressures are 18～22kg/cm
2, the emulsion fuel liquid measure that flows back to voltage-stablizer 5 through return duct 10 be oil pump 6 outputs liquid measure 65～72%; For further the effectively mobile of the liquid in the whole device that guarantee, on water inlet pipe 2, be provided with water meter 17, entering water electromagnetic valve 18 and control valve 19, on return duct 23, be provided with pressure check valve 20, can in time regulate water oil input or input ratio.
Water in the fuel combination that the utility model uses can account for total amount 5～30% in regulate, above-mentioned so-called water accounts for 5～30% and is meant that its burning is fully effectively, in actual use, emulsion fuel generally is through a nozzle combustion jet to be gone into combustion chamber, at this moment emulsion fuel must be have pressure and sufficient quantity, general quantity delivered is greater than the actual amount that sprays into combustion chamber, unnecessary fuel then can be back to voltage-stablizer 5 through a user's return duct 21 that is connected with voltage-stablizer 5, can guarantee that then whole device liquid in use is unobstructed; Be the damage of emulsifier 7 in oscillatory process that prevents to occur, behind oil pump 6, connect a preceding four-way 24, four-way 25 after one of the termination before the threeway 8, two outlets of preceding four-way 24 connect two inlets of four-way 25 afterwards after connecing an emulsifier 7 respectively again, another outlet of preceding four-way 24 directly is connected with an inlet of back four-way 25, then form two pipelines in fact with emulsifier 7, when a pipeline goes wrong, another pipeline then can start, between preceding four-way 24 and emulsifier 7, be provided with ball valve 26, for regulating the fluid pressure in the whole device at any time, in preceding four-way 24, be provided with a Pressure gauge 27 with monitor pressures; Voltage-stablizer 5 also is provided with user's return duct 21, also is provided with gas and oil separating plant on user's return duct 21.
Total of the present utility model is simple relatively, but because the good oscillation effect of emulsifier 7, make the fuel combination emulsifying effectiveness very good, the control of flow makes emulsification, combustion through repeatedly emulsification in the device simultaneously, the diameter that finally makes the particle water in the fuel combination is about 10 μ m, and most of particle water can be at 5-7 μ m particle diameter, and particle water distributing very evenly in fuel combination is so adapt to various combustion apparatus.The utility model is adapted to all size equipment, gasoline engine, diesel engine, heavy oil combustion stove etc., can reach at rate of economizing gasoline under the situation of 10-20%, also can greatly reduce the pollution of discharging, but be the emulsifying device that a kind of commercial scale is used, have crucial economic worth.
Claims (7)
1. the multistage emulsifier unit of a fuel combination, comprise the water inlet pipe (2) and the oil inlet pipe (3) that are communicated with premixer (1), premixer (1) is communicated with static mixer (4), it is characterized in that static mixer (4) is communicated with voltage-stablizer (5), after being communicated with, voltage-stablizer (5) oil pump (6) mobile with driving fuel combination connect an emulsifier (7) again, emulsifier (7) outlet connects threeway (8), one outlet (9) of threeway (8) is the final outlet of emulsion fuel, another outlet of threeway (8) connects return duct (23) and is communicated with voltage-stablizer (5), and oil pump (6) is connected with drive motors (10).
2. press the multistage emulsifier unit of the described fuel combination of claim 1, it is characterized in that described emulsifier (7) comprises a base (11), in the through hole of base (11) one ends, be provided with nozzle (12), nozzle (12) has a flat slit-shaped spout, the other end of base (11) be have a strip can be by the open channel (13) of liquid, be provided with the wedge shape oscillator (14) that on three-dimensional, to make micro-displacement in the open channel (13), the tip of wedge shape oscillator (14) is over against the flat slit-shaped spout of nozzle (12), and a cover plate (15) is fixed on the surface of open channel (13).
3. press the multistage emulsifier unit of the described fuel combination of claim 2, the sidewall that it is characterized in that described oscillator (14) has four blind holes (22), places above-mentioned blind hole (22) and makes oscillator (14) be positioned at the center of open channel (13) through the end of the screw thread holder (16) of open channel (13) sidewall.
4. press the multistage emulsifier unit of claim 1 or 2 or 3 described fuel combinations, it is characterized in that the described emulsion fuel that is back to voltage-stablizer (5) through return duct (9) be oil pump (6) output the fuel combination amount 50～80%, the output pressure of oil pump (6) is 10～25kg/cm
2
5. press the multistage emulsifier unit of the described fuel combination of claim 4, it is characterized in that the described emulsion fuel that is back to voltage-stablizer (5) through return duct (9) be oil pump (6) output the fuel combination amount 65～72%, and the output pressure of oil pump (6) is 18～22kg/cm
2
6. by the multistage emulsifier unit of the described fuel combination of claim 5, it is characterized in that described water inlet pipe (2) is provided with water meter (17), entering water electromagnetic valve (18) and control valve (19), is provided with pressure check valve (20) on return duct (9).
7. by the multistage emulsifier unit of the described fuel combination of claim 6, it is characterized in that described voltage-stablizer (5) also is provided with user's return duct (21), user's return duct (21) is provided with gas and oil separating plant.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200003872U CN201906579U (en) | 2011-01-04 | 2011-01-04 | Multi-stage emulsification device for blended fuel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200003872U CN201906579U (en) | 2011-01-04 | 2011-01-04 | Multi-stage emulsification device for blended fuel |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201906579U true CN201906579U (en) | 2011-07-27 |
Family
ID=44298789
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200003872U Expired - Fee Related CN201906579U (en) | 2011-01-04 | 2011-01-04 | Multi-stage emulsification device for blended fuel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201906579U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430359A (en) * | 2011-09-19 | 2012-05-02 | 大连维乐液压制造有限公司 | Oil-water mixing system |
| CN105223935A (en) * | 2015-10-21 | 2016-01-06 | 四川省绵竹兴远特种化工有限公司 | Emulsion [explosive emulsification production line safety control system |
| CN110230537A (en) * | 2019-06-21 | 2019-09-13 | 中国神华煤制油化工有限公司 | Fuel oil hybrid control system |
-
2011
- 2011-01-04 CN CN2011200003872U patent/CN201906579U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430359A (en) * | 2011-09-19 | 2012-05-02 | 大连维乐液压制造有限公司 | Oil-water mixing system |
| CN105223935A (en) * | 2015-10-21 | 2016-01-06 | 四川省绵竹兴远特种化工有限公司 | Emulsion [explosive emulsification production line safety control system |
| CN105223935B (en) * | 2015-10-21 | 2017-10-27 | 四川省绵竹兴远特种化工有限公司 | Emulsion emulsifies production line safety control system |
| CN110230537A (en) * | 2019-06-21 | 2019-09-13 | 中国神华煤制油化工有限公司 | Fuel oil hybrid control system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201906579U (en) | Multi-stage emulsification device for blended fuel | |
| JP5407090B2 (en) | Method for producing emulsion fuel | |
| WO2013169414A1 (en) | Bubble implosion reactor cavitation device, subassembly, and methods for utilizing the same | |
| US20240058773A1 (en) | Device and method for enhancing liquid-liquid emulsification | |
| CN102527284B (en) | Oil-water emulsifying device | |
| CN103657497B (en) | For three grades of hybrid systems of liquid mixing | |
| RU2689493C1 (en) | Device for homogenizing heavy fuel hydrodynamic treatment for marine diesels | |
| RU111455U1 (en) | LIQUID GAS CONTACT DEVICE | |
| CN203159167U (en) | Proportioning mixer suitable for producing milk beverage | |
| CN203694980U (en) | Ultrasonic field dosing static mixer | |
| CN104667776B (en) | A kind of many apparatus for combining liquids | |
| RU82582U1 (en) | MIXING DEVICE FOR GAS SYSTEMS - LIQUID | |
| SG182600A1 (en) | Apparatus and method for producing an emulsion of a fuel and an emulsifiable component | |
| CN201618533U (en) | Liquid-liquid inhomogeneous microcosmic mixing device | |
| CN201921659U (en) | Ultrasonic vibration liquid emulsifying device | |
| RU89417U1 (en) | LIQUID GAS CONTACT DEVICE | |
| RU2335337C2 (en) | Rotary-oscillatory device | |
| RU172559U1 (en) | DEVICE FOR MIXING LIQUIDS IN RESERVOIRS | |
| RU2265478C1 (en) | Universal hydrodynamic homonogenizing disperser | |
| CN212017437U (en) | Liquid fuel emulsifying device | |
| CN103611456B (en) | A kind of ultrasonic field static chemical feeding mixer | |
| CN212440887U (en) | Stirring device for oil-water mixing emulsification | |
| CN202778296U (en) | After-mixing device for liquid mixing | |
| RU2248251C1 (en) | Multipurpose hydrodynamic homogenizing dispenser | |
| RU107072U1 (en) | HYDRODYNAMIC MIXER |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHONG YAOJUN Free format text: FORMER OWNER: SHENZHEN SHENWEIDEQUN ENERGY TECHNOLOGY DEVELOPMENT CO., LTD. Effective date: 20130929 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 518118 SHENZHEN, GUANGDONG PROVINCE TO: 518000 SHANWEI, GUANGDONG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130929 Address after: Huang Qiang Zhen Huang Keng Cun, Guangdong County of Haifeng province No. 14 518000 Patentee after: Zhong Yaojun Address before: 518118 Guangdong Province, Shenzhen City Pingshan Pingshan street Shijing Hengtang Road No. 8 Patentee before: Shenzhen Shenweidequn Energy Technology Development Co., Ltd. |
|
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shenzhen City Ding Luyuan science and Technology Development Co Ltd Assignor: Zhong Yaojun Contract record no.: 2014440020013 Denomination of utility model: Multi-stage emulsification device for blended fuel Granted publication date: 20110727 License type: Exclusive License Record date: 20140113 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| DD01 | Delivery of document by public notice |
Addressee: Peng Niancai Document name: Notification of Passing Examination on Formalities |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110727 Termination date: 20160104 |