CN1088473A - Circulating emulsion device for viscous fuel oil - Google Patents
Circulating emulsion device for viscous fuel oil Download PDFInfo
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- CN1088473A CN1088473A CN 92113862 CN92113862A CN1088473A CN 1088473 A CN1088473 A CN 1088473A CN 92113862 CN92113862 CN 92113862 CN 92113862 A CN92113862 A CN 92113862A CN 1088473 A CN1088473 A CN 1088473A
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Abstract
A kind of circulating emulsion device for viscous fuel oil by heater, just mix device, pump, jet emulsifier, turbulent emulsifier, ultraemulsifier, magnetic emulsifying stabilizer, fluid reservoir, closed circuit and corresponding instrument, valve are formed automatically.This device is applicable to the circulating emulsion and the ultra-fine stable emulsion of viscous fuel oil, regular fuel, to strengthening the watering quantity of fuel oil, improves efficiency of combustion, and environment purification, energy savings have remarkable effect.
Description
The present invention relates to a kind of device of emulsifying liquid, especially the circulating emulsion device of viscous fuel oil.
As everyone knows, add water in the hydrocarbon liquid fuel and form emulsion and can bring benefit, in combustion process, wrap in the small globule in the oil reservoir, because of vaporization is exploded to the burning of fuel, make atomizing fuel oil, improved efficiency of combustion, when making fuel, because the existence of water with heavy oil, make the burning of heavy oil emulsive liquid clean, reduce fuel uncombusted part, purified environment, energy savings.
Domestic some fuel emulsification device that occurred in succession, reported " method and apparatus for preparing an oily water-in-oil emulsion " as CN1056262A, CN2095033L has reported that " spraying fuel emulsification machine " CN2100938L has reported " spiral-flow type fuel emulsification machine ", CN86104937 has reported " Subultrasonic fuel emulsifying magnetizing device " etc., these mulsers are only applicable to the fuel oil of viscosity less than 200 centistokes, as gasoline, diesel oil etc., for the viscous fuel oil of viscosity greater than 200 centistokes, because oil viscosity height, diffusion and the convection velocity of water in oil is slow, can't carry out uniformly emulsify with said apparatus.Another shortcoming of said apparatus is can not circulating emulsion.The liquid big for viscosity, that diffusion velocity is slow can not be realized ultra-fine emulsification.
The objective of the invention is to propose a kind of emulsifier unit, the uniformly emulsify of its suitable viscous liquid, the also emulsification of suitable low-viscosity (mobile) liquid simultaneously.And can realize the circulating emulsion of emulsion.
The fuel oil emulsifier that the utility model proposes is by the profit heating system, the profit hybrid system, pump, jet emulsifier unit, the turbulent flow emulsifier unit, phaco device or vibration emulsifier unit, magnetic emulsifier unit, the emulsion holding vessel, automatically circulating emulsion system and corresponding temperature show, pressure shows, flow shows, accessory instruments such as liquid level demonstration constitute.
Profit heating system employing tubular electric heating is placed in fuel tank or the water tank and heats, or adds deep fat or add hot water with oil with double pipe heat exchanger, tubular heat exchanger, spiral heat exchanger, water.The fuel tank import is provided with oil filter, is used for the impurity of filtering viscous oil.The top of fuel tank or water tank is provided with temperature display meter, and pressure display instrument table, the pipeline that oil, water flow out are provided with flow display device, adjust the valve and the servo-actuated oil-water ratio control valve of flow.
Profit heating system Jiang Shui and oil heat, and can reduce the viscosity of oil, water, and the intermolecular warm-up movement of profit is quickened in the convection current of accelerating liquid and diffusion, reduces the resistance of ducting, is beneficial to the emulsification of viscous oil and water.
The profit hybrid system is that the water that will give heat carries out initial mixing with the oil that gives heat, and one of scheme is aqueduct to be inserted profit is mixed.For increasing emulsifying effectiveness, a plurality of apertures that overflow are set around aqueduct, water flows out with oily even contact, mixes from a plurality of aperture that overflow.Two of scheme is that petroleum pipeline enters in the spiral fuel reserve tank, cover is a (operating) water nozzle above being furnished with many apertures, interior cover all around in the spiral fuel reserve tank, or a plurality of discharge orifices are set, interior cover below is the oil-water mixture tap hole, the oil that aperture sprays around the water of interior cover top (operating) water nozzle ejection and the interior cover mixes in interior mantle cavity, and the oil-water mixture flow export enters in the pump below the interior cover under the effect of gravity.
Pump will just mix liquid and add force feed jet emulsifier.
The jet emulsifier is that the liquid after the pressurization is injected in the emulsification chamber by emulsification chamber arrival end nozzle high pressure.Be to increase emulsifying effectiveness, nozzle can adopt now to be sold nozzle or establish spiral acceleration line, dividing plate or a plurality of jet orifice in nozzle, makes drop intersect mixing mutually.
The turbulent flow emulsifier is that the liquid after the emulsification of jet emulsifier is sent into emulsification in the turbulated tube.One of scheme is to be provided with the spiral stream guidance mixed plate in the turbulent emulsion tube, and the spiral stream guidance mixed plate is spiral yarn shapedly to be arranged in the turbulated tube or to adopt Double-spiral to be arranged in the turbulated tube, and emulsion is along the helix Turbulence Flow.Two of scheme is sleeve pipe turbulent mixture devices, be provided with interior pipe in the sleeve pipe turbulent mixture device, the hole and the seam that are distributing on the interior pipe and arranging by certain way, aperture or sealing are left in its end, in flowing into by hole and seam, emulsion in the interior pipe mixes emulsification between pipe and outer tube.Three of scheme is hydraulic barrier formula turbulent flow emulsifiers, and hydraulic barrier is designed to cross, annular, circle lacks on shape or the circular piece presses certain angle distribution circular hole, one or more of above-mentioned deflection plate are arranged in the turbulated tube by different angles, constantly change the emulsion flow direction, turbulent mixture.Four of scheme is turbulent emulsifier, and moving turbulent emulsifier is to be provided with blade or the rotating axle of helix blade in turbulated tube, and when emulsion passed through turbulated tube, mobile emulsion acted on and makes a moving blade on the blade, and emulsion is stirred.Turbulent emulsifier in the utility model can adopt any form in the said structure.
The shocking type emulsifier: be provided with one or more vibration reeds in the shocking type emulsifier, reed middle part is clamped in one, and to have on the vibration axle in reed slit a welding fixing.The vibration axle is installed on the shaft holder, and reed rotates along the vibration axle, and when emulsion process vibration sheet, the vibration sheet vibrates, and by pressurization constantly and release, the disperse in oil of the water in the emulsion distributes.The vibration sheet produces the vibration of different frequency, as follows ultrasonic vibration, ultrasonic vibration etc.The shocking type emulsifier ultra-fine emulsion process that suits.
Ultraemulsifier: ultraemulsifier is the cavity bubble that ultrasonic wave is imported into the intimate vacuum that produces disperse in the emulsion, and the cavity bubble quickens the migration of water, and the decentralization of emulsion is strengthened, and realizes ultra-fine emulsification.Ultra-fine emulsification can obtain stable emulsion.Ultraemulsifier is made up of supersonic source, transducer, supersonic source is to produce the sonic oscillation signal with rectangle, sine-wave generator, impulse generator, and transducer adopts the potsherd with piezo-electric effect or adopts the two-sided coated metal of thin slice of poly-inferior ethylene polymerization thing to make.After the oscillation signal that comes from supersonic source was added on the transducer, transducer produced ultrasonic wave, and hyperacoustic emulsion that penetrates produces cavitation phenomenon, makes the ultra-fine emulsification of emulsion.
The magnetic emulsifier unit: the magnetic emulsifier is by the effect of magnetic to emulsion, increases the stability of emulsion.The magnetizing assembly that this patent proposes adopts the magnetic field of strong magnet generation or with the magnetic field that magnetizing coil produces emulsifying agent is carried out polarity emulsification.
The emulsion holding vessel: the emulsion holding vessel is the device that the liquid with emulsification stores, and is provided with temperature indicator in jar, pressure display unit, vent valve, liquid level display and oil temperature adjustment heating tube.
Automatically circulating emulsion device is that emulsifying agent carries out repeatedly circulating emulsion device, and this device comprises the suction pipe that is arranged in the fluid reservoir, the manual control loop and the automatic control loop that link with the pump inlet end.
The advantage of this patent is: 1. the profit heating system is set on the emulsifier unit, makes viscous fuel oil reduce viscosity, strengthened flowability, increased diffusion velocity and the convection velocity of oil with water, make the emulsification of viscous oil become possibility.2. adapt to face width, the fuel oil of different viscosities is heated to different temperatures by heating system reaches the optimum emulsification state, less than the oil of 200 centistokes such as diesel oil, gasoline, can close heating system and carry out normal temperature emulsification for viscosity.3. adopted as jet emulsification, turbulent emulsification complex technique, strengthened emulsifying effectiveness.4. adopted ultrasonic emulsification technology and vibration emulsifying technology that emulsion is carried out ultra-fine emulsification.5. adopted the magnetic emulsifying technology to improve the stability of emulsion.6. adopt the circulating emulsion system, guarantee the emulsion dispersed uniform and carry out ultra-fine dispersion.
The viscous liquid circulating emulsion device that this patent proposes adopts the partial devices combination in the said apparatus to make or all install to make up and make.
The viscous liquid circulating emulsion device that this patent proposes i.e. the circulating emulsion of suitable viscous liquid, also the circulating emulsion of suitable non-viscous liq and the circulating emulsion that is added with the emulsifying agent fuel oil.
Below in conjunction with drawings and Examples a kind of combining structure of the present invention is discussed in detail.
Fig. 1 is a kind of combination assumption diagram of viscous fuel oil circulating emulsion device of the present invention;
Fig. 2 is Fig. 1 profit hybrid system structure chart;
Fig. 3 is the another kind of profit hybrid system of a Fig. 1 structure chart;
Fig. 4 is Fig. 1 jet emulsifier structure chart;
Fig. 5 is the moving turbulent emulsifier structure chart of Fig. 1;
Fig. 6 is the another kind of structure chart of the moving turbulent emulsifier of Fig. 1;
Fig. 7 is the structure chart of Fig. 1 ultraemulsifier;
Fig. 8 is the structure chart of Fig. 1 shocking type emulsifier;
Fig. 9 is Fig. 1 magnetic emulsifier unit structure chart.
Embodiment:
A kind of circulating emulsion device for viscous fuel oil as shown in Figure 1, wherein 1 is oil filter, its effect is the impurity in the clean oil.The 2nd, fuel reserve tank.The 3rd, the oil tubular electric heating.The 4th, oily temperature indicating meter.The 5th, the pressure indicating meter.The 6th, the spiral water-supply-pipe.The 7th, the water-supply-pipe flowmeter.The 8th, can regulate one-way throttle valve.The 9th, servo-actuated oil-water ratio distributing valve.The 10th, the profit hybrid system.The 11st, manual flow control valve.The 12nd, automatic circulating emulsion control valve.The 13rd, the piston oil guide pipe.The 14th, manual cycle emulsification control valve.The 15th, motor.The 16th, pump.The 17th, the jet emulsifier.The 18th, turbulent emulsifier.The 19th, ultraemulsifier or shocking type emulsifier.The 20th, the magnetic emulsifier.The 21st, oil storage tank.The 22nd, oily temperature indicating meter.The 23rd, the pressure indicating meter.The 24th, the circulating emulsion suction pipe.The 25th, vent valve.The 26th, temperature adjustment oil tubular electric heating.The 27th, liquid level display.The 28th, the oil export pipeline.The 29th, pipe insulation material.
The work engineering is as follows: viscous fuel oil filters out impurities by oil filter 1 and enters in the fuel reserve tank 2, with tubular electric heating 3 heating viscous oils, reduces oil viscosity through oil, indicates temperature and pressure by temperature indicating instrument 4 and pressure index instrument 5.Water in the spiral water-supply-pipe 6 heats through deep fat, indicates flow through flowmeter.Adjust the flow of profit mixed proportion with adjustable one-way throttle valve, through servo-actuated oil-water ratio distributing valve 9 oil, water are entered in the profit hybrid system 10, carry out the first mixing of profit, manually flow control valve 11 is controlled the flow and the flow velocity that mix back liquid.The pump 16 that drives with motor 15 pumps into first mixed liquid and carries out jet emulsification in the jet emulsifier 17, enter then in the turbulent emulsifier 18 and carry out turbulent emulsification, enter again and carry out ultrasonic ultra-fine emulsification or the ultra-fine emulsification of vibration in ultraemulsifier or the shocking type emulsifier 19.Liquid after the emulsification enters in the magnetic emulsifier 20, carries out the stable of magnetic emulsion.Liquid after the stable emulsion enters in the oil storage tank 21, because flow rate pump is generally 2 very soon, the 5-5 meter per second, short duct and local contraction place are the 5-7 meter per second, and the whole process of oily emulsification only is 2-3 second, therefore to obtain stable ultra-fine emulsion, must the design cycle emulsifying systems in the emulsifier unit.Circulating emulsion system in this patent is design like this, during design, what make pump pumps the flow of flow greater than oil export pipeline 28, during pump work, pressure in the oil storage tank 21 constantly raises, elevated pressure oil is delivered to the piston upper end of automatic circulation control valve 12 through pipeline by circulating emulsion suction pipe 24, piston is pressed down, piston is moved down, and the oil-water mixture outlet that piston will just mix ends, and opens the upper shed of automatic circulation control valve, form the loop with pump intake end pipeline, carry out circulating emulsion, along with continuously outflowing of oil storage tank oil emulsion, hypotension, just mix liquid by oil guide pipe 13 and the acting in conjunction of plug inner spring, with piston reset, carry out emulsification again to initial emulsion, the liquid of initial emulsion mixes pressurization again with the emulsion in the oil storage tank and repeats said process.The advantage of this circulatory system is an output emulsion pressure stability, and emulsion is emulsification repeatedly, emulsify well, and an available covering device uses for many cover burners.
Various structures in following this device of division
1, profit hybrid system
One of profit hybrid system structure is as shown in Figure 2: wherein 1 ' and be the oil-in pipe, 2 ' be oil storing tube, 3 ' be case lid, 4 ' be cover in the fuel reserve tank, in put and be furnished with aperture, 5 ' be interior cover water inlet pipe, 6 ' be (operating) water nozzle, 7 ' be mixture export, fuel reserve tank 2 during use ' in oil by interior cover 4 ' on aperture inject in the cover lumen in, come from water inlet pipe 5 ' in water by mixing with oil in the cover lumen in the jet blower 6 ' enter, under the gravity effect, use for pump along the mixed liquor flow export.
Profit hybrid system structure two as shown in Figure 3, wherein 8 ' be oil pipe, 9 ' be water pipe, water pipe 9 ' on be furnished with a plurality of current and portal, water pipe 9 ' in water portal by a plurality of current and mix with oil.
2, jet emulsifying systems
The jet emulsifying systems is made up of nozzle 1 " with jet emulsification chamber 2 " as shown in Figure 4, and the high-pressure emulsion of nozzle ejaculation is in jet emulsification chamber 2 " in mixing and emulsifying.
3, turbulent emulsifying systems:
Turbulent flow emulsifying systems such as Fig. 5, shown in Figure 6 introduce here be turbulent emulsifier unit.It is by ring flange 1 ' "; exocoel 2 ' ", emulsifying agent inlet porous chips 3 ' ", axle 4 ' ", helical blade 5 ' " or blade 6 ' ", emulsifying agent outlet porous chips 7 ' "; bearing 8 " formed, by inlet porous chips 3 ' " emulsion that comes act on the helical blade 5 that is welded on the axle ' " or blade 6 ' " on, axle is rotated; emulsion is stirred, and by outlet porous chips 7 ' " flow out.
4, ultraemulsifier
The ultraemulsifier structure chart as shown in Figure 7, wherein square frame 1 is supersonic source, supersonic source rectangle, sine-wave generator, impulse generator produces the sonic oscillation signal, square frame 2 is transducers, and transducer is with the potsherd with piezo-electric effect or adopt the polyvinylene polymer flake to make as the piezoelectric that (pvdf) thin slice two sides scribbles metal respectively.The sonic oscillation signal is added on the transducer.Transducer generation ultrasonic wave penetrates the emulsion in the emulsion tube 3, carries out ultrasonic emulsification.
5, shocking type emulsifier:
The shocking type emulsifier as shown in Figure 8, wherein 1 ° is the emulsifier housing, 2 ° is the vibration plate, 3 ° is central shaft, when emulsifying agent during from a side inflow, the vibration plate deflects along central shaft for 2 °, because down-off does not wait on the vibration plate, the less side emulsion flow velocity in slit is accelerated, enter in the less big cavity of pressure, and the emulsion of the bigger side in slit applies bigger pressure to 2 ° of vibration plates, force the upset of vibration plate, finish a vibration, repeat said process, make the emulsion that flows through constantly in pressurization, ultra-fine emulsification is carried out in decompression in the stirring, this shocking type emulsifier is by selecting different materials, and thickness and flow velocity can produce the ripple of different frequency.
6, magnetic emulsifying systems:
The magnetic emulsifying systems as shown in Figure 9, wherein 1 is magnetizing coil or strong magnetic force magnet, the 2nd, the emulsion pipe, the 3rd, overcoat, emulsion make emulsion produce polarization, stable emulsion through the effect of the magnetic field of magnetizing coil or strong magnetic force magnet.
Claims (7)
1, a kind of device of emulsifying liquid is by motor, pump, valve, instrument, blender, junction line, and filter, fluid reservoir, heater, emulsifier are formed, and it is characterized in that being equipped with on the emulsifier unit oil, water mixer, emulsifier, magnetizer.
2, device of emulsifying liquid as claimed in claim 1 is characterized in that also being equipped with on the emulsifier unit ultraemulsifier.
3, device of emulsifying liquid as claimed in claim 1 is characterized in that emulsifier unit is provided with the circulating emulsion system, and an end of circulating emulsion system and the liquid after the emulsification link, and the other end and pump intake front end assemblies link.
4, device of emulsifying liquid as claimed in claim 1 is characterized in that emulsifier unit is provided with heater, heat exchanger.
5, device of emulsifying liquid as claimed in claim 1 is characterized in that oil, water mixer are inserted by water-supply-pipe to make in the petroleum pipeline or by the oil-in, oil, water hybrid chamber, and water inlet, mixture export is formed.
6, device of emulsifying liquid as claimed in claim 1 is characterized in that magnetizer makes with strong magnet or magnetizing coil.
7, device of emulsifying liquid as claimed in claim 1 is characterized in that emulsifier is the jet emulsifier, spiral deflector turbulent flow emulsifier, sleeve pipe turbulent flow emulsifier, hydraulic barrier turbulent flow emulsifier, moving turbulent emulsifier, the one or more combination in the shocking type emulsifier is made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92113862 CN1088473A (en) | 1992-12-25 | 1992-12-25 | Circulating emulsion device for viscous fuel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92113862 CN1088473A (en) | 1992-12-25 | 1992-12-25 | Circulating emulsion device for viscous fuel oil |
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| Publication Number | Publication Date |
|---|---|
| CN1088473A true CN1088473A (en) | 1994-06-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92113862 Pending CN1088473A (en) | 1992-12-25 | 1992-12-25 | Circulating emulsion device for viscous fuel oil |
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| CN (1) | CN1088473A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2364067B (en) * | 2000-02-25 | 2004-07-14 | Jeong In Ryu | Ultrasonically operated liquid fuel modifying system |
| CN1293937C (en) * | 2002-10-16 | 2007-01-10 | 朴吉远 | Apparatus for producing water-in-oil emulsified fuel and supplying the same |
| CN1331580C (en) * | 2004-09-17 | 2007-08-15 | 天津大学 | Micro emulsifying method under magnetic field action |
| CN100531879C (en) * | 2005-03-08 | 2009-08-26 | 杭州电子科技大学 | Circulating multi-stage ultrasonic scattering method |
| CN102166493A (en) * | 2010-12-30 | 2011-08-31 | 海阳市圣士达涂装机械有限公司 | Automatic proportioning machine, automatic proportioning system of powder coating and proportioning method of powder coating |
| CN102371227A (en) * | 2011-10-19 | 2012-03-14 | 湖南天益高技术材料制造有限公司 | On-line emulsion coating equipment for wire rod rust prevention |
| CN109749793A (en) * | 2019-01-23 | 2019-05-14 | 上海众炅新能源科技有限公司 | A method of preparing pitch base fuel oil |
| WO2019161852A2 (en) | 2018-02-26 | 2019-08-29 | Kmitta Kurt | Method for operating an internal combustion engine, arrangement for carrying out said method and device for producing an emulsion |
| CN111122114A (en) * | 2020-01-08 | 2020-05-08 | 河海大学 | Automatic tracer feeding device for field tracer experiment in subsurface flow zone and implementation method of automatic tracer feeding device |
-
1992
- 1992-12-25 CN CN 92113862 patent/CN1088473A/en active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2364067B (en) * | 2000-02-25 | 2004-07-14 | Jeong In Ryu | Ultrasonically operated liquid fuel modifying system |
| CN1293937C (en) * | 2002-10-16 | 2007-01-10 | 朴吉远 | Apparatus for producing water-in-oil emulsified fuel and supplying the same |
| CN1331580C (en) * | 2004-09-17 | 2007-08-15 | 天津大学 | Micro emulsifying method under magnetic field action |
| CN100531879C (en) * | 2005-03-08 | 2009-08-26 | 杭州电子科技大学 | Circulating multi-stage ultrasonic scattering method |
| CN102166493A (en) * | 2010-12-30 | 2011-08-31 | 海阳市圣士达涂装机械有限公司 | Automatic proportioning machine, automatic proportioning system of powder coating and proportioning method of powder coating |
| CN102166493B (en) * | 2010-12-30 | 2014-04-02 | 海阳市圣士达涂装机械有限公司 | Automatic proportioning machine, automatic proportioning system of powder coating and proportioning method of powder coating |
| CN102371227A (en) * | 2011-10-19 | 2012-03-14 | 湖南天益高技术材料制造有限公司 | On-line emulsion coating equipment for wire rod rust prevention |
| WO2019161852A2 (en) | 2018-02-26 | 2019-08-29 | Kmitta Kurt | Method for operating an internal combustion engine, arrangement for carrying out said method and device for producing an emulsion |
| CN109749793A (en) * | 2019-01-23 | 2019-05-14 | 上海众炅新能源科技有限公司 | A method of preparing pitch base fuel oil |
| CN111122114A (en) * | 2020-01-08 | 2020-05-08 | 河海大学 | Automatic tracer feeding device for field tracer experiment in subsurface flow zone and implementation method of automatic tracer feeding device |
| CN111122114B (en) * | 2020-01-08 | 2022-02-11 | 河海大学 | Automatic tracer feeding device for field tracer experiment in subsurface flow zone and implementation method of automatic tracer feeding device |
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