CN102886237B - Liquid whistle type ultrasonic emulsifier and method thereof for processing plant oil - Google Patents
Liquid whistle type ultrasonic emulsifier and method thereof for processing plant oil Download PDFInfo
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- CN102886237B CN102886237B CN201110400696.3A CN201110400696A CN102886237B CN 102886237 B CN102886237 B CN 102886237B CN 201110400696 A CN201110400696 A CN 201110400696A CN 102886237 B CN102886237 B CN 102886237B
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Abstract
The invention discloses a liquid whistle type ultrasonic emulsifier which comprises an inlet and an outlet, wherein the inlet and the outlet are arranged on a shell; a resonator and reeds arranged on the resonator are arranged inside the shell; the ultrasonic emulsifier is characterized in that the inlet and the outlet are respectively arranged at two ends of the shell; the resonator is arranged at the middle part of the shell and the reeds are respectively arranged at the two ends of the resonator. The method of the whistle type ultrasonic emulsifier for processing plant oil is characterized in that mixture liquid of the plant oil and aqueous alcohol is pumped into the whistle type ultrasonic emulsifier to be emulsified through a pressure pump. Disturbance frequency of the liquid whistle type ultrasonic emulsifier provided by the invention is increased to nearly 200000HZ from 10000-100000HZ, so that oil and water mixture liquid can be sufficiently emulsified, and moreover a structure is simple, stable and reliable. The plant oil processed by the ultrasonic emulsifier is used for a diesel engine, discharged CO (carbon monoxide) is reduced by 20%, SO2 (Sulfur Dioxide) is approximately 0, the NOx is reduced by 25%, and smoke intensity is reduced to the first grade from the second grade, so that not only environment pollution is greatly reduced, but also a process is simple, raw materials are easy to obtain and cheap, equipment cost is low, and production cost is greatly reduced.
Description
Technical field
The present invention relates to a kind of liquid whistle formula ultraemulsifier and the method for vegetable oil process thereof.
Background technology
At present, China's fossil fuel oil (diesel oil, gasoline, heavy oil etc.) is widely used in vehicle, steamer, engineering machinery, generating set and the field such as oil burning boiler, kiln.But ubiquity incomplete combustion, the shortcomings such as oil consumption is high, and the thermal efficiency is low, and pernicious gas and discharge of poisonous waste are high, to atmosphere pollution and environmental disruption day by day serious.Because ultrasonic fuel emulsifying technology can prepare tiny, even, stable oil emulsion, and energy consumption is little, and technology is gradually improved, so more and more receive attention and the concern of the mankind.Fuel emulsification device is one of key technology of emulsified fuel, and fuel emulsification device kind is tired many, and wherein the application of liquid whistle formula phaco device is more, and effect is better.
Existing liquid whistle formula ultraemulsifier comprises the entrance being arranged on shell one end and the outlet be arranged in housing sidewall, and be provided with core shooting in housing, resonate and be arranged on the reed in resonance, described resonance is fixed on the end face of housing.Oil, water mixed liquid send into core shooting through compression pump, and core shooting produces high-speed jet, jet impulse reed, ultrasonic wave is produced by oil-water mixture and reed, jet and reed ultrasonic wave resonate, and oil-water mixture carries out emulsification and reaches ceiling capacity, then send through outlet.Because this liquid whistle formula ultraemulsifier adopts single cantilever reed or fixed reed, forcing frequency is lower, and the oil-water mixture emulsification entering the liquid whistle is incomplete, and therefore, emulsion quality is not high.
Vegetable Fuel Gasoline is a kind of reproducible energy, and the mankind carry out studying rear discovery, the energy that the fossil energy that a kind of ratio can be found from plant extensively to adopt now is more effective and clean.Scientist asserts, after 10 to 20 years, whole society technical merit promoted a level again, and energy-source plant will become one of the highest material of degree of dependence in our life.Expert thinks, bioenergy will become the pith of following sustainable energy, by 2015; estimate that global total energy consumption will have 40% from bioenergy; thus the fossil fuel such as Substitute coal, oil and natural gas, protect energy resources, alleviates the pollution that energy-consuming causes to environment.
According to estimates, the energy that green plants is fixed every year, is equivalent to 60,000,000,000 tons to 80,000,000,000 tons oil, i.e. 20 times to 27 times of the annual oil total output in the whole world, 10 times that are about equivalent to that world's main fuel consumes.And the energy that green plants is fixed every year is as the utilization rate of the energy, be less than the 0.l% of its total amount now.
Vegetable oil directly substitutes as fuel oil the great attention that petrochemical industry oil has caused various countries.At present, what the utilization of vegetable oil adopted is the method changing oiliness, main to refine biodiesel, the country such as the U.S., Germany is the most ripe, and oneself makes all kinds of technology preparation that uses Inner combustion engine bio-fuel-oil to reach and calorific value detects, discharges environmental protection standard, oneself is very ripe for bio-fuel-oil product and manufacturing technology and technique, and oneself is actively promoted the use of by various countries; But will carry out touching of rule with oil plant pattern to produce, equipment and production capacity are subject to raw material category unitary system about, and manufacturing cost is higher than petrochemical industry fuel oil more than one, three times.Biodiesel uses due to key technology unresolved (namely not decomposing the distinctive Long carbon chain molecular structure of vegetable oil completely) on internal combustion engine, engine combustion is insufficient, be short of power, carbon residue is high, black smoke is large, and carbon on engine is many, therefore can only add biodiesel mixed combustion in petrifaction diesel of 20%, and complex process, production cost is high.
Summary of the invention
The liquid whistle formula ultraemulsifier that the object of the present invention is to provide a kind of forcing frequency high.
Second object of the present invention is the method providing a kind of above-mentioned liquid whistle formula ultraemulsifier for vegetable oil process.
The object of the present invention is achieved like this, a kind of liquid whistle formula ultraemulsifier, comprise the entrance and exit be arranged on housing, the reed being provided with resonance in housing and being arranged in described resonance, it is characterized in that: described entrance and exit is separately positioned on the two ends of housing, described resonance is arranged on the middle part of housing and the two ends of resonance are respectively equipped with reed.
Above-mentioned reed is the compound of cantilever reed and fixed reed.
In order to improve forcing frequency further, above-mentioned resonance is two rows.
Simple in order to fastening structure, and be beneficial between two rows' resonance and form fluid passage, the both sides between above-mentioned two row's resonance are provided with press strip, centre is fluid passage.
In order to structure is reliable, above-mentioned resonance and reed integrated and be fixedly mounted on housing by gland.
In order to ensure the reliability and stability of relative position, the core shooting in the formula ultraemulsifier of the above-mentioned liquid whistle is by key or finger setting.
Second object of the present invention is achieved in that above-mentioned whistle formula ultraemulsifier is for the method for vegetable oil process, is characterized in that: vegetable oil and aqueous alcohol mixed liquor pumped in the formula ultraemulsifier of the described whistle through compression pump and carry out emulsification.
In above-mentioned vegetable oil and aqueous alcohol mixed liquor, aqueous alcoholic content is 30%-40%.
Water content in above-mentioned aqueous alcohol is 20%-30%.
Through mixing before above-mentioned vegetable oil and aqueous alcohol mixed liquor pump into above-mentioned whistle formula ultraemulsifier, described mixing comprises agitator and blender, the paddle of described agitator is axially to flow, and be aided with the radial flow of 30%, described agitator tank body is provided with radial spoiler.
Filter and ratio regulation and control respectively through coarse filtration, essence successively before above-mentioned vegetable oil and aqueous alcohol mixing.
Above-mentioned coarse filtration filter device therefor is 200 orders.
It is 300 orders that above-mentioned essence filters filter device therefor.
Aforementioned proportion regulation and control are carried out at ratio regulator control system, and described ratio regulator control system comprises constant displacement pump and regulated variable pump.
The present invention has following beneficial effect:
1, the present invention adopts combined type reed and is arranged in the middle of housing, by entrance and exit
Be arranged on the two ends of housing, forcing frequency brings up to nearly 200000HZ from existing 10000HZ-100000HZ, has increased substantially forcing frequency, and assembles in tail end energy produce power, oil-water mixture is obtained fully emulsified, improves emulsion quality.The whistle of the present invention formula ultraemulsifier uses on the engine, add water 15% oil emulsion suitable at power, under the condition that moment of torsion is identical, oil consumption on average reduces 0.006kg/kw/h than pure diesel oil oil consumption, rate of economizing gasoline, at 8-15%, has significant effects of energy saving and emission reduction and huge economic benefit.
2, vegetable oil processing method of the present invention, carries out chain rupture pulverizing by former many carbon (C18-22) Long carbon chain molecular structure, and produces microfabricated chemical reactor with alcohol and hydrone, synthesizes hydrocarbon mixing Water-In-Oil (W/O) structure, makes it close with petrochemical industry fuel quality.Vegetable oil and petrochemical industry oil power through process of the present invention is suitable, need not any additive, and machine oil doubles above service time, and carbon on engine is less, significantly extends service life of aeroengine.
3, in the present invention's vegetable oil used and aqueous alcohol mixed liquor, aqueous alcoholic content is 30%-40%, and the water content in aqueous alcohol is 20%-30%.Considerably reduce cost of material.Further, only need dewater to waste oil, after de-slag, adopt the whistle of the present invention formula ultraemulsifier to carry out emulsification; just can be used for combustion diesel engine, boiler, the burning of Zhu stove; the discarded energy can be made full use of, not only cost-saving, and be conducive to environmental protection.
4, the vegetable oil after the formula ultraemulsifier process of the whistle of the present invention is used for Diesel engine, and the CO of discharge reduces by 20%, SO2 and is tending towards 0, NOx minimizing 25%, and smoke intensity reduces to one-level by secondary, drastically reduce the area environmental pollution.
5, the whistle of the present invention formula ultraemulsifier structure is simple, stable, reliable; The method technique that the whistle of the present invention formula ultraemulsifier is used for vegetable oil process is simple, and raw material is easy to get, cheap, and equipment cost is low, considerably reduces production cost.
Accompanying drawing explanation
Fig. 1 is embodiment of the present invention structural representation;
Fig. 2 is Fig. 1 partial schematic diagram;
Fig. 3 is Fig. 1 top view.
Detailed description of the invention
Embodiment 1, see accompanying drawing, a kind of liquid whistle formula ultraemulsifier, comprise the entrance 1 be arranged on housing, osculum 2, outlet 7, the reed 4 being provided with core shooting 3, resonance 5 in housing and being arranged in resonance 5, entrance 1 and outlet 7 are separately positioned on the two ends of housing, core shooting 3 is by key or finger setting, resonance 5 is two rows and is arranged on the middle part of housing, between resonance 5 and upper-lower casing and two resonate between 5 and forms three fluid passages 8 altogether, resonate 5 and reed 4 be integrated and be fixedly mounted on by gland 6 in the groove on housing.
The present embodiment liquid whistle formula ultraemulsifier is used for the method for vegetable oil process, and its technique comprises: coarse filtration, essence are filtered, vegetable oil and the regulation and control of hydrous ethanol ratio, mixing, emulsification, Oil-gas Separation, water-oil separating.Coarse filtration filter device therefor is 200 orders, is arranged on the pump front end of induction system, point vegetable oil and absolute alcohol two paths; It is 300 orders that essence filters filter device therefor, and point vegetable oil and absolute alcohol two paths, filter all impurity; Ratio regulation and control are by constant displacement pump and regulated variable pump is supporting forms, and constant displacement pump is to vegetable oil, and regulated variable pump is to aqueous alcohol, and in vegetable oil and aqueous alcohol mixed liquor, aqueous alcoholic content is 30%, in aqueous alcohol water content be 20%.Vegetable oil and aqueous alcohol are mixed after ratio regulates and controls, hybrid system comprises agitator and blender, and the paddle of agitator is axially to flow, and be aided with the radial flow of 30%, agitator tank body is provided with radial spoiler; After mixing, vegetable oil and aqueous alcohol mixed liquor are pumped into whistle formula ultraemulsifier through compression pump to carry out being emulsified into oil emulsion, be separated through gs-oil separator to the gas in oil emulsion, the oil emulsion after divided gas flow just can use by direct-furnish fuel oil equipment.
Embodiment 2, see accompanying drawing, a kind of liquid whistle formula ultraemulsifier, comprise the entrance 1 be arranged on housing, osculum 2, outlet 7, core shooting 3 is provided with in housing, resonance 5 and the reed 4 be arranged in resonance 5, entrance 1 and outlet 7 are separately positioned on the two ends of housing, core shooting 3 is by key or finger setting, resonance 5 is two rows and is arranged on the middle part of housing, press strip 9 is provided with between two row's resonance 5, middle formation fluid passage 8, between resonance 5 and upper-lower casing and two resonate between 5 and form three fluid passages 8 altogether, resonance 5 and reed 4 are integrated and are fixedly mounted on by gland 6 in the groove on housing.
The present embodiment liquid whistle formula ultraemulsifier is used for the method for vegetable oil process, and see embodiment 1, wherein, in vegetable oil and aqueous alcohol mixed liquor, aqueous alcoholic content is 40%, in aqueous alcohol water content be 30%.
Embodiment 3, see accompanying drawing, a kind of liquid whistle formula ultraemulsifier, a kind of liquid whistle formula ultraemulsifier, comprise the entrance 1 be arranged on housing, osculum 2, outlet 7, core shooting 3 is provided with in housing, resonance 5 and the reed 4 be arranged in resonance 5, entrance 1 and outlet 7 are separately positioned on the two ends of housing, core shooting 3 is by key or finger setting, resonance 5 is two rows and is arranged on the middle part of housing, press strip 9 is provided with between two row's resonance 5, middle formation fluid passage 8, between resonance 5 and upper-lower casing and two resonate between 5 and form three fluid passages 8 altogether, the two ends of each resonance 5 are respectively equipped with the compound reed comprising cantilever reed and fixed reed, resonance 5 and reed 4 are integrated and are fixedly mounted on by gland 6 in the groove on housing.
The present embodiment liquid whistle formula ultraemulsifier is used for the method for vegetable oil process, and see embodiment 1, wherein, in vegetable oil and aqueous alcohol mixed liquor, aqueous alcoholic content is 35%, in aqueous alcohol water content be 25%.
Claims (9)
1. a liquid whistle formula ultraemulsifier, comprise the entrance (1) be arranged on housing, outlet (7), be provided with resonance (5) in housing and be arranged on the reed (4) in described resonance (5), it is characterized in that: described entrance (1) and outlet (7) are separately positioned on the two ends of housing, described resonance (5) is arranged on the middle part of housing and the two ends of resonance (5) are respectively equipped with reed; Described resonance (5) is for two rows and the both sides that described two rows resonate between (5) are provided with press strip (9), and centre is fluid passage (8).
2. the liquid whistle as claimed in claim 1 formula ultraemulsifier, is characterized in that: the compound that described reed (4) is cantilever reed and fixed reed.
3. the liquid whistle as claimed in claim 2 formula ultraemulsifier, is characterized in that: described resonance (5) and reed (4) integrated and pass through gland (6) and be fixed on housing.
4. the whistle formula ultraemulsifier as described in any one of claim 1-3 is used for the method for vegetable oil process, it is characterized in that: vegetable oil and aqueous alcohol mixed liquor are pumped into described whistle formula ultraemulsifier through compression pump and carries out emulsification.
5. the whistle as claimed in claim 4 formula ultraemulsifier is used for the method for vegetable oil process, it is characterized in that: in described vegetable oil and aqueous alcohol mixed liquor, aqueous alcoholic content is 30%-40%.
6. the whistle as claimed in claim 5 formula ultraemulsifier is used for the method for vegetable oil process, it is characterized in that: the water content in described aqueous alcohol is 20%-30%.
7. the whistle as claimed in claim 6 formula ultraemulsifier is used for the method for vegetable oil process, it is characterized in that: through mixing before described vegetable oil and aqueous alcohol mixed liquor pump into above-mentioned whistle formula ultraemulsifier, described mixing comprises agitator and blender, the paddle of described agitator is axially to flow, be aided with the radial flow of 30%, described agitator tank body is provided with radial spoiler.
8. the whistle as claimed in claim 7 formula ultraemulsifier is used for the method for vegetable oil process, it is characterized in that: filter and ratio regulation and control respectively through coarse filtration, essence successively before described vegetable oil and aqueous alcohol mixing.
9. the whistle as claimed in claim 8 formula ultraemulsifier is used for the method for vegetable oil process, it is characterized in that: described coarse filtration filter device therefor is 200 orders; It is 300 orders that described essence filters filter device therefor; Described ratio regulation and control comprise constant displacement pump and regulated variable pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110400696.3A CN102886237B (en) | 2011-12-06 | 2011-12-06 | Liquid whistle type ultrasonic emulsifier and method thereof for processing plant oil |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110400696.3A CN102886237B (en) | 2011-12-06 | 2011-12-06 | Liquid whistle type ultrasonic emulsifier and method thereof for processing plant oil |
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| Publication Number | Publication Date |
|---|---|
| CN102886237A CN102886237A (en) | 2013-01-23 |
| CN102886237B true CN102886237B (en) | 2015-03-11 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201110400696.3A Expired - Fee Related CN102886237B (en) | 2011-12-06 | 2011-12-06 | Liquid whistle type ultrasonic emulsifier and method thereof for processing plant oil |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5987026A (en) * | 1982-11-09 | 1984-05-19 | Nishi Nippon Flex Kk | Ultrasonic continuous mixing apparatus |
| CN2054491U (en) * | 1989-01-21 | 1990-03-14 | 沈智 | Emulsification oil-saving unit |
| CN2242727Y (en) * | 1995-12-15 | 1996-12-18 | 中国科学院声学研究所 | Supersonic mixing emulsifying device |
| CN2256882Y (en) * | 1996-07-05 | 1997-06-25 | 佟燕 | Machine for emulsifying light diesel oil |
| CN2770770Y (en) * | 2005-03-17 | 2006-04-12 | 何立 | Spiral-flow type ultrasonic fuel on-line emulsifier |
| WO2009100317A2 (en) * | 2008-02-08 | 2009-08-13 | Eilaz Babaev | Echoing ultrasound atomization and mixing system |
| CN202343186U (en) * | 2011-12-06 | 2012-07-25 | 成都市恒茂能源科技有限公司 | Liquid-whistle-type ultrasonic emulsifier |
-
2011
- 2011-12-06 CN CN201110400696.3A patent/CN102886237B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5987026A (en) * | 1982-11-09 | 1984-05-19 | Nishi Nippon Flex Kk | Ultrasonic continuous mixing apparatus |
| CN2054491U (en) * | 1989-01-21 | 1990-03-14 | 沈智 | Emulsification oil-saving unit |
| CN2242727Y (en) * | 1995-12-15 | 1996-12-18 | 中国科学院声学研究所 | Supersonic mixing emulsifying device |
| CN2256882Y (en) * | 1996-07-05 | 1997-06-25 | 佟燕 | Machine for emulsifying light diesel oil |
| CN2770770Y (en) * | 2005-03-17 | 2006-04-12 | 何立 | Spiral-flow type ultrasonic fuel on-line emulsifier |
| WO2009100317A2 (en) * | 2008-02-08 | 2009-08-13 | Eilaz Babaev | Echoing ultrasound atomization and mixing system |
| CN202343186U (en) * | 2011-12-06 | 2012-07-25 | 成都市恒茂能源科技有限公司 | Liquid-whistle-type ultrasonic emulsifier |
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| CN102886237A (en) | 2013-01-23 |
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