CN202342918U - Ultrasonic atomization concentrator - Google Patents
Ultrasonic atomization concentrator Download PDFInfo
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- CN202342918U CN202342918U CN2011205312603U CN201120531260U CN202342918U CN 202342918 U CN202342918 U CN 202342918U CN 2011205312603 U CN2011205312603 U CN 2011205312603U CN 201120531260 U CN201120531260 U CN 201120531260U CN 202342918 U CN202342918 U CN 202342918U
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- ultrasonic
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- storage tank
- heater
- liquid tank
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Abstract
The utility model discloses an ultrasonic atomization concentrator which comprises a raw material liquid tank, a heater, an ultrasonic transducer and an ultrasonic spray head thereof, an evaporation separator, a secondary separation chamber, a condenser, a cooling pipe, a vacuum pump, a concentrated liquid tank and the like, wherein an outlet of the raw material liquid tank is connected to the heater; raw materials are heated by the heater and then atomized by the ultrasonic transducer and the ultrasonic spray head of the ultrasonic transducer which are positioned just above the evaporation separator; after the raw materials are subjected to the secondary separation of the evaporation separator and the secondary separation chamber, the concentrated liquid medicine is collected into the concentrated liquid tank positioned below the evaporation separator; and the separated solvent vapor is vacuumized and exported through the condenser and the cooling pipe to be recovered. The ultrasonic atomization concentrator combines ultrasonic atomization with single-effect or double-effect vacuum concentration process and rapidly completes evaporation separation under a high vacuum environment by using ultrasonic atomization to form small particles, thereby achieving a rapid concentration effect with energy conservation and high quality.
Description
Technical field
The utility model relates to a kind of atomizing enrichment facility, particularly a kind of ultrasonic atomizatio enrichment facility that is applicable to food, medicine trade.
Technical background
In food, drug production process, the method for concentration that is adopted mainly contains freeze concentration, steam heating, evaporation and concentration, film is concentrated, the resin adsorption separation concentrates etc. at present.Wherein freeze concentration operation is with the weak solution cooling, and that water congeals into ice is brilliant for the part in solution, and ice crystal is separated, thereby makes solution thicken; Evaporation and concentration is to utilize the method for heating that solution is heated to fluidized state, makes wherein volatile solvent partly vaporize and shift out, to improve the solute concentration in the solution and to isolate the process of solvent; The reverse osmosis concentration technology that film one of concentrates is to be the mass transfer driving force with pressure, through film material is separated concentrated membrane process; It is aperture and the polar character than bigger serface, different sizes of utilizing macromolecule to have that resin adsorption is separated concentrated, the process of some useful compound compositions in the selective absorption extract.
Adopt the still dominate of evaporation and concentration at present in the suitability for industrialized production, be accompanied by the appearance of various new technologies, new technology, on the basis of traditional evaporation and concentration, some improved methods also occurred.As spray-drying, ultrasonic heat refluxing extraction concentrate, economic benefits and social benefits, the continuous charging of single-action up-down symphysis concentrate, vacuum decompression concentrates or the like; But these methods are in actual production process; Also successive exposure has gone out some problems:, inconvenient operation higher like energy consumption, heat transfer efficiency is low, the rate of recovery is not high, production efficiency is difficult to improve etc.; To above-mentioned situation, the utility model provides a kind of simple in structure, working stability, energy consumption is low, efficient is high ultrasonic atomizatio enrichment facility.
Summary of the invention
The purpose of the utility model be to provide a kind of fast, evenly, low energy consumption, high efficiency ultrasonic atomizatio enrichment facility, this ultrasonic atomizatio enrichment facility not only kept material active ingredient, but also can be comprehensively material is concentrated rapidly and efficiently.
The utility model is to realize like this; It comprises material liquid storage tank, ultrasonic atomizer, vapor seperator, second-stage separator, condenser, condenser pipe, vavuum pump, concentrate storage tank; It is characterized in that: the material liquid storage tank connects ultrasonic atomizer; The top central authorities of vapor seperator are stretched in the ullrasonic spraying head sealing of ultrasonic atomizer; The top of said vapor seperator connects second-stage separator through conduit, and second-stage separator, condenser, condenser pipe and vavuum pump are connected successively, and the bottom of said second-stage separator is connected the concentrate storage tank respectively with the bottom of vapor seperator.
Be connected heater between said material liquid storage tank and the ultrasonic atomizer.
Said ultrasonic atomizer is explosion-proof integral structure.
Ultrasonic atomizer can according to circumstances be adjusted operating frequency, and under the 70kHz, the atomizing particle average diameter is 40 microns, is 30 microns during 85kHz.
The external high-vacuum pump of said condenser and cooling tube, vacuum can reach 0.098.
On this basis, can select single-action or economic benefits and social benefits to concentrate as required.
The ultrasonic power of the utility model transfers the electric energy of 50/60Hz to high-frequency electrical energy.This electric energy is sent to the piezo-electric crystal in the transducer, thereby is converted into mechanical oscillation.Ultrasonic vibration is through horn amplification and concentrate on the bar head, i.e. the atomizing mouth.Flow of liquid is crossed horn until the bar head.The bar head of concussion with liquid be ground into molecule and with its be injected into low speed, soft, fly mist uniformly.
The utlity model has following beneficial effect: that liquid is ground into short grained fog-spray nozzle is different with traditional dependence pressure and high-speed motion, and the ultrasonic atomization head is to utilize lower ultrasonic vibratory energy to carry out the atomization of liquid.Liquid can be sent to fog-spray nozzle and realize continuous or the discontinuity atomizing through self gravitation or low pressure liquid pump.Under the situation of overrun not, atomization of liquid amount is only by the conveying capacity of liquid and the operating frequency decision of fog-spray nozzle.Generally, fog-spray nozzle operating frequency high atomization disposal ability more is more low.The minimum atomization quantity of liquid can reach 2 μ l/s.Various coating, chemical reagent, lubricating oil, particle suspension liquid etc. all can be atomized.Best atomizing effect, liquid viscosity should be below 50cps, and solids content should be lower than 30%.Compare with the conventional pressure shower nozzle, the feeding passage of shower nozzle and spray orifice are all relatively big, do not have the spraying of obstruction thereby reach, and fog-spray nozzle can adopt the form of single head or bull according to the condition of production.Adopt ultrasonic atomizatio to concentrate; Can obtain desirable concentrated effect within a short period of time, can concentrate, can produce continuously adaptable across the quick of industry material liquids such as food, medicine; Amount is big, matter is high; Simple to operate, energy consumption is low, and is safe and reliable, easy to maintenance, is a kind of comparatively ideal Chinese medicine concentrator of novelty.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Material liquid storage tank 2, heater 3, ultrasonic atomizer 4, vapor seperator 5, second-stage separator 6, condenser 7, condenser pipe 8, vavuum pump 9, concentrate storage tank in the drawings, 1.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing the utility model is further specified.
As shown in Figure 1; The utility model is to realize like this; Material liquid storage tank (1) connects ultrasonic atomizer (3); The top central authorities of vapor seperator (4) are stretched in the ullrasonic spraying head sealing of ultrasonic atomizer (3), and the top of said vapor seperator (4) connects second-stage separator (5) through conduit, and second-stage separator (5), condenser (6), condenser pipe (7) and vavuum pump (8) are connected successively; The bottom of the bottom of said second-stage separator (5) and vapor seperator (4) is connected concentrate storage tank (9) respectively, is connected heater (2) between said material liquid storage tank (1) and the ultrasonic atomizer (3).During use, wherein material liquid storage tank (1) outlet is connected to heater (2), and material liquid is after the low-lift pump pressurization is through the heater heating; Entering is positioned at ultrasonic atomizer (3) atomizing directly over the vapor seperator (4); Its ultrasonic power transfers the electric energy of 50/60Hz to high-frequency electrical energy, and this electric energy is sent to the piezo-electric crystal in the transducer, thereby is converted into mechanical oscillation; Ultrasonic vibration is through horn amplification and concentrate on the bar head, i.e. the atomizing mouth.Flow of liquid is crossed horn until the bar head, the bar head of concussion with liquid be ground into molecule and with its be injected into low speed, soft, fly mist uniformly.Material liquid after the atomizing forms concentrated medicament after the secondary of vapor seperator (4) and second-stage separator (5) separates; Discharge below by vapor seperator (4) and second-stage separator (5); And be collected in the concentrate storage (9) that is arranged in vapor seperator below; And the solvent gas after separating also vacuumizes to derive through condenser (6), condenser pipe (7) through vavuum pump (8) and reclaims, because the condition of high vacuum degree of vavuum pump (8) can reach 0.098, therefore can under normal temperature even low temperature, accomplish fast and evaporate and separate.
Should be appreciated that specific embodiment described above only is used to explain the utility model, and be not used in qualification the utility model.By the spirit conspicuous variation of being extended out of the utility model or change and still be among the protection domain of the utility model.
Claims (3)
1. ultrasonic atomizatio enrichment facility; It comprises material liquid storage tank, ultrasonic atomizer, vapor seperator, second-stage separator, condenser, condenser pipe, vavuum pump, concentrate storage tank; It is characterized in that: the material liquid storage tank connects ultrasonic atomizer; The top central authorities of vapor seperator are stretched in the ullrasonic spraying head sealing of ultrasonic atomizer; The top of said vapor seperator connects second-stage separator through conduit, and second-stage separator, condenser, condenser pipe and vavuum pump are connected successively, and the bottom of said second-stage separator is connected the concentrate storage tank respectively with the bottom of vapor seperator.
2. ultrasonic atomizatio enrichment facility according to claim 1 is characterized in that: be connected heater between material liquid storage tank and the ultrasonic atomizer.
3. ultrasonic atomizatio enrichment facility according to claim 1 is characterized in that: said ultrasonic atomizer is explosion-proof integral structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205312603U CN202342918U (en) | 2011-12-19 | 2011-12-19 | Ultrasonic atomization concentrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205312603U CN202342918U (en) | 2011-12-19 | 2011-12-19 | Ultrasonic atomization concentrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202342918U true CN202342918U (en) | 2012-07-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205312603U Expired - Fee Related CN202342918U (en) | 2011-12-19 | 2011-12-19 | Ultrasonic atomization concentrator |
Country Status (1)
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| CN (1) | CN202342918U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103340402A (en) * | 2013-06-28 | 2013-10-09 | 中国中医科学院中医临床基础医学研究所 | Cream of peanuts, red dates and edible fungus, and preparation method and application of cream |
| CN108709369A (en) * | 2018-04-20 | 2018-10-26 | 大连工业大学 | A kind of ultrasonic atomization freeze drying plant |
| JP2020164350A (en) * | 2019-03-28 | 2020-10-08 | 株式会社フジミインコーポレーテッド | Method for producing silica sol |
| CN112678900A (en) * | 2020-11-03 | 2021-04-20 | 江西中竹生物质科技有限公司 | Waste liquid treatment system |
-
2011
- 2011-12-19 CN CN2011205312603U patent/CN202342918U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103340402A (en) * | 2013-06-28 | 2013-10-09 | 中国中医科学院中医临床基础医学研究所 | Cream of peanuts, red dates and edible fungus, and preparation method and application of cream |
| CN108709369A (en) * | 2018-04-20 | 2018-10-26 | 大连工业大学 | A kind of ultrasonic atomization freeze drying plant |
| JP2020164350A (en) * | 2019-03-28 | 2020-10-08 | 株式会社フジミインコーポレーテッド | Method for producing silica sol |
| JP7181142B2 (en) | 2019-03-28 | 2022-11-30 | 株式会社フジミインコーポレーテッド | Method for producing silica sol |
| CN112678900A (en) * | 2020-11-03 | 2021-04-20 | 江西中竹生物质科技有限公司 | Waste liquid treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120725 Termination date: 20121219 |