CN206746528U - Ozone vegetable oil emulsifier unit and streamline - Google Patents
Ozone vegetable oil emulsifier unit and streamline Download PDFInfo
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- CN206746528U CN206746528U CN201720372016.4U CN201720372016U CN206746528U CN 206746528 U CN206746528 U CN 206746528U CN 201720372016 U CN201720372016 U CN 201720372016U CN 206746528 U CN206746528 U CN 206746528U
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- emulsion chamber
- emulsion
- vegetable oil
- ozone
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Abstract
The utility model provides ozone vegetable oil emulsifier unit and streamline, is related to the technical field of bactericide production technology, including emulsion chamber and vaporization chamber；Emulsion chamber is connected with vaporization chamber by communicating pipe；The emulsification rod for emulsification is provided with the emulsion chamber；In the emulsion chamber also at least provided with an air inlet pipe, and the air inlet pipe lower end is provided with solarization air cap, and the solarization air cap is located at the bottom of the cavity of the emulsion chamber；Emulsion chamber top is provided with blast pipe.Emulsion chamber's indoor ozone of the present utility model is reacted with vegetable oil, then moisture is added to it by vaporization chamber, and final production goes out ozone emulsification bactericide；Production efficiency is improved compared to existing equipment, shortens the production time of product, is supplied water by steam chamber to emulsion chamber, adds the temperature of water, do not had to so heat in emulsion chamber, be easily controlled the reaction temperature of emulsion chamber；And by steam to emulsion chamber Jia Shui, the speed of addition is slow, realizes the requirement that emulsion chamber slowly emulsifies.
Description
Technical field
Bactericide production technical field is the utility model is related to, more particularly, to a kind of ozone vegetable oil emulsifier unit and stream
Waterline.
Background technology
Ozone destroys the structure of microbial film with the oxidation of oxygen atom, to realize bactericidal action.Ozone is to bacterium
Inactivation reaction is always carried out rapidly, unlike other bactericide：Ozone can be anti-with the double bond of bacteria cell wall lipid
Should, penetrate inside thalline, act on albumen and lipopolysaccharides, change the permeability of cell, so as to cause bacterial death.
Ozone also acts on intracellular nuclear matter, as the purine in nucleic acid and pyrimidine destroy DNA.Ozone acts on first
Cell membrane, film composition is damaged, and causes dysbolism, ozone continues infiltration and penetrates film, and destroys film lactones
Albumen and lipopolysaccharides, change the permeability of cell, cause cell dissolving, death.
Ozone is a kind of strong oxidizer, and sterilization process category biochemical oxidation reacts.Ozone sterilization has following 3 kinds of forms：
1. the enzyme inside ozone energy oxidation Decomposition bacterium needed for degraded glucose, TCA circulations are caused not carry out, so as to lead
Cause the ATP needed for cell activities to be unable to supply, make bacteria inactivation dead.
2. directly destroy their organelle and DNA, RNA with bacterium, virus function, make the metabolism of bacterium by
Destroy, cause bacterial death.
3. passing through cell membrane tissue, intrusion is intracellular, acts on the lipoprotein of outer membrane and internal lipopolysaccharides, sends out bacterium
Give birth to penetrating sex distortion and dissolve death.
Ozone is inconvenient to use, and is typically now made ozone oil with ozone, but ozone oil is oily, easy pollution clothes,
And transport is inconvenient.
Utility model content
The purpose of this utility model is to provide ozone vegetable oil emulsifier unit and streamline, to solve in production ozone breast
Existing equipment can not meet that production requirement, existing equipment production time length are not suitable for producing ozone breast when changing bactericide
Change the technical problem of bactericide.
A kind of ozone vegetable oil emulsifier unit provided by the utility model, including emulsion chamber and vaporization chamber；The emulsion chamber
Connected with the vaporization chamber by communicating pipe；
The emulsification rod for emulsification is provided with the emulsion chamber；
In the emulsion chamber also at least provided with an air inlet pipe, and the air inlet pipe lower end is provided with solarization air cap, described
Solarization air cap is located at the bottom of the cavity of the emulsion chamber；The emulsion chamber top is provided with blast pipe；
The vaporization chamber upper end is provided with the inlet opening for water inlet, and lower end is provided with the apopore for water outlet, and
Secondary heating mechanism is provided with the vaporization chamber.
Further, the emulsion chamber upper end is provided with the charging hole for charging, is provided with the emulsion chamber lower end
Discharge opening for discharging.
Further, in addition to first heater, and the first heater is located at the cavity of the emulsion chamber
Bottom, the first heater are heater, and the heater is heating coil.
Further, the secondary heating mechanism is heater, and the heater is heating coil.
Further, chuck is provided with the emulsion chamber, and connected with chuck is provided with the emulsion chamber
One connecting tube and the second connecting tube.
Further, the vaporization chamber is made of high borosilicate heat-proof glass, and is provided with and is used on the vaporization chamber
The graduation mark of metering liquid volume.
Further, it is provided with apparatus for measuring temperature in the emulsion chamber and the vaporization chamber.
Further, the communicating pipe and the emulsion chamber junction with the vaporization chamber less than being connected the communicating pipe
Place.
Further, the emulsion chamber is made of stainless steel material.
The utility model also provides a kind of streamline, including ozone vegetable oil emulsifier unit described above.
The utility model provides ozone vegetable oil emulsifier unit and streamline, and ozone and vegetable oil can be made in emulsion chamber
Reacted, then moisture is added to it by vaporization chamber, final production goes out ozone emulsification bactericide；Improved compared to existing equipment
Production efficiency, shortens the production time of product, is supplied water by steam chamber to emulsion chamber, adds the temperature of water, so
Without being heated in emulsion chamber, the reaction temperature of emulsion chamber is easily controlled；And by steam to emulsion chamber Jia Shui, the speed of addition
Slowly, the requirement that emulsion chamber slowly emulsifies is realized.
Brief description of the drawings
, below will be right in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
The required accompanying drawing used is briefly described in embodiment or description of the prior art, it should be apparent that, describe below
In accompanying drawing be some embodiments of the present utility model, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the front view for the ozone vegetable oil emulsifier unit that the utility model embodiment provides；
Fig. 2 is the stereogram of ozone vegetable oil emulsifier unit shown in Fig. 1；
Fig. 3 is the internal structure schematic diagram of ozone vegetable oil emulsifier unit shown in Fig. 1；
Fig. 4 is another structural representation of the emulsion chamber of ozone vegetable oil emulsifier unit shown in Fig. 1.
Icon：100- emulsion chambers；200- vaporization chambers；300- communicating pipes；400- charging holes；500- blast pipes；
600- air inlet pipe；700- inlet openings；800- apopores；900- discharge openings；110- emulsifies rod；The heating dresses of 120- first
Put；130- secondary heating mechanisms；140- chucks；The connecting tubes of 150- first；The connecting tubes of 160- second.
Embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with accompanying drawing, it is clear that described
Embodiment is the utility model part of the embodiment, rather than whole embodiments.Based on the embodiment in the utility model, sheet
The every other embodiment that field those of ordinary skill is obtained under the premise of creative work is not made, belongs to this practicality
Novel protected scope.
, it is necessary to explanation in description of the present utility model, term " " center ", " on ", " under ", it is "left", "right", " perpendicular
Directly ", the orientation of the instruction such as " level ", " interior ", " outer " or position relationship are based on orientation shown in the drawings or position relationship, are only
Described for the ease of description the utility model and simplifying, rather than instruction or imply signified device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.In addition, term " the
One ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term " are pacified in description of the present utility model
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integratedly
Connection；Can be mechanical connection or electrical connection；Can be joined directly together, can also be indirectly connected by intermediary,
It can be the connection of two element internals.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
Concrete meaning of the language in the utility model.
As shown in Figure 1, Figure 2 and Figure 3, a kind of ozone vegetable oil emulsifier unit provided by the utility model, including emulsion chamber
100 and vaporization chamber 200；The emulsion chamber 100 is connected with the vaporization chamber 200 by communicating pipe 300；
The emulsification rod 110 for emulsification is provided with the emulsion chamber 100；
In the emulsion chamber 100 also at least provided with an air inlet pipe 600, and the lower end of the air inlet pipe 600 is provided with exposure
Stomata, the solarization air cap are located at the bottom of the cavity of the emulsion chamber 100；The top of emulsion chamber 100 is provided with blast pipe
500；
The upper end of vaporization chamber 200 is provided with the inlet opening 700 for water inlet, and lower end is provided with the apopore for water outlet
800, and it is provided with secondary heating mechanism 130 in the vaporization chamber 200.
In the present embodiment, there is communicating pipe 300 between emulsion chamber 100 and vaporization chamber 200, the second heating dress in evaporator
Put 130 water is heated after, vapor enters emulsion chamber 100 from communicating pipe 300.
There are multiple air inlet pipe 600 in emulsion chamber 100, air inlet pipe 600 connects the ozone machine of source of oxygen, multiple air inlet pipe
600 provide ozone by ozone machine simultaneously, and the lower end of air inlet pipe 600 is located at the cavity part on the lower side of emulsion chamber 100, so when to breast
When changing the addition vegetable oil of room 100, solarization air cap is in vegetable oil.
Inlet opening 700 on vaporization chamber 200 is used to add water from inlet opening 700, and apopore 800 is arranged on vaporization chamber
200 lower ends, when needing to change water in vaporization chamber 200, flowed out by apopore 800, in inlet opening 700 and apopore
Valve is provided with 800, for controlling the switch of apopore 800 and inlet opening 700.
The emulsification rod 110 set in emulsion chamber 100, general to use ultrasonic emulsification rod 110, ultrasonic emulsification rod 110 is in fact
Existing ultrasonic emulsification.
Ultrasonic emulsification refers in the case where ultrasonic energy acts on, and two kinds of (or two or more) immiscible liquids is well mixed shape
Into dispersion system, one of which liquid is evenly distributed among another liquid and forms the technical process of emulsion.
On above-described embodiment basis, further, the upper end of emulsion chamber 100 is provided with the charging hole for charging
400, the lower end of emulsion chamber 100 is provided with the discharge opening 900 for discharging.
In the present embodiment, have in emulsion chamber 100 for the materials such as vegetable oil, emulsifying agent to be entered into emulsion chamber 100
Charging hole 400, when emulsification complete after, product need from emulsion chamber 100 it is made when, there is discharging the lower end of emulsion chamber 100
Hole 900.
Charging hole 400 and discharge opening 900 are provided with can be set with the plugging device for preventing that material from coming out, charging hole 400
Lid is put, prevents ozone from largely being gone out from charging hole 400, foreign matter is also prevented from and is fallen into from charging hole 400, set in discharge opening 900
Valve, for it is suitable when, control discharge opening 900 switch.
In order to which ozone and vegetable oil preferably react, on above-described embodiment basis, further, in addition to first adds
Thermal 120, and the first heater 120 is located at the bottom of the cavity of the emulsion chamber 100, the first heater
120 be heater, and the heater is heating coil.
Because the environment residing for emulsion chamber 100 is change, when environment temperature is relatively low, ozone is with vegetable oil in breast
Change and be reacted into room 100 slowly, vegetable oil is heated by first heater 120, can so improve reaction speed
Degree.
Heating coil is set in the cavity lower end of emulsion chamber 100, and such in general reaction, vegetable oil can cover heating dish
Pipe, heating coil directly heat to vegetable oil, and heating is more rapidly.
In order to preferably make the water in vaporization chamber 200 heat up, on above-described embodiment basis, further, described
Two heaters 130 are heater, and the heater is heating coil.
There is heating coil in vaporization chamber 200, heating coil heats to water, and such water evaporation could pass through into steam
Communicating pipe 300 is entered in emulsion chamber 100.
The steam of high temperature, which enters in emulsion chamber 100, condenses into condensed water, and condensate temperature is higher, can so keep planting
Thing oil has higher temperature, it is not necessary to emulsion chamber 100 heated, and the water that steam enters in emulsion chamber 100 from vaporization chamber 200
Measure smaller, can so realize slow emulsification.
As shown in figure 4, in order to adapt to larger range of production, on above-described embodiment basis, further, the breast
Change and be provided with chuck 140 on room 100, and the first connecting tube 150 connected with chuck 140 is provided with the emulsion chamber 100
With the second connecting tube 160.
There is a chuck 140 emulsion chamber 100, and the first connecting tube 150 and the second connecting tube 160 connect into pipe network respectively, when
When needing heating, the first connecting tube 150 enters the high medium of temperature, such as steam, and steam enters after chuck 140, right
Emulsion chamber 100 is heated, and when temperature is too high in emulsion chamber 100, can switch pipe network, the first connecting tube 150 connects
To tap water pipe network, flowed by running water in chuck 140, make the reduction of its temperature, can so avoided warm in emulsion chamber 100
Spend the problem of high.
It is further, described on above-described embodiment basis in order to facilitate the height of liquid level in observation vaporization chamber 200
Vaporization chamber 200 is made of high borosilicate heat-proof glass, and the quarter for metering liquid volume is provided with the vaporization chamber 200
Spend line.
The high borosilicate heat-proof glass that vaporization chamber 200 uses is made, and can observe the height of the water in vaporization chamber 200 outside
Degree, has graduation mark on vaporization chamber 200, can read the volume of the water in vaporization chamber 200, pass through the lasting evaporation of water, water
Liquid level gradually reduce, the volume into the reclaimed water of emulsion chamber 100 is so calculated by liquid level difference.
In order to accurately measure, the temperature in emulsion chamber 100 and vaporization chamber 200, on above-described embodiment basis, enter one
Step, it is provided with apparatus for measuring temperature in the emulsion chamber 100 and the vaporization chamber 200.
The device of thermometric temperature can be thermometer, and thermometer lower end is inserted under emulsion chamber 100 and vaporization chamber 200
Portion, thermometer upper end is exposed outside emulsion chamber 100 and vaporization chamber 200, by external vision emulsion chamber 100 and vaporization chamber 200
Temperature.
The device of measurement temperature can also be temperature sensor, and temperature sensor is arranged on emulsion chamber 100 and vaporization chamber
In 200, the temperature measuring set of outside is connected, the temperature inside instrumental observation emulsion chamber 100 and vaporization chamber 200 can be passed through in real time
Degree.
Entered in order to facilitate current in emulsion chamber 100, on above-described embodiment basis, further, the connection
Pipe 300 is with the junction of emulsion chamber 100 less than the communicating pipe 300 and the junction of vaporization chamber 200.
In the present embodiment, steam enters phenomena such as condensation occurs after communicating pipe 300, and condensed water is along communicating pipe
300 are flowed into emulsion chamber 100, and the high other end in such one end of communicating pipe 300 is low, facilitates the inflow of condensed water.
On above-described embodiment basis, on further, the emulsion chamber 100 is made of stainless steel material.
The utility model also provides a kind of streamline, including ozone vegetable oil emulsifier unit described above.
In the present embodiment, streamline includes above-mentioned ozone vegetable oil emulsifier unit, is disguised by ozone trials of emulsion of plant oil
Put to produce ozone emulsification bactericide.
Ozone emulsification bactericide is used for sterilization, the skin care of skin, and nano particle, excitant is small, absorbs soon, has good
Sterilization and skin effect.Clothes is not polluted, it is easy to carry, it is widely used in skin of face, the sterilization of mucous membrane, nursing.
Air inlet pipe 600 provides ozone, and the source of ozone can be ozone gas cylinder or ozone machine；By vegetable oil and emulsifying agent
It is added in emulsion chamber 100 and is reacted, then steam heating indoor, substantial amounts of steam enters emulsion chamber from communicating pipe 300
Continue to react in 100, last ozone emulsification bactericide production is completed.
Ozone vegetable oil emulsifier unit can be adapted to the method production ozone emulsification bactericide, this kind of suitable ozone plant
The method of the ozone emulsification bactericide production of oily emulsifier unit.
Vegetable oil is added in emulsion chamber 100 by charging hole 400, then adds 20% breast that volume is vegetable oil volume
Agent, ozone is passed through to air inlet pipe 600 by ozone machine, ozone is entered to go in emulsion chamber 100 by solarization air cap, exothermic reaction 6
Hour, pure water is added into vaporization chamber 200, is heated by secondary heating mechanism 130, water is become vapor, passed through
Communicating pipe 300 is entered in emulsion chamber 100, when the water volume in vaporization chamber 200 reduces the 30% of vegetable oil volume, is stopped
Only vapor is added to emulsion chamber 100；When 200 casees emulsion chambers of vaporization chamber 100 add steam, ultrasonic emulsification is opened
Rod 110, carries out ultrasonic emulsification, ultrasonic emulsification obtains bactericide after 2 hours.
When ozone is aerated, the temperature in emulsion chamber 100 needs to control for 60 DEG C -75 DEG C；When temperature mistake
When high, ozone can be passed through to control temperature by the intake or stopping for controlling ozone, when ambient temperature compared with
The good inactivation of low heat emission effect, heated up by first heater 120 to emulsion chamber 100, ensure that it reacts in preference temperature.
Vegetable oil can use olive oil, safflower oil and soybean oil etc., and emulsifying agent can select oleic acid, the oil of anhydrous sorbitol three
Acid esters, glycol fatty acid ester etc..
Ozone emulsification bactericide is used for sterilization, the skin care of skin, and nano particle, excitant is small, absorbs soon, has good
Sterilization and skin effect.Clothes is not polluted, it is easy to carry, it is widely used in skin of face, the sterilization of mucous membrane, nursing.
The utility model provides ozone vegetable oil emulsifier unit and streamline, and ozone can be made in emulsion chamber 100 with planting
Thing oil is reacted, then moisture is added to it by vaporization chamber 200, and final production goes out ozone emulsification bactericide；Compared to existing
Equipment improves production efficiency, shortens the production time of product, is supplied water by steam chamber to emulsion chamber 100, adds water
Temperature, do not have to so heat in the emulsion chamber 100, be easily controlled the reaction temperature of emulsion chamber 100；And by steam to emulsification
Room 100 plus water, the speed of addition is slow, realizes the requirement that emulsion chamber 100 slowly emulsifies.
Finally it should be noted that：Various embodiments above is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the utility model is described in detail with reference to foregoing embodiments, one of ordinary skill in the art should
Understand：It can still modify to the technical scheme described in foregoing embodiments, either to which part or whole
Technical characteristic carries out equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly
The scope of each embodiment technical scheme of type.
Claims (10)
1. a kind of ozone vegetable oil emulsifier unit, it is characterised in that including emulsion chamber and vaporization chamber；The emulsion chamber and the steaming
Hair room is connected by communicating pipe；
The emulsification rod for emulsification is provided with the emulsion chamber；
In the emulsion chamber also at least provided with an air inlet pipe, and the air inlet pipe lower end is provided with solarization air cap, the aeration
Hole position is in the bottom of the cavity of the emulsion chamber；The emulsion chamber top is provided with blast pipe；
The vaporization chamber upper end is provided with the inlet opening for water inlet, and lower end is provided with the apopore for water outlet, and described
Secondary heating mechanism is provided with vaporization chamber.
2. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that the emulsion chamber upper end is provided with use
In the charging hole of charging, the emulsion chamber lower end is provided with the discharge opening for discharging.
3. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that also including first heater, and
The first heater is located at the bottom of the cavity of the emulsion chamber, and the first heater is heater, the heating
Device is heating coil.
4. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that the secondary heating mechanism is heating
Device, the heater are heating coil.
5. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that folder is provided with the emulsion chamber
Set, and the first connecting tube and the second connecting tube connected with chuck is provided with the emulsion chamber.
6. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that the vaporization chamber is resistance to using high borosilicate
Hot glass is made, and the graduation mark for metering liquid volume is provided with the vaporization chamber.
7. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that the emulsion chamber and the vaporization chamber
Inside it is provided with apparatus for measuring temperature.
8. ozone vegetable oil emulsifier unit according to claim 1, it is characterised in that the communicating pipe and the emulsion chamber
Junction is less than the communicating pipe and the vaporization chamber junction.
9. the ozone vegetable oil emulsifier unit according to claim any one of 1-8, it is characterised in that the emulsion chamber is adopted
It is made of stainless steel material.
10. a kind of streamline, it is characterised in that including any one of the claim 1-9 ozone vegetable oil emulsifier units.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720372016.4U CN206746528U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil emulsifier unit and streamline |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720372016.4U CN206746528U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil emulsifier unit and streamline |
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| Publication Number | Publication Date |
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| CN206746528U true CN206746528U (en) | 2017-12-15 |
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ID=60612702
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| CN201720372016.4U Active CN206746528U (en) | 2017-04-10 | 2017-04-10 | Ozone vegetable oil emulsifier unit and streamline |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589812A (en) * | 2018-12-20 | 2019-04-09 | 常州大学 | A kind of device preparing ozonated water emulsion and preparation process |
-
2017
- 2017-04-10 CN CN201720372016.4U patent/CN206746528U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589812A (en) * | 2018-12-20 | 2019-04-09 | 常州大学 | A kind of device preparing ozonated water emulsion and preparation process |
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