CN206262467U - Vacuum homogeneous emulsifying machine - Google Patents
Vacuum homogeneous emulsifying machine Download PDFInfo
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- CN206262467U CN206262467U CN201621384630.4U CN201621384630U CN206262467U CN 206262467 U CN206262467 U CN 206262467U CN 201621384630 U CN201621384630 U CN 201621384630U CN 206262467 U CN206262467 U CN 206262467U
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Abstract
The utility model is related to a kind of vacuum homogeneous emulsifying machine, belong to emulsifying apparatus field, including oil phase storage tank, water phase storage tank, tank body, material enters tank body after vacuum pumping material confluxes through branch pipe(tube) and mixes into total pipeline in oil phase storage tank, water phase storage tank, heat exchanger is set on total pipeline, the efficiency of heating surface is high, easy temperature control system, it is to avoid the energy waste that storage tank heating tape is come；Tank body peripheral hardware vacuum jacket, adiabatic space can be provided after extracting vacuum to tank body, while vacuum jacket is provided with two interfaces, is passed through steam or cooling water is heated or cooled to tank body；The pipeline that vavuum pump is connected with tank body is provided with surge tank, and the bubble to be formed, stable gas pressure are emulsified using the negative pressure extracting in surge tank, it is to avoid subsidiary water phase or oil phase material enter in vavuum pump when extracting gas, improve service life of vacuum pump；It is close to inner tank wall and sets high-pressure nozzle, high-pressure nozzle is opened at the end of use inner tank wall is rinsed, solves the problems, such as that material scraping plate scraper is not net.
Description
Technical field
The utility model is related to a kind of vacuum homogeneous emulsifying machine, belongs to emulsifying apparatus field.
Background technology
The principle of emulsifying equipment is after material carries out hybrid reaction in kettle, oil cauldron by heating, stirring, by true
Empty pumping enters to emulsify pot, and agitated kettle body is catered to all the time by emulsifying the center stirring of pot internal upper part, polytetrafluoroethylene (PTFE) scraper plate, sweeps
Net wall built-up sizing, makes the material for being scraped constantly produce new interface, then cutting, compression, folding by blade and rotary vane,
Make its stirring, mix and be downwardly toward in the homogenizer below pot, material is in cutting wheel and the fixation by telling rotation
The process such as produced cutting, impact, sinuous flow of strength between cutting set, material is cut in seam is sheared, is broken into rapidly
The particulate of 200nm-2um, because emulsification pot is in vacuum state, the bubble that material is produced in whipping process is pumped in time.
Existing emulsifying equipment has the following disadvantages：
(1) heating is generally required during material emulsifying to obtain more preferable effect, existing mode of heating is typically used
First heated in storage tank in transporting to emulsifying tank again, or chuck be set outside tank body, heated by being passed through steam,
These modes use more complicated, and temperature is not easily controlled, while extremely wasting the energy, increase cost；
(2) vavuum pump is directly connected to emulsifying tank, unstable during vacuum pump work, meanwhile, vavuum pump is to more in tank body
The gas that the gas for going out is extracted is contained within some subsidiary moisture, a small amount of oil phase thing and a small amount of aqueous-phase material, these things
Matter can reduce the service life of vavuum pump after entering vavuum pump；
(3) because institute's general viscosity of spent material is higher, it is easily sticked in inner tank wall during emulsifying, material scraping plate scraper
Effect is not satisfactory.
Utility model content
The utility model purpose is to provide a kind of vacuum homogeneous emulsifying machine, with energy saving, protection vavuum pump, cleaning
The advantages of inner tank wall.
Vacuum homogeneous emulsifying machine described in the utility model, including oil phase storage tank, water phase storage tank, tank body, oil phase storage
Material in batch can, water phase storage tank is confluxed through branch pipe(tube) by the first vavuum pump and the second vacuum pumping material enter house steward respectively
Enter in tank body after road mixing, heat exchanger is set on total pipeline, tank body top sets motor, and machine shaft is connected with central shaft, center
Axle is provided with emulsifying head, and " u "-shaped material scraping plate is further fixed on central shaft, and material scraping plate is provided with some puddlers arranged in parallel；
Also set in tank body and be close to the equally distributed high-pressure nozzle of inwall, high-pressure nozzle is equipped with organic washing agent by pipeline with outside
Pressure pan is connected, and tank body also sets the vavuum pump for communicating therewith, surge tank, the shell of tank body are set on the pipeline that tank body is connected with vavuum pump
Vacuum jacket is set in vitro, tank base sets the discharge gate for communicating therewith.
Material circulation device is also set outside tank body, material circulation device includes the pipeline on connection discharge gate and tank body top, pipe
Road is provided with circulating pump, and during emulsifying, tank base concentration is higher, and bottoms material is sent back to tank body by the effect of circulating pump
Inside it is sufficiently mixed it, emulsifying effect is more preferable.
The first agitating device and the second agitating device are set respectively in oil phase storage tank, water phase storage tank, if the first stirring dress
It is to make the material concentration entered before tank body uniform to put with the purpose of the second agitating device, the first agitating device and the second agitating device
Include the paddle that motor drives.
Total pipeline sets the first valve with the junction of tank body, and the second valve is set at discharge gate.
First interface and second interface are also set on vacuum jacket, valve is all provided with first interface and second interface, on the one hand
Can be used for connecting outside vaccum-pumping equipment, on the other hand can be used for being passed through the import and export that steam is heated or cooled water cooling.
The utility model compared with prior art, has the advantages that.
(1) heat exchanger is provided with pipeline of the utility model after oil phase, water are mixed, the efficiency of heating surface is high, easy temperature control
System, while avoiding the energy waste come in multiple storage tank heating tapes；The utility model tank body peripheral hardware vacuum jacket, extracts true
Adiabatic space can be provided to tank body after sky, save energy, while chuck is provided with two interfaces, steam or cooling water pair can be passed through
Tank body is heated or cooled；
(2) the utility model is provided with surge tank on the pipeline that vavuum pump is connected with tank body, using what is formed in vacuum tank
The bubble that negative pressure extracting tank body internal emulsification is formed, stable gas pressure, while subsidiary water phase or oil phase material enter when avoiding extracting gas
Enter in vavuum pump, improve the service life of vavuum pump；
(3) the utility model is close to inner tank wall and is provided with high-pressure nozzle, and high-pressure nozzle has by pipeline with outside
The pressure pan connection of machine cleaning agent, opens high-pressure nozzle to inner tank wall spray irrigation, solution at the end of the utility model use
The unnet problem of material scraping plate scraper of having determined.
Brief description of the drawings
Fig. 1, the example structure schematic diagram of the utility model one.
In figure：1st, the first agitating device 2, total pipeline 3, the first vavuum pump 4, the second vavuum pump 5, heat exchanger 6, true
Empty pump 7, surge tank 8, the first valve 9, motor 10, high-pressure nozzle 11, first interface 12, circulating pump 13, the second valve
14th, discharge gate 15, emulsifying head 16, puddler 17, material scraping plate 18, second interface 19, the second agitating device 20, water are mutually stored up
Batch can 21, oil phase storage tank 22, tank body 23, vacuum jacket 24, central shaft.
Specific embodiment
The utility model is described further with reference to Figure of description and embodiment.
As shown in figure 1, vacuum homogeneous emulsifying machine described in the utility model, including oil phase storage tank 21, water phase storage tank
20th, tank body 22, the material in oil phase storage tank 21, water phase storage tank 20 is taken out by the first vavuum pump 3 and the second vavuum pump 4 respectively
Material confluxes through branch pipe(tube) and enters in tank body 22 into after the mixing of total pipeline 2, and heat exchanger 5 is set on total pipeline 2, and the top of tank body 22 sets electricity
Machine 9, the rotating shaft of motor 9 is connected with central shaft 24, and central shaft 24 is provided with emulsifying head 15, and being further fixed on " u "-shaped on central shaft 24 scrapes
Flitch 17, material scraping plate 17 is provided with some puddlers 16 arranged in parallel；Also set in tank body 22 and be close to the equally distributed of inwall
High-pressure nozzle 10, tank body 22 also sets the vavuum pump 6 for communicating therewith, and surge tank 7 is set on the pipeline that tank body 22 is connected with vavuum pump 6,
The housing peripheral hardware vacuum jacket 23 of tank body 22, the bottom of tank body 22 sets the discharge gate 14 for communicating therewith.
Tank body 22 is outer also to set material circulation device, and material circulation device includes the pipe on connection discharge gate 14 and the top of tank body 22
Road, pipeline is provided with circulating pump 12.
The first agitating device 1 and the second agitating device 19 are set respectively in oil phase storage tank 21, water phase storage tank 20.
Total pipeline 2 sets the first valve 8 with the junction of tank body 22, and the second valve 13 is set at discharge gate 14.
First interface 11 and second interface 18 are also set on vacuum jacket 23.
The utility model is compared with the improvement of prior art：
(1) the utility model is provided with heat exchanger 5 on oil phase, the mixed total pipeline 2 of aqueous-phase material material, and the efficiency of heating surface is high,
Easy temperature control system, while avoiding the energy waste come in multiple storage tank heating tapes；The peripheral hardware vacuum of the utility model tank body 22
Chuck 23, adiabatic space can be provided after extracting vacuum to tank body 22, energy is saved, while vacuum jacket 23 is provided with first interface
11 and second interface 18, steam or cooling water can be passed through tank body 22 is heated or cooled；
(2) the utility model is provided with surge tank 7 on the pipeline that vavuum pump 6 is connected with tank body 22, using shape in surge tank 7
Into the bubble that is formed of the internal emulsification of negative pressure extracting tank body 22, stable gas pressure, while avoiding extracting subsidiary water phase or oil phase during gas
Material enters in vavuum pump 6, improves the service life of vavuum pump 6；
(3) the utility model is close to the inwall of tank body 22 and is provided with high-pressure nozzle 10, high-pressure nozzle 10 by pipeline with it is outside
Pressure pan connection equipped with organic washing agent, opens high-pressure nozzle 10 to the spray of the inwall of tank body 22 at the end of the utility model use
Drench and rinse, solve the problems, such as that the scraper of material scraping plate 17 is not net.
Claims (5)
1. a kind of vacuum homogeneous emulsifying machine, including oil phase storage tank (21), water phase storage tank (20), tank body (22), oil phase storing
Material in tank (21), water phase storage tank (20) takes out material through branch pipe(tube) by the first vavuum pump (3) and the second vavuum pump (4) respectively
Conflux and enter in tank body (22) into after total pipeline (2) mixing, it is characterised in that：Heat exchanger (5), tank body are set on total pipeline (2)
(22) top sets motor (9), and motor (9) rotating shaft is connected with central shaft (24), and central shaft (24) is provided with emulsifying head (15), center
" u "-shaped material scraping plate (17) is further fixed on axle (24), material scraping plate (17) is provided with some puddlers (16) arranged in parallel；Tank body
(22) also set in and be close to the equally distributed high-pressure nozzle (10) of inwall, tank body (22) also sets the vavuum pump (6) for communicating therewith, tank
Surge tank (7), housing peripheral hardware vacuum jacket (23) of tank body (22), tank body are set on the pipeline that body (22) is connected with vavuum pump (6)
(22) bottom sets the discharge gate (14) for communicating therewith.
2. vacuum homogeneous emulsifying machine according to claim 1, it is characterised in that：Tank body (22) also sets outward Matter Transfer dress
Put, material circulation device includes the pipeline on connection discharge gate (14) and tank body (22) top, pipeline is provided with circulating pump (12).
3. vacuum homogeneous emulsifying machine according to claim 1, it is characterised in that：Oil phase storage tank (21), water phase storage tank
(20) the first agitating device (1) and the second agitating device (19) are set respectively in.
4. vacuum homogeneous emulsifying machine according to claim 1, it is characterised in that：The connection of total pipeline (2) and tank body (22)
Place sets the first valve (8), and discharge gate (14) place sets the second valve (13).
5. vacuum homogeneous emulsifying machine according to claim 1, it is characterised in that：Vacuum jacket also sets first interface on (23)
And second interface (18) (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621384630.4U CN206262467U (en) | 2016-12-16 | 2016-12-16 | Vacuum homogeneous emulsifying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621384630.4U CN206262467U (en) | 2016-12-16 | 2016-12-16 | Vacuum homogeneous emulsifying machine |
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| Publication Number | Publication Date |
|---|---|
| CN206262467U true CN206262467U (en) | 2017-06-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201621384630.4U Active CN206262467U (en) | 2016-12-16 | 2016-12-16 | Vacuum homogeneous emulsifying machine |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108325485A (en) * | 2018-01-13 | 2018-07-27 | 安徽金禾实业股份有限公司 | A kind of method that Wet hydrogen sulfide corrosion is reduced in sulfur-melting technology |
| CN108479620A (en) * | 2018-03-23 | 2018-09-04 | 天能电池集团（安徽）有限公司 | A kind of paste mixing machine device for monitoring temperature, system and method |
| CN108654436A (en) * | 2018-07-16 | 2018-10-16 | 江苏省苏安能节能建材科技有限公司 | A kind of preparation facilities of nano-silicon rubber latex |
| CN109159230A (en) * | 2018-11-06 | 2019-01-08 | 肇庆力合技术发展有限公司 | A kind of process units of waterproofing agent and preparation method thereof and waterproofing agent |
| CN110129184A (en) * | 2019-06-04 | 2019-08-16 | 银川亿源肥料有限公司 | It is a kind of for producing the Negative Pressure Difference sprayization system equipment of biological fermentation feed or fertilizer |
| CN111821183A (en) * | 2019-10-30 | 2020-10-27 | 上海上药新亚药业有限公司 | Injection microemulsion preparation system and method |
| CN112660626A (en) * | 2020-12-14 | 2021-04-16 | 江西长通实业有限公司 | Material structure is failed to storage of antibacterial gel production usefulness |
| CN113786370A (en) * | 2021-11-10 | 2021-12-14 | 广州华夏职业学院 | Whitening and moisturizing mask and preparation equipment thereof |
| CN113976052A (en) * | 2021-11-03 | 2022-01-28 | 健进制药有限公司 | Preparation system and preparation method of multivesicular liposome |
| CN114100396A (en) * | 2021-11-26 | 2022-03-01 | 深圳市真味生物科技有限公司 | Compounding device is used in production of electron atomized liquid with anti-blocking function |
-
2016
- 2016-12-16 CN CN201621384630.4U patent/CN206262467U/en active Active
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108325485A (en) * | 2018-01-13 | 2018-07-27 | 安徽金禾实业股份有限公司 | A kind of method that Wet hydrogen sulfide corrosion is reduced in sulfur-melting technology |
| CN108479620A (en) * | 2018-03-23 | 2018-09-04 | 天能电池集团（安徽）有限公司 | A kind of paste mixing machine device for monitoring temperature, system and method |
| CN108654436A (en) * | 2018-07-16 | 2018-10-16 | 江苏省苏安能节能建材科技有限公司 | A kind of preparation facilities of nano-silicon rubber latex |
| CN109159230A (en) * | 2018-11-06 | 2019-01-08 | 肇庆力合技术发展有限公司 | A kind of process units of waterproofing agent and preparation method thereof and waterproofing agent |
| CN110129184A (en) * | 2019-06-04 | 2019-08-16 | 银川亿源肥料有限公司 | It is a kind of for producing the Negative Pressure Difference sprayization system equipment of biological fermentation feed or fertilizer |
| CN110129184B (en) * | 2019-06-04 | 2023-11-24 | 银川亿源肥料有限公司 | Negative pressure differential spraying system equipment for producing biological fermentation feed or fertilizer |
| CN111821183A (en) * | 2019-10-30 | 2020-10-27 | 上海上药新亚药业有限公司 | Injection microemulsion preparation system and method |
| CN112660626A (en) * | 2020-12-14 | 2021-04-16 | 江西长通实业有限公司 | Material structure is failed to storage of antibacterial gel production usefulness |
| CN113976052A (en) * | 2021-11-03 | 2022-01-28 | 健进制药有限公司 | Preparation system and preparation method of multivesicular liposome |
| CN113786370A (en) * | 2021-11-10 | 2021-12-14 | 广州华夏职业学院 | Whitening and moisturizing mask and preparation equipment thereof |
| CN113786370B (en) * | 2021-11-10 | 2023-09-05 | 广州华夏职业学院 | Whitening and moisturizing facial mask mixing equipment |
| CN114100396A (en) * | 2021-11-26 | 2022-03-01 | 深圳市真味生物科技有限公司 | Compounding device is used in production of electron atomized liquid with anti-blocking function |
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