CN203494459U - Homogenizing equipment for producing emulsion - Google Patents
Homogenizing equipment for producing emulsion Download PDFInfo
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- CN203494459U CN203494459U CN201320575664.1U CN201320575664U CN203494459U CN 203494459 U CN203494459 U CN 203494459U CN 201320575664 U CN201320575664 U CN 201320575664U CN 203494459 U CN203494459 U CN 203494459U
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- homogenizer
- agitated kettle
- high pressure
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- homogenizing
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Abstract
The utility model relates to homogenizing equipment for producing emulsion. The equipment comprises a vacuum agitating device and a high-pressure homogenizing machine, wherein the vacuum agitating device and the high-pressure homogenizing machine are connected by virtue of a pipeline; the vacuum agitating device is driven by a first motor; the high-pressure homogenizing machine is driven by a second motor. According to the homogenizing equipment, emulsion with the viscosity which is less than 2000cps is obtained; the grain diameter of an emulsion product can be reduced by using the equipment and the grain size is determined according to repeated homogenizing times in the high-pressure homogenizing machine; the common grain diameter is in a range from 100 nanometers to 500 nanometers; effective components can be rapidly penetrated into keratoderma and the greatest effect is expressed; the homogenizing equipment is changed according to different grain diameters to realize economical and efficient effects and save the cost.
Description
Technical field
The utility model relates to a kind of homogenizer, especially relates to a kind of homogenizer of emulsion production use, and it can effectively reduce emulsification particle diameter.
Background technology
Homogeneous is a technology often will using during food or chemical industry are produced.Under the triple role that the feed liquid of material that just refers to homogeneous expands in extruding, thump and decompression, make material refinement, thereby material can be mixed more uniformly mutually.Homogeneous is mainly undertaken by homogenizer, and the tissue dispersion, the preparation of samples of field of medicaments, the enzyme of food industry that homogenizer is mainly used in biological technical field processed and at aspects such as pharmaceuticals industry, cosmetics industry, paint industry and petrochemical industries.The operation principle of homogenizer is: high cut disperse emulsification be exactly efficiently, fast, equably by a phase or a plurality of being distributed to mutually in another continuous phase, and each is mutually insoluble mutually under normal conditions.Because rotor high-speed rotates high tangential velocity and the next powerful kinetic energy of high frequency machinery effect belt producing, thereby make immiscible solid phase, liquid phase, gas phase under the acting in conjunction of corresponding maturation process and appropriate additive, moment uniform, fine ground dispersion and emulsion, through moving in circles of high frequency, finally obtain stable high-quality product.
In emulsion production process, existingly for reducing emulsification particle diameter method, generally by mixing plant, complete, although can reduce the particle diameter of certain emulsification goods, but because of the cooperation without high pressure homogenizer, emulsification particle diameter is after treatment undesirable, the particle diameter of emulsification goods cannot be reduced to less more effective scope, causes the functional components in emulsion can only rest on keratoderma surface, cannot effectively absorb, cannot bring into play active ingredient maximum effect.
Utility model content
The deficiency existing in order to overcome prior art, the utility model provides a kind of homogenizer that can effectively reduce the emulsion production use of emulsification particle diameter.
A homogenizer for emulsion production use, described equipment comprises vacuum stirring device and high pressure homogenizer, vacuum stirring device is connected by pipeline with high pressure homogenizer; Described vacuum stirring device is driven by the first motor, and high pressure homogenizer is driven by the second motor.
Preferably, described vacuum stirring device comprises having the agitated kettle of outside sandwich, the agitator that is positioned at agitated kettle inner chamber, vavuum pump, agitated kettle top is provided with charging aperture, agitated kettle inner chamber is connected with vavuum pump, agitated kettle bottom is provided with discharging opening, discharging opening is communicated with high pressure homogenizer through pipeline, and this pipeline is provided with outlet valve; Described agitator is driven by the first motor.
Described agitated kettle and agitator material all adopt 316L stainless steel, there is resistance to acids and bases, in Cosmetic Manufacture, can effectively prevent because raw material itself has compared with the material of strong acid base number, and then cause corrosion of steel in process, conductivity is significantly drawn high, cause the generation of the phenomenons such as converted products is unstable.
Preferably, described high pressure homogenizer comprises the high pressure pump housing, plunger, homogenizing valve, Pressure gauge, regulating hand wheel of pressure, controller, and described plunger is connected with the second motor, and described the second motor and homogenizing valve are connected to controller.
The described high pressure pump housing adopts the two-way special stainless steel forging and stamping of the special high density of single SAF2507 module, and has passed through ultrasonic examination and detected definite its modular structure not damaged; Described plunger adopts the processing of high-purity mangesium oxide zirconium, and surface finish, to 0.2u, has high-wear resistance, and two all can be used; Described homogenizing valve adopts German KFC high strength and high hardness high density composite carbide alloy valve group, has high-wear resistance, and adopts two-sided use design; Described Pressure gauge adopts sanitation-grade diaphragm type digital pressure gauge, and sanitation-grade diaphragm type digital pressure gauge is located maximum 2000bar, actual homogeneous operating pressure 1800bar; Described regulating hand wheel of pressure adopts 316L stainless steel, the impact material body of avoiding getting rusty.
Preferably, described agitator is provided with and scrapes wall blade.Agitator drive is scraped wall blade and is scraped wall action, allows the raw material that is attached to pot wall get back in pot, continues to stir, disperse.
Preferably, described agitated kettle outside sandwich bottom is provided with water inlet pipe, and agitated kettle outside sandwich top is provided with outlet pipe, and described water inlet pipe is provided with the first control valve, and outlet pipe is provided with the second control valve.
The utility model has been realized the emulsion of viscosity below 2000cps, all available this equipment reduces latex product particle diameter, the requirement of particle size is determined according to the homogenization cycles that repeatedly enters high pressure homogenizer, the processing of general particle diameter can be between 100～500 how between rice, can make active ingredient infiltrate fast in keratoderma, performance maximum effect, because the difference of particle diameter changes, reach economical and effective rate, cost-effective function.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail, but protection domain of the present utility model is not limited to this.
With reference to Fig. 1, a kind of homogenizer of emulsion production use, described equipment comprises vacuum stirring device and high pressure homogenizer, vacuum stirring device is connected by pipeline with high pressure homogenizer; Described vacuum stirring device is driven by the first motor 1, and high pressure homogenizer is driven by the second motor 7.
Described vacuum stirring device comprises having the agitated kettle 2 of outside sandwich, the agitator 16 that is positioned at agitated kettle inner chamber, vavuum pump 5, agitated kettle 2 tops are provided with charging aperture, agitated kettle 2 inner chambers are connected with vavuum pump, agitated kettle 2 bottoms are provided with discharging opening, discharging opening is communicated with high pressure homogenizer through pipeline 15, and this pipeline is provided with outlet valve 6.Described agitator 16 is driven by the first motor 1, and described agitator is provided with scrapes wall blade 3.Described agitated kettle 2 outside sandwich bottoms are provided with water inlet pipe, and agitated kettle 2 outside sandwich tops are provided with outlet pipe, and described water inlet pipe is provided with the first control valve 4, and outlet pipe is provided with the second control valve 13.
Described agitated kettle and agitator material all adopt 316L stainless steel, there is resistance to acids and bases, in Cosmetic Manufacture, can effectively prevent because raw material itself has compared with the material of strong acid base number, and then cause corrosion of steel in process, conductivity is significantly drawn high, cause the generation of the phenomenons such as converted products is unstable.
Described high pressure homogenizer comprises the high pressure pump housing 8, plunger 9, homogenizing valve 10, sanitation-grade diaphragm type digital pressure gauge 11, regulating hand wheel of pressure 12, controller 14, and described plunger 9 is connected with the second motor 7, and described the second motor 7 and homogenizing valve 10 are all connected to controller 14.
Operation principle of the present utility model is:
(1) material is added by agitated kettle top, under vacuum, by the first motor, drives agitator Final 16 power to stir, and tentatively reduces particle diameter, and agitated kettle outside sandwich is by recirculated water temperature control;
(2) material after stirring enters pipeline 15 through outlet valve 6, then enters high pressure homogenizer and further reduce particle diameter, finally from high pressure homogenizer discharging.
The described high pressure pump housing adopts the two-way special stainless steel forging and stamping of the special high density of single SAF2507 module, and has passed through ultrasonic examination and detected definite its modular structure not damaged; Described plunger adopts the processing of high-purity mangesium oxide zirconium, and surface finish, to 0.2u, has high-wear resistance, and two all can be used; Described homogenizing valve adopts German KFC high strength and high hardness high density composite carbide alloy valve group, has high-wear resistance, and adopts two-sided use design; Described sanitation-grade diaphragm type digital pressure gauge is located maximum 2000bar, actual homogeneous operating pressure 1800bar; Described regulating hand wheel of pressure adopts 316L stainless steel, the impact material body of avoiding getting rusty.
No matter the utility model is the big or small difference of HLB value of its emulsifying agent, and the difference of ionic, all can use this complete equipment to reach default emulsification particle diameter, as long as any type emulsion end article viscosity is controlled at below 2000cps, all available this equipment reduces latex product particle diameter, the requirement of particle size is determined according to the homogenization cycles that repeatedly enters high pressure homogenizer, its homogeneous principle is that emulsifying material is subject to the effect of multiple turbulent form power, the air pocket dither effect that strong turbulent flow produces also produces shearing force and produces impact with homogenizing valve baffle ring with homogenizing valve edge, the processing of general particle diameter can be between 100～500 how between rice, reaching active ingredient can infiltrate in keratoderma fast, performance maximum effect, excessive without produce emulsification particle diameter through processing unlike conventional emulsification formulation, can only rest on keratoderma surface, cannot bring into play active ingredient maximum effect, utilize on the other hand this high-pressure homogeneous function effectively to reduce the consumption of functional components, can reach the effect with conventional emulsification functional components equivalent, because the difference of particle diameter changes, reach economical and effective rate, cost-effective function.
Claims (5)
1. a homogenizer for emulsion production use, is characterized in that: described homogenizer comprises vacuum stirring device and high pressure homogenizer, and vacuum stirring device is connected by pipeline with high pressure homogenizer; Described vacuum stirring device is driven by the first motor, and high pressure homogenizer is driven by the second motor.
2. the homogenizer of emulsion production use according to claim 1, it is characterized in that: described vacuum stirring device comprises having the agitated kettle of outside sandwich, the agitator that is positioned at agitated kettle inner chamber, vavuum pump, agitated kettle top is provided with charging aperture, agitated kettle inner chamber is connected with vavuum pump, agitated kettle bottom is provided with discharging opening, discharging opening is communicated with high pressure homogenizer through pipeline, and this pipeline is provided with outlet valve; Described agitator is driven by the first motor.
3. the homogenizer of emulsion production use according to claim 1, it is characterized in that: described high pressure homogenizer comprises the high pressure pump housing, plunger, homogenizing valve, Pressure gauge, regulating hand wheel of pressure, controller, described plunger is connected with the second motor, and described the second motor and homogenizing valve are connected to controller.
4. the homogenizer of emulsion production use according to claim 1, is characterized in that: described agitator is provided with scrapes wall blade.
5. the homogenizer of emulsion production use according to claim 2, it is characterized in that: described agitated kettle outside sandwich bottom is provided with water inlet pipe, agitated kettle outside sandwich top is provided with outlet pipe, and described water inlet pipe is provided with the first control valve, and outlet pipe is provided with the second control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320575664.1U CN203494459U (en) | 2013-09-17 | 2013-09-17 | Homogenizing equipment for producing emulsion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320575664.1U CN203494459U (en) | 2013-09-17 | 2013-09-17 | Homogenizing equipment for producing emulsion |
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| Publication Number | Publication Date |
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| CN203494459U true CN203494459U (en) | 2014-03-26 |
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| CN201320575664.1U Expired - Fee Related CN203494459U (en) | 2013-09-17 | 2013-09-17 | Homogenizing equipment for producing emulsion |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9615601B2 (en) | 2005-10-04 | 2017-04-11 | Jimmyash Llc | Process for the controlled introduction of oil into food products |
| US9894918B2 (en) | 2005-10-04 | 2018-02-20 | Jimmyash Llc | Fried food products having reduced fat content |
| US10542769B2 (en) | 2005-10-04 | 2020-01-28 | Jimmyash Llc | Methods of making snack food products and products made thereby |
-
2013
- 2013-09-17 CN CN201320575664.1U patent/CN203494459U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9615601B2 (en) | 2005-10-04 | 2017-04-11 | Jimmyash Llc | Process for the controlled introduction of oil into food products |
| US9839231B2 (en) | 2005-10-04 | 2017-12-12 | Jimmyash Llc | Process for the controlled introduction of oil into food products |
| US9894918B2 (en) | 2005-10-04 | 2018-02-20 | Jimmyash Llc | Fried food products having reduced fat content |
| US10542769B2 (en) | 2005-10-04 | 2020-01-28 | Jimmyash Llc | Methods of making snack food products and products made thereby |
| US10721951B2 (en) | 2005-10-04 | 2020-07-28 | Jimmy Ash Llc | Process for the controlled introduction of oil into food products |
| US10743571B2 (en) | 2005-10-04 | 2020-08-18 | Jimmy Ash Llc | Fried food products having reduced fat content |
| US11439167B2 (en) | 2005-10-04 | 2022-09-13 | Jimmyash Llc | Process for the controlled introduction of oil into food products |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171121 Address after: Hangzhou City, Zhejiang Province, 311231 block of South Xiaoshan economic and Technological Development Zone Chunchao Road No. 93 Patentee after: Yu Xingjun Address before: Hangzhou City, Zhejiang Province, 311231 block of South Xiaoshan economic and Technological Development Zone Chunchao Road No. 93 Patentee before: YALU BAYER BIOLOGICAL SCIENCE AND TECHNOLOGY (HANGZHOU) CO., LTD. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171206 Address after: 310000 Sunshine Road No. 688, Chunan County, Chunan County, Hangzhou, 103-4 Patentee after: Only treasure limited company Address before: Hangzhou City, Zhejiang Province, 311231 block of South Xiaoshan economic and Technological Development Zone Chunchao Road No. 93 Patentee before: Yu Xingjun |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140326 Termination date: 20190917 |
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| CF01 | Termination of patent right due to non-payment of annual fee |