CN203061126U - Stirring and mixing device of continuous wet-type high-speed ultra-micron granulator for producing mud facial masks - Google Patents
Stirring and mixing device of continuous wet-type high-speed ultra-micron granulator for producing mud facial masks Download PDFInfo
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- CN203061126U CN203061126U CN 201220742325 CN201220742325U CN203061126U CN 203061126 U CN203061126 U CN 203061126U CN 201220742325 CN201220742325 CN 201220742325 CN 201220742325 U CN201220742325 U CN 201220742325U CN 203061126 U CN203061126 U CN 203061126U
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- granulation machine
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Abstract
The utility model relates to a stirring and mixing device of a continuous wet-type high-speed ultra-micron granulator for producing mud facial masks. The stirring and mixing device provided by the utility model can be used for producing a uniformly-dispersed mud material body and is simple in structure and easy to manufacture. According to a technical scheme, the stirring and mixing device comprises a continuous wet-type high-speed ultra-micron granulator and a vacuum stirring kettle which is communicated through a pipeline, wherein the granulator comprises a containing cavity formed by a conical shell; and an opening in the top end of the containing cavity is used as a material inlet. The stirring and mixing device is characterized in that the granulator is internally provided with a gap adjuster for adjusting grinding gaps; a semi-finished material outlet in one side of the granulator is communicated with the vacuum stirring kettle through a pipeline which is provided with a rotor pump; and the stirring kettle is internally provided with a high-viscosity stirrer.
Description
Technical field
The utility model also relates to a kind of novel lapping device, is used for the ground and mixed equipment that special oil suction starch compound mud mask is produced, and belongs to the Cosmetic Manufacture equipment technical field.
Background technology
Fat secretion vigorous (summer is especially obvious) is that a lot of reasons causes in the human body skin; The relation of having plenty of congenital heredity has plenty of that acquired environment causes; Especially puberty more obvious, the generation of the vigorous easy initiation whelk of fat secretion, T word position is especially obvious.In addition, sebaceous glands is subjected to the influence of high temperature and pungent fry, also can allow sebaceous glands constantly secrete grease, causes pore to block, and then causes the activity of 5, makes the hyperplasia of sebaceous cell differentiation and seat sore bacillus, and then causes the generation of acne and seat sore; Outpatient service often has the patient fuel-displaced because of face, worry the glossy normal mad suction of face-sebum absorbing paper of taking of whole face, its practical face-sebum absorbing paper can only adsorb or wash away grease, reach the of short duration effect of deoiling, fundamentally do not solve the problem of skin fat secretion, long-term use skin is become more drier oil is greasy responsive, be unfavorable for skin health.
In the Cosmetic Manufacture process, form complete, the finely dispersed emulsified body of composition of oil-water emulsion for making the material body, often carry out high-speed stirred, high speed homogenization by mechanical force, reach the purpose of dispersion and emulsion.
The general mixing plant that adopts is formed the high speed dispersion dish by gate stirrer and high speed homogenization dispersion emulsifying machine usually.
Gate stirrer is usually used in the mixing of general emulsifiable paste shape material, and its mixing speed is generally relatively slow, for the bigger material-mud body of proportion, stirs the torsion underpower to stir the material body, can't form the material body of homogeneous.
The high speed homogenization dispersion emulsifying machine is made up of rotor and stator, is generally used for emulsification and disperses the less and mobile good material body of general proportion.Yet the material-mud body is bigger because itself expecting body thickness and proportion, can't obtain desirable emulsification dispersion effect; Too high as rotor speed, also easily cause the overheated and axle center distortion of mechanical shaft seal, can't make the good material-mud body of homogeneity.
The utility model content
The purpose of this utility model is at the deficiencies in the prior art, and a kind of lapping device of above-mentioned mud mask is provided, and this device should be able to be produced finely dispersed material-mud body, and simple in structure, easy to manufacture.
The technical solution adopted in the utility model is:
Produce mud mask continous way wet type high speed ultra micro granulation machine agitation mixer, comprise continuous high-speed ultra micro granulation machine and the vacuum stirring pot that is communicated with by pipeline; The cavity volume that described granulation facility have a conical shell to form, the cavity volume top end opening is as feeding mouth; It is characterized in that: be equipped with in the granulation machine to regulate and grind the clearance adjuster that the gap is used, the semi-finished product discharge gate on granulation machine limit is communicated with the vacuum stirring pot by the pipeline that has impeller pump, is provided with the high viscosity agitator in this agitated kettle.
Described continuous high-speed ultra micro granulation machine, high viscosity agitator, impeller pump are by motor-driven.
Described clearance adjuster is the circular stone clearance adjuster that supports.
Also be provided with the intermediate water device for cooling in the described granulation machine.
Described high viscosity stirrer configuration the high viscosity stirring vane.
The equipment that the utility model provides can be produced oil-water emulsion equal refining body completely effectively, is fit to very much the production of mud mask.Wherein, continuous high-speed ultra micro granulation machine (wet type) can the production high viscosity, than pulp product great, mobile difference, carries out the mixing dispersion and powder grinding of material; Cream frost latex product that also can the production mixed flow; The vacuum stirring pot also can be used as Water-In-Oil cream frost emulsion, the emulsifying homogenizer of oil-in-water cream frost emulsion.It is bigger that this device is handled the mud mask amount, can adjust with the variation of conical shell volume; Can contrast great, viscosity is high, the lotion of mobile difference disperses effectively with evenly, grind out the material-mud body of homogeneous particle diameter.
Description of drawings
Fig. 1 is the structural representation of equipment described in the utility model.
Have among the figure: 1, feeding mouth; 2, clearance adjuster; 3, intermediate water device for cooling; 4, first motor; 5, semi-finished product discharge gate; 6, impeller pump; 7, second motor; 8, high viscosity stirring vane; 9, vacuum stirring pot; 10, pipeline.
The specific embodiment
The utility model is described in further detail below by non-limiting examples.
As shown in Figure 1, the continous way wet type high speed ultra micro granulation machine agitation mixer for the production of mud mask comprises continuous high-speed ultra micro granulation machine and vacuum stirring pot; The conical shell of described continuous high-speed ultra micro granulation machine forms an open cavity volume, housing is provided with feeding mouth 1, connect the circular inside of supporting stone clearance adjuster 2 intermediate water device for cooling 3 is arranged, semi-finished product discharge gate 5 belows are connected with first motor 4, and the semi-finished product discharge gate is communicated with vacuum stirring pot 9 by the pipeline 10 that has impeller pump 6; In the vacuum stirring pot, the output shaft of second motor 7 is vertically down arranged, is being fixed high viscosity stirring vane 8 on the output shaft.
Above-mentioned continous way wet type high speed ultra micro granulation machine, the equal outsourcing of vacuum stirring pot obtain.
During concrete the application, A, B phase raw material are added in the conical shell 1, the first motor semi-finals power of opening is mixed and is stirred, and adjusts the circular stone clearance adjuster 2(of supporting and opens intermediate water device for cooling 3) the grinding gap, make material body particle diameter reach the regulation requirement; Open impeller pump 6 again, semi-finished product are carried move in the fixed vacuum stirring pot 9, open second motor 7 then high viscosity stirring vane 8 is stirred; Mixing speed 900-11,00rpm, vacuum behind the stirring 25-35Mins, carries dischargings to get final product by the pipeline 5 that has impeller pump 6 to – 0.8Mpa again.
Need progressively turn down during grinding and grind the gap; Usually turn down circular support the gap of stone clearance adjuster after, will semi-finished product material body add in the conical shell and grind 5-10Mins, be disposed to by the semi-finished product discharge gate then and leave standstill that (pipeline that has impeller pump is removed from the semi-finished product discharge gate in advance in the bucket 11; Leaving standstill bucket 11 is conventional vessels, represents with double dot dash line among the figure); Then turn the circular gap of supporting the stone clearance adjuster again down, again semi-finished product material body is added in the conical shell and grind 5-10Mins, be disposed to by the semi-finished product discharge gate again and leave standstill in the bucket; So circulation is at least three times, the particle diameter of semi-finished product material body could be ground to＜below the 10 μ m.
Embodiment one
Get glycerine 10.0Kg, kaolin 10.0Kg, green clay 5.0Kg, bentonite 2.0Kg, silica 1.0Kg, starch ocentyl succinic aluminium 0.5Kg, acrylic acid (ester) analog copolymer 0.15Kg, magnesium carbonate 0.1Kg, xanthans 0.1Kg, allantoin 0.05Kg, EDTA disodium 0.05Kg, DMDM hydantoins 0.05Kg, iodine propilolic alcohol butyl mephenesin Carbamate 0.05Kg, essence 0.02Kg, deionized water 70.98Kg.
By formula ratio xanthans, allantoin, EDTA disodium, bentonite, glycerine, deionized water are heated to 55 ℃, fully after the dissolving, by continous way wet type high speed ultra micro granulation machine, motor rotary speed is fixed 3,000rpm, adjusts and supports crack between the stone clearance adjuster, the each adjustment dwindled to stone gap 2mm, grind above more than 3 times, reach to＜10 μ m, mutually standby as A;
By behind the irradiation 30mins, sterilization is finished with green clay, as the B phase;
Mixed material with A adds in the granulation machine more again at last, opens machine, in regular turn with B item and the raw material that do not add, add A mutually in, treat that whole raw materials add to grind after finishing mixing; The each adjustment dwindled to stone gap 2mm, grinds repeatedly 5 times, and particle diameter＜below the 5 μ m, barrelling is standby to make it reach the material body;
The compound of last step is transported to fixed vacuumizing in the agitated kettle by impeller pump, open the high viscosity stirring vane, mixing speed 1,000rpm, open the Chou vacuum Zhi – 0.8Mpa, after stirring 30Mins, carry discharging by impeller pump again, get final product the special oil suction starch compound of a kind of interpolation mud mask finished product.
Embodiment two
Get glycerine 12.0Kg, kaolin 15.0Kg, green clay 8.0Kg, bentonite 3.5Kg, silica 2.0Kg, starch ocentyl succinic aluminium 0.6Kg, acrylic acid (ester) analog copolymer 0.2Kg, magnesium carbonate 0.2Kg, xanthans 0.1Kg, allantoin 0.2Kg, EDTA disodium 0.05Kg, DMDM hydantoins 0.05Kg, iodine propilolic alcohol butyl mephenesin Carbamate 0.05Kg, essence 0.1Kg, deionized water 57.95Kg;
Just xanthans, allantoin, EDTA disodium, bentonite, glycerine, deionized water are heated to 65 ℃ by formula ratio, fully after the dissolving, by continous way wet type high speed ultra micro granulation machine, motor rotary speed is fixed 3,000rpm, adjusts and supports crack between the stone, the each adjustment dwindled to stone gap 2mm, grind above more than 3 times, reach to＜10 μ m, mutually standby as A;
By behind the irradiation 30mins, sterilization is finished with green clay, as the B phase;
Mixed material with A adds putting in the charging basket of granulation machine more again at last, open machine, in regular turn the B item is reached the raw material that does not add, add A mutually in, treat to grind after mixing is finished in whole raw materials addings, the each adjustment dwindled to stone gap 2mm, grinds repeatedly 4 times, particle diameter＜below the 5 μ m, barrelling is standby to make it reach the material body;
The compound of last step is transported to fixed vacuumizing in the agitated kettle by impeller pump, open fixed high viscosity stirring vane, mixing speed 1,000rpm, open the Chou vacuum Zhi – 0.8Mpa, after stirring 30Mins, carry discharging by impeller pump again, get final product the special oil suction starch compound of a kind of interpolation mud mask finished product.
Claims (5)
1. produce mud mask continous way wet type high speed ultra micro granulation machine agitation mixer, comprise continuous high-speed ultra micro granulation machine and the vacuum stirring pot (9) that is communicated with by pipeline; The cavity volume that described granulation facility have a conical shell to form, the cavity volume top end opening is as feeding mouth (1); It is characterized in that: be equipped with in the granulation machine to regulate and grind the clearance adjuster (2) that the gap is used, the semi-finished product discharge gate (5) on granulation machine limit is communicated with the vacuum stirring pot by the pipeline (10) that has impeller pump (6), is provided with the high viscosity agitator in this agitated kettle.
2. according to the described production mud mask of claim 1 continous way wet type high speed ultra micro granulation machine agitation mixer, it is characterized in that described continuous high-speed ultra micro granulation machine, high viscosity agitator, impeller pump are by motor-driven.
3. according to the described production mud mask of claim 2 continous way wet type high speed ultra micro granulation machine agitation mixer, it is characterized in that described clearance adjuster is the circular stone clearance adjuster that supports.
4. according to the described production mud mask of claim 3 continous way wet type high speed ultra micro granulation machine agitation mixer, it is characterized in that also being provided with in the described granulation machine intermediate water device for cooling (3).
5. according to the described production mud mask of claim 4 continous way wet type high speed ultra micro granulation machine agitation mixer, it is characterized in that described high viscosity stirrer configuration high viscosity stirring vane (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220742325 CN203061126U (en) | 2012-12-28 | 2012-12-28 | Stirring and mixing device of continuous wet-type high-speed ultra-micron granulator for producing mud facial masks |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220742325 CN203061126U (en) | 2012-12-28 | 2012-12-28 | Stirring and mixing device of continuous wet-type high-speed ultra-micron granulator for producing mud facial masks |
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| Publication Number | Publication Date |
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| CN203061126U true CN203061126U (en) | 2013-07-17 |
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| CN 201220742325 Expired - Fee Related CN203061126U (en) | 2012-12-28 | 2012-12-28 | Stirring and mixing device of continuous wet-type high-speed ultra-micron granulator for producing mud facial masks |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103040639A (en) * | 2012-12-28 | 2013-04-17 | 雅露拜尔生物科技（杭州）有限公司 | Oil absorption starch compound slurry mask, preparation technology and grinding devices thereof |
-
2012
- 2012-12-28 CN CN 201220742325 patent/CN203061126U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103040639A (en) * | 2012-12-28 | 2013-04-17 | 雅露拜尔生物科技（杭州）有限公司 | Oil absorption starch compound slurry mask, preparation technology and grinding devices thereof |
| CN103040639B (en) * | 2012-12-28 | 2014-04-30 | 雅露拜尔生物科技（杭州）有限公司 | Oil absorption starch compound slurry mask, preparation technology |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171128 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, the 311231 Xiaoshan economic and Technological Development Zone, 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: 20171213 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20191228 |