CN105311986A - Cosmetic powder pretreatment device and pretreatment method - Google Patents
Cosmetic powder pretreatment device and pretreatment method Download PDFInfo
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- CN105311986A CN105311986A CN201510847634.5A CN201510847634A CN105311986A CN 105311986 A CN105311986 A CN 105311986A CN 201510847634 A CN201510847634 A CN 201510847634A CN 105311986 A CN105311986 A CN 105311986A
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- powder
- agitator tank
- solvent
- tank
- pretreatment unit
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Abstract
The invention provides a cosmetic powder pretreatment device and pretreatment method. The device comprises a stirring tank and a filtering tank which are communicated with each other through a communicating pipe, the outer side wall of the stirring tank is sleeved with a clamping sleeve, a powder feed pipe is arranged on the clamping sleeve in a penetrating mode, and the powder feed pipe extends to the bottom of the stirring tank. The method comprises the following steps that solvent is added through a solvent feed hole, and the liquid level of the solvent is not lower than the lowest point of the powder feed pipe extending into the stirring tank; the vacuum degree is regulated, and the powder is pumped into the stirring tank through the powder feed pipe; a stirring motor is started, stirring and mixing are conducted through stirring paddles, and initial feed liquid is obtained; the initial feed liquid is conveyed into the filtering tank through the communicating pipe, by means of filtration of a filtration medium, supernate flows out through a mixed liquor outlet and is collected, and waste residues are discharged through a residue discharge port. The cosmetic powder pretreatment device and pretreatment method have the advantages that the accuracy of feeding is improved, environmental protection is achieved, the health of operating personnel is protected, and the caking problem is solved.
Description
Technical field
The present invention relates to a kind of cosmetics powder pretreatment unit and preprocess method, belong to cosmetics manufacturing technology field.
Background technology
Cosmetics (cream, frost, breast, liquid etc.) the general capital equipment of preparation process is emulsification pot, can produce more inconvenience: 1. dust from flying when using the raw material of powdery type, causes metering inaccurate, harm operator ' s health, contaminated environment, flushing, the problems such as cleaning difficulty; 2. conglomeration, extends time of dissolving or causes in product and occur that pimple etc. affects the uniformity of product, and then affecting security and validity; 3. dissolve not exclusively, some powder stocks particularly plant origin, complicated component, the polarity difference of ingredient is larger, be not easy all to dissolve in single solvent, insoluble composition retains the stability that can affect product in the product, also may cause the adverse effect of outward appearance, effect aspect.
Summary of the invention
For defect of the prior art, the object of this invention is to provide a kind of cosmetics powder pretreatment unit and preprocess method, be in particular solution powder, especially the inconvenience of the powder stock interpolation of plant origin, design powder pretreatment unit, utilize the solvent in cosmetic formulations to carry out with powder in advance mixing, dissolve, filtration etc., facilitate the carrying out of subsequent technique.
The present invention is achieved by the following technical solutions:
First aspect, the invention provides a kind of cosmetics powder pretreatment unit, it comprises: agitator tank and filtering tank, described filtering tank is communicated with by communicating pipe with agitator tank, the lateral wall of described agitator tank is arranged with chuck, be equipped with powder feed pipe above described chuck, described powder feed pipe extends to the bottom of agitator tank.
Preferably, the top of described agitator tank is also provided with bleeding point and solvent feed mouth.
Preferably, be provided with stirring motor between described bleeding point and solvent feed mouth, described stirring motor is provided with the paddle extending to agitator tank inside.
Preferably, the bottom of described agitator tank is also provided with leakage fluid dram.
Preferably, the top of described filtering tank is provided with mixture export, and the bottom of filtering tank is provided with slag-drip opening.
Preferably, also filter medium is filled with in described filtering tank.
Preferably, described filter medium is filter bag or ceramic membrane; The aperture of described filter bag is 100 ~ 800 orders, and the aperture of described ceramic membrane is 0.03 ~ 2 μm.
Second aspect, present invention also offers a kind of preprocess method based on aforesaid cosmetic product powder pretreatment unit, it comprises the steps:
Add solvent by solvent feed mouth, make the liquid level of solvent be not less than powder feed pipe and extend to minimum point in agitator tank;
Regulate vacuum, by powder feed pipe by powder suction agitator tank;
Start stirring motor, paddle starts to be uniformly mixed, and obtains initial feed liquid;
Vacuumize by described initial feed liquid by communicating pipe input filtering tank, through the filtration of filter medium, supernatant is flowed out by mixture export, and collect, waste residue is discharged by slag-drip opening.
Preferably, described powder is the raw material of cosmetics, can be monomer, also can be compound, as dipotassium glycyrrhizinate, lotus leaf extractive of general flavone, aloe frozen-dried powder, pachymaran powder.
Preferably, the consumption of described solvent is 10 ~ 200 times of powder quality.
Preferably, the stir speed (S.S.) of described paddle is 30 ~ 200r/min.
Compared with prior art, the present invention has following beneficial effect:
1, improve the accuracy fed intake, can not fly upward because of powder, conglomeration etc. causes the impairment adding raw material;
2, environmental protection, not contaminated air;
3, operator ' s health is protected;
4, conglomeration problem when powder adds is solved;
5, can insoluble composition be filtered, improve the stability of cosmetics.
Accompanying drawing explanation
By reading the detailed description done non-limiting example with reference to the following drawings, other features, objects and advantages of the present invention will become more obvious:
Fig. 1 is the structural representation of cosmetics powder pretreatment unit in the present invention;
In figure: 1, agitator tank; 2, filtering tank; 3, chuck; 4, powder feed pipe; 5, stirring motor; 6, paddle; 7, communicating pipe; 11, bleeding point; 12, solvent feed mouth; 13, leakage fluid dram; 21, mixture export; 22, slag-drip opening.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is described in detail.Following examples will contribute to those skilled in the art and understand the present invention further, but not limit the present invention in any form.It should be pointed out that to those skilled in the art, without departing from the inventive concept of the premise, some distortion and improvement can also be made.These all belong to protection scope of the present invention.
As shown in Figure 1, the invention provides a kind of cosmetics powder pretreatment unit to comprise: agitator tank 1 and filtering tank 2, filtering tank is communicated with by communicating pipe 7 with agitator tank, the lateral wall of agitator tank 1 is arranged with chuck 3, be equipped with powder feed pipe 4 above chuck 3, powder feed pipe 4 extends to the bottom of agitator tank 1.
Conveniently the adding of solvent and powder, the top of agitator tank 1 is also provided with bleeding point 11 and solvent feed mouth 12.
In order to promote mixing of powder and solvent, be provided with stirring motor 5 between bleeding point 11 and solvent feed mouth 12, stirring motor 5 is provided with the paddle 6 extending to agitator tank inside.
The conveniently discharge of waste liquid, is also provided with leakage fluid dram 13 in the bottom of agitator tank 1.
For the ease of being separated of extract and waste residue, be provided with mixture export 21 at the top of filtering tank 2, the bottom of filtering tank is provided with slag-drip opening 22.
In order to improve filter effect, in filtering tank 2, be also filled with filter medium 23.
Preferably, filter medium is filter bag or ceramic membrane; The aperture of described filter bag is 100 ~ 800 orders, and the aperture of described ceramic membrane is 0.03 ~ 2 μm.
embodiment 1
The present embodiment relates to the preprocess method of pachymaran, comprises the steps:
The aqueous solution of pachymaran powder quality 100 times is added in agitator tank, open stirring 200 turns/min, vacuumize and suck pachymaran powder, 10min is stirred after completing, open the vacuum plant on emulsification pot, the liquid in agitator tank is sucked in filtering tank, the materials such as the ceramic membrane that filter medium is 2 μm, after filtering in suction emulsification pot, solution is clarified.
embodiment 2
The present embodiment relates to the preprocess method of lotus leaf general flavone, comprises the steps:
1 of 4% of lotus leaf extractive of general flavone quality 200 times is added in agitator tank, the 3-butanediol aqueous solution, opens stirring 30 turns/min, vacuumizes and sucks lotus leaf extractive of general flavone, 60 DEG C are heated to after completing, stir 10min, be cooled to < 35 DEG C, open the vacuum plant on emulsification pot, liquid in agitator tank is sucked in filtering tank, the materials such as the ceramic membrane that filter medium is 0.03 μm, after filtering in suction emulsification pot, solution is clarified.
embodiment 3
The present embodiment relates to the preprocess method of aloe, comprises the steps:
The aqueous solution of aloe frozen-dried powder quality 10 times is added in agitator tank, open stirring 70 turns/min, vacuumize suction aloe frozen-dried powder, stir 5min after completing, open the vacuum plant on emulsification pot, the liquid in agitator tank is sucked in filtering tank, filter medium 800 order filter bag, after filtering in suction emulsification pot, solution is clarified, and the reinforced proportion of goods damageds of test are 0.21%.
embodiment 4
The present embodiment relates to the preprocess method of dipotassium glycyrrhizinate, comprises the steps:
The aqueous solution of dipotassium glycyrrhizinate quality 100 times is added in agitator tank, open stirring 100 turns/min, vacuumize suction dipotassium glycyrrhizinate, stir 15min after completing, open the vacuum plant on emulsification pot, the liquid in agitator tank is sucked in filtering tank, filter medium 100 order filter bag, after filtering in suction emulsification pot, solution is clarified, and the reinforced proportion of goods damageds of test are 0.15%.
comparative example 1
In emulsification pot, add the aqueous solution of pachymaran powder quality 100 times, open stirring 200 turns/min, add pachymaran powder, dust flies upward in a large number, stirs 10min, and solution is muddy.
comparative example 2
1 of 4% of lotus leaf extractive of general flavone quality 200 times is added in emulsification pot, the 3-butanediol aqueous solution, open stirring 30 turns/min, add lotus leaf extractive of general flavone, dust flies upward in a large number, is heated to 60 DEG C after completing, and stirs 10min, be cooled to < 35 DEG C, solution muddiness also has conglomeration.
comparative example 3
In emulsification pot, add the aqueous solution of aloe frozen-dried powder quality 10 times, open stirring 70 turns/min, add aloe frozen-dried powder, dust flies upward in a large number, stirs 5min after completing, and solution is clarified, and the reinforced proportion of goods damageds of test are 1.5%.
comparative example 4
In emulsification pot, add the aqueous solution of dipotassium glycyrrhizinate quality 100 times, open stirring 100 turns/min, add dipotassium glycyrrhizinate, dust flies upward in a large number, stirs 15min after completing, and solution is clarified, and the reinforced proportion of goods damageds of test are 2.3%.
The computing formula of the reinforced proportion of goods damageds is as follows:
The reinforced proportion of goods damageds=(1-C
1* V
1/ M
0) * 100%;
C
1: liquid solid content kg/L after reinforced;
V
1: liquid volume L after reinforced;
M
0: powder input amount kg.
Above specific embodiments of the invention are described.It is to be appreciated that the present invention is not limited to above-mentioned particular implementation, those skilled in the art can make various distortion or amendment within the scope of the claims, and this does not affect flesh and blood of the present invention.
Claims (10)
1. a cosmetics powder pretreatment unit, it is characterized in that, comprise: agitator tank and filtering tank, described filtering tank is communicated with by communicating pipe with agitator tank, the lateral wall of described agitator tank is arranged with chuck, be equipped with powder feed pipe above described chuck, described powder feed pipe extends to the bottom of agitator tank.
2. cosmetics powder pretreatment unit as claimed in claim 1, it is characterized in that, the top of described agitator tank is also provided with bleeding point and solvent feed mouth.
3. cosmetics powder pretreatment unit as claimed in claim 2, it is characterized in that, be provided with stirring motor between described bleeding point and solvent feed mouth, described stirring motor is provided with the paddle extending to agitator tank inside.
4. cosmetics powder pretreatment unit as claimed in claim 2, it is characterized in that, the bottom of described agitator tank is also provided with leakage fluid dram.
5. cosmetics powder pretreatment unit as claimed in claim 1, it is characterized in that, the top of described filtering tank is provided with mixture export, and the bottom of filtering tank is provided with slag-drip opening.
6. the cosmetics powder pretreatment unit as described in claim 1 or 5, is characterized in that, be also filled with filter medium in described filtering tank.
7. cosmetics powder pretreatment unit as claimed in claim 6, it is characterized in that, described filter medium is filter bag or ceramic membrane; The aperture of described filter bag is 100 ~ 800 orders, and the aperture of described ceramic membrane is 0.03 ~ 2 μm.
8., based on a preprocess method for cosmetics powder pretreatment unit described in any one in claim 1 ~ 7, it is characterized in that, comprise the steps:
Add solvent by solvent feed mouth, make the liquid level of solvent be not less than powder feed pipe and extend to minimum point in agitator tank;
Regulate vacuum, by powder feed pipe by powder suction agitator tank;
Start stirring motor, paddle starts to be uniformly mixed, and obtains initial feed liquid;
Vacuumize by described initial feed liquid by communicating pipe input filtering tank, through the filtration of filter medium, supernatant is flowed out by mixture export, and collect, waste residue is discharged by slag-drip opening.
9. preprocess method as described in claim 8, it is characterized in that, the consumption of described solvent is 10 ~ 200 times of powder quality.
10. preprocess method as described in claim 8, it is characterized in that, the stir speed (S.S.) of described paddle is 30 ~ 200r/min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510847634.5A CN105311986A (en) | 2015-11-26 | 2015-11-26 | Cosmetic powder pretreatment device and pretreatment method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510847634.5A CN105311986A (en) | 2015-11-26 | 2015-11-26 | Cosmetic powder pretreatment device and pretreatment method |
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| CN105311986A true CN105311986A (en) | 2016-02-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201510847634.5A Pending CN105311986A (en) | 2015-11-26 | 2015-11-26 | Cosmetic powder pretreatment device and pretreatment method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107790088A (en) * | 2017-10-30 | 2018-03-13 | 四川爱尔西科技有限公司 | A kind of manufacturing equipment for environmental protection catalyst |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202823229U (en) * | 2012-08-31 | 2013-03-27 | 杨洪永 | Closed type liquid filter |
| CN203777986U (en) * | 2014-04-04 | 2014-08-20 | 广州艾科化学有限公司 | Surface active agent mixing and dispersing device |
| CN104607091A (en) * | 2014-12-04 | 2015-05-13 | 佛山市特赛化工设备有限公司 | Vacuum powder charging method capable of not raising dust during discharging |
| JP3199107U (en) * | 2015-05-26 | 2015-08-06 | 日本富升環保開発 有限会社 | Solution preparation equipment |
| CN205146054U (en) * | 2015-11-26 | 2016-04-13 | 上海清轩生物科技有限公司 | Cosmetics powder preprocessing device |
-
2015
- 2015-11-26 CN CN201510847634.5A patent/CN105311986A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202823229U (en) * | 2012-08-31 | 2013-03-27 | 杨洪永 | Closed type liquid filter |
| CN203777986U (en) * | 2014-04-04 | 2014-08-20 | 广州艾科化学有限公司 | Surface active agent mixing and dispersing device |
| CN104607091A (en) * | 2014-12-04 | 2015-05-13 | 佛山市特赛化工设备有限公司 | Vacuum powder charging method capable of not raising dust during discharging |
| JP3199107U (en) * | 2015-05-26 | 2015-08-06 | 日本富升環保開発 有限会社 | Solution preparation equipment |
| CN205146054U (en) * | 2015-11-26 | 2016-04-13 | 上海清轩生物科技有限公司 | Cosmetics powder preprocessing device |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107790088A (en) * | 2017-10-30 | 2018-03-13 | 四川爱尔西科技有限公司 | A kind of manufacturing equipment for environmental protection catalyst |
| CN107790088B (en) * | 2017-10-30 | 2024-01-26 | 金华市达生机电有限公司 | Manufacturing equipment for environment-friendly catalyst |
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Application publication date: 20160210 |