CN203990558U - A kind of preparation system of microcapsules pulvis - Google Patents
A kind of preparation system of microcapsules pulvis Download PDFInfo
- Publication number
- CN203990558U CN203990558U CN201420498070.XU CN201420498070U CN203990558U CN 203990558 U CN203990558 U CN 203990558U CN 201420498070 U CN201420498070 U CN 201420498070U CN 203990558 U CN203990558 U CN 203990558U
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- tank
- spray drying
- drying tower
- oil phase
- preparation system
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- Fats And Perfumes (AREA)
Abstract
The utility model discloses a kind of preparation system of microcapsules pulvis, comprise that water tank, oil phase tank, two inlets connect respectively water tank and the mix and blend tank of oil phase pot bottom liquid outlet, surge tank, homogenizer, collecting tank, spray drying tower and cyclone separator that then pipeline is connected successively.The high embedding of the utility model embedding rate is effective, pulvis good fluidity, particle diameter distribute rationally, can according to different demands, carry out repeatedly homogeneous to mixed mixed liquor; By simple equipment, coordinated and obtained meal and two kinds of products of fine powder, simple in structure, effect is remarkable, when being particularly suitable for microcapsules and preparing, uses.
Description
Technical field
The utility model relates to food additives technology of preparing, more particularly, relates in particular to a kind of preparation system of microcapsules pulvis.
Background technology
At present, product microencapsulation generally adopts press spray seasoning to be prepared, during preparation, just core (oil phase) is scattered in the weak solution of cyst material (water), stirring, shearing make to form emulsion, with pump, this emulsion is delivered in the atomizer of pressure type drying machine (or centrifugal spray dryer), emulsion is atomized into droplet, and in drop, contained solvent evaporates rapidly and makes wall material separate out encystation.
In prior art, produce the preparation system that microcapsules pulvis there is no sizing, the manufacturer of industrialization is home-built equipment, and prepared microcapsules pulvis quality is uneven, ubiquity great number of issues.That, microcapsule powder footpath low such as microcapsules pulvis embedding rate distributes is wide, pulvis poor fluidity etc.
Utility model content
The purpose of this utility model is for above-mentioned the deficiencies in the prior art, provides that the high embedding of a kind of embedding rate is effective, pulvis good fluidity, particle diameter distribute rational microcapsules pulvis preparation system.
The technical solution of the utility model is achieved in that a kind of preparation system of microcapsules pulvis, comprise water tank, oil phase tank, two inlets connect respectively the mix and blend tank of water tank and oil phase pot bottom liquid outlet, the surge tank that then pipeline connects successively, homogenizer, collecting tank, spray drying tower and cyclone separator, between described mix and blend tank and surge tank, be provided with emulsification pump, between described homogenizer and collecting tank and between collecting tank and spray drying tower, be provided with the first peristaltic pump and the second peristaltic pump, an opening established by pipeline between described the first peristaltic pump and collecting tank and pipeline connects temporary tank, described temporary pot bottom outlet is located between surge tank and homogenizer, described spray drying tower and cyclone separator bottom are equipped with powder collector.
As to further improvement of the utility model, between described spray drying tower and cyclone separator, the head end of pipeline is arranged on the middle part of spray drying tower taper tower body.
As to further improvement of the utility model, described water tank and mix and blend tank are anchor formula agitator tank, and described oil phase tank is the jacket canister that electrical heating heats up, and is furnished with autoclave cutter.
The utility model adopts said structure, and embedding rate is high, pulvis good fluidity, particle diameter distribute rationally, and can according to different demands, carry out repeatedly homogeneous to mixed mixed liquor; Can also coordinate and obtain meal and two kinds of products of fine powder by simple equipment; The utility model is simple in structure effective, when being particularly suitable for microcapsules and preparing, uses.
Accompanying drawing explanation
Below in conjunction with the embodiment in accompanying drawing, the utility model is described in further detail, but do not form any restriction of the present utility model.
Fig. 1 is structural representation of the present utility model.
In figure: 1-water tank; 2-oil phase tank; 3-mix and blend tank; 4-surge tank; 5-homogenizer; 6-collecting tank; 7-spray drying tower; 8-cyclone separator; 9-emulsification pump; 10-the first peristaltic pump; 11-the second peristaltic pump; 12-keeps in tank; 13-powder collector.
The specific embodiment
Consult shown in Fig. 1, the preparation system of a kind of microcapsules pulvis of the present utility model, comprise water tank 1, oil phase tank 2, two inlets connect respectively water tank 1 with the mix and blend tank 3 of oil phase tank 2 bottom liquid outlets, surge tank 4, homogenizer 5, collecting tank 6, spray drying tower 7 and cyclone separator 8 that then pipeline is connected successively.Between described mix and blend tank 3 and surge tank 4, be provided with emulsification pump 9, between described homogenizer 5 and collecting tank 6 and between collecting tank 6 and spray drying tower 7, be provided with the first peristaltic pump 10 and the second peristaltic pump 11, an opening established by pipeline between described the first peristaltic pump 10 and collecting tank 6 and pipeline connects temporary tank 12, described temporary tank 12 outlet at bottoms are located between surge tank 4 and homogenizer 5, and described spray drying tower 7 and cyclone separator 8 bottoms are equipped with powder collector 13.
In the utility model, between described spray drying tower 7 and cyclone separator 8, the head end of pipeline is arranged on the middle part of spray drying tower 7 taper tower bodies.
In the utility model, described water tank 1 and mix and blend tank 3 are anchor formula agitator tank, the jacket canister that described oil phase tank 2 heats up for electrical heating, and be furnished with autoclave cutter.
When the utility model is implemented, first the required water material of configuration emulsion is joined in water tank 1 and adds thermal agitation, configuration emulsion required oil phase material is joined and in oil phase tank 2, carries out electrical heating stirring, then according to required proportion, both are joined in mix and blend tank 3 and carry out mix and blend, the thick emulsion obtaining is delivered in surge tank 4 and is waited for homogeneous by emulsification pump 9.According to technique is required, thick emulsion is sent into and in homogenizer 5, carried out homogeneous, the emulsion of first homogeneous is admitted in temporary tank 12 temporary by the first peristaltic pump 10, for tackling different demands, emulsion in temporary tank 12 is carried out to repeatedly homogeneous, the emulsion reaching after requirement is sent in collecting tank 6, through peristaltic pump 11, send in spray drying tower 7 and spray and be dried again, meal is collected hereinto, fine powder is all positioned at the middle part of taper tower body, so pipeline communication cyclone separator 8 is set in the middle, collect fine powder, granulometric impurity is drained by air outlet.
Claims (3)
1. the preparation system of a microcapsules pulvis, comprise water tank, oil phase tank, two inlets connect respectively the mix and blend tank of water tank and oil phase pot bottom liquid outlet, the surge tank that then pipeline connects successively, homogenizer, collecting tank, spray drying tower and cyclone separator, it is characterized in that: between described mix and blend tank and surge tank, be provided with emulsification pump, between described homogenizer and collecting tank and between collecting tank and spray drying tower, be provided with the first peristaltic pump and the second peristaltic pump, an opening established by pipeline between described the first peristaltic pump and collecting tank and pipeline connects temporary tank, described temporary pot bottom outlet is located between surge tank and homogenizer, described spray drying tower and cyclone separator bottom are equipped with powder collector.
2. the preparation system of a kind of microcapsules pulvis according to claim 1, is characterized in that: between described spray drying tower and cyclone separator, the head end of pipeline is arranged on the middle part of spray drying tower taper tower body.
3. the preparation system of a kind of microcapsules pulvis according to claim 1, is characterized in that: described water tank and mix and blend tank are anchor formula agitator tank, and described oil phase tank is the jacket canister that electrical heating heats up, and is furnished with autoclave cutter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420498070.XU CN203990558U (en) | 2014-08-19 | 2014-08-19 | A kind of preparation system of microcapsules pulvis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420498070.XU CN203990558U (en) | 2014-08-19 | 2014-08-19 | A kind of preparation system of microcapsules pulvis |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203990558U true CN203990558U (en) | 2014-12-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420498070.XU Expired - Fee Related CN203990558U (en) | 2014-08-19 | 2014-08-19 | A kind of preparation system of microcapsules pulvis |
Country Status (1)
| Country | Link |
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| CN (1) | CN203990558U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032312A (en) * | 2015-09-02 | 2015-11-11 | 山东省科学院能源研究所 | Equipment for rapidly and continuously manufacturing droplet microspheres and application thereof |
| CN112544731A (en) * | 2020-12-30 | 2021-03-26 | 浙江工业大学 | Preparation process of antarctic krill oil nanoemulsion |
| CN116672962A (en) * | 2023-08-03 | 2023-09-01 | 山东中舜生物科技有限公司 | Preparation equipment and method of microcapsule embedding powder |
-
2014
- 2014-08-19 CN CN201420498070.XU patent/CN203990558U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032312A (en) * | 2015-09-02 | 2015-11-11 | 山东省科学院能源研究所 | Equipment for rapidly and continuously manufacturing droplet microspheres and application thereof |
| CN112544731A (en) * | 2020-12-30 | 2021-03-26 | 浙江工业大学 | Preparation process of antarctic krill oil nanoemulsion |
| CN116672962A (en) * | 2023-08-03 | 2023-09-01 | 山东中舜生物科技有限公司 | Preparation equipment and method of microcapsule embedding powder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141210 Termination date: 20210819 |
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| CF01 | Termination of patent right due to non-payment of annual fee |