CN203582771U - Continuous preparation device of polymerized whey protein powder - Google Patents
Continuous preparation device of polymerized whey protein powder Download PDFInfo
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- CN203582771U CN203582771U CN201320772827.5U CN201320772827U CN203582771U CN 203582771 U CN203582771 U CN 203582771U CN 201320772827 U CN201320772827 U CN 201320772827U CN 203582771 U CN203582771 U CN 203582771U
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- polymerization
- drying tower
- protein powder
- whey protein
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Abstract
The utility model provides a continuous preparation device of polymerized whey protein powder, and relates to whey protein powder production equipment. The device comprises a polymerization reaction tank, a vacuum concentration device and a spray drying tower, wherein the polymerization reaction tank is sequentially connected with the vacuum concentration device and the spray drying tower; an automatic temperature pH regulator is arranged at the bottom of the polymerization reaction tank; the spray drying tower is connected with an air heater. The stacked combination structure from the polymerization reaction tank to a condition controller and the spray drying tower is adopted, so that the polymerization, the concentration and the drying of whey proteins are continuously and automatically carried out. Thus, the polymerization, the concentration and the drying of the polymerized whey protein powder are realized. The concentration process is carried out twice, so that the production efficiency of the polymerized whey protein powder is effectively improved. Therefore, the working performance is improved and the production time is shortened. As a result, the continuity of the polymerization and the drying of the whey proteins is realized. Meanwhile, the device is simple to operate and convenient to use.
Description
Technical field
The utility model relates to a kind of lactalbumin powder production unit, particularly a kind of polymerization lactalbumin powder continuous preparation device.
Background technology
Whey-protein is a kind of main protein in milk, and its content is only second to casein, accounts for the 18-20% of protein quality in milk.Whey-protein has higher nutritive value and functional performance, is widely used in foodstuffs industry all the time.The U.S. reaches 3,300 ten thousand tons owing to making the whey that cheese produces every year, and the whole world reaches 11,000 ten thousand tons, only has 55% whey further to be processed in the U.S..Process whey very difficult, and expense is high, because it has very high BOD value.Produce new high value added product very important to the development of whey-protein.At present, lactalbumin powder is the major auxiliary burden of infant formula powder, in addition, also has the report that whey-protein is applied to sports beverages and fast food.Generally speaking, the protein of polymerization has higher thermostability.And the polymerization of whey-protein can increase the functional performances such as thermostability of protein.Although the polymkeric substance of gained has very large molecular weight, due to the decline of its surface hydrophobicity, in water, be soluble, and emulsifying property, foaminess are all significantly improved.In the technology of producing at existing lactalbumin powder, great majority are all intermittent operations, and especially polygalacto white protein needed through polyreaction before dry, caused equipment continuity poor, and need to regulate and control reaction conditions, thereby affect the further raising of production efficiency.
Utility model content
For the deficiency of existing similar reactor, the utility model design is made improvement to its structure, designed a kind of after polymerization the equipment of the production polymerization lactalbumin powder of continuous and automatic.
Polymerization lactalbumin powder continuous preparation device of the present utility model comprises polyreaction tank, vacuum concentrating apparatus, spray-drying tower, polyreaction tank is connected with vacuum concentrating apparatus, spray-drying tower, cyclonic separator successively, the bottom of polyreaction tank is provided with temperature pH self-operated regulator, and spray-drying tower is connected with airheater.
In said apparatus, also comprise ultra-filtration equipment, described ultra-filtration equipment is arranged on polyreaction tank ingress.
In said apparatus, also comprise cyclonic separator, described cyclonic separator is connected with spray-drying tower through pipeline, and cyclonic separator is connected with last gas fly-ash separator.
The utility model adopts the stack combinations structure to condition controller and spray-drying tower by polyreaction tank, and the polymerization that makes whey-protein is with concentrated and dryly automatically carry out continuously, has realized the polymerization, concentrated and be dried of product.This device is mainly applicable to the albuminised continuous automatic production of polygalacto, also can be used for the automatic production that various and polymerization lactalbumin powder are produced similar polymerization, concentrated, drying products simultaneously.Set system parameter, after stock liquid is entered, through a series of, automatically react and directly just can collect product continuously.The utility model can improve the production efficiency of polymerization lactalbumin powder effectively via twice concentration process, improves serviceability and shortens the production time, has realized the polymerization of whey-protein and dry serialization, and this device is simple to operate, easy to use simultaneously.
Accompanying drawing explanation
Fig. 1 is the structural representation of polymerization lactalbumin powder continuous preparation device of the present utility model, in figure: 1-whey stock liquid, 2-ultra-filtration equipment, 3-polyreaction tank, 4-temperature pH self-operated regulator, 5-vacuum concentrating apparatus, 6-air filter, 7-blower fan, 8-airheater, 9-spray-drying tower, 10-cyclonic separator, 11-end gas fly-ash separator, 12-spray-drying tower discharge port, 13-cyclonic separator discharge port.
Embodiment
Below in conjunction with accompanying drawing, technical scheme of the present invention is further described; but be not limited to this; every technical solution of the present invention is modified or is equal to replacement, and not departing from the spirit and scope of technical solution of the present invention, all should be encompassed in protection scope of the present invention.
As shown in Figure 1, polymerization lactalbumin powder continuous preparation device of the present utility model comprises ultra-filtration equipment 2, polyreaction tank 3, vacuum concentrating apparatus 5, spray-drying tower 9, cyclonic separator 10, polyreaction tank 3 is connected with vacuum concentrating apparatus 5, spray-drying tower 9, cyclonic separator 10 successively, the ingress of polyreaction tank 3 is provided with ultra-filtration equipment 2, the bottom of polyreaction tank 3 is provided with temperature pH self-operated regulator 4, spray-drying tower 9 is connected with airheater 8, and cyclonic separator 10 is connected with last gas fly-ash separator 11.
Whey stock liquid 1 concentrated solution after ultra-filtration equipment 2 is processed enters polyreaction tank 3, under applicable temperature and pH condition, carry out polyreaction, realize the polymerization of whey-protein, polygalacto white protein enters in spray-drying tower 9 after vacuum concentrating apparatus 8 is further concentrated again, after the finished product of super-dry is via spray-drying tower discharge port 12 or the gas solid separation that realizes product through cyclonic separator 10, by cyclonic separator discharge port 13, is discharged.
Claims (4)
1. polymerization lactalbumin powder continuous preparation device, it is characterized in that described device comprises polyreaction tank, vacuum concentrating apparatus, spray-drying tower, polyreaction tank is connected with vacuum concentrating apparatus, spray-drying tower successively, the bottom of polyreaction tank is provided with temperature pH self-operated regulator, and spray-drying tower is connected with airheater.
2. polymerization lactalbumin powder continuous preparation device according to claim 1, is characterized in that described device also comprises ultra-filtration equipment, and ultra-filtration equipment is arranged on polyreaction tank ingress.
3. polymerization lactalbumin powder continuous preparation device according to claim 1 and 2, is characterized in that described device also comprises cyclonic separator, and cyclonic separator is connected with spray-drying tower through pipeline.
4. polymerization lactalbumin powder continuous preparation device according to claim 3, is characterized in that described cyclonic separator is connected with last gas fly-ash separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320772827.5U CN203582771U (en) | 2013-11-29 | 2013-11-29 | Continuous preparation device of polymerized whey protein powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320772827.5U CN203582771U (en) | 2013-11-29 | 2013-11-29 | Continuous preparation device of polymerized whey protein powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203582771U true CN203582771U (en) | 2014-05-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320772827.5U Expired - Fee Related CN203582771U (en) | 2013-11-29 | 2013-11-29 | Continuous preparation device of polymerized whey protein powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203582771U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106172875A (en) * | 2016-08-26 | 2016-12-07 | 浙江奇异鸟生物科技有限公司 | A kind of whey powder preparation method |
-
2013
- 2013-11-29 CN CN201320772827.5U patent/CN203582771U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106172875A (en) * | 2016-08-26 | 2016-12-07 | 浙江奇异鸟生物科技有限公司 | A kind of whey powder preparation method |
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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: 20140507 Termination date: 20141129 |
|
| EXPY | Termination of patent right or utility model |