CN201188850Y - Foremilk degerming, concentrating integrated equipment - Google Patents
Foremilk degerming, concentrating integrated equipment Download PDFInfo
- Publication number
- CN201188850Y CN201188850Y CNU2008200360149U CN200820036014U CN201188850Y CN 201188850 Y CN201188850 Y CN 201188850Y CN U2008200360149 U CNU2008200360149 U CN U2008200360149U CN 200820036014 U CN200820036014 U CN 200820036014U CN 201188850 Y CN201188850 Y CN 201188850Y
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- membrane filter
- colostrum
- cylinder
- filter
- degerming
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Abstract
The utility model discloses a colostrum degerming and condensing device, which belongs to a membrane device. The device comprises a filtration system, a collecting system, wherein the filtration system is connected with the collecting system by a pipeline; the filtration system is a membrane filter; the membrane filter comprises a set of primary membrane filters and a set of secondary membrane filters; and discharge ports of the primary membrane filters are connected with feeding ports of the secondary membrane filters. The primary membrane filters are used for degerming, and the secondary membrane filters are used for condensing and removing water. The colostrum degerming and condensing device has the advantages of reasonable installation and manufacture, convenient operation, and reliable use.
Description
Technical field
The utility model device relates to a kind of film device, relates to particularly to remove just Ruzhong bacterium and the ceramic membrane complexes concentrated to colostrum.
Background technology
In the present colostrum freeze-drying powder production technique, radiation treatment has been used in sterilization, and irradiation can make the active component inactivation in Ruzhong just in kill microorganisms; In the present colostrum freeze-drying powder production technique, stoste is not concentrated, when freeze drying, sublimation drying is elongated, and the freeze drying power consumption strengthens, and freeze-dried powder moisture is higher, and colostrum freeze-dried powder quality is low.
Summary of the invention
The degerming of the utility model colostrum, be condensed into the covering device application aims and be to overcome above-mentioned deficiency, and a kind of cold degerming is provided, concentrate the device that anhydrates.Through the stoste that degerming is anhydrated, when being used for freeze drying, sublimation drying shortens, and the freeze drying power consumption reduces significantly.Concrete technical scheme is as follows:
A kind of colostrum degerming, be condensed into covering device, comprise filtration system, gathering system, filtration system is connected with gathering system by pipeline, and described filtration system is a film filter, and film filter comprises one group of primary membrane filter and one group of secondary membrane filter; The discharging opening of primary membrane filter connects the feeding mouth of secondary membrane filter.The primary membrane filter is a degerming usefulness, and the secondary membrane filter is to concentrate the usefulness of anhydrating.
Be connected with raw cylinder before the described primary membrane filter, be provided with milk pump between raw cylinder and the primary membrane filter; Be connected with feed pipe on the raw cylinder, feed pipe is provided with valve; Also connect the feed back pipe on the raw cylinder, the other end of feed back pipe connects the liquid outlet of damming of primary membrane filter.The discharging opening of secondary membrane filter is connected vacuum system with the liquid outlet of damming.
Damming of secondary membrane filter is provided with the collecting colostrum cylinder between liquid outlet and the vacuum system, and damming of collecting colostrum cylinder and this film filter also is provided with magnetic valve between the liquid outlet; Be provided with between the discharging opening of secondary membrane filter and the vacuum system and produce the liquid collection cylinder, connect milk pump and liquid level control lever on this collection cylinder, the output of liquid level control lever connects milk pump start-up control end.
Also be provided with airtight collection cylinder between the feeding mouth of the discharging opening of primary membrane filter and secondary membrane filter; Be provided with magnetic valve between the feeding mouth of collection cylinder and secondary membrane filter; Collection cylinder is provided with the liquid level control lever, and the output magnetic valve of liquid level control lever control connects opens control end.
Described film filter is the ceramic membrane filter device.The aperture of the ceramic membrane of described elementary ceramic membrane filter device is 1.2～1.4um; The aperture of the ceramic membrane of described secondary ceramic membrane filter device is to be not more than 50nm.
On the collection cylinder on the described film filter, on the collecting colostrum cylinder, between primary membrane filter and the secondary membrane filter and all be provided with hand-operated valve between this collection cylinder and the primary membrane filter.
It is that 1.2 ~ 1.4um ceramic membrane can be removed most bacteriums that the degerming of the utility model colostrum, the advantage that is condensed into covering device are to select the aperture, meets the food hygiene requirement.Greatly avoid simultaneously radiation sterilizing to give the injury that active component is brought of first Ruzhong; Selecting the aperture is the 50nm ceramic membrane, and the thickening efficiency height that anhydrates when being used for freeze drying, can reduce power consumption, improves the freeze-dried powder quality.The utility model device manufacturing installation is reasonable, easy to operate, use is reliable.
Description of drawings
Fig. 1 is the utility model device schematic diagram
Fig. 2 is the utility model mounting ceramics film film rod structure cutaway view
Among Fig. 1, raw cylinder 1, feed pipe 2, hand-operated valve 3,7,8,10,15,16,25, magnetic valve 11 contains the magnetic valve 18 of the time relay, milk pump (1.1Kw) 5, milk pump (0.75Kw) 21, elementary ceramic membrane filter device 9, secondary ceramic membrane filter 17, collection cylinder 13, production liquid collection cylinder 22, collecting colostrum cylinder 24, liquid level control lever 14,20, stainless steel feed and exhaust tube 4,6,12,23, vacuum system 26, vacuum tube 19
Among Fig. 2, contain the filter end cap 27 of screw thread, filter stainless steel casing 28, filter membrane post 29, filter membrane post holder 30, feeding mouth 31, discharging opening 32, the liquid that dams outlet 33, filter sealed silicon rubber cushion 34,35, Butterworth Hatch and valve 36.
The specific embodiment
The combination accompanying drawing further specifies the utility model device below:
Among the embodiment, the utility model comprises filtration system, gathering system, and filtration system is connected with gathering system by pipeline, and described filtration system is a film filter, and film filter comprises one group of primary membrane filter 9 and one group of secondary membrane filter 17; The discharging opening 32 of primary membrane filter 9 connects the feeding mouth 31 of secondary membrane filter.
Be connected with raw cylinder 1 before the described primary membrane filter 9, be provided with milk pump 5 between raw cylinder 1 and the primary membrane filter 9; Be connected with feed pipe 2 on the raw cylinder 1, feed pipe 2 is provided with hand-operated valve 3; Also connect feed back pipe 4 on the raw cylinder 1, the other end of feed back pipe 4 connects the liquid outlet 33 of damming of primary membrane filter 9.The discharging opening 32 of secondary membrane filter is connected vacuum system 26 with the liquid outlet 33 of damming.
Damming of secondary membrane filter 17 is provided with collecting colostrum cylinder 24 between liquid outlet 33 and the vacuum system 26, and damming of collecting colostrum cylinder 24 and this film filter 17 also is provided with the magnetic valve 18 that contains the time relay between the liquid outlet 33; Be provided with between the discharging opening 32 of secondary membrane filter 17 and the vacuum system 26 and produce liquid collection cylinder 22, connect milk 21 pumps and liquid level control lever 20 on this collection cylinder, the output of liquid level control lever 20 connects milk pump 21 start-up control ends.
Also be provided with airtight collection cylinder 13 between the discharging opening 32 of primary membrane filter 9 and the feeding mouth 31 of secondary membrane filter; Be provided with magnetic valve 11 between the feeding mouth of collection cylinder 13 and secondary membrane filter 17; Collection cylinder 13 is provided with liquid level control lever 14, and the control output end of liquid level control lever 14 connects the unlatching control end of magnetic valve 11.Described film filter is the ceramic membrane filter device.The aperture of the ceramic membrane of described elementary ceramic membrane filter device 9 is 1.3um; The aperture of the ceramic membrane of described secondary ceramic membrane filter device is 50nm.
On the collection cylinder on the described film filter, on the collecting colostrum cylinder, between primary membrane filter and the secondary membrane filter and all be provided with hand-operated valve between this collection cylinder and the primary membrane filter.
In this example, this device comprises except above-mentioned explanation: frame, pipe-line system, ceramic membrane filter system, milk pump gathering system, valve system, vacuum system, colostrum are produced the liquid collection cylinder.Frame is used for fixing pipe-line system, ceramic membrane filter system, milk pump gathering system etc., for stainless steel material is made; Pipe-line system is used to connect vacuum system, gathering system, ceramic membrane filter system, is used to conduct vacuum and liquid, and pipeline is made of 316 stainless steel tubes of Ф 51, Ф 38; The ceramic membrane filter system comprises two groups of film filters, and film filter is made of base, ceramic membrane filter post, end cap, seal.The milk pump gathering system comprises collection cylinder, liquid level control lever and stainless steel sanitary pump composition; Valve system is used for the control of pipeline liquid flow, and two kinds of hand-operated valve and magnetic valves are arranged, and hand-operated valve is a stainless steel material; Vacuum system provides liquid flow power, and vavuum pump is 800L/ hour for revolving living formula vacuum pump, is furnished with air cleaner, voltage-stablizer, guarantees the stable and health of vacuum.
The degerming of the utility model colostrum, be condensed into two groups of film filters of covering device, one group of film filter is joined membrane aperture a 1.2～1.4um, film column diameter 40mm, the ceramic membrane filter post of film column length 1.06m; Another group film filter is joined a membrane aperture 50nm, film column diameter 40mm, the ceramic membrane filter post of film column length 1.06m.
Among Fig. 1, raw cylinder 1, feed pipe 2, hand-operated valve 3,7,8,10,15,16,25, magnetic valve 11 contains the magnetic valve 18 of the time relay, milk pump (1.1Kw) 5, milk pump (0.75Kw) 21, elementary ceramic membrane filter device 9, secondary ceramic membrane filter 17, collection cylinder 13, production liquid collection cylinder 22, collecting colostrum cylinder 24, liquid level control lever 14,20, stainless steel feed and exhaust tube 4,6,12,23, vacuum system 26, vacuum tube 19
Among Fig. 2, contain the filter end cap 27 of screw thread, filter stainless steel casing 28, filter membrane post 29, filter membrane post holder 30, feeding mouth 31, discharging opening 32, the liquid that dams outlet 33, filter sealed silicon rubber cushion 34,35, Butterworth Hatch and valve 36.
When the utility model used, operation one is the degerming process: this process was a power with milk pump 5, and raw material is pressed into ceramic membrane filter device 9, must set intermediate after filtration.Open hand-operated valve 3, add pending colostrum in raw cylinder, open milk pump 5, open hand-operated valve 8,10, regulate hand-operated valve 8 (this valve is established third gear) control feed back amount, this moment, colostrum was filtered by ceramic membrane filter device 9.Ceramic membrane is held back (liquid) thing and is flowed along film pipeline direction, and filtrate and trapped substance trend are vertical direction, and filter 9 has been used aperture 1.3um ceramic membrane, and therefore, the filtrate of ceramic membrane filter device 9 is the working solution of degerming, is discharged in the collection cylinder 13 by discharge nozzle 12.Simultaneously, holding back (liquid) gets back in the raw cylinder 1 along feed back pipe 4.Operation two is to concentrate the process of anhydrating: this process is a power with the negative pressure that vacuum system 26 work produce, and draws working solutions from collection cylinder 13, gets target product after filtration.Collection cylinder 13 is normal pressure sealing cylinder, when the working solution liquid level rising of degerming reaches working depth, liquid level control lever 14 closures, magnetic valve 11 is connected, collection cylinder 13 is connected with ceramic membrane filter device 17 feeding mouths, the working solution of degerming sucks ceramic membrane filter device 17, filter 17 has been used aperture 50nm ceramic membrane, and therefore, the filtrate of ceramic membrane filter device 17 is based on water, suck collection cylinder 22 through discharge nozzle 23, starting or stoping of milk pump 21 is subjected to 20 controls of liquid level control lever, and liquid level rises when reaching working depth, liquid level control lever closure, the milk pump startup is outside the water discharge system in the collection cylinder 22.Simultaneously, magnetic valve 18 is connected, and aseptic colostrum concentrate sucks collection cylinder 24, and because of magnet valve 18 has connected the adjustable time relay, the working time can be according to raw material and Product Status adjustment.Because of the second operation power source is a negative pressure, guaranteed that bacteria-removing liquid continues the health level of processing.
Claims (8)
1, a kind of colostrum degerming, is condensed into covering device, comprise filtration system, gathering system, filtration system is connected with gathering system by pipeline, it is characterized in that described filtration system is a film filter, and film filter comprises one group of primary membrane filter and one group of secondary membrane filter; The discharging opening of primary membrane filter connects the feeding mouth of secondary membrane filter; The discharging opening of secondary membrane filter connects gathering system.
2, colostrum degerming according to claim 1, be condensed into covering device, it is characterized in that described film filter is the ceramic membrane filter device.
3, colostrum degerming according to claim 1 and 2, be condensed into covering device, it is characterized in that being connected with raw cylinder before the described primary membrane filter, be provided with milk pump between raw cylinder and the primary membrane filter; Be connected with feed pipe on the raw cylinder, feed pipe is provided with valve; Also connect the feed back pipe on the raw cylinder, the other end of feed back pipe connects the liquid outlet of damming of primary membrane filter.
4, colostrum degerming according to claim 3, be condensed into covering device, it is characterized in that the discharging opening of secondary membrane filter is connected vacuum system with the liquid outlet of damming.
5, colostrum degerming according to claim 4, be condensed into covering device, it is characterized in that described gathering system comprises the collecting colostrum cylinder; Damming of secondary membrane filter is provided with the collecting colostrum cylinder between liquid outlet and the vacuum system, and damming of collecting colostrum cylinder and this film filter also is provided with magnetic valve between the liquid outlet; Be provided with between the discharging opening of secondary membrane filter and the vacuum system and produce the liquid collection cylinder, connect milk pump and liquid level control lever on this collection cylinder, the output of liquid level control lever connects milk pump start-up control end.
6, colostrum degerming according to claim 5, be condensed into covering device, it is characterized in that also being provided with airtight collection cylinder between the feeding mouth of the discharging opening of primary membrane filter and secondary membrane filter; Be provided with magnetic valve between the feeding mouth of collection cylinder and secondary membrane filter; Collection cylinder is provided with the liquid level control lever, and the output magnetic valve of liquid level control lever control connects opens control end.
7, colostrum degerming according to claim 6, be condensed into covering device, the aperture that it is characterized in that the ceramic membrane of described elementary ceramic membrane filter device is 1.2～1.4um; The aperture of the ceramic membrane of described secondary ceramic membrane filter device is to be not more than 50nm.
8, colostrum degerming according to claim 7, be condensed into covering device, it is characterized in that on the described film filter, on the collection cylinder on the collecting colostrum cylinder, between primary membrane filter and the secondary membrane filter and all be provided with hand-operated valve between this collection cylinder and the primary membrane filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200360149U CN201188850Y (en) | 2008-05-22 | 2008-05-22 | Foremilk degerming, concentrating integrated equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008200360149U CN201188850Y (en) | 2008-05-22 | 2008-05-22 | Foremilk degerming, concentrating integrated equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201188850Y true CN201188850Y (en) | 2009-02-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008200360149U Expired - Fee Related CN201188850Y (en) | 2008-05-22 | 2008-05-22 | Foremilk degerming, concentrating integrated equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201188850Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111213712A (en) * | 2019-10-23 | 2020-06-02 | 内蒙古蒙牛乳业（集团）股份有限公司 | Concentration method and apparatus |
-
2008
- 2008-05-22 CN CNU2008200360149U patent/CN201188850Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111213712A (en) * | 2019-10-23 | 2020-06-02 | 内蒙古蒙牛乳业（集团）股份有限公司 | Concentration method and apparatus |
| CN111213712B (en) * | 2019-10-23 | 2023-09-19 | 内蒙古蒙牛乳业（集团）股份有限公司 | Concentration method and apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090204 Termination date: 20120522 |