CN202635524U - Development integration pilot scale equipment for livestock ossein and derivative thereof - Google Patents
Development integration pilot scale equipment for livestock ossein and derivative thereof Download PDFInfo
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- CN202635524U CN202635524U CN2012202625583U CN201220262558U CN202635524U CN 202635524 U CN202635524 U CN 202635524U CN 2012202625583 U CN2012202625583 U CN 2012202625583U CN 201220262558 U CN201220262558 U CN 201220262558U CN 202635524 U CN202635524 U CN 202635524U
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Abstract
The utility model discloses development integration pilot scale equipment for livestock ossein and derivative thereof, which comprises a cage, a deslagging hopper, an extraction tank, a concentrator, a vacuum system and a multifunctional blending tank, wherein the cage can be arranged on the deslagging hopper and in the extraction tank; the deslagging hole of the deslagging hopper is communicated with a colloid mill; after being connected with a duplex strainer, the colloid mill is communicated with the multifunctional blending tank; the bottom outlet of the extraction tank is communicated with the concentrator by a circulating tank and the duplex strainer successively; the bottom outlet of the concentrator is communicated with the multifunctional blending tank; and the multifunctional blending tank is connected with the vacuum system. The pilot scale equipment has the advantages of good integrality and flexibility, reasonable integral design structure, perfect internal pipeline installation, small investment, low energy consumption cost, good operation convenience, reasonable and attractive appearance design and small land occupation, and single equipment has an advanced structure which is consistent with a big production line and can embody real production data.
Description
Technical field
The utility model relates to a kind of livestock and poultry ossein and derivative is developed integrated pilot plant.
Background technology
At present, domestic ossein manufacturer does not all have the complete pilot production line of whole piece, can not test according to the technique of big scale production equipment.What have is extractor or the retort of monomer often, can not realize the from front to back simulation production of whole production line.If exploitation new product or exploration new technology need to be carried out with large production equipment, can waste time and energy.
The utility model content
The purpose of this utility model provides a kind of livestock and poultry ossein and derivative is developed integrated pilot plant.
A kind of livestock and poultry ossein provided by the utility model and derivative thereof are developed integrated pilot plant, comprise cage, deslagging bucket, extracting tank, inspissator, vacuum system and Multifunctional blending tank;
Described cage can be arranged on the described deslagging bucket and described extracting tank in; The slag-drip opening of described deslagging bucket is connected with colloid mill; After being connected with duplex strainer, described colloid mill is connected with described Multifunctional blending tank;
The outlet at bottom of described extracting tank is connected with described inspissator by circulating pump and duplex strainer successively;
The outlet at bottom of described inspissator is connected with described Multifunctional blending tank;
Described Multifunctional blending tank is connected with described vacuum system.
In the above-mentioned pilot plant, described extracting tank can be connected with air compressor, when the liquid in the described extracting tank can not be pumped in the described inspissator fully, can residual liquid be blown to described inspissator by the compressed air that described air compressor produces.
In the above-mentioned pilot plant, described extracting tank can be the jacket type extracting tank, can realize the temperature of described extracting tank is controlled by vapor recycle and condensate water circulatory.
In the above-mentioned pilot plant, described Multifunctional blending tank can be connected with condenser, can carry out Maillard reaction fragrance this moment and reclaim.
In the above-mentioned pilot plant, described Multifunctional blending tank can be connected with homogenizer, can make material more even.
In the above-mentioned pilot plant, described Multifunctional blending tank can be connected with emulsification pump by duplex strainer, can making material more even, and can filter out hard thing impurity to protect described emulsification pump.
In the above-mentioned pilot plant, described Multifunctional blending tank can be connected with spray tower by peristaltic pump, to produce power-product.
The utlity model has following advantage: this pilot plant configuration integrity, flexibility are good, and global design internal duct rational in infrastructure is installed perfect, and the single devices structure is advanced can to embody true creation data with production line is consistent greatly; And the advantages such as it is little to have investment, and energy consumption cost is low, and operation ease is good, and configuration design is rationally attractive in appearance, and floor space is little.
Description of drawings
The structural representation of the pilot plant that Fig. 1 provides for the utility model, each mark is as follows among the figure: 1 cage, 2 deslagging buckets, 3 extracting tanks, 4 inspissators, 5 vacuum systems, 6 Multifunctional blending tanks, 7 colloid mills, 81,82,83 duplex strainers, 9 circulating pumps, 10 condensers, 11 homogenizers, 12 emulsification pumps, 13 peristaltic pumps, 14 spray towers.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further, but the utility model is not limited to following examples.
The livestock and poultry ossein that the utility model provides and derivative thereof are developed integrated pilot plant and are comprised cage 1, deslagging bucket 2, extracting tank 3, inspissator 4, vacuum system 5 and Multifunctional blending tank 6; Cage 1 can be arranged on and carry out deslagging on the deslagging bucket 2, can be placed in the extracting tank 3 and extract; The slag-drip opening of deslagging bucket 2 is connected with colloid mill 7, and the slag of 7 pairs of discharges of colloid mill grinds; Be connected with Multifunctional blending tank 6 after colloid mill 7 is connected with duplex strainer 81, react thereby enter Multifunctional blending tank 6 after residue grinds through colloid mill 7; Extracting tank 3 is the jacket type extracting tank, can realize the temperature of extracting tank 3 is controlled by vapor recycle and condensate water circulatory; This extracting tank 3 also is connected with the air compressor (not shown), when the liquid in the extracting tank 3 can not be pumped in the inspissator 4 fully, can residual liquid be blown to inspissator 4 by the compressed air that air compressor produces, to reduce loss of material; The outlet at bottom of extracting tank 3 is connected with inspissator 4 by circulating pump 9 and duplex strainer 82 successively, and the extract in the extracting tank 4 concentrates through entering in the inspissator 4 after the filtration of duplex strainer 82; The outlet at bottom of inspissator 4 is connected with Multifunctional blending tank 6, and Multifunctional blending tank 6 is connected with vacuum system 5, extract through be concentrated to need concentration after, react in the material inspiration Multifunctional blending tank 6 that uses the vacuum of vacuum system 5 to concentrate; Multifunctional blending tank 6 also is connected with condenser 10, reclaims to carry out Maillard reaction fragrance; For making material more even, Multifunctional blending tank 6 also is connected with homogenizer 11, and also is connected with emulsification pump 12 with duplex strainer 83; When producing power-product, Multifunctional blending tank 6 is connected with spray tower 14 by peristaltic pump 13.
When simulation was produced, the bone after pulverizing of packing in cage 1 maybe needed the material that extracts, after packing into cage 1 is put into extracting tank 3, closed heat temperature raising behind the lid, extracted; ON cycle pump 9 circulates in the leaching process, guarantees extracting tank 3 interior feed liquids fully and mixing of materials; After extraction is finished, cage 1 is placed on deslagging on the deslagging bucket 2; After the slag of discharging grinds through colloid mill 7, after entering Multifunctional blending tank 6 after duplex strainer 81 filtrations, carry out next procedure;
82 filtrations enter into inspissator 4 through duplex strainer to extract the extract that generates in the extracting tank 3, under the effect of vacuum, and quick concentrated extracting solution under inspissator 4 low temperature; Be concentrated to need concentration after, use in the material inspiration Multifunctional blending tank 6 that the vacuum of vacuum system 5 will concentrate; If in the time of need to carrying out the recovery of Maillard reaction fragrance, open cold condenser 10; Allocation process need to recycle with homogenizer 11 and emulsification pump 12, can allow material more even; When producing power-product, the peristaltic pump 13 of extracting tank 3 interior materials by spray tower 14 entered into spray tower 14 sprays become dry powder.
Claims (7)
1. a livestock and poultry ossein and derivative thereof are developed integrated pilot plant, and it is characterized in that: it comprises cage, deslagging bucket, extracting tank, inspissator, vacuum system and Multifunctional blending tank;
Described cage can be arranged on the described deslagging bucket and described extracting tank in; The slag-drip opening of described deslagging bucket is connected with colloid mill; After being connected with duplex strainer, described colloid mill is connected with described Multifunctional blending tank;
The outlet at bottom of described extracting tank is connected with described inspissator by circulating pump and duplex strainer successively;
The outlet at bottom of described inspissator is connected with described Multifunctional blending tank;
Described Multifunctional blending tank is connected with described vacuum system.
2. pilot plant according to claim 1, it is characterized in that: described extracting tank is connected with air compressor.
3. pilot plant according to claim 1 and 2, it is characterized in that: described extracting tank is the jacket type extracting tank.
4. pilot plant according to claim 1 and 2, it is characterized in that: described Multifunctional blending tank is connected with condenser.
5. pilot plant according to claim 1 and 2, it is characterized in that: described Multifunctional blending tank is connected with homogenizer.
6. pilot plant according to claim 1 and 2, it is characterized in that: described Multifunctional blending tank is connected with emulsification pump by duplex strainer.
7. pilot plant according to claim 1 and 2, it is characterized in that: described Multifunctional blending tank is connected with spray tower by peristaltic pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202625583U CN202635524U (en) | 2012-06-05 | 2012-06-05 | Development integration pilot scale equipment for livestock ossein and derivative thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012202625583U CN202635524U (en) | 2012-06-05 | 2012-06-05 | Development integration pilot scale equipment for livestock ossein and derivative thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202635524U true CN202635524U (en) | 2013-01-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012202625583U Expired - Fee Related CN202635524U (en) | 2012-06-05 | 2012-06-05 | Development integration pilot scale equipment for livestock ossein and derivative thereof |
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| CN (1) | CN202635524U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103071419A (en) * | 2013-01-30 | 2013-05-01 | 中国农业科学院农产品加工研究所 | Soup stock production equipment preventing fat from floating |
| CN105231380A (en) * | 2015-08-31 | 2016-01-13 | 中国农业科学院农产品加工研究所 | Device and method for gradient concentration by coupling enzyme-membrane method using residual heat for mechanical supercharging |
| CN106261813A (en) * | 2016-08-04 | 2017-01-04 | 河南普乐泰生物科技股份有限公司 | The heating power extraction device of fowl osteotrophy material |
-
2012
- 2012-06-05 CN CN2012202625583U patent/CN202635524U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103071419A (en) * | 2013-01-30 | 2013-05-01 | 中国农业科学院农产品加工研究所 | Soup stock production equipment preventing fat from floating |
| CN103071419B (en) * | 2013-01-30 | 2015-07-08 | 中国农业科学院农产品加工研究所 | Soup stock production equipment preventing fat from floating |
| CN105231380A (en) * | 2015-08-31 | 2016-01-13 | 中国农业科学院农产品加工研究所 | Device and method for gradient concentration by coupling enzyme-membrane method using residual heat for mechanical supercharging |
| CN105231380B (en) * | 2015-08-31 | 2018-12-25 | 中国农业科学院农产品加工研究所 | The device and method of gradient centrifugation is carried out using waste heat engine driven supercharging conjugate enzyme embrane method |
| CN106261813A (en) * | 2016-08-04 | 2017-01-04 | 河南普乐泰生物科技股份有限公司 | The heating power extraction device of fowl osteotrophy material |
| CN106261813B (en) * | 2016-08-04 | 2019-07-16 | 河南普乐泰生物科技股份有限公司 | The heating power extraction device of fowl osteotrophy substance |
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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: 20130102 Termination date: 20140605 |