CN204637028U - Processing system for reducing peroxide value and anisidine value of fat emulsion - Google Patents
Processing system for reducing peroxide value and anisidine value of fat emulsion Download PDFInfo
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- CN204637028U CN204637028U CN201520253497.8U CN201520253497U CN204637028U CN 204637028 U CN204637028 U CN 204637028U CN 201520253497 U CN201520253497 U CN 201520253497U CN 204637028 U CN204637028 U CN 204637028U
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- tank
- communicated
- pipeline
- homogenizing
- colostrum
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- BHAAPTBBJKJZER-UHFFFAOYSA-N p-anisidine Chemical compound COC1=CC=C(N)C=C1 BHAAPTBBJKJZER-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 150000002978 peroxides Chemical class 0.000 title claims abstract description 16
- 238000012545 processing Methods 0.000 title claims abstract description 11
- 239000002960 lipid emulsion Substances 0.000 title 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 60
- 235000013336 milk Nutrition 0.000 claims abstract description 34
- 239000008267 milk Substances 0.000 claims abstract description 34
- 210000004080 milk Anatomy 0.000 claims abstract description 34
- 210000003022 colostrum Anatomy 0.000 claims abstract description 33
- 235000021277 colostrum Nutrition 0.000 claims abstract description 33
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 29
- 230000004087 circulation Effects 0.000 claims abstract description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 14
- 230000017531 blood circulation Effects 0.000 claims description 8
- 238000000265 homogenisation Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 3
- 235000011187 glycerol Nutrition 0.000 abstract description 2
- 238000003860 storage Methods 0.000 abstract description 2
- 229910001873 dinitrogen Inorganic materials 0.000 abstract 2
- 210000000481 breast Anatomy 0.000 abstract 1
- 238000009924 canning Methods 0.000 abstract 1
- 235000005687 corn oil Nutrition 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 238000006392 deoxygenation reaction Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000004224 protection Effects 0.000 description 3
- 230000036541 health Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000008215 water for injection Substances 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 108010004103 Chylomicrons Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 210000001268 chyle Anatomy 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000002496 gastric effect Effects 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 230000035479 physiological effects, processes and functions Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
Landscapes
- Dairy Products (AREA)
Abstract
The utility model discloses a reduce fat breast peroxide number and anisidine value processing system, it includes oxygen-eliminating device (1), isotropic symmetry (5), homogenizing pump (6), the configuration jar, liquid filling machine (8) and nitrogen gas conveyer pipe (9), nitrogen gas conveyer pipe (9) communicate with each preparation jar respectively, oxygen-eliminating device (1) communicate with glycerine jar (2) and colostrum jar (3) respectively through the pipeline, colostrum jar (3), isotropic symmetry (5), homogenizing pump (6) and isotropic symmetry jar (4) constitute closed circulation autonomous system through the pipeline, isotropic symmetry jar (4) and filling jar (7) intercommunication, filling jar (7) and canning machine (8) intercommunication, filling machine (8) below is provided with a plurality of evacuating device. The utility model has the advantages that: it has the advantages of improving the quality of fat milk, prolonging the storage time of the fat milk and reducing the peroxide value and the anisidine value of the fat milk.
Description
Technical field
This utility model relates to fat milk preparation field, particularly reduces fat milk peroxide value and anisidine value processing system.
Background technology
Fat milk is a kind of not only even but also stable lipomul be made up of refined soybean oil, glycerol, lecithin etc., provides high-energy and required fatty acid under the importance that its is treated is non-bowel provisions.Proved that the fat that human body is taken in first forms Chylomicron through gastrointestinal absorption from physiology and threpsology, and the form of these product is all extremely similar to chyle with composition, directly to the venous patient infusion that can not take food, can provide lipid nutrition.
But, lipomul peroxide value aborning and anisidine value compare and are difficult to control, directly affect product quality and quality, thus jeopardize user health of human body, therefore for ensureing the quality of lipomul, ensure the health of human body of user, the lipomul that peroxide value and anisidine value are all lower must be used.
Utility model content
The purpose of this utility model is the shortcoming overcoming prior art, provides a kind of processing system improving product quality, can reduce fat milk peroxide value and anisidine value.
The purpose of this utility model is achieved through the following technical solutions: reduce fat milk peroxide value and anisidine value processing system, it comprises oxygen-eliminating device, glycerol tank, colostrum tank, homogenizing tank, homogenizer, Homogenizing pump, fill tank, filling machine and nitrogen carrier pipe, described nitrogen carrier pipe respectively with glycerol tank, colostrum tank, homogenizing tank, fill tank is communicated with filling machine, the bypass line that it is communicated with is provided with valve, and described oxygen-eliminating device is communicated with colostrum tank with glycerol tank respectively by pipeline, and described glycerol tank and colostrum tank pass through pipeline communication, and on its pipeline, be provided with bivalve, described colostrum tank, homogenizer, Homogenizing pump and homogenizing tank form closed circulation robot control system(RCS) by pipeline, described homogenizing tank is communicated with fill tank, and bivalve is provided with on its pipeline be communicated with, fill tank is communicated with can packing machine, and bivalve is provided with on its pipeline be communicated with, be provided with multiple vacuum extractor below described filling machine, the front end of vacuum extractor is provided with valve.
Described closed circulation robot control system(RCS) is made up of a homogenisation cycle system and second homogenate blood circulation, wherein in a homogenisation cycle system, the port of export of colostrum tank is communicated with the entrance point of Homogenizing pump, and bivalve is provided with on its pipeline be communicated with, the port of export of Homogenizing pump is communicated with homogenizer, the port of export of described homogenizer is communicated with fill tank, and the pipeline that it is communicated with is provided with bivalve; In second homogenate blood circulation, the bottom of homogenizing tank is communicated with the entrance point of Homogenizing pump, and is provided with bivalve on its pipeline be communicated with, and the port of export of Homogenizing pump is communicated with homogenizer, the port of export of described homogenizer is communicated with colostrum tank, and the pipeline that it is communicated with is provided with bivalve.
Described filling machine lower end arranges three vacuum extractors.
Described glycerol tank and the tank connected pipeline of colostrum are provided with a delivery pump and filter.
This utility model has the following advantages: this utility model arranges oxygen-eliminating device in the source of preparation water, reach the object of alternate source head processed deoxygenation, and in lipomul production process, under being all in the protective effect of nitrogen, the contact of isolated lipomul and extraneous oxygen, reduces the peroxide value in lipomul; In fat milk preparation process, fat milk repeatedly enters homogenizing in homogenizer by blood circulation, reduces the anisidine value in fat milk; And in fat milk pouring process, repeatedly evacuation and fill nitrogen, further ensure that fat milk does not contact with extraneous oxygen, makes the oxygen content of fat milk on the low side, extend the storage time of fat milk, improve the quality of fat milk.
Accompanying drawing explanation
Fig. 1 is the device schematic flow sheet of this utility model embodiment;
In figure, 1-oxygen-eliminating device, 2-glycerol tank, 3-colostrum tank, 4-homogenizing tank, 5-homogenizer, 6-Homogenizing pump, 7-fill tank, 8-filling machine, 9-nitrogen carrier pipe.
Detailed description of the invention
Be further described this utility model below in conjunction with accompanying drawing, protection domain of the present utility model is not limited to the following stated:
As shown in Figure 1, reduce fat milk peroxide value and anisidine value processing system, it comprises oxygen-eliminating device 1, glycerol tank 2, colostrum tank 3, homogenizing tank 4, homogenizer 5, Homogenizing pump 6, fill tank 7, filling machine 8 and nitrogen carrier pipe 9, described nitrogen carrier pipe 9 respectively with glycerol tank 2, colostrum tank 3, homogenizing tank 4, fill tank 7 is communicated with filling machine 8, the bypass line that it is communicated with is provided with valve, valve is in normally open herein, whole lipomul is all in nitrogen protection in preparation process, isolated lipomul, glycerol tank 2, colostrum tank 3, homogenizing tank 4, fill tank 7 contacts with extraneous oxygen with filling machine 8, thus the peroxide value reduced in fat milk, and make its content maintain in a less interval all the time, described oxygen-eliminating device 1 is communicated with colostrum tank 3 with glycerol tank 2 respectively by pipeline, water for injection is through oxygen-eliminating device 1 deoxygenation, thus described glycerol tank 2 passes through pipeline communication with colostrum tank 3, and bivalve is provided with on its pipeline, the water for injection that configuration emulsion products uses, all deoxygenation process has been carried out enter glycerol tank 2 and colostrum tank after oxygen-eliminating device 1 deoxygenation before, reach the dissolved oxygen amount that Sources controlling prepares use water, described colostrum tank 3, homogenizer 5, Homogenizing pump 6 and homogenizing tank 4 form closed circulation robot control system(RCS) by pipeline, described homogenizing tank 4 is communicated with fill tank 7, and bivalve is provided with on its pipeline be communicated with, fill tank 7 is communicated with can packing machine 8, and bivalve is provided with on its pipeline be communicated with, lipomul in fill tank 7 is pushed down in filling machine 8 in the effect of nitrogen pressure, multiple vacuum extractor is provided with below described filling machine 8, the front end of vacuum extractor is provided with valve, in the present embodiment, described filling machine 8 lower end arranges three vacuum extractors, vacuum extractor, regulate vacuum extractor can carry out three evacuation and three nitrogen filled protections to the lipomul of fill, and can according to practical situation, at each evacuation with when filling nitrogen, can one by one to single evacuation amount and the parameter adjustment of filling nitrogen quantity, ensure the existence of medicinal liquid bottle noresidue oxygen.
In this enforcement, described closed circulation robot control system(RCS) is made up of a homogenisation cycle system and second homogenate blood circulation, wherein in a homogenisation cycle system, the port of export of colostrum tank 3 is communicated with the entrance point of Homogenizing pump 6, and bivalve is provided with on its pipeline be communicated with, the port of export of Homogenizing pump 6 is communicated with homogenizer 5, the port of export of described homogenizer 5 is communicated with fill tank 7, the pipeline that it is communicated with is provided with bivalve, fat milk in colostrum tank 3 delivers in homogenizer through Homogenizing pump 6, fat milk enters in homogenizing tank 4 and stores after the anisidine value that homogenizer reduces fat milk, after the fat milk in colostrum tank drains, close and open corresponding valve, fat milk is made to enter in second homogenate blood circulation, in second homogenate blood circulation, the bottom of homogenizing tank 4 is communicated with the entrance point of Homogenizing pump 6, and bivalve is provided with on its pipeline be communicated with, the port of export of Homogenizing pump 6 is communicated with homogenizer 5, the port of export of described homogenizer 5 is communicated with colostrum tank 3, the pipeline that it is communicated with is provided with bivalve, fat milk in homogenizing tank 4 is transported in homogenizer through Homogenizing pump 6, fat milk enters in colostrum tank 3 and stores after the anisidine value that homogenizer reduces fat milk again, after the fat milk in homogenizing tank 4 drains, close and open corresponding valve, fat milk is made to enter in a homogenisation cycle system, repeatedly repeat above-mentioned action, anisidine value in fat milk is significantly reduced.
In the present embodiment, the pipeline that described glycerol tank 2 is connected with colostrum tank 3 is provided with a delivery pump and filter, and do not indicate in the drawings, medicinal liquid enters into colostrum tank 3 by delivery pump and metre filter.
In the present embodiment, the pipeline be communicated with arranges bivalve, can valves leakage be prevented, improve safety coefficient, be also provided with blow-off pipe in the bottom of glycerol tank 2, colostrum tank 3, homogenizing tank 4, fill tank 7, blow-off pipe be provided with valve, do not indicate in figure.
Claims (4)
1. reduce fat milk peroxide value and anisidine value processing system, it is characterized in that: it comprises oxygen-eliminating device (1), glycerol tank (2), colostrum tank (3), homogenizing tank (4), homogenizer (5), Homogenizing pump (6), fill tank (7), filling machine (8) and nitrogen carrier pipe (9), described nitrogen carrier pipe (9) respectively with glycerol tank (2), colostrum tank (3), homogenizing tank (4), fill tank (7) is communicated with filling machine (8), the bypass line that it is communicated with is provided with valve, described oxygen-eliminating device (1) is communicated with colostrum tank (3) with glycerol tank (2) respectively by pipeline, described glycerol tank (2) and colostrum tank (3) pass through pipeline communication, and on its pipeline, be provided with bivalve, described colostrum tank (3), homogenizer (5), Homogenizing pump (6) and homogenizing tank (4) form closed circulation robot control system(RCS) by pipeline, described homogenizing tank (4) is communicated with fill tank (7), and bivalve is provided with on its pipeline be communicated with, fill tank (7) is communicated with can packing machine (8), and bivalve is provided with on its pipeline be communicated with, described filling machine (8) below is provided with multiple vacuum extractor, and the front end of vacuum extractor is provided with valve.
2. reduction fat milk peroxide value according to claim 1 and anisidine value processing system, it is characterized in that: described closed circulation robot control system(RCS) is made up of a homogenisation cycle system and second homogenate blood circulation, wherein in a homogenisation cycle system, the port of export of colostrum tank (3) is communicated with the entrance point of Homogenizing pump (6), and bivalve is provided with on its pipeline be communicated with, the port of export of Homogenizing pump (6) is communicated with homogenizer (5), the port of export of described homogenizer (5) is communicated with fill tank (7), and the pipeline that it is communicated with is provided with bivalve; In second homogenate blood circulation, the bottom of homogenizing tank (4) is communicated with the entrance point of Homogenizing pump (6), and bivalve is provided with on its pipeline be communicated with, the port of export of Homogenizing pump (6) is communicated with homogenizer (5), the port of export of described homogenizer (5) is communicated with colostrum tank (3), and the pipeline that it is communicated with is provided with bivalve.
3. reduction fat milk peroxide value according to claim 1 and anisidine value processing system, is characterized in that: described filling machine (8) lower end arranges three vacuum extractors.
4. reduction fat milk peroxide value according to claim 1 and anisidine value processing system, is characterized in that: the pipeline that described glycerol tank (2) is connected with colostrum tank (3) is provided with a delivery pump and filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520253497.8U CN204637028U (en) | 2015-04-24 | 2015-04-24 | Processing system for reducing peroxide value and anisidine value of fat emulsion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520253497.8U CN204637028U (en) | 2015-04-24 | 2015-04-24 | Processing system for reducing peroxide value and anisidine value of fat emulsion |
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| Publication Number | Publication Date |
|---|---|
| CN204637028U true CN204637028U (en) | 2015-09-16 |
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| CN201520253497.8U Active CN204637028U (en) | 2015-04-24 | 2015-04-24 | Processing system for reducing peroxide value and anisidine value of fat emulsion |
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| CN (1) | CN204637028U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950285A (en) * | 2016-04-21 | 2016-09-21 | 内蒙古蒙牛乳业（集团）股份有限公司 | Extraction method for fat in dairy product and determination method for peroxide value of fat |
| CN108069828A (en) * | 2018-01-09 | 2018-05-25 | 山东福富新材料科技有限公司 | A kind of production biodiesel byproduct crude glycerin high-purity purification technique |
-
2015
- 2015-04-24 CN CN201520253497.8U patent/CN204637028U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105950285A (en) * | 2016-04-21 | 2016-09-21 | 内蒙古蒙牛乳业（集团）股份有限公司 | Extraction method for fat in dairy product and determination method for peroxide value of fat |
| CN108069828A (en) * | 2018-01-09 | 2018-05-25 | 山东福富新材料科技有限公司 | A kind of production biodiesel byproduct crude glycerin high-purity purification technique |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |