CN204637028U - Reduce fat milk peroxide value and anisidine value processing system - Google Patents
Reduce fat milk peroxide value and anisidine value processing system 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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Abstract
The utility model discloses and reduce fat milk peroxide value and anisidine value processing system, it comprises oxygen-eliminating device (1), homogenizer (5), Homogenizing pump (6), batch tank, filling machine (8) and nitrogen carrier pipe (9), nitrogen carrier pipe (9) is communicated with each preparing tank respectively, oxygen-eliminating device (1) is communicated with colostrum tank (3) with glycerol tank (2) respectively by pipeline, colostrum tank (3), homogenizer (5), Homogenizing pump (6) and homogenizing tank (4) form closed circulation robot control system(RCS) by pipeline, homogenizing tank (4) is communicated with fill tank (7), fill tank (7) is communicated with can packing machine (8), filling machine (8) below is provided with multiple vacuum extractor.The beneficial effects of the utility model are: it has and improves fat milk quality, extend the fat milk storage time and can reduce the advantage of fat milk peroxide value and anisidine value.
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 | Reduce fat milk peroxide value and anisidine value processing system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520253497.8U CN204637028U (en) | 2015-04-24 | 2015-04-24 | Reduce fat milk peroxide value and anisidine value processing system |
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| CN204637028U true CN204637028U (en) | 2015-09-16 |
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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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