CN107258903A - After " reduction " high-temperature process in milk vitamin A Processes and apparatus - Google Patents
After " reduction " high-temperature process in milk vitamin A Processes and apparatus Download PDFInfo
- Publication number
- CN107258903A CN107258903A CN201710465645.6A CN201710465645A CN107258903A CN 107258903 A CN107258903 A CN 107258903A CN 201710465645 A CN201710465645 A CN 201710465645A CN 107258903 A CN107258903 A CN 107258903A
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- China
- Prior art keywords
- milk
- sterilizer
- vitamin
- threeway
- drain tube
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/02—Preservation of milk or milk preparations by heating
- A23C3/03—Preservation of milk or milk preparations by heating the materials being loose unpacked
- A23C3/033—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
- A23C3/037—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus in direct contact with the heating medium, e.g. steam
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C3/00—Preservation of milk or milk preparations
- A23C3/04—Preservation of milk or milk preparations by freezing or cooling
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C9/00—Milk preparations; Milk powder or milk powder preparations
- A23C9/152—Milk preparations; Milk powder or milk powder preparations containing additives
- A23C9/158—Milk preparations; Milk powder or milk powder preparations containing additives containing vitamins or antibiotics
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Dairy Products (AREA)
Abstract
After one kind " reduction " high-temperature process of the present invention in milk vitamin A equipment, including sterilizer, it is characterized in that the milk drain tube of sterilizer again through a cooler cool down after unlap machine, equipped with two threeways on the milk drain tube of described sterilizer, one or three connects cleaning loading system, and the second threeway is connected to charge pump.Use the technique of vitamin A in milk after " reduction " high-temperature process of the said equipment, it is characterized in that the milk temperature control that goes out of sterilizer is 42~48 DEG C, start the charge pump that the second threeway is connect, retinol acetate is added to the milk that goes out of milk drain tube, then go out milk and enter cooler, cool again, control out milk temperature to enter packing machine for 5~8 DEG C.The present invention is sterilized suitable for the processing of any milk.
Description
Technical field
The present invention relates to food industry, relate in particular to " reduce " after high-temperature process in milk the technique of vitamin A and
Equipment.
Background technology
Vitamin A in fresh vegetable, carrot, fresh corn will could be by human body after multiple conversions in human body
Absorb, the vitamin A in milk has been changed in ox body to be finished, and need not be changed directly with regard to that can be absorbed by the body.Existing fresh milk
The method of processing sterilization has two kinds, and one kind is pasteurization, with board-like or tubular sterilizer, uses 85 DEG C of temperature-sterilizeds;Separately
One kind is that superhigh temperature is gone out Jun method, with tubular sterilizer, uses 136 DEG C of temperature-sterilizeds.Both approaches are all side heating sterilization oxen
Milk, while using frozen water(0~2 DEG C)Cooling, milk cools, milk goes out to disappear to cooling section frozen water at once by sterilization section heating sterilization
Milk temperature can drop to 5~8 DEG C and be packed to packing machine after malicious device.Both sterilization methods have the shortcomings that one very big, exactly sterilize
The vitamin A in milk is without " oxidation " is fallen, and fresh milk does not have vitamin A to be fresh milk, and industrial production is " oxygen afterwards
Change ", you must " reduction ", in milk original vitamin A you process " oxidation " fall, you should " reduction ".But existing China shows
Also without this " reduction " technique.
The content of the invention
It is an object of the invention to provide the Processes and apparatus of vitamin A in milk after a kind of " reduction " high-temperature process.This
Planting the milk after " reduction " can produce actively and beneficial effect to human body.
After one kind " reduction " high-temperature process of the present invention in milk vitamin A equipment, including sterilizer, it is characterised in that
Equipped with two threeways on unlap machine after the milk drain tube of sterilizer is cooled down through a cooler again, the milk drain tube of described sterilizer,
One or three connects cleaning loading system, and the second threeway is connected to charge pump.
Use the technique of vitamin A in milk after " reduction " high-temperature process of the said equipment, it is characterised in that sterilizer
Go out milk temperature control for 42~48 DEG C, start the charge pump that the second threeway is connect, food-grade vinegar is added to the milk drain tube of sterilizer
Sour vitamin A1 esters, subsequently into cooler, cools again, controls out milk temperature to enter packing machine for 5~8 DEG C.
Further, the milk drain tube to sterilizer adds acetic acid vitamin A1 esters, and addition is that per kilogram milk adds food
The μ g of level acetic acid vitamin A1 esters 600~1000.
After " reduction " high-temperature process of the present invention in milk vitamin A Processes and apparatus, add to the milk drain tube of sterilizer
Go out milk temperature control when entering acetic acid vitamin A1 esters for 42~48 DEG C, less than " oxidation " temperature 60 C of vitamin A in milk, production
Enter cooler after milk sterilization, cool again, be cooled to 5~8 DEG C of packagings, in 2~5 DEG C of preservations, 7 days shelf-lifves, bag
Load onto and indicate when drinking not above 50 DEG C.The effect of vitamin A in milk after " reduction " high-temperature process could so be embodied.This
The Processes and apparatus of vitamin A is applied to the processing sterilization of any milk in milk after " reduction " high-temperature process of invention.
" the Hunan Co., Ltd of CCIC " for sending State Council subordinate using sample produced by the invention examines,
Provide survey report, certificate number NO.430316098637-Q date of certification Date2016 October 08, assay:Dimension
Raw element A is 65.2 μ g/100g survey report conclusions:Meet the requirements.
Drinking milk after " reduction " high-temperature process for a long time can mend " calcium "(Glycogen)Kidney tonifying, can element culturing fixed folder, can strengthen immune
The generation of power, resist the disease and cancer, not only leads to blood vessel, moreover it is possible to leads to endocrine glandular tube, can reduce blood and lymph flow
Resistance, the regulation factor of epithelial cell and bone cell differentiation can be promoted, the elasticity of various glandular tubes, energy can be recovered to a certain extent
Replenish the calcium, production of sperm, have good medical care effect to human body.
The present invention has actively and beneficial effect, it is adaptable to the processing sterilization of any milk.
Brief description of the drawings
Fig. 1 is one of structural representation of the embodiment of the present invention;
In above figure:1st, be sterilizer, 2, be milk container, 3, be milk pump, 4, be ice model tank, 5, be CHP, 6, be cooler, 7,
For packing machine, 8, be charge pump, 9, be check-valves, 10, be pressure gauge, 11, be the second threeway, 11.1, be dish valve, 12 be first
Threeway, 12.1, be dish valve, 13, steam pipe, 14, for switching pipe, 14.1, be loose joint, 14.2, be threeway loose joint.
Embodiment
With reference to embodiment, present invention is described:
Embodiment one
The glad Sheng in Guiyang Wudang District of present patent application people's one-man business and food factory employ the present invention:" reduction " high temperature
After processing in milk vitamin A Processes and apparatus, as shown in figure 1, milk squeezes into sterilizer 1 from milk container 2 through milk pump 3, sterilization
Device 1 is board-like or tubular sterilizer, and steam enters the sterilization section of sterilizer 1 through steam pipe 13, is disappeared using 85 DEG C or 136 DEG C of temperature
Poison, by being cooled after set disinfecting time sterilization to cooling section with frozen water at once, frozen water is that CHP 5 is got from ice model tank 4
Into sterilizer 1;The invention is characterised in that the milk drain tube of the sterilizer 1 again through a cooler 6 cool down after unlap machine 7,
Cooler 6 is with board-like or tubular type, and the cooling medium of cooler 6 and sterilizer 1 uses the same system of ice model tank 4, and frozen water is 0
~2 DEG C, equipped with two threeways on the milk drain tube of described sterilizer 1, two 1~1.5 meter of threeway intervals are connect in the first threeway 12
Have and connect dish valve 11.1 and check-valves 9 in dish valve 12.1 and loose joint 14.1, the second threeway 11, filled between dish valve 11.1 and check-valves 9
There is pressure gauge 10, check-valves 9 connects threeway loose joint 14.2 and connects charge pump 8 again;Periodic cleaning cooler 6 and sterilizer 1, it is first during cleaning
Charge pump 8 is removed from threeway loose joint 14.2, the end is blocked, then switching pipe 14 is passed through into loose joint 14.1 and threeway loose joint 14.2
Access cleaning loading system, starts cleaning loading system, is cleaned with acid, alkali, boiling water during cleaning, the He of dish valve 12.1 is closed after cleaning
Connecing for threeway loose joint 14.2 switches the end of pipe 14, and connects charge pump 8, and will switch pipe 14 from loose joint 14.1 and threeway loose joint 14.2
On remove;The milk temperature control that goes out of sterilizer 1 is 42~48 DEG C, starts the charge pump 8 that the second threeway 11 is connect, to sterilizer
Milk drain tube adds food-grade acetic acid vitamin A1 esters, and addition is the μ g of per kilogram milk addition food-grade acetic acid vitamin A1 esters 600~1000, so
Enter cooler 6 afterwards, cool again, control out milk temperature to enter packing machine 7 for 5~8 DEG C.
The charge pump 8 that embodiment one is used is the serial Electromagnetic diaphragm metering pumps of TX.
The milk that the Processes and apparatus of vitamin A is produced in milk after " reduction " high-temperature process of the invention has good
Medical care effect, receives liking for people.The present invention has filled up the sky of vitamin A in milk after " reduction " high-temperature process
In vain, there are good market prospects.
Claims (3)
- After " 1. reduction " high-temperature process in milk vitamin A equipment, including sterilizer (1), it is characterised in that described sterilization Two are equipped with unlap machine (7) after the milk drain tube of device (1) is cooled down through a cooler (6) again, the milk drain tube of described sterilizer (1) Individual threeway, the first threeway (12) connects cleaning loading system, and the second threeway (11) is connected to charge pump (8).
- 2. " reducing " the use technique of the equipment of vitamin A in milk after high-temperature process according to claim 1, its feature exists In sterilizer(1)Go out milk temperature control for 42~48 DEG C, start the second threeway(11)The charge pump connect(8), to sterilizer (1)Milk drain tube adds acetic acid vitamin A1 esters, subsequently into cooler(6), cool again, control out milk temperature to enter bag for 5~8 DEG C Installation(7).
- 3. the use technique of the equipment of vitamin A in milk after high-temperature process, its feature " are reduced " according to claim 2 It is described to sterilizer(1)Milk drain tube adds acetic acid vitamin A1 esters, and addition is that per kilogram milk adds food-grade acetic acid vitamin A1 esters 600~1000 μ g.
Priority Applications (1)
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CN201710465645.6A CN107258903A (en) | 2017-06-19 | 2017-06-19 | After " reduction " high-temperature process in milk vitamin A Processes and apparatus |
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CN201710465645.6A CN107258903A (en) | 2017-06-19 | 2017-06-19 | After " reduction " high-temperature process in milk vitamin A Processes and apparatus |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN86203061U (en) * | 1986-06-21 | 1987-03-25 | 上海市农场管理局农业机械研究所 | Milk-sterilizing equipment with microwave |
CN101327028A (en) * | 2008-07-23 | 2008-12-24 | 内蒙古伊利实业集团股份有限公司 | Method for adding fruit juice during foodstuff production process |
CN101564059A (en) * | 2008-04-25 | 2009-10-28 | 内蒙古伊利实业集团股份有限公司 | Liquid dairy product containing heat-sensitive substance and preparation method thereof |
CN201647160U (en) * | 2010-02-23 | 2010-11-24 | 利乐拉瓦尔集团及财务有限公司 | Aseptic filling system for online particle adding |
CN102283284A (en) * | 2011-06-16 | 2011-12-21 | 上海理工大学 | Transcritical carbon dioxide heat pump milk disinfecting and cooling system and method |
US8460733B2 (en) * | 2005-05-06 | 2013-06-11 | The Quaker Oats Company | Hot-fill beverage production with flavor injection |
CN105667870A (en) * | 2015-12-30 | 2016-06-15 | 内蒙古伊利实业集团股份有限公司 | On-line aseptic adding device and method for granular additives in liquid food |
-
2017
- 2017-06-19 CN CN201710465645.6A patent/CN107258903A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN86203061U (en) * | 1986-06-21 | 1987-03-25 | 上海市农场管理局农业机械研究所 | Milk-sterilizing equipment with microwave |
US8460733B2 (en) * | 2005-05-06 | 2013-06-11 | The Quaker Oats Company | Hot-fill beverage production with flavor injection |
CN101564059A (en) * | 2008-04-25 | 2009-10-28 | 内蒙古伊利实业集团股份有限公司 | Liquid dairy product containing heat-sensitive substance and preparation method thereof |
CN101327028A (en) * | 2008-07-23 | 2008-12-24 | 内蒙古伊利实业集团股份有限公司 | Method for adding fruit juice during foodstuff production process |
CN201647160U (en) * | 2010-02-23 | 2010-11-24 | 利乐拉瓦尔集团及财务有限公司 | Aseptic filling system for online particle adding |
CN102283284A (en) * | 2011-06-16 | 2011-12-21 | 上海理工大学 | Transcritical carbon dioxide heat pump milk disinfecting and cooling system and method |
CN105667870A (en) * | 2015-12-30 | 2016-06-15 | 内蒙古伊利实业集团股份有限公司 | On-line aseptic adding device and method for granular additives in liquid food |
Non-Patent Citations (1)
Title |
---|
利乐中国加工设备部: "灵活便捷的无菌添加设备", 《中国奶业协会第五届会员代表大会论文集》 * |
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