CN109744324A - A kind of Milk powder for middle-aged and old people and preparation method thereof - Google Patents
A kind of Milk powder for middle-aged and old people and preparation method thereof Download PDFInfo
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Abstract
In order to solve the above-mentioned technical problem, the present invention provides a kind of Milk powder for middle-aged and old people, and required component is as follows: raw sheep cream: 420~600 parts, D90 desalted whey powder: 245~300 parts, concentration is 34% whey protein concentrate: 30~60 parts, phytosterin ester: 30~60 parts, galactooligosaccharide: 10~40 parts, oligofructose: 10~40 parts, xylo-oligosaccharide: 5~30 parts, composite nutrient: 1~10 part, compound AB bacterium: 0.2~2 part, streptococcus thermophilus TH-4:0.3~2 part.The present invention also provides a kind of preparation methods, the Milk powder for middle-aged and old people prepared by this method, while full nutrition is provided, the phytosterin ester is under the action of compound AB bacterium, it decomposes and generates largely free phytosterol, the content of blood lipid can be effectively reduced and reduce cholesterol in human body content.
Description
Technical field
The present invention relates to a kind of milk powder, especially a kind of Milk powder for middle-aged and old people and preparation method thereof.
Background technique
Under normal circumstances, since 50 years old, the phenomenon that physiological aging, the secretion function of various bodies of gland will gradually occur in people
It can decline, resistivity reduces, and is easy illness.In order to slow down the appearance of such case, need to give some function of mid-aged population
Energy property food strengthens some functional nutrient ingredients in food, and now relatively common nutriment is Milk powder for middle-aged and old people,
And the reinforcing of nutrition is carried out to milk powder.
It was found that the Bifidobacterium in long lived elder enteron aisle and the bifidobacteria difference in weak old man's enteron aisle are huge
Greatly, the former is close to young man, and the latter then sharply declines, or even cannot detect.The number of Bifidobacterium is related with aging degree,
Also be human body whether Jian Kang important symbol.
According to intestinal flora to the interaction property of body, enteric bacteria can be divided into beneficial bacterium, harmful bacteria and other bacterium three
Major class.Probiotics has improvement intestinal microflora, inhibits pathogen, eliminates carcinogen, improves the immunity of organism factor, reduces
The physiological functions such as cholesterol.In general, the flora in enteron aisle is maintained at certain balance, however, disadvantaged group (the elderly, baby
Child), living and diet is irregular, frequent Smoking And Drinking, using antibiotic, diarrhea constipation situations such as, the quantity of probiotics by
It destroys, to need to take measures, restores the superiority of beneficial bacterium.
In existing technology, a kind of Milk powder for middle-aged and old people (Publication No. for adding synbiotic has been disclosed
CN101449830A), by adding probiotics, addition can be passed through to benefit with the increase of short time internal stimulus beneficial bacterium quantity
The prebiotics of the raw selective value-added effect of bacterium can make the probiotics rapid field planting of addition, maintain beneficial bacterium in intestinal flora
Advantage.Milk powder of the invention can also improve the absorptivity and retention rate of calcium.It also added compound dimension in milk powder of the invention
Raw element, composite mineral matter and other nutriments can provide comprehensive nutrition to mid-aged population.
A kind of its technical solution provided are as follows: Milk powder for middle-aged and old people for adding synbiotic, which is characterized in that including with the following group
Point: fresh milk, 35~65 grams；Desalted whey powder, 12~32 grams；Granulated sugar, 2~6 grams；Vegetable oil, 3~8 grams；Complex prebiotics, 0.4
~20 grams；Compound probiotic, 1.0 × 105~1.0 × 1014cfu.
Summary of the invention
In order to solve the above-mentioned technical problem, the main object of the present invention is to provide a kind of full-cream sweet milk powder and its preparation side
Method.
Its technical solution is:
A kind of Milk powder for middle-aged and old people, required component are as follows:
Raw sheep cream: 420~600 parts,
D90 desalted whey powder: 245~300 parts,
Concentration is 34% whey protein concentrate: 30~60 parts,
Phytosterin ester: 30~60 parts,
Galactooligosaccharide: 10~40 parts,
Oligofructose: 10~40 parts,
Xylo-oligosaccharide: 5~30 parts,
Composite nutrient: 1~10 part,
Compound AB bacterium: 0.2~2 part,
Streptococcus thermophilus TH-4:0.3~2 part.
Further, required component is as follows:
Raw sheep cream: 500~590 parts,
D90 desalted whey powder: 260~280 parts,
Concentration is 34% whey protein concentrate: 45~55 parts,
Phytosterin ester: 50~55 parts,
Galactooligosaccharide: 20~30 parts,
Oligofructose: 20~30 parts,
Xylo-oligosaccharide: 10~20 parts,
Composite nutrient: 1~5 part,
Compound AB bacterium: 0.2~1 part,
Streptococcus thermophilus TH-4:0.3~1 part.
Further, the compound AB bacterium is animal bifidobacteria Bb-12 and lactobacillus acidophilus La-5.
The present invention also provides a kind of preparation methods of Milk powder for middle-aged and old people, include the following steps:
Step 1): it is spare to weigh quantitatively full-cream fresh goat milk inspection；
Step 2): filtering removes mechanical admixture；
Step 3): net cream；
Step 4): cold storage；
Step 5): pasteurize；
Step 6): standardization ingredient；
Step 7): homogeneous；
Step 8): concentration and evaporation；
Step 9): ultra high temperature sterilization；
Step 10): spray drying；
Step 11): fluidized bed is cooling；
Step 12): closed conveying, scratch system；
Step 13): detection lactoferrin, bifidobacterium lactis content；
Step 14): tunnel sterilization；
Step 15): metering mixing；
Step 16): nitrogen-filled packaging；.
Step 17): outer packing；
Step 18): storage；
Step 19): outbound is examined.
It is removed in fresh milk after fresh milk qualified by inspection metering by the filtering of the nylon leaching net of 80 mesh or 120 mesh in step 2
Mechanical admixture；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 0~4 DEG C, and acidity is 6~13 ° of T, and whether regular check temperature and acidity meet the requirements；
In step 5 by board-like sterilization machine carry out pre-sterilizing, kill fresh milk in part microorganism, sterilization parameter be 80~
90℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 10~15min is continuously stirred in pill tank after material mixing, so that material is sufficiently mixed dissolution, subsequently into next
Road production process, entire blending process are no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, and homogenizer pressure 12~
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 18Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: by load weighted probiotics powder agent；It is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
The step 8): specific step is as follows for concentration and evaporation:
Step S1: confirm that all system supplies are normal before falling film type evaporation system boot, electric power is normal, steam pressure ﹥
0.5bar, compressed air ﹥ 0.5bar, softened water is normal, and cooling water is normal；
Step S2: all equipment that operate in confirmation operation interface are in auto state；Become to operate to boot program
State clicks start button, starts automatic running booting；Start to vacuumize, steps are as follows: all vacuum pumps is opened, to system
Air is emptied；All materials pump is opened, water circular flow is carried out；Open compression fan oil pump, hydraulic oil circular flow；
Step S3: both vapor compression fan operation:
Step S4: charging production
1. compensating cylinder empties
Ready signal is sent in pre-treatment, and " productready " is lighted, and is clicked production routine and is run button, and charging life is prepared
It produces, while finding that " productrequest " signal, outlet valve, condensation water valve start row ground to pre-treatment；Compensating cylinder occurs low
When liquid level, inlet valve is opened, and starts to be fed to compensating cylinder, and the stabilization of compensating cylinder liquid level is kept by charging regulating valve；Simultaneously
Superhigh temperature compensating cylinder, which is issued, to ultra high temperature sterilization empties signal.
2. evaporation is stablized, discharging: simultaneously, charging pump, compression fan revolving speed, steam pressure are set by manufacturing parameter respectively for charging
Definite value is automatically adjusted to production setting value；When discharge port density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve,
It is recycled, and waits the request signal that expect of ultra high temperature sterilization, waited density to reach discharging and require；Condensation-water drain valve is tangential
Condense water vat；After discharge port density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to feed out.
Ultra high temperature sterilization includes the following steps: in the step 9)
A: pre-sterilizing, when set temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B: sterile water is added and is recycled；
C: charging: confirmation pretreated material detection is qualified, and ingredient sends production signal, presses production button and operation button,
Program is automatically into production status, and soda acid tank meeting automatic feeding water is that emptying compensating cylinder is prepared, and the temperature of production is lower than 85 DEG C.
Step 10) the spray drying step is as follows:
A: dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water first；Nozzle is installed after the completion of disinfection
And be put into clean and reuse sink, it opens high-pressure pump pressurization and examines at spray head atomizing effect and high-pressure rubber pipe loose joint that whether there is or not leakage feelings
Spray gun is mounted in agglomeration system by condition again after having checked, and is fixed by required angle；Main steam line valve is slight
0.1Mpa is opened, and opens the condensate water blowoff valve of primary heater water collection tank, empties the condensed water in pipeline；
B: drying tower inspection and closes drain valve, manhole, hand hole after closing all pyllers of system, checks all thin powder recoveries
System is correctly installed and is in production status；Main air inlet fan, main exhaust fan are opened in Central Control Room frequency conversion, by negative pressure control in tower
System is in prescribed limit.By adjusting steam automatic regulating valve aperture by main steam pressure control in 0.1Mpa or so, or will air inlet
Investment, which automatically controls, after temperature is set in 100 DEG C starts to dry tower.Open simultaneously 1~3 section of fixed bed air inlet fan and fluidized bed into
Blower and steam valve are fluidized bed drying sterilization；Temperature of outgoing air when drying tower should control within 85 DEG C；When temperature of outgoing air reaches
Continue 15~20min of drying after to requirement；
C: production: each section of inlet air temperature of fluidized bed is adjusted to production required temperature after drying tower, and adjusts tower internal pressure
Power is -150pa or so, fully opens main steam valve, when inlet air temperature reaches 140 DEG C or more, temperature of outgoing air reaches 85 simultaneously
DEG C or more when starting high-pressure pump start spraying production.
While providing full nutrition, the phytosterin ester is decomposed and is generated under the action of compound AB bacterium the present invention
Largely free phytosterol can effectively reduce the content of blood lipid and reduce cholesterol in human body content.
Meanwhile whey protein concentrate, under the action of compound AB bacterium, fabulous solubility property can be with other nutriments
It is combined, promotes absorption of human body.
Detailed description of the invention
Fig. 1 is process flow chart of the invention；
Fig. 2 is hybrid packed flow chart in the present invention.
Specific embodiment
Below in conjunction with attached drawing and specific embodiment, the present invention will be described in detail, herein illustrative examples of the invention
And explanation is used to explain the present invention, but not as a limitation of the invention.
A kind of Milk powder for middle-aged and old people, required component are as follows:
Raw sheep cream: 420~600 parts,
D90 desalted whey powder: 245~300 parts,
Concentration is 34% whey protein concentrate: 30~60 parts,
Phytosterin ester: 30~60 parts,
Galactooligosaccharide: 10~40 parts,
Oligofructose: 10~40 parts,
Xylo-oligosaccharide: 5~30 parts,
Composite nutrient: 1~10 part,
Compound AB bacterium: 0.2~2 part,
Streptococcus thermophilus TH-4:0.3~2 part.
Further, required component is as follows:
Raw sheep cream: 500~590 parts,
D90 desalted whey powder: 260~280 parts,
Concentration is 34% whey protein concentrate: 45~55 parts,
Phytosterin ester: 50~55 parts,
Galactooligosaccharide: 20~30 parts,
Oligofructose: 20~30 parts,
Xylo-oligosaccharide: 10~20 parts,
Composite nutrient: 1~5 part,
Compound AB bacterium: 0.2~1 part,
Streptococcus thermophilus TH-4:0.3~1 part.
Further, the compound AB bacterium is animal bifidobacteria Bb-12 and lactobacillus acidophilus La-5.
A kind of preparation method of Milk powder for middle-aged and old people, includes the following steps:
Step 1): it is spare to weigh quantitatively full-cream fresh goat milk inspection；
Step 2): filtering removes mechanical admixture；
Step 3): net cream；
Step 4): cold storage；
Step 5): pasteurize；
Step 6): standardization ingredient；
Step 7): homogeneous；
Step 8): concentration and evaporation；
Step 9): ultra high temperature sterilization；
Step 10): spray drying；
Step 11): fluidized bed is cooling；
Step 12): closed conveying, scratch system；
Step 13): detection lactoferrin, bifidobacterium lactis content；
Step 14): tunnel sterilization；
Step 15): metering mixing；
Step 16): nitrogen-filled packaging；.
Step 17): outer packing；
Step 18): storage；
Step 19): outbound is examined.
It is removed in fresh milk after fresh milk qualified by inspection metering by the filtering of the nylon leaching net of 80 mesh or 120 mesh in step 2
Mechanical admixture；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 0~4 DEG C, and acidity is 6~13 ° of T, and whether regular check temperature and acidity meet the requirements；
In step 5 by board-like sterilization machine carry out pre-sterilizing, kill fresh milk in part microorganism, sterilization parameter be 80~
90℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 10~15min is continuously stirred in pill tank after material mixing, so that material is sufficiently mixed dissolution, subsequently into next
Road production process, entire blending process are no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, and homogenizer pressure 12~
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 18Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: by load weighted probiotics powder agent；It is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
The step 8): specific step is as follows for concentration and evaporation:
Step S1: confirm that all system supplies are normal before falling film type evaporation system boot, electric power is normal, steam pressure ﹥
0.5bar, compressed air ﹥ 0.5bar, softened water is normal, and cooling water is normal；
Step S2: all equipment that operate in confirmation operation interface are in auto state；Become to operate to boot program
State clicks start button, starts automatic running booting；Start to vacuumize, steps are as follows: all vacuum pumps is opened, to system
Air is emptied；All materials pump is opened, water circular flow is carried out；Open compression fan oil pump, hydraulic oil circular flow；
Step S3: both vapor compression fan operation:
Step S4: charging production
1. compensating cylinder empties
Ready signal is sent in pre-treatment, and " productready " is lighted, and is clicked production routine and is run button, and charging life is prepared
It produces, while finding that " productrequest " signal, outlet valve, condensation water valve start row ground to pre-treatment；Compensating cylinder occurs low
When liquid level, inlet valve is opened, and starts to be fed to compensating cylinder, and the stabilization of compensating cylinder liquid level is kept by charging regulating valve；Simultaneously
Superhigh temperature compensating cylinder, which is issued, to ultra high temperature sterilization empties signal.
2. evaporation is stablized, discharging: simultaneously, charging pump, compression fan revolving speed, steam pressure are set by manufacturing parameter respectively for charging
Definite value is automatically adjusted to production setting value；When discharge port density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve,
It is recycled, and waits the request signal that expect of ultra high temperature sterilization, waited density to reach discharging and require；Condensation-water drain valve is tangential
Condense water vat；After discharge port density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to feed out.
Ultra high temperature sterilization includes the following steps: in the step 9)
A: pre-sterilizing, when set temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B: sterile water is added and is recycled；
C: charging: confirmation pretreated material detection is qualified, and ingredient sends production signal, presses production button and operation button,
Program is automatically into production status, and soda acid tank meeting automatic feeding water is that emptying compensating cylinder is prepared, and the temperature of production is lower than 85 DEG C.
Specific technological parameter is as follows:
Technological parameter requirement:
Further, the step 10) spray drying step is as follows:
A: dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water first；Nozzle is installed after the completion of disinfection
And be put into clean and reuse sink, it opens high-pressure pump pressurization and examines at spray head atomizing effect and high-pressure rubber pipe loose joint that whether there is or not leakage feelings
Spray gun is mounted in agglomeration system by condition again after having checked, and is fixed by required angle；Main steam line valve is slight
0.1Mpa is opened, and opens the condensate water blowoff valve of primary heater water collection tank, empties the condensed water in pipeline；
B: drying tower inspection and closes drain valve, manhole, hand hole after closing all pyllers of system, checks all thin powder recoveries
System is correctly installed and is in production status；Main air inlet fan, main exhaust fan are opened in Central Control Room frequency conversion, by negative pressure control in tower
System is in prescribed limit.By adjusting steam automatic regulating valve aperture by main steam pressure control in 0.1Mpa or so, or will air inlet
Investment, which automatically controls, after temperature is set in 100 DEG C starts to dry tower.Open simultaneously 1~3 section of fixed bed air inlet fan and fluidized bed into
Blower and steam valve are fluidized bed drying sterilization；Temperature of outgoing air when drying tower should control within 85 DEG C；When temperature of outgoing air reaches
Continue 15~20min of drying after to requirement；
C: production: each section of inlet air temperature of fluidized bed is adjusted to production required temperature after drying tower, and adjusts tower internal pressure
Power is -150pa or so, fully opens main steam valve, when inlet air temperature reaches 140 DEG C or more, temperature of outgoing air reaches 85 simultaneously
DEG C or more when starting high-pressure pump start spraying production.
Technological parameter requirement:
Embodiment 1
It is spare that step 1 weighs the raw sheep cream of 560kg；
It is filtered after fresh milk qualified by inspection metering by 80 mesh purpose nylon leaching nets in step 2, removes the machine in fresh milk
Tool impurity；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 1 DEG C, and acidity is 6 ° of T, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, kills the part microorganism in fresh milk, sterilization parameter is 80
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 10min is continuously stirred in pill tank after material mixing, material is made to be sufficiently mixed dissolution, subsequently into lower raw together
Process is produced, entire blending process is no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, homogenizer pressure
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 12Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: load weighted probiotics powder agent is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
Embodiment 2
It is spare that step 1 weighs the raw sheep cream of 550kg；
It is filtered after fresh milk qualified by inspection metering by 80 mesh purpose nylon leaching nets in step 2, removes the machine in fresh milk
Tool impurity；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 2 DEG C, and acidity is 8 ° of T, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, kills the part microorganism in fresh milk, sterilization parameter is 80
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 10min is continuously stirred in pill tank after material mixing, material is made to be sufficiently mixed dissolution, subsequently into lower raw together
Process is produced, entire blending process is no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, homogenizer pressure
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 15Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: load weighted probiotics powder agent is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
Embodiment 3
It is spare that step 1 weighs the raw sheep cream of 570kg；
Nylon leaching net in step 2 after fresh milk qualified by inspection metering by 120 mesh filters, and removes the machinery in fresh milk
Impurity；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 4 DEG C, and acidity is 13 ° of T, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, kills the part microorganism in fresh milk, sterilization parameter is 90
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 15min is continuously stirred in pill tank after material mixing, material is made to be sufficiently mixed dissolution, subsequently into lower raw together
Process is produced, entire blending process is no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, homogenizer pressure
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 18Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: load weighted probiotics powder agent is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
Embodiment 4
It is spare that step 1 weighs the raw sheep cream of 540kg；
Nylon leaching net in step 2 after fresh milk qualified by inspection metering by 120 mesh filters, and removes the machinery in fresh milk
Impurity；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in it is spare in refrigerant tank, when storage
Temperature control is being 2 DEG C, and acidity is 10 ° of T, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, kills the part microorganism in fresh milk, sterilization parameter is 90
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, successively addition is sought
Hardening agent is supported, 15min is continuously stirred in pill tank after material mixing, material is made to be sufficiently mixed dissolution, subsequently into lower raw together
Process is produced, entire blending process is no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, homogenizer pressure
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 15Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated through separator
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Drying tower is pumped into be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: qualified bifidobacterium lactis etc. will be examined to need dry-mixed material, according to wanting for dry process
It asks, sloughs outsourcing, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: load weighted probiotics powder agent is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to institute
Specification is needed to carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product is piled up as required and is stored in warehouse for finished product, product must be deposited in pallet
On, and maintained a certain distance with metope, and distinguish pile by date of manufacture/lot number, kind/specification, carry out mark.Keep storehouse
Library sanitation and hygiene, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
In above-mentioned steps, further illustrate:
(1) supplementary material is checked and accepted, storage and is used: the desalted whey powder purchased from qualified supplier, whey protein concentrate, full-cream
The various raw materials such as milk powder, lactose are stored by supplementary material library is entered after relevant criterion acceptance(check).It is counted when production and application according to production
The dosage for drawing product per ton, carries out ingredient after sloughing packing material.
(2) vegetable oil is checked and accepted, stores and used: the plant oil purchased from qualified supplier is put in storage storage after the assay was approved
It deposits.In advance vegetable oil is squeezed into measure after pre- heat of solution in carburetion cylinder according to production expense when production and application and be used.
(3) nutrient (hardening agent) is checked and accepted, storage and is used: the multi-vitamins and compound micro- purchased from qualified supplier
Enter food additives storehouse after secondary element is qualified by inspection to store.It is received according to production plan from warehouse, with 35-45 DEG C of water
It is added in material-compound tank after dissolution.
(4) lactoferrin, bifidobacterium lactis are checked and accepted, store and are used: lactoferrin, the newborn bifid purchased from qualified supplier
Enter food additives storehouse after bacillus is qualified by inspection to store, be received according to production plan dry-mixed with milk powder as required.
(5) packaging material is checked and accepted, stores and is used: the packaging such as carton, can, carton, wound membrane purchased from qualified supplier
Enter packaging material library after material is qualified by inspection to store, interior packaging material wound membrane is needed before use by sterilization processing.
(6) compressed air: pipeline milk powder is used for through drying compressed air made of cold dehumidifying, dry and deodorization.
(7) inflated with nitrogen: compressed air is isolated into nitrogen through dehumidifying, drying and deodorization and is used for nitrogen-filled packaging.
(8) CIP is cleaned: being mainly used for purchase, ingredient, sterilization enrichment process, including the circulation to milk cylinder, basin, pipeline
Cleaning and sterilizing is controlled acid, concentration of lye, cleaning temperature in cleaning process, and is made a record by scavenging period.
Technical solution disclosed in the embodiment of the present invention is described in detail above, specific implementation used herein
Example is expounded the principle and embodiment of the embodiment of the present invention, and the explanation of above embodiments is only applicable to help to understand
The principle of the embodiment of the present invention；At the same time, for those skilled in the art is being embodied according to an embodiment of the present invention
There will be changes in mode and application range, in conclusion the contents of this specification are not to be construed as limiting the invention.
Claims (8)
1. a kind of Milk powder for middle-aged and old people, which is characterized in that required component is as follows:
Raw sheep cream: 420~600 parts,
D90 desalted whey powder: 245~300 parts,
Concentration is 34% whey protein concentrate: 30~60 parts,
Phytosterin ester: 30~60 parts,
Galactooligosaccharide: 10~40 parts,
Oligofructose: 10~40 parts,
Xylo-oligosaccharide: 5~30 parts,
Composite nutrient: 1~10 part,
Compound AB bacterium: 0.2~2 part,
Streptococcus thermophilus TH-4:0.3~2 part.
2. Milk powder for middle-aged and old people according to claim 1, which is characterized in that required component is as follows:
Raw sheep cream: 500~590 parts,
D90 desalted whey powder: 260~280 parts,
Concentration is 34% whey protein concentrate: 45~55 parts,
Phytosterin ester: 50~55 parts,
Galactooligosaccharide: 20~30 parts,
Oligofructose: 20~30 parts,
Xylo-oligosaccharide: 10~20 parts,
Composite nutrient: 1~5 part,
Compound AB bacterium: 0.2~1 part,
Streptococcus thermophilus TH-4:0.3~1 part.
3. Milk powder for middle-aged and old people according to claim 1, which is characterized in that the compound AB bacterium is animal bifidobacteria Bb-
12 and lactobacillus acidophilus La-5.
4. a kind of preparation method of Milk powder for middle-aged and old people, which comprises the steps of:
Step 1): it is spare to weigh quantitatively full-cream fresh goat milk inspection；
Step 2): filtering removes mechanical admixture；
Step 3): net cream；
Step 4): cold storage；
Step 5): pasteurize；
Step 6): standardization ingredient；
Step 7): homogeneous；
Step 8): concentration and evaporation；
Step 9): ultra high temperature sterilization；
Step 10): spray drying；
Step 11): fluidized bed is cooling；
Step 12): closed conveying, scratch system；
Step 13): detection lactoferrin, bifidobacterium lactis content；
Step 14): tunnel sterilization；
Step 15): metering mixing；
Step 16): nitrogen-filled packaging；.
Step 17): outer packing；
Step 18): storage；
Step 19): outbound is examined.
5. according to the method described in claim 4, it is characterized in that,
The machine in fresh milk is removed by the filtering of the nylon leaching net of 80 mesh or 120 mesh after fresh milk qualified by inspection metering in step 2
Tool impurity；
Fresh milk carries out net cream by seperator in step 3, removes the impurity in fresh milk, it is desirable that impurity degree≤2.0mg/kg；
In step 4 by purified fresh milk through plate heat exchanger carry out it is cooling after be stored in spare in refrigerant tank, temperature when storage
Control is being 0~4 DEG C, and acidity is 6~13 ° of T, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, kills the part microorganism in fresh milk, sterilization parameter is 80~90
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the specific gravity requirement ingredient in claim 1, it is strong successively to add nutrition
Agent continuously stirs 10~15min in pill tank after material mixing, material is made to be sufficiently mixed dissolution, subsequently into lower raw together
Process is produced, entire blending process is no more than 30min；
Feed liquid is entered in step 7 with the temperature no more than 60 DEG C carries out homogeneous in high pressure homogenizer, and homogenizer pressure 12~
Lipochondrion is broken into lesser fat globule, and is dispersed in cream by 18Mpa；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and is evaporated concentration through separator
It removes moisture and forms dense milk；
Milk after being concentrated in step 9 is sterilized by heat-exchangers of the plate type, and most of bacterium in feed liquid is made to be killed；
Dense milk is squeezed into sterile storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then pumped with high-pressure pump
Enter drying tower to be spray-dried；
In step 11 from drying tower come out milk powder by fluidized bed three times dry after；
Closed conveying system is accessed in step 12 and is kept in；
Step 13 lactoferrin, bifidobacterium lactis etc.；
The sterilization of step 14 tunnel: will examine qualified bifidobacterium lactis etc. to need dry-mixed material, according to the requirement of dry process, take off
Outsourcing is gone, after packing inside bag is cleaned, process of passing through tunnel sterilization is sent into dry-mixed；
Step 15 metering mixing: by load weighted probiotics powder agent；It is mixed with the milk powder that step 14 obtains；
Step 16 nitrogen-filled packaging: after the milk powder after mixing is sieved by vibrating screen, it is delivered to quantitative package machine, according to required rule
Lattice carry out nitrogen-filled packaging, sealing；
Step 17 outer packing: canned or box-packed, then sealing, coding is carried out by product variety requirement, is finally cased；
Step 18 storage: packaged finished product being piled up as required and is stored in warehouse for finished product, and product must be deposited on pallet, and
It is maintained a certain distance with metope, and distinguishes pile by date of manufacture/lot number, kind/specification, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry and ventilated, protection against rodents, dust-proof, moisture-proof, fireproofing installation remain intact.
6. method according to claim 4 or 5, which is characterized in that
The step 8): specific step is as follows for concentration and evaporation:
Step S1: confirming that all system supplies are normal before falling film type evaporation system boot, electric power is normal, steam pressure ﹥ 0.5bar,
Compressed air ﹥ 0.5bar, softened water is normal, and cooling water is normal；
Step S2: all equipment that operate in confirmation operation interface are in auto state；Become operable state to boot program,
Start button is clicked, automatic running booting is started；Start to vacuumize, steps are as follows: opening all vacuum pumps, to system air into
Row emptying；All materials pump is opened, water circular flow is carried out；Open compression fan oil pump, hydraulic oil circular flow；
Step S3: both vapor compression fan operation:
Step S4: charging production
1. compensating cylinder empties
Ready signal is sent in pre-treatment, and " productready " is lighted, and is clicked production routine and is run button, and charging production is prepared,
Find that " productrequest " signal, outlet valve, condensation water valve start row ground to pre-treatment simultaneously；There is low liquid level in compensating cylinder
When, inlet valve is opened, and starts to be fed to compensating cylinder, and keep the stabilization of compensating cylinder liquid level by charging regulating valve；Simultaneously to super
High temperature sterilization issues superhigh temperature compensating cylinder and empties signal.
2. evaporation is stablized, discharging: simultaneously, charging pump, compression fan revolving speed, steam pressure press manufacturing parameter setting respectively for charging
Value is automatically adjusted to production setting value；When discharge port density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve, into
Row circulation, and the request signal that expect of ultra high temperature sterilization is waited, it waits density to reach discharging and requires；Condensation-water drain valve is tangentially cold
Condenser cylinder；After discharge port density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to feed out.
7. method according to claim 4 or 5, which is characterized in that ultra high temperature sterilization includes following step in the step 9)
It is rapid:
A: pre-sterilizing, when set temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B: sterile water is added and is recycled；
C: charging: confirmation pretreated material detection is qualified, and ingredient sends production signal, presses production button and operation button, program
Automatically into production status, soda acid tank meeting automatic feeding water is that emptying compensating cylinder is prepared, and the temperature of production is lower than 85 DEG C.
8. method according to claim 4 or 5, which is characterized in that the step 10) spray drying step is as follows:
A: dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water first；Nozzle is installed after the completion of disinfection and is put
Enter in clean and reuse sink, opens high-pressure pump pressurization and examine at spray head atomizing effect and high-pressure rubber pipe loose joint that whether there is or not leak case, inspections
Spray gun is mounted in agglomeration system again after the completion of looking into, and is fixed by required angle；Main steam line valve is slightly turned on
0.1Mpa, and the condensate water blowoff valve of primary heater water collection tank is opened, empty the condensed water in pipeline；
B: drying tower inspection and closes drain valve, manhole, hand hole after closing all pyllers of system, checks all fines recovery systems
It correctly installs and is in production status；Main air inlet fan, main exhaust fan are opened in Central Control Room frequency conversion, vacuum cavitations in tower are existed
Prescribed limit.By adjusting steam automatic regulating valve aperture by main steam pressure control in 0.1Mpa or so, or by inlet air temperature
Investment, which automatically controls, after being set in 100 DEG C starts to dry tower.1~3 section of air inlet fan of fixed bed air inlet fan and fluidized bed is opened simultaneously
And steam valve is fluidized bed drying sterilization；Temperature of outgoing air when drying tower should control within 85 DEG C；It is wanted when temperature of outgoing air reaches
Continue 15~20min of drying after asking；
C: production: dry tower after by each section of inlet air temperature of fluidized bed adjust to production required temperature, and adjust tower pressure interior force be-
150pa or so fully opens main steam valve, when inlet air temperature reaches 140 DEG C or more, temperature of outgoing air reaches 85 DEG C or more simultaneously
Shi Qidong high-pressure pump starts spraying production.
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| CN113519631A (en) * | 2021-07-06 | 2021-10-22 | 黑龙江谱华威乳业集团有限公司 | Middle-aged and old modified milk powder assisting in reducing blood sugar and having low blood sugar load and preparation method thereof |
| CN113812464A (en) * | 2021-08-10 | 2021-12-21 | 美庐生物科技股份有限公司 | Formula of milk powder helpful for preventing hypertension, hyperglycemia and hyperlipidemia of middle-aged and old people and preparation method of milk powder |
| CN114651873A (en) * | 2022-02-22 | 2022-06-24 | 黑龙江益得莱乳业科技有限公司 | Health-care modified milk powder assisting in reducing high blood pressure, high blood sugar and low blood Glucose (GI) and preparation method thereof |
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Application publication date: 20190514 |