CN106922827A - A kind of full-cream sweet milk powder and preparation method thereof - Google Patents
A kind of full-cream sweet milk powder and preparation method thereof Download PDFInfo
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- CN106922827A CN106922827A CN201710168482.5A CN201710168482A CN106922827A CN 106922827 A CN106922827 A CN 106922827A CN 201710168482 A CN201710168482 A CN 201710168482A CN 106922827 A CN106922827 A CN 106922827A
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- 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
- A23C9/16—Agglomerating or granulating milk powder; Making instant milk powder; Products obtained thereby
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- 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
- A23C9/1522—Inorganic additives, e.g. minerals, trace elements; Chlorination or fluoridation of milk; Organic salts or complexes of metals other than natrium or kalium; Calcium enrichment of milk
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- 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
- A23C9/156—Flavoured milk preparations ; Addition of fruits, vegetables, sugars, sugar alcohols or sweeteners
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- 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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Abstract
In order to solve the above-mentioned technical problem, the present invention provides a kind of full-cream sweet milk powder, and required component and weight portion is as follows：White granulated sugar 2.91~3.05, maltodextrin 0.76~1.17, glucose 0.76~1.17, nutrition fortifier 0.0001~0.00015, balance of goat milk.Present invention also offers a kind of preparation method of full-cream sweet milk powder, comprise the following steps：Step 1)：Weigh quantitatively full-cream fresh goat milk inspection standby；Step 2)：Filtering, removes mechanical admixture；Step 3)：Net breast；Step 4)：Cold storage；Step 5)：Pasteurize；Step 6)：Standardization dispensing；Step 7)：Homogeneous；Step 8)：Concentration and evaporation；Step 9)：Ultra high temperature sterilization；Step 10)：Spray drying；Step 11)：Fluid bed is cooled down；Step 12)：Canned or box-packed and then sealing, coding, finally case；Step 13)：Storage；Step 14)：Inspection outbound.Full-cream foreign milk powder and its production technology that the present invention is provided, it is ensured that the nutritional ingredient in fresh goat milk, and protein curd is tiny, softness, and digestion is easy to compared with fresh milk.Protein, fat, lactose have reached international standard simultaneously.
Description
Technical field
The present invention relates to a kind of milk powder, particularly a kind of full-cream sweet milk powder and preparation method thereof.
Background technology
Goat milk is nutritious, rich hop protein matter, lactose, fat, mineral matter and multivitamin, it is easy to digest and assimilate, its
Physical and chemical composition is described as " fine work in breast " close to human milk.Milk powder species in the market is various, and taste differs, for disappear
Expense person is also not quite similar.
Whole milk powder is closed the mineral matters such as good protein in goat milk, fat, multivitamin and calcium, phosphorus, iron, is
It is adapted to the nutrient excellent product drunk everyday, dry skin and obscure can be prevented, makes whitening skin, it is glossy；Also can supplement abundant
It is calcareous, it is adapted to people, juvenile, irritability, insomniac and the big people of operating pressure of calcium deficiency.Whole milk powder is after being sterilized by fresh goat milk
It is concentrated, spraying, dry.Protein is not less than 24% in the whole milk powder of current international standard definition, and fat is not low
In 26%, lactose is not less than 37%.
Existing whole milk powder is unable to reach international standard.
The content 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 scheme is：
A kind of full-cream sweet milk powder, required component and weight portion is as follows：
White granulated sugar 2.91~3.05,
Maltodextrin 0.76~1.17,
Glucose 0.76~1.17,
Nutrition fortifier 0.0001~0.00015,
Balance of goat milk.
Further, the goat milk is full-cream fresh goat milk.
Further, one or more in the nutrition fortifier supplementary material, B B-complex, composite trace element
Combination.
A kind of preparation method of full-cream sweet milk powder, comprises the following steps：
Step 1)：Weigh quantitatively full-cream fresh goat milk inspection standby；
Step 2)：Filtering, removes mechanical admixture；
Step 3)：Net breast；
Step 4)：Cold storage；
Step 5)：Pasteurize；
Step 6)：Standardization dispensing；
Step 7)：Homogeneous；
Step 8)：Concentration and evaporation；
Step 9)：Ultra high temperature sterilization；
Step 10)：Spray drying；
Step 11)：Fluid bed is cooled down；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Storage；
Step 14)：Inspection outbound.
Further, filtered by the nylon leaching net of 80 mesh or 120 mesh after fresh milk metering qualified by inspection in step 2,
Mechanical admixture in removal fresh milk；
Fresh milk carries out net breast, the impurity in removal fresh milk, it is desirable to impurity degree≤2.0mg/kg by seperator in step 3；
Be stored in after the fresh milk after purification is cooled down through plate type heat exchanger in step 4 it is standby in refrigerant tank, during storage
Being 0~4 DEG C, acidity is 6~13OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, the part microorganism in fresh milk is killed, sterilized parameter is 80~
90℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the proportion requirement dispensing in claim 1, addition successively is sought
Hardening agent is supported, 10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into next
Road production process, whole blending process is no more than 30min；
In step 7 feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Dense milk is squeezed into aseptic storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；
In step 11 from after drying tower three dryings of milk powder by fluidized bed out, accessing closed conveying system is simultaneously carried out temporarily
Deposit；
Packaged finished product is piled up on request in step 13 is stored in warehouse for finished product, product must be deposited on pallet,
And maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse
Sanitation and hygiene, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact.
Further, the step 8)：Concentration and evaporation is comprised the following steps that：
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 are normal, and cooling water is normal；
Step S2：Confirm that all operable equipment of operation interface are in auto state；Treat that boot program is changed into operable
State, clicks on start button, starts automatic running start；Start to vacuumize, step is as follows：All vavuum pumps are opened, to system
Air is emptied；All materials pump is opened, water circulation operation 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 emptying
Ready signal is sent in pre-treatment, " product ready ", lights, and clicks on production routine operation button, prepares charging
Production, while finding " product request " signal to pre-treatment, outlet valve, condensation water valve start row ground；Compensating cylinder occurs
During low liquid level, inlet valve is opened, and is started to compensating cylinder feed, and the stabilization of compensating cylinder liquid level is kept by feeding regulating valve；Together
When to ultra high temperature sterilization send superhigh temperature compensating cylinder emptying signal.
2. stabilization, discharging are evaporated：Simultaneously, charging pump, compression fan rotating speed, steam pressure are set by manufacturing parameter respectively for charging
Definite value, is automatically adjusted to produce setting value；When discharging opening density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve,
It is circulated, and waits the request signal that to expect of ultra high temperature sterilization, waits density to reach discharging and require；Condensation-water drain valve is tangential
Condensation water vat；After discharging opening density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to going out feed.
Further, the step 9) in ultra high temperature sterilization comprise the following steps：
A：Pre-sterilizing, when design temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B：Sterilized water is added to be circulated；
C：Charging：Confirm that pretreated material detection is qualified, dispensing sends production signal, press production button and operation button,
Program is prepared automatically into production status, soda acid tank meeting automatic feeding water for emptying compensating cylinder, and the temperature of production is less than 85 DEG C.
Further, the step 10) spray drying step is as follows：
A：First dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water；Nozzle is installed after the completion of sterilization
And be put into clean and reuse tank, to open and whether there is leakage feelings at high-pressure pump pressurization inspection shower nozzle atomizing effect and high-pressure rubber pipe loose joint
, be arranged on spray gun in agglomeration system again after having checked, and fixed by required angle by condition；Main steam line valve is light
It is crack to open 0.1Mpa, and the condensate water blowoff valve of primary heater water collection tank is opened, the condensed water in emptying pipeline；
B：Dry tower to check and close draining valve, manhole, hand hole after closing all pyllers of system, check all thin powder recoveries
System has correctly been installed and 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 by air intake
Temperature is set in 100 DEG C and puts into automatically control afterwards and starts to dry tower.Open fixed bed air inlet fan simultaneously and 1~3 section of fluid bed enters
Blower fan and steam valve are that fluid bed dries sterilization；Temperature of outgoing air when drying tower should be controlled within 85 DEG C；When temperature of outgoing air reaches
Continue to dry 15~20min to after requiring；
C：Production：Dry after tower terminates and each section of EAT of fluid bed is adjusted into the temperature to needed for production, and adjust tower internal pressure
Power is -150pa or so, fully opens main steam valve, reaches more than 140 DEG C when EAT, while temperature of outgoing air reaches 85
Start high-pressure pump when more than DEG C and start spraying production.
Full-cream foreign milk powder and its production technology that the present invention is provided, it is ensured that the nutritional ingredient in fresh goat milk, and albumen
Matter grumeleuse is tiny, softness, and digestion is easy to compared with fresh milk.Protein, fat, lactose have reached international standard simultaneously.
Specific embodiment
The present invention will be described in detail with specific embodiment below, illustrative examples of the invention and explanation herein is used
It is to explain the present invention but not as a limitation of the invention.
A kind of preparation method of full-cream sweet milk powder, comprises the following steps：
Step 1)：Weigh quantitatively full-cream fresh goat milk inspection standby；
Step 2)：Filtering, removes mechanical admixture；
Step 3)：Net breast；
Step 4)：Cold storage；
Step 5)：Pasteurize；
Step 6)：Standardization dispensing；
Step 7)：Homogeneous；
Step 8)：Concentration and evaporation；
Step 9)：Ultra high temperature sterilization；
Step 10)：Spray drying；
Step 11)：Fluid bed is cooled down；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Storage；
Step 14)：Inspection outbound.
Further, filtered by the nylon leaching net of 80 mesh or 120 mesh after fresh milk metering qualified by inspection in step 2,
Mechanical admixture in removal fresh milk；
Fresh milk carries out net breast, the impurity in removal fresh milk, it is desirable to impurity degree≤2.0mg/kg by seperator in step 3；
Be stored in after the fresh milk after purification is cooled down through plate type heat exchanger in step 4 it is standby in refrigerant tank, during storage
Being 0~4 DEG C, acidity is 6~13OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, the part microorganism in fresh milk is killed, sterilized parameter is 80~
90℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, and by the proportion requirement dispensing in claim 1, addition successively is sought
Hardening agent is supported, 10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into next
Road production process, whole blending process is no more than 30min；
In step 7 feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Milk after being concentrated in step 9 carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Dense milk is squeezed into aseptic storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；
In step 11 from after drying tower three dryings of milk powder by fluidized bed out, accessing closed conveying system is simultaneously carried out temporarily
Deposit；
Packaged finished product is piled up on request in step 13 is stored in warehouse for finished product, product must be deposited on pallet,
And maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse
Sanitation and hygiene, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact.
Further, the step 8)：Concentration and evaporation is comprised the following steps that：
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 are normal, and cooling water is normal；
Step S2：Confirm that all operable equipment of operation interface are in auto state；Treat that boot program is changed into operable
State, clicks on start button, starts automatic running start；Start to vacuumize, step is as follows：All vavuum pumps are opened, to system
Air is emptied；All materials pump is opened, water circulation operation 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 emptying
Ready signal is sent in pre-treatment, and " product ready " is lighted, and clicks on production routine operation button, prepares charging
Production, while finding " product request " signal to pre-treatment, outlet valve, condensation water valve start row ground；Compensating cylinder occurs
During low liquid level, inlet valve is opened, and is started to compensating cylinder feed, and the stabilization of compensating cylinder liquid level is kept by feeding regulating valve；Together
When to ultra high temperature sterilization send superhigh temperature compensating cylinder emptying signal.
2. stabilization, discharging are evaporated：Simultaneously, charging pump, compression fan rotating speed, steam pressure are set by manufacturing parameter respectively for charging
Definite value, is automatically adjusted to produce setting value；When discharging opening density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve,
It is circulated, and waits the request signal that to expect of ultra high temperature sterilization, waits density to reach discharging and require；Condensation-water drain valve is tangential
Condensation water vat；After discharging opening density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to going out feed.
Further, the step 9) in ultra high temperature sterilization comprise the following steps：
A：Pre-sterilizing, when design temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B：Sterilized water is added to be circulated；
C：Charging：Confirm that pretreated material detection is qualified, dispensing sends production signal, press production button and operation button,
Program is prepared automatically into production status, soda acid tank meeting automatic feeding water for emptying compensating cylinder, and the temperature of production is less than 85 DEG C.
Specific technological parameter such as following table：
Technological parameter requirement such as table 1：
Further, the step 10) spray drying step is as follows：
A：First dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water；Nozzle is installed after the completion of sterilization
And be put into clean and reuse tank, to open and whether there is leakage feelings at high-pressure pump pressurization inspection shower nozzle atomizing effect and high-pressure rubber pipe loose joint
, be arranged on spray gun in agglomeration system again after having checked, and fixed by required angle by condition；Main steam line valve is slight
Unlatching 0.1Mpa, and open the condensate water blowoff valve of primary heater water collection tank, the condensed water in emptying pipeline；
B：Dry tower to check and close draining valve, manhole, hand hole after closing all pyllers of system, check all thin powder recoveries
System has correctly been installed and 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 by air intake
Temperature is set in 100 DEG C and puts into automatically control afterwards and starts to dry tower.Open fixed bed air inlet fan simultaneously and 1~3 section of fluid bed enters
Blower fan and steam valve are that fluid bed dries sterilization；Temperature of outgoing air when drying tower should be controlled within 85 DEG C；When temperature of outgoing air reaches
Continue to dry 15~20min to after requiring；
C：Production：Dry after tower terminates and each section of EAT of fluid bed is adjusted into the temperature to needed for production, and adjust tower internal pressure
Power is -150pa or so, fully opens main steam valve, reaches more than 140 DEG C when EAT, while temperature of outgoing air reaches 85
Start high-pressure pump when more than DEG C and start spraying production.
Technological parameter requirement such as table 2：
Embodiment 1
Step 1)：Weigh the full-cream fresh goat milk inspections of 5000Kg standby；
Step 2)：Filtered by the nylon leaching net of 80 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 0 DEG C, acidity is 6OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 80
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.254Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 80Kg, glucose 80Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
Embodiment 2
Step 1)：Weigh the full-cream fresh goat milk inspections of 6500Kg standby；
Step 2)：Filtered by the nylon leaching net of 80 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 4 DEG C, acidity is 13OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 80
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.381Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 40Kg, glucose 40Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
Embodiment 3
Step 1)：Weigh the full-cream fresh goat milk inspections of 6000Kg standby；
Step 2)：Filtered by the nylon leaching net of 80 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 2 DEG C, acidity is 9OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 80
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.300Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 60Kg, glucose 60Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
Embodiment 4
Step 1)：Weigh the full-cream fresh goat milk inspections of 5000Kg standby；
Step 2)：Filtered by the nylon leaching net of 120 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 0 DEG C, acidity is 6OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 90
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.254Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 80Kg, glucose 80Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
Embodiment 5
Step 1)：Weigh the full-cream fresh goat milk inspections of 6500Kg standby；
Step 2)：Filtered by the nylon leaching net of 120 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 4 DEG C, acidity is 13OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 90
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.381Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 40Kg, glucose 40Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
Embodiment 6
Step 1)：Weigh the full-cream fresh goat milk inspections of 6000Kg standby；
Step 2)：Filtered by the nylon leaching net of 120 mesh after fresh milk metering qualified by inspection, the machinery in removal fresh milk
Impurity；
Step 3)：Fresh milk carries out net breast, the impurity in removal fresh milk by seperator after going the removal of impurity, it is desirable to and impurity degree≤
2.0mg/kg；
Step 4)：Be stored in after fresh milk after purification is cooled down through plate type heat exchanger it is standby in refrigerant tank, during storage
Being 2 DEG C, acidity is 9OT to temperature control, and whether regular check temperature and acidity meet the requirements；
Step 5)：Pre-sterilizing is carried out by board-like sterilization machine, the part microorganism in fresh milk is killed, sterilized parameter is 90
℃/15S；
Step 6)：Step 5 is squeezed into pill tank by metering, by the proportion requirement dispensing in claim 1, is added successively
0.300Kg supplementary materials, B B-complex, the mixture of composite trace element, and maltodextrin 60Kg, glucose 60Kg, thing
10~15min is continuously stirred in pill tank after material mixing, material is sufficiently mixed dissolving, subsequently into lower one production process,
Whole blending process is expected no more than 30min；
Step 7)：Feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Step 8)：Milk after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated
Concentration removes moisture and forms dense milk；
Step 9)：Milk after concentration carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Step 10)：Dense milk is squeezed into aseptic storage milk cylinder through discharging pump, uses filter screen filtration before squeezing into milk cylinder, then use high pressure
Pump pumps into drying tower and is spray-dried；；
Step 11)：From after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and carry out temporarily
Deposit；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Packaged finished product is piled up stored in warehouse for finished product on request, and product must be deposited on pallet, and
Maintained a certain distance with metope, and by date of manufacture/lot number, kind/specification difference pile, carry out mark.Keep warehouse clear
Clean health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact；
Step 14)：Inspection outbound.
100, sample in Example 1 to embodiment 6 is tested respectively.Test table is as follows：
Table 3 is the test list position of above-described embodiment：Percentage gram content
From table 3 it can be seen that finger of the embodiment of the present invention 1 to each nutritional ingredient of the whole milk powder of 6 times preparations of embodiment
Mark meets international standard.
The technical scheme disclosed in the embodiment of the present invention is described in detail above, specific implementation used herein
Example is set forth to the principle and implementation method of the embodiment of the present invention, and the explanation of above example is only applicable to help and understands
The principle of the embodiment of the present invention；Simultaneously for those of ordinary skill in the art, according to the embodiment of the present invention, in specific implementation
Be will change in mode and range of application, in sum, this specification content should not be construed as to limit of the invention
System.
Claims (8)
1. a kind of full-cream sweet milk powder, it is characterised in that required component and weight portion is as follows：
White granulated sugar 2.91~3.05,
Maltodextrin 0.76~1.17,
Glucose 0.76~1.17,
Nutrition fortifier 0.0001~0.00015,
Balance of goat milk.
2. full-cream sweet milk powder according to claim 1, it is characterised in that the goat milk is full-cream fresh goat milk.
3. full-cream sweet milk powder according to claim 1, it is characterised in that the nutrition fortifier supplementary material, compound dimension life
Element, one or more in composite trace element of combination.
4. a kind of preparation method of full-cream sweet milk powder, it is characterised in that comprise the following steps：
Step 1)：Weigh quantitatively full-cream fresh goat milk inspection standby；
Step 2)：Filtering, removes mechanical admixture；
Step 3)：Net breast；
Step 4)：Cold storage；
Step 5)：Pasteurize；
Step 6)：Standardization dispensing；
Step 7)：Homogeneous；
Step 8)：Concentration and evaporation；
Step 9)：Ultra high temperature sterilization；
Step 10)：Spray drying；
Step 11)：Fluid bed is cooled down；
Step 12)：Canned or box-packed and then sealing, coding, finally case；
Step 13)：Storage；
Step 14)：Inspection outbound.
5. method according to claim 4, it is characterised in that
Filtered by the nylon leaching net of 80 mesh or 120 mesh after fresh milk metering qualified by inspection in step 2, the machine in removal fresh milk
Tool impurity；
Fresh milk carries out net breast, the impurity in removal fresh milk, it is desirable to impurity degree≤2.0mg/kg by seperator in step 3；
Standby, temperature during storage in refrigerant tank is stored in after the fresh milk after purification is cooled down through plate type heat exchanger in step 4
Be 0~4 DEG C, acidity is 6~13OT for control, and whether regular check temperature and acidity meet the requirements；
Pre-sterilizing is carried out by board-like sterilization machine in step 5, the part microorganism in fresh milk is killed, sterilized parameter is 80~90
℃/15S；
Fresh milk squeezes into pill tank by metering in step 6, by the proportion requirement dispensing in claim 1, nutrition is added successively strong
Agent, 10~15min is continuously stirred after material mixing in pill tank, material is sufficiently mixed dissolving, subsequently into lower raw together
Operation is produced, whole blending process is no more than 30min；
In step 7 feed liquid with the temperature no more than 60 DEG C into carrying out homogeneous in high pressure homogenizer, homogenizer pressure 10~
18Mpa, is broken into less fat globule, and be dispersed in breast by lipochondrion；
Milk in step 8 after homogeneous is sterilized again through sterilizer by falling film type evaporation system and separated device is evaporated concentration
Remove moisture and form dense milk；
Milk after being concentrated in step 9 carries out sterilization by heat-exchangers of the plate type, the most of bacterium in feed liquid is killed；
Dense milk is squeezed into aseptic storage milk cylinder through discharging pump in step 10, uses filter screen filtration before squeezing into milk cylinder, then use high-pressure pump pump
Enter drying tower to be spray-dried；
In step 11 from after drying tower three dryings of milk powder by fluidized bed out, access closed conveying system and simultaneously kept in；
Packaged finished product is piled up on request in step 13 is stored in warehouse for finished product, product must be deposited on pallet, and with
Metope is maintained a certain distance, and by date of manufacture/lot number, kind/specification difference pile, carries out mark.Keep warehouse cleaning
Health, shady and cool, dry ventilation, protection against rodents, dust-proof, moistureproof, fireproofing installation are remained intact.
6. the method according to claim 4 or 5, it is characterised in that
The step 8)：Concentration and evaporation is comprised the following steps that：
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 are normal, and cooling water is normal；
Step S2：Confirm that all operable equipment of operation interface are in auto state；Treat that boot program is changed into operable state,
Start button is clicked on, starts automatic running start；Start to vacuumize, step is as follows：All vavuum pumps are opened, system air is entered
Row emptying；All materials pump is opened, water circulation operation 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 emptying
Ready signal is sent in pre-treatment, and " product ready " is lighted, and clicks on production routine operation button, prepares charging production,
" product request " signal is found to pre-treatment simultaneously, outlet valve, condensation water valve start row ground；There is low liquid in compensating cylinder
During position, inlet valve is opened, and is started to compensating cylinder feed, and the stabilization of compensating cylinder liquid level is kept by feeding regulating valve；While to
Ultra high temperature sterilization sends superhigh temperature compensating cylinder emptying signal.
2. stabilization, discharging are evaporated：Simultaneously, charging pump, compression fan rotating speed, steam pressure are set by manufacturing parameter respectively for charging
Value, is automatically adjusted to produce setting value；When discharging opening density reaches minimum setting value, the tangential compensating cylinder of material line outlet valve enters
Row circulation, and the request signal that to expect of ultra high temperature sterilization is waited, wait density to reach discharging and require；Condensation-water drain valve is tangentially cold
Condenser cylinder；After discharging opening density reaches discharging setting value, the tangential ultra high temperature sterilization area of outlet valve starts to going out feed.
7. the method according to claim 4 or 5, it is characterised in that the step 9) in ultra high temperature sterilization include following step
Suddenly：
A：Pre-sterilizing, when design temperature >=133 DEG C, into sterilizing；The sterilizing of this step needs 1800S；
B：Sterilized water is added to be circulated；
C：Charging：Confirm that pretreated material detection is qualified, dispensing sends production signal, press production button and operation button, program
Automatically into production status, soda acid tank meeting automatic feeding water is prepared for emptying compensating cylinder, and the temperature of production is less than 85 DEG C.
8. the method according to claim 4 or 5, it is characterised in that the step 10) spray drying step is as follows：
A：First dense milk cylinder, high pressure line and spray gun cleaning and sterilizing are given with 90 DEG C of hot water；Nozzle is installed after the completion of sterilization and is put
Enter in clean and reuse tank, to open and whether there is leak case at high-pressure pump pressurization inspection shower nozzle atomizing effect and high-pressure rubber pipe loose joint, examine
Spray gun is arranged 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, the condensed water in emptying pipeline；
B：Dry tower to check and close draining valve, manhole, hand hole after closing all pyllers of system, check all fines recovery systems
Correctly install and 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 EAT
It is set in 100 DEG C and puts into automatically control afterwards and starts to dry tower.1~3 section of air inlet fan of fixed bed air inlet fan and fluid bed is opened simultaneously
And steam valve is that fluid bed dries sterilization；Temperature of outgoing air when drying tower should be controlled within 85 DEG C；Wanted when temperature of outgoing air reaches
Continue to dry 15~20min after asking；
C：Production：Dry tower terminate after by each section of EAT of fluid bed adjust to production needed for temperature, and adjust tower pressure interior force for-
150pa or so, fully opens main steam valve, reaches more than 140 DEG C when EAT, while temperature of outgoing air reaches more than 85 DEG C
Shi Qidong high-pressure pumps start spraying production.
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