CN106074672A - Constant temperature system for improving quality of fat milk product - Google Patents
Constant temperature system for improving quality of fat milk product Download PDFInfo
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- CN106074672A CN106074672A CN201610565235.4A CN201610565235A CN106074672A CN 106074672 A CN106074672 A CN 106074672A CN 201610565235 A CN201610565235 A CN 201610565235A CN 106074672 A CN106074672 A CN 106074672A
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- coolant
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- 235000013336 milk Nutrition 0.000 title claims description 45
- 239000008267 milk Substances 0.000 title claims description 45
- 210000004080 milk Anatomy 0.000 title claims description 45
- 210000003022 colostrum Anatomy 0.000 claims abstract description 48
- 235000021277 colostrum Nutrition 0.000 claims abstract description 48
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000000110 cooling liquid Substances 0.000 claims abstract description 6
- 238000002347 injection Methods 0.000 claims abstract description 6
- 239000007924 injection Substances 0.000 claims abstract description 6
- 239000002826 coolant Substances 0.000 claims description 63
- 238000012806 monitoring device Methods 0.000 claims description 48
- 239000008215 water for injection Substances 0.000 claims description 23
- 238000001514 detection method Methods 0.000 claims description 5
- 210000000481 breast Anatomy 0.000 claims description 2
- 238000003860 storage Methods 0.000 abstract description 12
- 239000002960 lipid emulsion Substances 0.000 abstract description 5
- 150000002978 peroxides Chemical class 0.000 abstract description 5
- 238000000265 homogenisation Methods 0.000 abstract description 4
- BHAAPTBBJKJZER-UHFFFAOYSA-N p-anisidine Chemical compound COC1=CC=C(N)C=C1 BHAAPTBBJKJZER-UHFFFAOYSA-N 0.000 abstract description 4
- 235000011187 glycerol Nutrition 0.000 abstract description 3
- 239000000047 product Substances 0.000 description 23
- 230000001804 emulsifying effect Effects 0.000 description 16
- 239000011265 semifinished product Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- 230000002977 hyperthermial effect Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 108010004103 Chylomicrons Proteins 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000001268 chyle Anatomy 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 150000002118 epoxides Chemical class 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000002496 gastric effect Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000035479 physiological effects, processes and functions Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 208000011580 syndromic disease Diseases 0.000 description 1
Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K36/00—Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
- A61K36/18—Magnoliophyta (angiosperms)
- A61K36/185—Magnoliopsida (dicotyledons)
- A61K36/48—Fabaceae or Leguminosae (Pea or Legume family); Caesalpiniaceae; Mimosaceae; Papilionaceae
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J3/00—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
- A61J3/002—Compounding apparatus specially for enteral or parenteral nutritive solutions
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/045—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates
- A61K31/047—Hydroxy compounds, e.g. alcohols; Salts thereof, e.g. alcoholates having two or more hydroxy groups, e.g. sorbitol
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/66—Phosphorus compounds
- A61K31/683—Diesters of a phosphorus acid with two hydroxy compounds, e.g. phosphatidylinositols
- A61K31/685—Diesters of a phosphorus acid with two hydroxy compounds, e.g. phosphatidylinositols one of the hydroxy compounds having nitrogen atoms, e.g. phosphatidylserine, lecithin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/10—Dispersions; Emulsions
- A61K9/107—Emulsions ; Emulsion preconcentrates; Micelles
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- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Medicinal Chemistry (AREA)
- Pharmacology & Pharmacy (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Natural Medicines & Medicinal Plants (AREA)
- Dispersion Chemistry (AREA)
- Nutrition Science (AREA)
- Engineering & Computer Science (AREA)
- Alternative & Traditional Medicine (AREA)
- Biotechnology (AREA)
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Abstract
The invention discloses a constant temperature system for improving the quality of a fat emulsion product, which comprises an injection water inlet pipe, a colostrum tank, a homogenization tank, a glycerin pipe, a delivery pump, a homogenizer, a cooling liquid inlet pipe, a cooling liquid outlet pipe and a constant temperature system, wherein the injection water inlet pipe is hermetically communicated with the colostrum tank, a heat exchanger is hermetically communicated between the injection water inlet pipe and the colostrum tank, the colostrum tank is hermetically communicated with the glycerin pipe through a pipeline, the constant temperature system comprises a constant temperature device A, a constant temperature device B and a constant temperature device C which are arranged in parallel, the delivery pump, the constant temperature device C, the homogenizer, the constant temperature device B and the constant temperature device A are sequentially hermetically communicated, and the constant temperature device A is respectively hermetically communicated with the colostrum tank and the homogenization tank. The invention ensures the uniformity of the fat emulsion product, reduces the peroxide value and the anisidine value of the fat emulsion, ensures the product quality, ensures that the fat emulsion product ingested by a human body has more stable and higher quality, and also ensures the storage period of the product.
Description
Technical field
The present invention relates to fat milk preparation field, particularly relate to a kind of constant temperature system for improving fat milk product quality
System.
Background technology
Fat milk is a kind of the most uniform but also stable lipomul being made up of refined soybean oil, glycerol, lecithin etc.,
The importance of its treatment is under non-bowel provisions to provide high-energy and required fatty acid.From physiology and threpsology's channel syndrome
The fat that person of good sense's body is taken in first forms Chylomicron through gastrointestinal absorption, and the form of these product is all the most similar to chyle with composition,
Directly to the venous patient infusion that can not take food, it is provided that lipid nutrition.Peroxide value and first in the production of conventional fat Emulsion
Epoxide aniline value is relatively difficult to control, and directly affects product quality and quality, thus jeopardizes user health of human body.
Summary of the invention
The weak point existed for prior art, it is an object of the invention to provide a kind of for improving fat milk product
The constant temperature system of quality, it is ensured that the uniformity of fat milk product, reduces fat milk peroxide value and anisidine value, protects
Demonstrate,prove product quality, ensured that the fat milk product quality that human body is taken in is more stable, more high-end, also ensure that product storage cycle.
The purpose of the present invention is achieved through the following technical solutions:
A kind of constant temperature system for improving fat milk product quality, including water for injection inlet pipe, colostrum tank, homogenizing tank,
Glycerol pipe, delivery pump, homogenizer, coolant inlet pipe, coolant go out pipe and constant temperature system, described water for injection inlet pipe and colostrum tank
Airtight connection, between water for injection inlet pipe with colostrum tank, airtight connection is provided with heat exchanger, and described colostrum tank passes through pipeline and glycerol
Manage airtight connection, the pipeline between colostrum tank and glycerol pipe is provided with pneumatic diaphragm valve K；Described colostrum tank enters with delivery pump
Mouthful end is connected by pipeline closed, the pipeline between colostrum tank and delivery pump is sequentially provided with pneumatic diaphragm valve A and pneumatic every
Film valve D；Described constant temperature system includes thermostat A, thermostat B and thermostat C arranged in parallel, described delivery pump
The port of export airtight with the arrival end of thermostat C connect, the described port of export of thermostat C passes through with the arrival end of homogenizer
Pipeline closed connects, and the pipeline between thermostat C and homogenizer is provided with temperature control detection device C, going out of described homogenizer
Mouth end is connected by pipeline closed with the arrival end of thermostat B, the port of export of thermostat B and the arrival end of thermostat A
Airtight connection, the pipeline between thermostat B and thermostat A is provided with Temperature-control Monitoring device B, described thermostat A's
The port of export is airtight is communicated with delivery main, and delivery main is the most airtight is communicated with conveying arm A and conveying arm B, carries arm A
Airtight with colostrum tank top connecting, arm B is airtight with homogenizing tank top connects in conveying, total in the conveying of the thermostat A port of export
Pipe is provided with Temperature-control Monitoring device A and pneumatic diaphragm valve F, is provided with pneumatic diaphragm valve G on conveying arm A, on conveying arm B
It is provided with pneumatic diaphragm valve H and pneumatic diaphragm valve I；Described homogenizing pot bottom connects by pipeline is airtight with the arrival end of delivery pump,
Pneumatic diaphragm valve C it is provided with on pipeline between homogenizing tank and delivery pump；It is communicated with coolant inlet pipe on described coolant inlet pipe
Arm A, coolant inlet pipe arm B and coolant inlet pipe arm C, described coolant inlet pipe arm A and the airtight company of thermostat A
Logical, coolant inlet pipe arm A is provided with flow control valve A, is communicated with coolant bottom thermostat A and goes out pipe arm A, cold
But liquid goes out pipe arm A and is provided with flow control valve F, and described coolant inlet pipe arm B is airtight with thermostat B to be connected, in cooling
Liquid inlet pipe arm B is provided with flow control valve B, is communicated with coolant and goes out pipe arm B bottom thermostat B, goes out pipe in coolant
Arm B is provided with flow control valve E, and described coolant inlet pipe arm C is airtight with thermostat C to be connected, and props up at coolant inlet pipe
Pipe C is provided with flow control valve C, is communicated with coolant and goes out pipe arm C, go out in coolant and set on pipe arm C bottom temperature device C
Have flow control valve D, described coolant to go out pipe arm A, coolant goes out pipe arm B, coolant go out pipe arm C respectively with coolant
Go out and manage airtight connection；Described temperature control detection device C is connected with flow control valve C, flow control valve D respectively, described Temperature-control Monitoring
Device B is connected with flow control valve B, flow control valve E respectively, described Temperature-control Monitoring device A respectively with flow control valve A, stream
Adjustable valve F connects.
In order to the present invention is better achieved, between described water for injection inlet pipe and colostrum tank, airtight connection is provided with Temperature-control Monitoring
Device D, described water for injection inlet pipe is provided with pneumatic diaphragm valve L and pneumatic diaphragm valve M, described heat exchanger, Temperature-control Monitoring device
D, pneumatic diaphragm valve L, pneumatic diaphragm valve M and colostrum tank set gradually.
In order to strengthen the glycerol pipe power to colostrum tank conveying material, on the pipeline between described colostrum tank and glycerol pipe also
It is provided with pneumatic diaphragm valve J.
As preferably, the pipeline between described colostrum tank and delivery pump is additionally provided with pneumatic diaphragm valve B, described pneumatic diaphragm
Valve B is between pneumatic diaphragm valve A and pneumatic diaphragm valve D.
Present invention ensures that the uniformity of fat milk product, reduce fat milk peroxide value and anisidine value, protect
Demonstrate,prove product quality, ensured that the fat milk product quality that human body is taken in is more stable, more high-end, also ensure that product storage cycle.
The workflow of constant temperature system of the present invention is as follows:
1) water for injection injects preparation water spot through water for injection inlet pipe 16, and colostrum tank 1 passes through heat exchanger 12 to injection
Having carried out hyperthermic treatment with water, Temperature-control Monitoring device D13 storage inside has water for injection temperature optimum range, Temperature-control Monitoring device
D13 monitors the coolant-temperature gage in water for injection inlet pipe 16 in real time, and then Temperature-control Monitoring device D13 controls the intensification switch of heat exchanger 12
And the control of intensification size reaches to control fat milk in water for injection inlet pipe 16 and prepares use water and maintain optimum temperature range
In, it is finally reached fat milk and prepares the optimum temperature of use water.
2) during emulsifying, colostrum tank 1, homogenizing tank 2, delivery pump 4, homogenizer 5 and constant temperature system by pipeline and
Valve connection constitutes a self-control circulating system closed, and delivery pump 4 and thermostat C8 connect simultaneously, Temperature-control Monitoring device
C11 storage inside has the optimum temperature range needed for emulsifying, Temperature-control Monitoring device C11 to monitor thermostat C8 in real time with equal
The temperature of fat milk elementary semi-finished products in pipeline between matter machine 5, then Temperature-control Monitoring device C11 control flow control valve C23 and
The on-off control of flow control valve D24 reaches to control between thermostat C8 and homogenizer 5 fat milk primary half in pipeline and becomes
Product maintain in optimum temperature range.Temperature-control Monitoring device B10 storage inside has the optimum temperature range needed for emulsifying, temperature
Control monitoring device B10 monitors between thermostat B7 and thermostat A6 the temperature of fat milk elementary semi-finished products in pipeline in real time,
Then the on-off control of Temperature-control Monitoring device B10 control flow control valve B22 and flow control valve E25 reaches to control constant temperature dress
Put between B7 and thermostat A6 fat milk elementary semi-finished products in pipeline to maintain in optimum temperature range.Temperature-control Monitoring device A9
Storage inside has the optimum temperature range needed for emulsifying, and it is defeated that Temperature-control Monitoring device A9 monitors the thermostat A6 port of export in real time
Sending the temperature of fat milk elementary semi-finished products in main pipe, then Temperature-control Monitoring device A9 controls flow control valve A21 and flow
The on-off control of regulation valve F26 reaches to control fat milk elementary semi-finished products dimension in thermostat A6 port of export delivery main's pipeline
Hold in optimum temperature range so that the fat milk elementary semi-finished products entered into colostrum tank 1 from conveying arm A maintains most preferably
In temperature range so that the fat milk elementary semi-finished products entered into homogenizing tank 2 from conveying arm B maintains optimum temperature range
In.The fat milk elementary semi-finished products entered in colostrum tank 1, homogenizing tank 2 is being transported to a next emulsifying through delivery pump 4
Process, after self-control circulating system self-loopa emulsifying process repeatedly, the fat milk product that high-quality, homogenization is high
Just can be discharged by this constant temperature system, in case follow-up use.
3) emulsifying completes the port of export and connects with thermostat B7 and thermostat A6 respectively, passes through flow control valve
B22, flow control valve E25, flow control valve A21, flow control valve F26, with reference to Temperature-control Monitoring device B10 and Temperature-control Monitoring dress
Put A9, it is achieved thermostatic control after emulsifying.
The present invention compared with the prior art, has the following advantages and beneficial effect:
Present invention ensures that the uniformity of fat milk product, reduce fat milk peroxide value and anisidine value, protect
Demonstrate,prove product quality, ensured that the fat milk product quality that human body is taken in is more stable, more high-end, also ensure that product storage cycle.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Wherein, entitled corresponding to the reference in accompanying drawing:
1-colostrum tank, 2-homogenizing tank, 3-glycerol pipe, 4-delivery pump, 5-homogenizer, 6-thermostat A, 7-are permanent
Temperature device B, 8-thermostat C, 9-Temperature-control Monitoring device A, 10-Temperature-control Monitoring device B, 11-Temperature-control Monitoring device C,
12-heat exchanger, 13-Temperature-control Monitoring device D, 14-coolant inlet pipe, 15-coolant goes out to manage, 16-water for injection inlet pipe,
21-flow control valve A, 22-flow control valve B, 23-flow control valve C, 24-flow control valve D, 25-Flow-rate adjustment
Valve E, 26-flow control valve F, 31-pneumatic diaphragm valve A, 32-pneumatic diaphragm valve B, 33-pneumatic diaphragm valve C, 34-is pneumatic
Diaphragm valve D, 35-pneumatic diaphragm valve E, 36-pneumatic diaphragm valve F, 37-pneumatic diaphragm valve G, 38-pneumatic diaphragm valve H, 39-
Pneumatic diaphragm valve I, 40-pneumatic diaphragm valve J, 41-pneumatic diaphragm valve K, 42-pneumatic diaphragm valve L, 43-pneumatic diaphragm valve M.
Detailed description of the invention
Below in conjunction with embodiment, the present invention is described in further detail:
Embodiment
As it is shown in figure 1, a kind of constant temperature system for improving fat milk product quality, including water for injection inlet pipe 16, just
Breast tank 1, homogenizing tank 2, glycerol pipe 3, delivery pump 4, homogenizer 5, coolant inlet pipe 14, coolant go out pipe 15 and constant temperature system, note
Penetrating and connect with water inlet pipe 16 is airtight with colostrum tank 1, between water for injection inlet pipe 16 with colostrum tank 1, airtight connection is provided with heat exchanger
12, colostrum tank 1 connects by pipeline is airtight with glycerol pipe 3, the pipeline between colostrum tank 1 and glycerol pipe 3 is provided with pneumatic every
Film valve K41；Colostrum tank 1 is connected by pipeline closed with the arrival end of delivery pump 4, the pipeline between colostrum tank 1 and delivery pump 4
On be sequentially provided with pneumatic diaphragm valve A31 and pneumatic diaphragm valve D34；Constant temperature system include thermostat A6 arranged in parallel,
Thermostat B7 and thermostat C8, the port of export of delivery pump 4 is airtight with the arrival end of thermostat C8 to be connected, thermostat C8
The port of export connected by pipeline closed with the arrival end of homogenizer 5, the pipeline between thermostat C8 and homogenizer 5 sets
Having temperature control to detect device C11, the port of export of homogenizer 5 is connected by pipeline closed with the arrival end of thermostat B7, and constant temperature fills
Put that the port of export of B7 is airtight with the arrival end of thermostat A6 to be connected, on the pipeline between thermostat B7 and thermostat A6
Being provided with Temperature-control Monitoring device B10, the port of export of thermostat A6 is airtight is communicated with delivery main, delivery main's airtight connection respectively
Having conveying arm A and conveying arm B, arm A is airtight with colostrum tank 1 top connects in conveying, conveying arm B and homogenizing tank 2 top
Airtight connection, is provided with Temperature-control Monitoring device A9 and pneumatic diaphragm valve F36, defeated on the delivery main of the thermostat A6 port of export
Send arm A to be provided with pneumatic diaphragm valve G37, conveying arm B is provided with pneumatic diaphragm valve H38 and pneumatic diaphragm valve I39；Homogenizing
Connect by pipeline is airtight with the arrival end of delivery pump 4 bottom tank 2, the pipeline between homogenizing tank 2 and delivery pump 4 is provided with gas
Dynamic diaphragm valve C33；It is communicated with coolant inlet pipe arm A, coolant inlet pipe arm B and coolant inlet pipe on coolant inlet pipe 14 to prop up
Pipe C, coolant inlet pipe arm A is airtight with thermostat A6 to be connected, and is provided with flow control valve A21 on coolant inlet pipe arm A,
It is communicated with coolant bottom thermostat A6 and goes out pipe arm A, go out in coolant and be provided with flow control valve F26 on pipe arm A, cooling
Liquid inlet pipe arm B is airtight with thermostat B7 to be connected, and is provided with flow control valve B22, thermostat on coolant inlet pipe arm B
Being communicated with coolant bottom B7 and go out pipe arm B, go out to be provided with flow control valve E25 on pipe arm B in coolant, coolant inlet pipe props up
Pipe C is airtight with thermostat C8 to be connected, and is provided with flow control valve C23 on coolant inlet pipe arm C, connects bottom temperature device C8
Being connected with coolant and go out pipe arm C, go out in coolant and be provided with flow control valve D24 on pipe arm C, coolant goes out pipe arm A, cooling
Liquid goes out pipe arm B, coolant goes out pipe arm C and goes out that pipe 15 is airtight to be connected respectively with coolant；Temperature control detection device C11 respectively with stream
Adjustable valve C23, flow control valve D24 connect, Temperature-control Monitoring device B10 respectively with flow control valve B22, flow control valve
E25 connects, and Temperature-control Monitoring device A9 is connected with flow control valve A21, flow control valve F26 respectively.
Between currently preferred water for injection inlet pipe 16 and colostrum tank 1, airtight connection is provided with Temperature-control Monitoring device D13, note
Penetrate and be provided with pneumatic diaphragm valve L42 and pneumatic diaphragm valve M43 with water inlet pipe 16, heat exchanger 12, Temperature-control Monitoring device D13, pneumatic
Diaphragm valve L42, pneumatic diaphragm valve M43 and colostrum tank 1 set gradually.
It is additionally provided with pneumatic diaphragm valve J40 on pipeline between currently preferred colostrum tank 1 and glycerol pipe 3.
It is additionally provided with pneumatic diaphragm valve B32, pneumatic diaphragm on pipeline between currently preferred colostrum tank 1 and delivery pump 4
Valve B32 is between pneumatic diaphragm valve A31 and pneumatic diaphragm valve D34.
The workflow of constant temperature system of the present invention is as follows:
1) water for injection injects preparation water spot through water for injection inlet pipe 16, and colostrum tank 1 passes through heat exchanger 12 to injection
Having carried out hyperthermic treatment with water, Temperature-control Monitoring device D13 storage inside has water for injection temperature optimum range, Temperature-control Monitoring device
D13 monitors the coolant-temperature gage in water for injection inlet pipe 16 in real time, and then Temperature-control Monitoring device D13 controls the intensification switch of heat exchanger 12
And the control of intensification size reaches to control fat milk in water for injection inlet pipe 16 and prepares use water and maintain optimum temperature range
In, it is finally reached fat milk and prepares the optimum temperature of use water.
2) during emulsifying, colostrum tank 1, homogenizing tank 2, delivery pump 4, homogenizer 5 and constant temperature system by pipeline and
Valve connection constitutes a self-control circulating system closed, and delivery pump 4 and thermostat C8 connect simultaneously, Temperature-control Monitoring device
C11 storage inside has the optimum temperature range needed for emulsifying, Temperature-control Monitoring device C11 to monitor thermostat C8 in real time with equal
The temperature of fat milk elementary semi-finished products in pipeline between matter machine 5, then Temperature-control Monitoring device C11 control flow control valve C23 and
The on-off control of flow control valve D24 reaches to control between thermostat C8 and homogenizer 5 fat milk primary half in pipeline and becomes
Product maintain in optimum temperature range.Temperature-control Monitoring device B10 storage inside has the optimum temperature range needed for emulsifying, temperature
Control monitoring device B10 monitors between thermostat B7 and thermostat A6 the temperature of fat milk elementary semi-finished products in pipeline in real time,
Then the on-off control of Temperature-control Monitoring device B10 control flow control valve B22 and flow control valve E25 reaches to control constant temperature dress
Put between B7 and thermostat A6 fat milk elementary semi-finished products in pipeline to maintain in optimum temperature range.Temperature-control Monitoring device A9
Storage inside has the optimum temperature range needed for emulsifying, and it is defeated that Temperature-control Monitoring device A9 monitors the thermostat A6 port of export in real time
Sending the temperature of fat milk elementary semi-finished products in main pipe, then Temperature-control Monitoring device A9 controls flow control valve A21 and flow
The on-off control of regulation valve F26 reaches to control fat milk elementary semi-finished products dimension in thermostat A6 port of export delivery main's pipeline
Hold in optimum temperature range so that the fat milk elementary semi-finished products entered into colostrum tank 1 from conveying arm A maintains most preferably
In temperature range so that the fat milk elementary semi-finished products entered into homogenizing tank 2 from conveying arm B maintains optimum temperature range
In.The fat milk elementary semi-finished products entered in colostrum tank 1, homogenizing tank 2 is being transported to a next emulsifying through delivery pump 4
Process, after self-control circulating system self-loopa emulsifying process repeatedly, the fat milk product that high-quality, homogenization is high
Just can be discharged by this constant temperature system, in case follow-up use.
3) emulsifying completes the port of export and connects with thermostat B7 and thermostat A6 respectively, passes through flow control valve
B22, flow control valve E25, flow control valve A21, flow control valve F26, with reference to Temperature-control Monitoring device B10 and Temperature-control Monitoring dress
Put A9, it is achieved thermostatic control after emulsifying.
The foregoing is only presently preferred embodiments of the present invention, not in order to limit the present invention, all essences in the present invention
Any amendment, equivalent and the improvement etc. made within god and principle, should be included within the scope of the present invention.
Claims (4)
1. one kind for improving the constant temperature system of fat milk product quality, it is characterised in that: include water for injection inlet pipe (16), just
Breast tank (1), homogenizing tank (2), glycerol pipe (3), delivery pump (4), homogenizer (5), coolant inlet pipe (14), coolant go out pipe (15)
And constant temperature system, described water for injection inlet pipe (16) is airtight with colostrum tank (1) to be connected, water for injection inlet pipe (16) and colostrum tank
(1) between, airtight connection is provided with heat exchanger (12), and described colostrum tank (1) connects, at colostrum by pipeline is airtight with glycerol pipe (3)
Pipeline between tank (1) and glycerol pipe (3) is provided with pneumatic diaphragm valve K (41)；Described colostrum tank (1) enters with delivery pump (4)
Mouth end is connected by pipeline closed, and the pipeline between colostrum tank (1) and delivery pump (4) is sequentially provided with pneumatic diaphragm valve A
And pneumatic diaphragm valve D (34) (31)；Described constant temperature system includes thermostat A (6), thermostat B (7) arranged in parallel
With thermostat C (8), the port of export of described delivery pump (4) is airtight with the arrival end of thermostat C (8) to be connected, and described constant temperature fills
The arrival end of the port of export and homogenizer (5) of putting C (8) is connected by pipeline closed, thermostat C (8) and homogenizer (5) it
Between pipeline be provided with temperature control detection device C (11), the arrival end of the port of export of described homogenizer (5) and thermostat B (7) leads to
The airtight connection of piping, the port of export of thermostat B (7) is airtight with the arrival end of thermostat A (6) to be connected, at thermostat B
(7) pipeline and between thermostat A (6) is provided with Temperature-control Monitoring device B (10), and the port of export of described thermostat A (6) is close
Closing and be communicated with delivery main, delivery main is the most airtight is communicated with conveying arm A and conveying arm B, conveying arm A and colostrum tank
(1) the airtight connection in top, arm B is airtight with homogenizing tank (2) top connects in conveying, total in the conveying of thermostat A (6) port of export
Pipe is provided with Temperature-control Monitoring device A (9) and pneumatic diaphragm valve F (36), is provided with pneumatic diaphragm valve G (37) on conveying arm A,
Conveying arm B is provided with pneumatic diaphragm valve H (38) and pneumatic diaphragm valve I (39)；Pipeline is passed through with defeated in described homogenizing tank (2) bottom
Send the airtight connection of arrival end of pump (4), the pipeline between homogenizing tank (2) and delivery pump (4) is provided with pneumatic diaphragm valve C
(33)；It is communicated with coolant inlet pipe arm A, coolant inlet pipe arm B and coolant inlet pipe on described coolant inlet pipe (14) to prop up
Pipe C, described coolant inlet pipe arm A and thermostat A (6) is airtight to be connected, and is provided with Flow-rate adjustment on coolant inlet pipe arm A
Valve A (21), thermostat A (6) bottom is communicated with coolant and goes out pipe arm A, goes out in coolant and is provided with Flow-rate adjustment on pipe arm A
Valve F (26), described coolant inlet pipe arm B and thermostat B (7) is airtight to be connected, and is provided with flow on coolant inlet pipe arm B
Regulation valve B (22), thermostat B (7) bottom is communicated with coolant and goes out pipe arm B, goes out in coolant and be provided with flow on pipe arm B
Regulation valve E (25), described coolant inlet pipe arm C and thermostat C (8) is airtight to be connected, and is provided with on coolant inlet pipe arm C
Flow control valve C (23), is communicated with coolant in temperature device C (8) bottom and goes out pipe arm C, go out in coolant and be provided with on pipe arm C
Flow control valve D (24), described coolant goes out pipe arm A, coolant goes out pipe arm B, coolant go out pipe arm C respectively with cooling
Liquid goes out pipe (15) airtight connection；Described temperature control detection device C (11) respectively with flow control valve C (23), flow control valve D (24)
Connecting, described Temperature-control Monitoring device B (10) is connected with flow control valve B (22), flow control valve E (25) respectively, described temperature control
Monitoring device A (9) is connected with flow control valve A (21), flow control valve F (26) respectively.
2. according to the constant temperature system for improving fat milk product quality described in claim 1, it is characterised in that: described injection
It is provided with Temperature-control Monitoring device D (13), described water for injection inlet pipe (16) with airtight connection between water inlet pipe (16) with colostrum tank (1)
It is provided with pneumatic diaphragm valve L (42) and pneumatic diaphragm valve M (43), described heat exchanger (12), Temperature-control Monitoring device D (13), pneumatic
Diaphragm valve L (42), pneumatic diaphragm valve M (43) and colostrum tank (1) set gradually.
3. according to the constant temperature system for improving fat milk product quality described in claim 1, it is characterised in that: described colostrum
Pneumatic diaphragm valve J (40) it is additionally provided with on pipeline between tank (1) and glycerol pipe (3).
4. according to the constant temperature system for improving fat milk product quality described in claim 1, it is characterised in that: described colostrum
Being additionally provided with pneumatic diaphragm valve B (32) on pipeline between tank (1) and delivery pump (4), described pneumatic diaphragm valve B (32) is positioned at pneumatic
Between diaphragm valve A (31) and pneumatic diaphragm valve D (34).
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