CN106074672B - 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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- CN106074672B CN106074672B CN201610565235.4A CN201610565235A CN106074672B CN 106074672 B CN106074672 B CN 106074672B CN 201610565235 A CN201610565235 A CN 201610565235A CN 106074672 B CN106074672 B CN 106074672B
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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
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- 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
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- 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
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- 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
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- 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
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- 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
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 invention relates to the field of fat emulsion preparation, in particular to a constant temperature system for improving the quality of fat emulsion products.
Background
Fat emulsion is a homogeneous and stable fat emulsion composed of refined soybean oil, glycerol, lecithin, etc., and its therapeutic importance is to provide high energy and essential fatty acids under parenteral feeding. The fat which is absorbed by human body from the stomach and intestine is proved to be absorbed by physiology and nutrition to form chylomicron, and the product has the shape and the composition which are extremely similar to those of chylomicron, and can be directly infused into the vein of a patient who cannot eat food to provide fat nutrition. In the production of the traditional fat emulsion, the peroxide value and the anisidine value are difficult to control, and the quality and quality of the product are directly influenced, so that the personal health of a user is harmed.
Disclosure of Invention
Aiming at the defects in the prior art, the invention aims to provide the constant temperature system for improving the quality of the fat emulsion product, so that the uniformity of the fat emulsion product is ensured, the peroxide value and the anisidine value of the fat emulsion are reduced, the product quality is ensured, the quality of the fat emulsion product ingested by a human body is more stable and higher, and the storage period of the product is also ensured.
The purpose of the invention is realized by the following technical scheme:
a constant temperature system for improving the quality of a fat emulsion product comprises an injection water inlet pipe, a colostrum tank, a homogenizing 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 communicated with the colostrum tank in a sealing way, a heat exchanger is arranged between the injection water inlet pipe and the colostrum tank in a sealing way, the colostrum tank is communicated with the glycerin pipe in a sealing way through a pipeline, and a pneumatic diaphragm valve K is arranged on the pipeline between the colostrum tank and the glycerin pipe; the colostrum tank is communicated with the inlet end of the delivery pump in a sealing way through a pipeline, and a pneumatic diaphragm valve A and a pneumatic diaphragm valve D are sequentially arranged on the pipeline between the colostrum tank and the delivery pump; 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 outlet end of the conveying pump is hermetically communicated with the inlet end of the constant temperature device C, the outlet end of the constant temperature device C is hermetically communicated with the inlet end of the homogenizer through a pipeline, a temperature control detection device C is arranged on the pipeline between the constant temperature device C and the homogenizer, the outlet end of the homogenizer is hermetically communicated with the inlet end of the constant temperature device B through a pipeline, the outlet end of the constant temperature device B is hermetically communicated with the inlet end of the constant temperature device A, a temperature control monitoring device B is arranged on the pipeline between the constant temperature device B and the constant temperature device A, the outlet end of the constant temperature device A is hermetically communicated with a conveying main pipe, the conveying main pipe is hermetically communicated with a conveying branch pipe A and a conveying branch pipe B respectively, the conveying branch pipe A is hermetically communicated with the top of the colostrum tank, and the conveying branch pipe B is hermetically communicated with the top of the homogenization tank, a temperature control monitoring device A and a pneumatic diaphragm valve F are arranged on a conveying main pipe at the outlet end of the constant temperature device A, a pneumatic diaphragm valve G is arranged on a conveying branch pipe A, and a pneumatic diaphragm valve H and a pneumatic diaphragm valve I are arranged on a conveying branch pipe B; the bottom of the homogenizing tank is hermetically communicated with the inlet end of the delivery pump through a pipeline, and a pneumatic diaphragm valve C is arranged on the pipeline between the homogenizing tank and the delivery pump; the cooling liquid inlet pipe is communicated with a cooling liquid inlet pipe branch pipe A, a cooling liquid inlet pipe branch pipe B and a cooling liquid inlet pipe branch pipe C, the cooling liquid inlet pipe branch pipe A is hermetically communicated with the constant temperature device A, the cooling liquid inlet pipe branch pipe A is provided with a flow regulating valve A, the bottom of the constant temperature device A is communicated with the cooling liquid outlet pipe branch pipe A, the cooling liquid outlet pipe branch pipe A is provided with a flow regulating valve F, the cooling liquid inlet pipe branch pipe B is hermetically communicated with the constant temperature device B, the cooling liquid inlet pipe branch pipe B is provided with a flow regulating valve B, the bottom of the constant temperature device B is communicated with the cooling liquid outlet pipe branch pipe B, the cooling liquid outlet pipe branch pipe B is provided with a flow regulating valve E, the cooling liquid inlet pipe branch pipe C is hermetically communicated with the constant temperature device C, the bottom of the temperature device C is communicated with the cooling liquid outlet pipe branch pipe C, the cooling liquid outlet pipe branch pipe C is provided with a flow regulating valve D, the cooling liquid outlet pipe branch A, the cooling liquid outlet pipe branch B and the cooling liquid outlet pipe branch C are respectively communicated with the cooling liquid outlet pipe in a sealing way; the temperature control detection device C is respectively connected with the flow regulating valve C and the flow regulating valve D, the temperature control monitoring device B is respectively connected with the flow regulating valve B and the flow regulating valve E, and the temperature control monitoring device A is respectively connected with the flow regulating valve A and the flow regulating valve F.
In order to better realize the invention, a temperature control monitoring device D is hermetically communicated between the injection water inlet pipe and the colostrum tank, a pneumatic diaphragm valve L and a pneumatic diaphragm valve M are arranged on the injection water inlet pipe, and the heat exchanger, the temperature control monitoring device D, the pneumatic diaphragm valve L, the pneumatic diaphragm valve M and the colostrum tank are sequentially arranged.
In order to enhance the power of the glycerin pipe for conveying materials to the colostrum tank, a pneumatic diaphragm valve J is further arranged on the pipeline between the colostrum tank and the glycerin pipe.
Preferably, a pneumatic diaphragm valve B is further arranged on a pipeline between the colostrum tank and the delivery pump, and the pneumatic diaphragm valve B is located between the pneumatic diaphragm valve A and the pneumatic diaphragm valve D.
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.
The constant temperature system of the invention has the following working procedures:
1) injection water is injected into a preparation water point through the injection water inlet pipe 16, the colostrum tank 1 carries out heating treatment on the injection water through the heat exchanger 12, the optimal temperature range of the injection water is stored in the temperature control monitoring device D13, the temperature control monitoring device D13 monitors the temperature of the injection water in the injection water inlet pipe 16 in real time, and then the temperature control monitoring device D13 controls the heating switch of the heat exchanger 12 and controls the heating size to control the fat emulsion preparation water in the injection water inlet pipe 16 to be maintained in the optimal temperature range and finally reach the optimal temperature of the fat emulsion preparation water.
2) In the homogenizing and emulsifying process, the primary emulsion tank 1, the homogenizing tank 2, the delivery pump 4, the homogenizer 5 and the constant temperature system are communicated by a pipeline and a valve thereof to form a closed self-control circulating system, meanwhile, the delivery pump 4 is connected with the constant temperature device C8, the optimal temperature range required by homogenizing and emulsifying is stored in the temperature control monitoring device C11, the temperature control monitoring device C11 monitors the temperature of the primary fat emulsion semi-finished product in the pipeline between the constant temperature device C8 and the homogenizer 5 in real time, and then the temperature control monitoring device C11 controls the on-off control of the flow regulating valve C23 and the flow regulating valve D24 to control the primary fat emulsion semi-finished product in the pipeline between the constant temperature device C8 and the homogenizer 5 to be maintained in the optimal temperature range. The optimal temperature range required by homogenizing and emulsifying is stored in the temperature control monitoring device B10, the temperature control monitoring device B10 monitors the temperature of the primary semi-finished product of the fat milk in the pipeline between the thermostatic device B7 and the thermostatic device A6 in real time, and then the temperature control monitoring device B10 controls the on-off control of the flow regulating valve B22 and the flow regulating valve E25 to control the primary semi-finished product of the fat milk in the pipeline between the thermostatic device B7 and the thermostatic device A6 to be maintained in the optimal temperature range. The temperature control monitoring device A9 stores the optimal temperature range required by homogenization, the temperature control monitoring device A9 monitors the temperature of the primary semi-finished product of the fat milk in the delivery main pipe at the outlet end of the thermostatic device A6 in real time, and then the temperature control monitoring device A9 controls the on-off control of the flow regulating valve A21 and the flow regulating valve F26 to control the primary semi-finished product of the fat milk in the delivery main pipe at the outlet end of the thermostatic device A6 to be maintained in the optimal temperature range, so that the primary semi-finished product of the fat milk entering the primary emulsion tank 1 from the delivery branch pipe A is maintained in the optimal temperature range, and the primary semi-finished product of the fat milk entering the homogenizing tank 2 from the delivery branch pipe B is maintained in the optimal temperature range. The primary semi-finished products of the fat milk entering the primary emulsion tank 1 and the primary semi-finished products of the fat milk entering the homogenizing tank 2 are conveyed to a next homogenizing and emulsifying process through the conveying pump 4, and after the primary semi-finished products of the fat milk pass through the self-circulation homogenizing and emulsifying process of the self-control circulation system for a plurality of times, high-quality and high-homogenization fat milk products can be discharged through the constant temperature system for subsequent use.
3) The outlet end of the homogenized emulsifying device is respectively connected with a thermostatic device B7 and a thermostatic device A6 in series, and thermostatic control after emulsification is realized by a flow regulating valve B22, a flow regulating valve E25, a flow regulating valve A21 and a flow regulating valve F26 according to a temperature control monitoring device B10 and a temperature control monitoring device A9.
Compared with the prior art, the invention has the following advantages and beneficial effects:
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.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Wherein, the names corresponding to the reference numbers in the drawings are:
1-a colostrum tank, 2-a homogenizing tank, 3-a glycerin pipe, 4-a delivery pump, 5-a homogenizer, 6-a constant temperature device A, 7-a constant temperature device B, 8-a constant temperature device C, 9-a temperature control monitoring device A, 10-a temperature control monitoring device B, 11-a temperature control monitoring device C, 12-a heat exchanger, 13-a temperature control monitoring device D, 14-a cooling liquid inlet pipe, 15-a cooling liquid outlet pipe, 16-an injection water inlet pipe, 21-a flow regulating valve A, 22-a flow regulating valve B, 23-a flow regulating valve C, 24-a flow regulating valve D, 25-a flow regulating valve E, 26-a flow regulating valve F, 31-a pneumatic diaphragm valve A, 32-a pneumatic diaphragm valve B, 33-a pneumatic diaphragm valve C, 34-a pneumatic diaphragm valve D, 35-a pneumatic diaphragm valve E, 36-a pneumatic diaphragm valve F, 37-a pneumatic diaphragm valve G, 38-a pneumatic diaphragm valve H, 39-a pneumatic valve I, 40-pneumatic diaphragm valves J, 41-pneumatic diaphragm valves K, 42-pneumatic diaphragm valves L, 43-pneumatic diaphragm valves M.
Detailed Description
The present invention will be described in further detail with reference to the following examples:
examples
As shown in fig. 1, a constant temperature system for improving the quality of a fat emulsion product comprises an injection water inlet pipe 16, a colostrum tank 1, a homogenization tank 2, a glycerin pipe 3, a delivery pump 4, a homogenizer 5, a cooling liquid inlet pipe 14, a cooling liquid outlet pipe 15 and a constant temperature system, wherein the injection water inlet pipe 16 is hermetically communicated with the colostrum tank 1, a heat exchanger 12 is hermetically communicated between the injection water inlet pipe 16 and the colostrum tank 1, the colostrum tank 1 is hermetically communicated with the glycerin pipe 3 through a pipeline, and a pneumatic diaphragm valve K41 is arranged on the pipeline between the colostrum tank 1 and the glycerin pipe 3; the colostrum tank 1 is communicated with the inlet end of the delivery pump 4 in a sealing way through a pipeline, and a pneumatic diaphragm valve A31 and a pneumatic diaphragm valve D34 are sequentially arranged on the pipeline between the colostrum tank 1 and the delivery pump 4; the constant temperature system comprises a constant temperature device A6, a constant temperature device B7 and a constant temperature device C8 which are arranged in parallel, the outlet end of the delivery pump 4 is communicated with the inlet end of the constant temperature device C8 in a sealing way, the outlet end of the constant temperature device C8 is communicated with the inlet end of the homogenizer 5 in a sealing way through a pipeline, a temperature control detection device C11 is arranged on the pipeline between the constant temperature device C8 and the homogenizer 5, the outlet end of the homogenizer 5 is communicated with the inlet end of the constant temperature device B7 in a sealing way, the outlet end of the constant temperature device B7 is communicated with the inlet end of the constant temperature device A6 in a sealing way, a temperature control monitoring device B10 is arranged on the pipeline between the constant temperature device B7 and the constant temperature device A6, the outlet end of the constant temperature device A6 is communicated with a delivery main pipe in a sealing way, the delivery main pipe is respectively communicated with a delivery branch pipe A and a delivery branch pipe B in a sealing way, the delivery branch pipe A and the delivery branch B A are communicated with the top of the tank 1 in a sealing way, the delivery branch B is communicated with the top of the tank 2 in a sealing way, a temperature control monitoring device A9 and a pneumatic diaphragm valve F36 are arranged on a conveying main pipe at the outlet end of the thermostatic device A6, a pneumatic diaphragm valve G37 is arranged on the conveying branch pipe A, and a pneumatic diaphragm valve H38 and a pneumatic diaphragm valve I39 are arranged on the conveying branch pipe B; the bottom of the homogenizing tank 2 is hermetically communicated with the inlet end of the delivery pump 4 through a pipeline, and a pneumatic diaphragm valve C33 is arranged on the pipeline between the homogenizing tank 2 and the delivery pump 4; a cooling liquid inlet pipe branch pipe A, a cooling liquid inlet pipe branch pipe B and a cooling liquid inlet pipe branch pipe C are communicated with the cooling liquid inlet pipe 14, the cooling liquid inlet pipe branch pipe A is communicated with a constant temperature device A6 in a sealing way, a flow regulating valve A21 is arranged on the cooling liquid inlet pipe branch pipe A, the bottom of a constant temperature device A6 is communicated with the cooling liquid outlet pipe branch pipe A, a flow regulating valve F26 is arranged on the cooling liquid outlet pipe branch pipe A, the cooling liquid inlet pipe branch pipe B is communicated with the constant temperature device B7 in a sealing way, a flow regulating valve B22 is arranged on the cooling liquid inlet pipe branch pipe B, the bottom of a constant temperature device B7 is communicated with the cooling liquid outlet pipe branch pipe B, a flow regulating valve E25 is arranged on the cooling liquid outlet pipe branch pipe B, the cooling liquid inlet pipe branch pipe C is communicated with the constant temperature device C8 in a sealing way, a flow regulating valve C23 is arranged on the cooling liquid inlet pipe branch pipe C, a cooling liquid outlet pipe branch pipe C is communicated with the bottom of the temperature device C8, a flow regulating valve D24 is arranged on the cooling liquid outlet pipe branch pipe C, the cooling liquid outlet pipe branch A, the cooling liquid outlet pipe branch B and the cooling liquid outlet pipe branch C are respectively communicated with the cooling liquid outlet pipe 15 in a sealing way; the temperature control detection device C11 is respectively connected with the flow regulating valve C23 and the flow regulating valve D24, the temperature control monitoring device B10 is respectively connected with the flow regulating valve B22 and the flow regulating valve E25, and the temperature control monitoring device A9 is respectively connected with the flow regulating valve A21 and the flow regulating valve F26.
According to the invention, a temperature control monitoring device D13 is preferably arranged between the injection water inlet pipe 16 and the colostrum tank 1 in a sealing and communicating manner, a pneumatic diaphragm valve L42 and a pneumatic diaphragm valve M43 are arranged on the injection water inlet pipe 16, and the heat exchanger 12, the temperature control monitoring device D13, the pneumatic diaphragm valve L42, the pneumatic diaphragm valve M43 and the colostrum tank 1 are sequentially arranged.
The preferred pipeline between the colostrum tank 1 and the glycerin pipe 3 is also provided with a pneumatic diaphragm valve J40.
The pipeline between the preferable colostrum tank 1 and the delivery pump 4 is also provided with a pneumatic diaphragm valve B32, and a pneumatic diaphragm valve B32 is positioned between the pneumatic diaphragm valve A31 and a pneumatic diaphragm valve D34.
The constant temperature system of the invention has the following working procedures:
1) injection water is injected into a preparation water point through the injection water inlet pipe 16, the colostrum tank 1 carries out heating treatment on the injection water through the heat exchanger 12, the optimal temperature range of the injection water is stored in the temperature control monitoring device D13, the temperature control monitoring device D13 monitors the temperature of the injection water in the injection water inlet pipe 16 in real time, and then the temperature control monitoring device D13 controls the heating switch of the heat exchanger 12 and controls the heating size to control the fat emulsion preparation water in the injection water inlet pipe 16 to be maintained in the optimal temperature range and finally reach the optimal temperature of the fat emulsion preparation water.
2) In the homogenizing and emulsifying process, the primary emulsion tank 1, the homogenizing tank 2, the delivery pump 4, the homogenizer 5 and the constant temperature system are communicated by a pipeline and a valve thereof to form a closed self-control circulating system, meanwhile, the delivery pump 4 is connected with the constant temperature device C8, the optimal temperature range required by homogenizing and emulsifying is stored in the temperature control monitoring device C11, the temperature control monitoring device C11 monitors the temperature of the primary fat emulsion semi-finished product in the pipeline between the constant temperature device C8 and the homogenizer 5 in real time, and then the temperature control monitoring device C11 controls the on-off control of the flow regulating valve C23 and the flow regulating valve D24 to control the primary fat emulsion semi-finished product in the pipeline between the constant temperature device C8 and the homogenizer 5 to be maintained in the optimal temperature range. The optimal temperature range required by homogenizing and emulsifying is stored in the temperature control monitoring device B10, the temperature control monitoring device B10 monitors the temperature of the primary semi-finished product of the fat milk in the pipeline between the thermostatic device B7 and the thermostatic device A6 in real time, and then the temperature control monitoring device B10 controls the on-off control of the flow regulating valve B22 and the flow regulating valve E25 to control the primary semi-finished product of the fat milk in the pipeline between the thermostatic device B7 and the thermostatic device A6 to be maintained in the optimal temperature range. The temperature control monitoring device A9 stores the optimal temperature range required by homogenization, the temperature control monitoring device A9 monitors the temperature of the primary semi-finished product of the fat milk in the delivery main pipe at the outlet end of the thermostatic device A6 in real time, and then the temperature control monitoring device A9 controls the on-off control of the flow regulating valve A21 and the flow regulating valve F26 to control the primary semi-finished product of the fat milk in the delivery main pipe at the outlet end of the thermostatic device A6 to be maintained in the optimal temperature range, so that the primary semi-finished product of the fat milk entering the primary emulsion tank 1 from the delivery branch pipe A is maintained in the optimal temperature range, and the primary semi-finished product of the fat milk entering the homogenizing tank 2 from the delivery branch pipe B is maintained in the optimal temperature range. The primary semi-finished products of the fat milk entering the primary emulsion tank 1 and the primary semi-finished products of the fat milk entering the homogenizing tank 2 are conveyed to a next homogenizing and emulsifying process through the conveying pump 4, and after the primary semi-finished products of the fat milk pass through the self-circulation homogenizing and emulsifying process of the self-control circulation system for a plurality of times, high-quality and high-homogenization fat milk products can be discharged through the constant temperature system for subsequent use.
3) The outlet end of the homogenized emulsifying device is respectively connected with a thermostatic device B7 and a thermostatic device A6 in series, and thermostatic control after emulsification is realized by a flow regulating valve B22, a flow regulating valve E25, a flow regulating valve A21 and a flow regulating valve F26 according to a temperature control monitoring device B10 and a temperature control monitoring device A9.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents and improvements made within the spirit and principle of the present invention are intended to be included within the scope of the present invention.
Claims (4)
1. A constant temperature system for improving the quality of a fat emulsion product, characterized in that: the device comprises an injection water inlet pipe (16), a colostrum tank (1), a homogenizing tank (2), a glycerin pipe (3), a delivery pump (4), a homogenizer (5), a cooling liquid inlet pipe (14), a cooling liquid outlet pipe (15) and a constant temperature system, wherein the injection water inlet pipe (16) is hermetically communicated with the colostrum tank (1), a heat exchanger (12) is hermetically communicated between the injection water inlet pipe (16) and the colostrum tank (1), the colostrum tank (1) is hermetically communicated with the glycerin pipe (3) through a pipeline, and a pneumatic diaphragm valve K (41) is arranged on the pipeline between the colostrum tank (1) and the glycerin pipe (3); the colostrum tank (1) is communicated with the inlet end of the delivery pump (4) in a sealed manner through a pipeline, and a pneumatic diaphragm valve A (31) and a pneumatic diaphragm valve D (34) are sequentially arranged on the pipeline between the colostrum tank (1) and the delivery pump (4); the constant temperature system comprises a constant temperature device A (6), a constant temperature device B (7) and a constant temperature device C (8) which are arranged in parallel, the outlet end of the delivery pump (4) is hermetically communicated with the inlet end of the constant temperature device C (8), the outlet end of the constant temperature device C (8) is hermetically communicated with the inlet end of the homogenizer (5) through a pipeline, a temperature control detection device C (11) is arranged on a pipeline between the constant temperature device C (8) and the homogenizer (5), the outlet end of the homogenizer (5) is hermetically communicated with the inlet end of the constant temperature device B (7), the outlet end of the constant temperature device B (7) is hermetically communicated with the inlet end of the constant temperature device A (6), a temperature control monitoring device B (10) is arranged on a pipeline between the constant temperature device B (7) and the constant temperature device A (6), and the outlet end of the constant temperature device A (6) is hermetically communicated with a delivery main pipe, the conveying main pipe is respectively communicated with a conveying branch pipe A and a conveying branch pipe B in a sealing manner, the conveying branch pipe A is communicated with the top of the primary emulsion tank (1) in a sealing manner, the conveying branch pipe B is communicated with the top of the homogenizing tank (2) in a sealing manner, the conveying main pipe at the outlet end of the constant temperature device A (6) is provided with a temperature control monitoring device A (9) and a pneumatic diaphragm valve F (36), the conveying branch pipe A is provided with a pneumatic diaphragm valve G (37), and the conveying branch pipe B is provided with a pneumatic diaphragm valve H (38) and a pneumatic diaphragm valve I (39); the bottom of the homogenizing tank (2) is hermetically communicated with the inlet end of the delivery pump (4) through a pipeline, and a pneumatic diaphragm valve C (33) is arranged on the pipeline between the homogenizing tank (2) and the delivery pump (4); the cooling liquid inlet pipe (14) is communicated with a cooling liquid inlet pipe branch pipe A, a cooling liquid inlet pipe branch pipe B and a cooling liquid inlet pipe branch pipe C, the cooling liquid inlet pipe branch pipe A is hermetically communicated with a constant temperature device A (6), the cooling liquid inlet pipe branch pipe A is provided with a flow regulating valve A (21), the bottom of the constant temperature device A (6) is communicated with a cooling liquid outlet pipe branch pipe A, the cooling liquid outlet pipe branch pipe A is provided with a flow regulating valve F (26), the cooling liquid inlet pipe branch pipe B is hermetically communicated with a constant temperature device B (7), the cooling liquid inlet pipe branch pipe B is provided with a flow regulating valve B (22), the bottom of the constant temperature device B (7) is communicated with a cooling liquid outlet pipe branch pipe B, the cooling liquid outlet pipe branch pipe B is provided with a flow regulating valve E (25), the cooling liquid inlet pipe branch pipe C is hermetically communicated with a constant temperature device C (8), and the cooling liquid inlet pipe branch pipe C is provided with a flow regulating valve C (23), a cooling liquid outlet pipe branch pipe C is communicated with the bottom of the temperature device C (8), a flow regulating valve D (24) is arranged on the cooling liquid outlet pipe branch pipe C, and the cooling liquid outlet pipe branch pipe A, the cooling liquid outlet pipe branch pipe B and the cooling liquid outlet pipe branch pipe C are respectively communicated with a cooling liquid outlet pipe (15) in a sealing manner; temperature control detection device C (11) are connected with flow control valve C (23), flow control valve D (24) respectively, temperature control monitoring devices B (10) are connected with flow control valve B (22), flow control valve E (25) respectively, temperature control monitoring devices A (9) are connected with flow control valve A (21), flow control valve F (26) respectively.
2. Thermostatic system for improving the quality of fat milk products according to claim 1, characterized in that: the injection water advances to be equipped with temperature control monitoring devices D (13) between pipe (16) and colostrum jar (1) airtight intercommunication, the injection water advances to be equipped with pneumatic diaphragm valve L (42) and pneumatic diaphragm valve M (43) on pipe (16), heat exchanger (12), temperature control monitoring devices D (13), pneumatic diaphragm valve L (42), pneumatic diaphragm valve M (43) and colostrum jar (1) set gradually.
3. Thermostatic system for improving the quality of fat milk products according to claim 1, characterized in that: and a pneumatic diaphragm valve J (40) is further arranged on a pipeline between the primary emulsion tank (1) and the glycerin pipe (3).
4. Thermostatic system for improving the quality of fat milk products according to claim 1, characterized in that: and a pneumatic diaphragm valve B (32) is further arranged on a pipeline between the primary emulsion tank (1) and the delivery pump (4), and the pneumatic diaphragm valve B (32) is positioned between the pneumatic diaphragm valve A (31) and the pneumatic diaphragm valve D (34).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201610565235.4A CN106074672B (en) | 2016-07-18 | 2016-07-18 | Constant temperature system for improving quality of fat milk product |
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| CN201610565235.4A CN106074672B (en) | 2016-07-18 | 2016-07-18 | Constant temperature system for improving quality of fat milk product |
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| CN106074672B true CN106074672B (en) | 2021-10-29 |
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Citations (8)
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