CN211794193U - Fruit and vegetable juice beverage production system - Google Patents

Fruit and vegetable juice beverage production system Download PDF

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Publication number
CN211794193U
CN211794193U CN202020354519.0U CN202020354519U CN211794193U CN 211794193 U CN211794193 U CN 211794193U CN 202020354519 U CN202020354519 U CN 202020354519U CN 211794193 U CN211794193 U CN 211794193U
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tank
filter
juice
communicated
heat exchanger
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陈俭春
张慧东
赵丽静
李雪莲
杨宁宁
张秀涛
贾文强
李俊雅
陈媛媛
张子谦
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Henan Labpark Chemical Equipment Manufacturing Co ltd
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Henan Labpark Chemical Equipment Manufacturing Co ltd
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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
    • A23N1/00—Machines or apparatus for extracting juice
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
    • A23L2/04—Extraction of juices
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/42—Preservation of non-alcoholic beverages
    • A23L2/46—Preservation of non-alcoholic beverages by heating
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/72—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
    • A23L2/76—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by removal of gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/16—Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Non-Alcoholic Beverages (AREA)

Abstract

The utility model discloses a fruit and vegetable juice beverage production system, fruit and vegetable juice beverage production system includes the juice extractor, the colloid mill, former juice jar, the metering tank, the tank of reassembling, first filter, vacuum degassing jar, the isotropic symmetry, the buffer tank, plate heat exchanger, second filter and product jar, juice extractor and colloid mill intercommunication, colloid mill and former juice jar intercommunication, former juice jar and metering tank intercommunication, metering tank and compound jar intercommunication, compound jar and first filter intercommunication, first filter and vacuum degassing jar intercommunication, vacuum degassing jar and isotropic symmetry intercommunication, isotropic symmetry and buffer tank intercommunication, buffer tank and plate heat exchanger intercommunication, plate heat exchanger and second filter intercommunication, second filter and product jar intercommunication. The utility model discloses system safety and stability is high-efficient, can synthesize production fruit vegetables juice.

Description

Fruit and vegetable juice beverage production system
Technical Field
The utility model belongs to the technical field of beverage production, concretely relates to fruit and vegetable juice beverage production system.
Background
The beverage is a daily food, provides water required by human body, and can supplement various nutrient elements of various vitamins and mineral elements, and is an indispensable food. The beverage industry in China is relatively late in development, starts to rise in the 80 s, and has a very long history in foreign countries, so that the beverage production in China has great progress space from many aspects such as scale, process, equipment and the like. According to statistics, the average annual growth rate of the beverage market in China is more than 16% from less than 30 ten thousand tons in 1980 to 18345.24 ten thousand tons in 2016. But compared with developed countries such as Europe and America, the beverage industry in China has huge development prospect.
The current situation faced by the development of the beverage industry in China currently faces the following difficulties: (1) the beverage production equipment is relatively backward and lacks innovation capability; (2) the beverage formula has single multifunctionality and insufficient scientific research and development capability; (3) the beverage industry lacks standard and unified standardized production requirements; (4) there is a lack of processing equipment for various, high quality beverage industries. Therefore, the current production situation of the industrial fresh fruit and vegetable juice beverage needs to be improved, and a production system and a process capable of producing the fruit and vegetable juice beverage safely and efficiently are sought.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a fruit and vegetable juice beverage production system that safety and stability is high-efficient, can synthesize fruit and vegetable juice.
Based on the above-mentioned purpose, the utility model discloses take following technical scheme:
a fruit and vegetable juice beverage production system comprises a juicer, a colloid mill, a raw juice tank, a metering tank, a compound tank, a first filter, a vacuum degassing tank, a homogenizer, a buffer tank, a plate heat exchanger, a second filter and a product tank.
Furthermore, the fruit and vegetable juice beverage production system further comprises a steam device, a vacuum device, a cooling water return device, a tap water feeding device and a pure water feeding device, wherein the steam device is respectively communicated with the compound tank, the buffer tank and the plate heat exchanger, the vacuum device is respectively communicated with the metering tank, the compound tank, the vacuum degassing tank, the buffer tank and the product tank, the cooling water return device is respectively communicated with the colloid mill and the plate heat exchanger, the tap water feeding device is respectively communicated with the colloid mill and the plate heat exchanger, and the pure water feeding device is respectively communicated with the colloid mill and the metering tank.
Further, the number of the plate heat exchangers is at least 2, and the plate heat exchangers are connected in series.
Furthermore, the fruit and vegetable juice beverage production system also comprises a CIP cleaning device which is respectively communicated with the raw juice tank, the compound tank, the first filter, the vacuum degassing tank, the buffer tank and the product tank.
Furthermore, the fruit and vegetable juice beverage production system further comprises a pollution discharge device, and the pollution discharge device is respectively communicated with the compound tank, the first filter, the buffer tank, the plate type heat exchanger and the product tank.
Further, colloid mill and stock tank between be equipped with first three-way valve, first three-way valve intercommunication colloid mill's material import, colloid mill's material export and stock juice tank's material import, be equipped with the second three-way valve between isotropic symmetry and the buffer tank, the material import of second three-way valve intercommunication isotropic symmetry, the material export of isotropic symmetry and the material import of buffer tank, be equipped with the third three-way valve between plate heat exchanger and the second filter, the material export of third three-way valve intercommunication plate filter, the material import of second filter and the material import of buffer tank.
Furthermore, a raw material pump is connected between a material outlet of the compound tank and a material inlet of the compound tank, an electric pump is connected between the vacuum degassing tank and the homogenizer, and a centrifugal pump is connected between the buffer tank and the plate heat exchanger.
Furthermore, a compound tank viewing mirror opening is formed in the top of the compound tank, and a buffer tank viewing mirror opening is formed in the top of the buffer tank.
A method of using a juice production system, comprising the steps of: (1) putting fruits and vegetables into a juicer to squeeze juice, enabling the juice to flow into a colloid mill to be subjected to self-circulation homogenization, then enabling the juice to enter a raw juice tank for storage, then introducing the juice into a metering tank for metering, then enabling the juice to enter a compounding tank from the metering tank, adding sugar, citric acid and a compound stabilizer into the compounding tank, and mixing and stirring the juice together to generate a compounding liquid;
(2) and (2) enabling the compound liquid in the compound tank in the step (1) to flow into a first filter for filtering, then entering a vacuum degassing tank for degassing, entering a homogenizer for homogenizing and refining, then flowing into a buffer tank for collection, introducing into a plate heat exchanger for sterilization, and finally flowing into a product tank after being filtered by a second filter.
Further, the composite stabilizer comprises carboxymethyl cellulose, carrageenan and xanthan gum.
The utility model discloses the juice extractor carries out the fruit vegetables breakage in the system, the juice flesh separation, and then produce the juice, the colloid mill plays the self-loopa homogeneity, the effect of juice emulsification, the juice can be stored to the fumet jar, the metering tank can accurately measure the juice, the quantity of pure water, juice and other auxiliary materials can mix the stirring in compound jar, carry out the prefilter of compound liquid through first filter, the vacuum degassing jar can realize the degasification of compound liquid, the effect of isotropic symmetry is that the homogeneity of compound liquid refines, the compound liquid after the homogeneity refines can be collected to the buffer tank, plate heat exchanger has the effect of disinfecting and cooling, the second filter carries out final filtration to compound liquid, the product jar is used for collecting final product fruit vegetables juice.
The vacuum device in the system of the utility model is used for keeping the vacuum environment of part of devices; the tap water feeding device and the pure water feeding device are respectively convenient for providing tap water and pure water; the steam device and the cooling water backwater device adopt CIP cleaning devices, so that the online cleaning can be carried out in time, the whole system is enabled to operate stably, the continuous work can be carried out for a long time, and the practical use requirements are met; the sewage draining device is used for conveniently draining the waste generated in the system.
The utility model discloses each device cooperation of system is inseparable, and the method is simple, low in production cost, and the safety and stability is high-efficient, can synthesize production fruit vegetables juice, and production efficiency is high.
Drawings
FIG. 1 is a general system diagram of the present invention;
figure 2 is a schematic view of the juice extractor in communication with a first filter;
FIG. 3 is a schematic view of the communication between the vacuum degassing tank and the product tank;
FIG. 4 is a schematic structural view of a reconstitution tank;
FIG. 5 is a schematic structural view of a buffer tank;
fig. 6 is a schematic structural view of a plate heat exchanger.
Detailed Description
As shown in fig. 1-6, the system for producing fruit and vegetable juice beverage comprises a juicer 1, a colloid mill 2, a raw juice tank 3, a metering tank 4, a blending tank 5, a first filter 6, a vacuum degassing tank 7, a homogenizer 8, a buffer tank 9, a plate heat exchanger 10, a second filter 11 and a product tank 12. The material outlet 102 of the juice extractor is communicated with a colloid mill material inlet 201, the colloid mill material outlet 202 is communicated with a raw juice tank material inlet 301, the raw juice tank material outlet 302 is communicated with a metering tank material inlet 401, the metering tank material outlet 402 is communicated with a compounding tank first material inlet 501, a compounding tank material outlet 502 is communicated with a first filter material inlet 601, a first filter material outlet 602 is communicated with a vacuum degassing tank material inlet 701, a vacuum degassing tank material outlet 702 is communicated with a homogenizer material inlet 801, a homogenizer material outlet 802 is communicated with a buffer tank first material inlet 901, a buffer tank material outlet 902 is communicated with a plate heat exchanger first material inlet 1001, 2 plate heat exchangers 10 are connected in series, a plate heat exchanger first material outlet 1007 is communicated with a plate heat exchanger second material inlet 1008, a plate heat exchanger second material outlet 1002 is communicated with a second filter material inlet 1101, the second filter material outlet 1102 is in communication with the product tank material inlet 1201.
The fruit and vegetable juice beverage production system further comprises a steam device 13, and the steam device 13 is respectively communicated with the compound tank steam inlet 503, the buffer tank steam inlet 903 and the plate type heat exchanger steam inlet 1003. The fruit and vegetable juice beverage production system further comprises a vacuum device 14, wherein the vacuum device 14 is respectively communicated with the metering tank vacuum inlet 403, the compounding tank vacuum inlet 504, the vacuum degassing tank vacuum inlet 703, the buffer tank vacuum inlet 904 and the product tank vacuum inlet 1203. The fruit and vegetable juice beverage production system further comprises a cooling water return device 15, and the cooling water return device 15 is respectively communicated with the colloid mill cooling water outlet 203 and the plate heat exchanger cooling water outlet 1004. The fruit and vegetable juice beverage production system further comprises a tap water feeding device 16, and the tap water feeding device 16 is respectively communicated with the colloid mill tap water inlet 204 and the plate heat exchanger tap water inlet 1005. The fruit and vegetable juice beverage production system further comprises a pure water watering device 17, and the pure water watering device 17 is respectively communicated with the colloid mill material inlet 201 and the metering tank material inlet 401.
The fruit and vegetable juice beverage production system further comprises a CIP cleaning device 19, the CIP cleaning device 19 comprises a CIP liquid outlet 1901 and a CIP liquid inlet 1902, the CIP liquid outlet 1901 is respectively communicated with the juice tank CIP inlet 303, the compound tank CIP inlet 506, the first filter material outlet 602, the vacuum degassing tank CIP inlet 704, the buffer tank CIP inlet 907 and the product tank CIP inlet 1204, and the CIP liquid inlet 1902 is respectively communicated with the juice tank material outlet 302, the first filter material inlet 601, the vacuum degassing tank material outlet 702, the buffer tank material outlet 902 and the product tank material outlet 1202. The fruit and vegetable juice beverage production system further comprises a pollution discharge device 20, and the pollution discharge device 20 is respectively communicated with the compound tank pollution discharge outlet 505, the first filter material inlet 601, the buffer tank pollution discharge outlet 905, the plate heat exchanger pollution discharge outlet 1006 and the product tank material outlet 1202.
A first three-way valve 21 is arranged between the colloid mill material outlet 202 and the raw juice tank material inlet 301, and the first three-way valve 21 is communicated with the colloid mill material inlet 201, the colloid mill material outlet 202 and the raw juice tank material inlet 301. A second three-way valve 22 is arranged between the homogenizer material outlet 802 and the buffer tank first material inlet 901, and the second three-way valve 22 is communicated with the homogenizer material inlet 801, the homogenizer material outlet 802 and the buffer tank first material inlet 901. A third three-way valve 23 is arranged between the plate type heat exchanger second material outlet 1002 and the second filter material inlet 1101, and the third three-way valve 23 is communicated with the plate type heat exchanger second material outlet 1002, the second filter material inlet 1101 and the buffer tank second material inlet 906. A raw material pump 24 is connected between the material outlet 502 of the compound tank and the second material inlet 507 of the compound tank, an electric pump 25 is connected between the vacuum degassing tank 7 and the homogenizer 8, and a centrifugal pump 26 is connected between the buffer tank 9 and the plate heat exchanger 10. The top of the compound tank 5 is provided with a compound tank sight glass port 508, and the top of the buffer tank 9 is provided with a buffer tank sight glass port 908.
A method of using a juice production system, comprising the steps of: (1) putting fruits and vegetables into a juicer 1 to squeeze juice, enabling the juice to flow into a colloid mill 2 to be subjected to self-circulation homogenization, then enabling the juice to enter a raw juice tank 3 to be stored, then enabling the juice to enter a metering tank 4 to be metered, enabling the juice to enter a compounding tank 5 from the metering tank 4, adding sugar, citric acid and a compound stabilizer into the compounding tank 5, mixing and stirring the mixture and the juice together, and enabling the compound stabilizer to comprise carboxymethyl cellulose, carrageenan and xanthan gum to generate a compound liquid;
(2) and (2) enabling the compound liquid in the compound tank 5 in the step (1) to flow into a first filter 6 for filtering, then enabling the compound liquid to enter a vacuum degassing tank 7 for degassing, then entering a homogenizer 8 for homogenizing and refining, then flowing into a buffer tank 9 for collecting, introducing into a plate heat exchanger 10 for sterilization, and finally enabling the compound liquid to flow into a product tank 12 after being filtered by a second filter 11.
When the fruit and vegetable juice refining and homogenizing device is used, fresh fruits and vegetables are cleaned and cut into pieces, the fresh fruits and vegetables are added into a Weifeng WF-A3000 juicer 1, the juicer 1 is operated, fruit and vegetable juice flows from a material outlet 102 of the juicer to a material inlet 201 of a high-fidelity JM-L65 colloid mill, self-circulation homogenization is carried out in a colloid mill 3, a material outlet 202 of the colloid mill and the material inlet 201 of the colloid mill are communicated by a first three-way valve 21 during the self-circulation homogenization, after the fruit and vegetable juice particles are refined and homogenized, the fruit and vegetable juice flows from the material outlet 202 of the colloid mill to a material inlet 301 of a raw juice tank, the fruit and vegetable juice is stored in the raw juice tank 3, a small amount of pure water is used for. Fruit and vegetable juice in the raw juice tank 3 flows into a metering tank material inlet 401 from a raw juice tank material outlet 302 for metering, then flows into a first material inlet 501 of a compounding tank from a metering tank material outlet 402, after the metering tank is reset and calibrated, pure water is added into a metering tank 4 for metering, then flows into the first material inlet 501 of the compounding tank from the metering tank material outlet 402, internal circulation slow stirring is carried out in the compounding tank 5, steam is sent into a steam inlet 503 of the compounding tank through a steam device 13, when the required temperature is reached, sugar, citric acid and a composite stabilizer which are dried and uniformly mixed are slowly added through a vision mirror port 508 of the compounding tank, and the mass ratio of the fruit and vegetable juice, the sugar, the citric acid and the composite stabilizer is 1-2.5 Kg: 1-2.5 Kg: 10-25 g: 25-62.5g, wherein the composite stabilizer comprises carboxymethyl cellulose, carrageenan and xanthan gum, and the mass ratio of the carboxymethyl cellulose to the carrageenan to the xanthan gum is 15-37.5 g: 4-10 g: 6-15g, after the dissolution of the larger powder particles in the compounding tank 5 is finished, starting the raw material pump 24, enabling the materials to flow into a second material inlet 507 of the compounding tank through a material outlet 502 of the compounding tank for external circulation stirring, and stopping the internal and external circulation stirring after the materials in the compounding tank 5 are uniformly stirred.
The fruit and vegetable compound liquid in the compound tank 5 flows into a first filter material inlet 601 from a compound tank material outlet 502, a first filter 6 is a pipeline filter, primary filtration is carried out in the first filter 6, the filtered fruit and vegetable compound liquid flows into a vacuum degassing tank material inlet 701 from a first filter material outlet 602, the initial degassing pressure of a vacuum degassing tank 7 is-0.03 MPa, a vacuum environment is kept, the temperature of the fruit and vegetable compound liquid is 50-70 ℃ during degassing, in order to avoid boiling of materials, the negative pressure in the vacuum degassing tank 7 is below-0.07 MPa during thermal degassing. The vacuum degassed fruit and vegetable compound liquid flows into a homogenizer material inlet 801 of a bench laboratory through a vacuum degassing tank material outlet 702 by an electric pump, homogenization and refinement are carried out within the range of 25-35 Mpa, and meanwhile, a homogenizer material outlet 802 and the homogenizer material inlet 801 are communicated by a second three-way valve 22, so that circulation homogenization and refinement are realized. After homogenizing and refining, the homogenized material flows into a first material inlet 901 of a buffer tank from a material outlet 802 of the homogenizer, when the homogenized material is collected, the pressure in the buffer tank 9 is controlled at-0.03 to-0.06 Mpa, the state is changed into the normal pressure state after the collection is finished, if other auxiliary materials need to be added, the auxiliary materials can be added and stirred uniformly through a viewing port 908 of the buffer tank, the collected fruit and vegetable compound liquid is heated to 60 ℃ through steam, and the fruit and vegetable compound liquid flows into the first material inlet 1001 of the plate heat exchanger from a material outlet 902 of the buffer tank through a centrifugal pump 26. When the fruit and vegetable compound liquid flows out of the first material outlet 1007 of the plate heat exchanger, the temperature of the first material outlet 1007 of the plate heat exchanger is guaranteed to be 105-110 ℃, 2 plate heat exchangers 10 are connected in series, the fruit and vegetable compound liquid is sterilized and cooled in the plate heat exchanger 10, tap water is introduced to reduce the temperature of the second outlet 1002 of the plate heat exchanger to 60 ℃, and the fruit and vegetable compound liquid flows into the material inlet 1101 of the second filter from the second material outlet 1002 of the plate heat exchanger. If the sterilization process of the plate heat exchanger 10 does not meet the above conditions, the fruit and vegetable compound liquid can flow from the plate heat exchanger 10 to the buffer tank 9 through the second material inlet 906 of the buffer tank through the third three-way valve 23, and the sterilization operation is performed again. The second filter 11 is also a pipeline filter, the fruit and vegetable compound liquid is finally filtered in the second filter 11, and flows into the material inlet 1201 of the product tank after being filtered, and is stored as fruit and vegetable juice beverage in the product tank 12.

Claims (8)

1. The fruit and vegetable juice beverage production system is characterized by comprising a juicer, a colloid mill, a raw juice tank, a metering tank, a compound tank, a first filter, a vacuum degassing tank, a homogenizer, a buffer tank, a plate type heat exchanger, a second filter and a product tank, wherein the juicer is communicated with the colloid mill, the colloid mill is communicated with the raw juice tank, the raw juice tank is communicated with the metering tank, the metering tank is communicated with the compound tank, the compound tank is communicated with the first filter, the first filter is communicated with the vacuum degassing tank, the vacuum degassing tank is communicated with the homogenizer, the homogenizer is communicated with the buffer tank, the buffer tank is communicated with the plate type heat exchanger, the plate type heat exchanger is communicated with the second filter, and the second filter is communicated with the product tank.
2. The system for producing fruit and vegetable juice beverage according to claim 1, further comprising a steam device, a vacuum device, a cooling water returning device, a tap water feeding device and a pure water feeding device, wherein the steam device is respectively communicated with the blending tank, the buffer tank and the plate heat exchanger, the vacuum device is respectively communicated with the metering tank, the blending tank, the vacuum degassing tank, the buffer tank and the product tank, the cooling water returning device is respectively communicated with the colloid mill and the plate heat exchanger, the tap water feeding device is respectively communicated with the colloid mill and the plate heat exchanger, and the pure water feeding device is respectively communicated with the colloid mill and the metering tank.
3. The juice beverage production system according to claim 1, wherein the number of plate heat exchangers is at least 2, and the plate heat exchangers are connected in series.
4. The juice beverage producing system according to claim 1, further comprising a CIP cleaning device, wherein the CIP cleaning device is connected to the juice tank, the reconstitution tank, the first filter, the vacuum degassing tank, the buffer tank, and the product tank.
5. The juice beverage producing system according to claim 1, further comprising a blowdown device, wherein the blowdown device is respectively communicated with the blending tank, the first filter, the buffer tank, the plate heat exchanger, and the product tank.
6. The system of claim 1, wherein a first three-way valve is disposed between the colloid mill and the juice tank, the first three-way valve is connected to the material inlet of the colloid mill, the material outlet of the colloid mill and the material inlet of the juice tank, a second three-way valve is disposed between the homogenizer and the buffer tank, the second three-way valve is connected to the material inlet of the homogenizer, the material outlet of the homogenizer and the material inlet of the buffer tank, a third three-way valve is disposed between the plate heat exchanger and the second filter, and the third three-way valve is connected to the material outlet of the plate filter, the material inlet of the second filter and the material inlet of the buffer tank.
7. The system for producing fruit and vegetable juice beverage according to claim 1, wherein a raw material pump is connected between the material outlet of the compounding tank and the material inlet of the compounding tank, an electric pump is connected between the vacuum degassing tank and the homogenizer, and a centrifugal pump is connected between the buffer tank and the plate heat exchanger.
8. The fruit and vegetable juice beverage production system according to claim 1, wherein a compound tank viewing mirror opening is arranged at the top of the compound tank, and a buffer tank viewing mirror opening is arranged at the top of the buffer tank.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111165833A (en) * 2020-01-16 2020-05-19 河南莱帕克化工设备制造有限公司 Fruit and vegetable juice beverage production system and method

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FR860684A (en) * 1939-07-01 1941-01-21 Method and apparatus for processing fruit, grape and vegetable juices for preservation
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CN211794193U (en) * 2020-01-16 2020-10-30 河南莱帕克化工设备制造有限公司 Fruit and vegetable juice beverage production system

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Publication number Priority date Publication date Assignee Title
CN111165833A (en) * 2020-01-16 2020-05-19 河南莱帕克化工设备制造有限公司 Fruit and vegetable juice beverage production system and method
CN111165833B (en) * 2020-01-16 2023-12-29 河南莱帕克化工设备制造有限公司 Fruit and vegetable juice beverage production system and method thereof

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