CN110562905A - Soda water beverage production system based on heat pump - Google Patents

Soda water beverage production system based on heat pump Download PDF

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Publication number
CN110562905A
CN110562905A CN201910907424.9A CN201910907424A CN110562905A CN 110562905 A CN110562905 A CN 110562905A CN 201910907424 A CN201910907424 A CN 201910907424A CN 110562905 A CN110562905 A CN 110562905A
Authority
CN
China
Prior art keywords
water
pipeline
heat exchanger
water tank
heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201910907424.9A
Other languages
Chinese (zh)
Inventor
苏传霞
吴国江
徐乐源
郭浩
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Stuart Warner Air Conditioning Equipment Co Ltd
Shanghai Jiaotong University
Original Assignee
Shanghai Stuart Warner Air Conditioning Equipment Co Ltd
Shanghai Jiaotong University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Stuart Warner Air Conditioning Equipment Co Ltd, Shanghai Jiaotong University filed Critical Shanghai Stuart Warner Air Conditioning Equipment Co Ltd
Priority to CN201910907424.9A priority Critical patent/CN110562905A/en
Publication of CN110562905A publication Critical patent/CN110562905A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65BMACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
    • B65B63/00Auxiliary devices, not otherwise provided for, for operating on articles or materials to be packaged
    • B65B63/08Auxiliary devices, not otherwise provided for, for operating on articles or materials to be packaged for heating or cooling articles or materials to facilitate packaging
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67CCLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C7/00Concurrent cleaning, filling, and closing of bottles; Processes or devices for at least two of these operations
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B30/00Heat pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D3/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium flows in a continuous film, or trickles freely, over the conduits
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices For Dispensing Beverages (AREA)

Abstract

The invention relates to the technical field of beverage processing, and particularly discloses a steam-water beverage production system based on a heat pump, which comprises a raw material channel and a raw material water pipeline, wherein the raw material channel is connected with an inlet of a mixing cylinder; the outlet of the mixing cylinder is connected with the filling and capping device through a mixed liquid pipeline, and a cooler is arranged on the mixed liquid pipeline; a thermos bottle machine is arranged at the downstream of the filling and sealing device, and comprises a spraying device and a water tank positioned below the spraying device; the water tank is connected with a spray water pipeline, and the spray water pipeline firstly flows through a cold side channel of the heat exchanger from the water tank; and a third heat exchanger is arranged in the water tank. The embodiment of the invention can realize the full utilization of energy, reduces the electric energy consumed by the heater and the cooler in the production line simultaneously, thereby realizing the soda water beverage production line with the aim of energy saving and further providing free cooling for operators at each station on site.

Description

Soda water beverage production system based on heat pump
Technical Field
the invention relates to a production line, in particular to a soda water beverage production line, and specifically relates to a soda water beverage production system based on a heat pump.
Background
The prior production process of the carbonated beverage usually comprises four processes of mixing ratio/carbonization, filling and sealing, thermos bottle and packaging, wherein the mixing ratio/carbonization process refers to a process of mixing syrup and other raw materials (raw juice) with raw water in a mixing cylinder, and the mixing cylinder needs to be cooled from about 28 ℃ to 7 ℃ before the carbonated beverage is filled, so that the electric energy of a refrigerator needs to be consumed to realize cooling; the thermos bottle process refers to heating the product after filling or before packaging from about 8 ℃ to the dew point temperature to avoid the occurrence of condensed water on the surface of the product, so that the water in a water tank of the thermos bottle machine is heated to 38-44 ℃ by steam, and then atomized spraying is carried out above the moving product to realize heating.
In the existing soda water beverage filling production line, a thermos bottle heating system, a mixing ratio cooling system and a connecting pipeline thereof are independent, so that energy is consumed in the cooling and heating processes, and the energy consumption of the whole production line is large. Therefore, how to provide a soda water beverage production line which can realize the effective transmission of heat and cold by mutually linking a cooling link and a heating link in the production line through a heat pump technology and a heat exchange device, thereby realizing the purpose of energy conservation is a technical problem which needs to be solved urgently.
Disclosure of Invention
An object of an embodiment of the present invention is to provide a system for producing carbonated beverages based on a heat pump, so as to solve the problems mentioned in the background art. In order to achieve the above purpose, the embodiments of the present invention provide the following technical solutions:
A heat pump-based soda water beverage production system comprises a raw material channel and a raw material water pipeline, wherein the raw material channel is connected with an inlet of a mixing cylinder;
The outlet of the mixing cylinder is connected with the filling and capping device through a mixed liquid pipeline, and a cooler is arranged on the mixed liquid pipeline; a thermos bottle machine is arranged at the lower part of the filling and capping device, the thermos bottle machine comprises a spraying device and a water tank positioned below the spraying device, the spraying device sprays atomized steam onto the beverage bottle to heat the beverage bottle, and water sprayed onto the beverage bottle is cooled and flows into the water tank;
The water tank is connected with a spray water pipeline, the spray water pipeline firstly flows through a cold side channel of the heat exchanger by the water tank, then flows through a heater and finally is connected with the spray device, and the cyclic utilization of spray water is realized;
A third heat exchanger is arranged in the water tank, two sides of the third heat exchanger are connected with a condenser side interface of the heat pump through pipelines, the third heat exchanger circularly heats water in the water tank through the heat pump, and an evaporator side of the heat pump absorbs heat from a mixing operation station, a filling operation station, a thermos bottle operation station, a fan coil in a packaging operation station and the second heat exchanger through water circulation in the pipelines, and sends the heat to one side connected with the water tank heat exchanger through internal conversion of the heat pump, so that the water in the water tank is heated by the third heat exchanger;
The water tank is also connected with a water taking pipeline; a water level valve is arranged in the water tank and connected to the water replenishing pipeline; the water level valve adopts a float valve, when the water in the water tank is lower than a preset height in the working process of the production line, the water level valve is opened, and external water enters the water tank through a water replenishing pipeline.
As a further scheme of the invention: a first water pump is arranged on the raw material water pipeline; and a second water pump is arranged on the spray water pipeline.
As a further scheme of the invention: and a third water pump is arranged on a pipeline at the side where the heat pump is connected with the third heat exchanger in the water tank.
As a further scheme of the invention: and a fourth water pump is arranged on a pipeline connecting the heat pump and the second heat exchanger of the raw water pipeline so as to provide pressure for the flow of water in the pipeline.
as a further scheme of the invention: the heater adopts a steam heater, and the steam heater is a coil type steam heater.
As a further scheme of the invention: the first heat exchanger and the second heat exchanger adopt plate heat exchangers.
As a further scheme of the invention: the cooler is a heat exchanger filled with chilled water, in particular a plate heat exchanger.
compared with the prior art, the embodiment of the invention connects the raw water pipeline and the spray water pipeline by the heat exchanger and the water source heat pump, interconnects the cooling link and the heating link in the production line, transfers the energy extracted from the cooling link to the heating link through the heat pump and the heat exchanger, realizes the full utilization of the energy, reduces the electric energy consumed by the heater and the cooler in the production line at the same time, thereby realizing the soda water beverage production line with the purpose of energy saving and further providing free cooling for operators at each station on site.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention.
Fig. 1 is a schematic structural diagram of a beverage production system based on a heat pump according to an embodiment of the present invention.
In the figure: 1-a raw material channel, 2-a first water pump, 3-a first heat exchanger, 4-a second heat exchanger, 5-a raw material water pipeline, 6-a mixing cylinder, 7-a cooler, 8-a second water pump, 9-a filling and capping device and 10-a heater;
11-a thermos bottle machine, 12-a third heat exchanger, 13-a spraying device, 14-a water level valve, 15-an electromagnetic valve heat exchanger, 16-a packaging machine, 17-a water taking pipeline, 18-a water replenishing pipeline, 19-a heat pump heating side pipeline and 20-a heat pump heating side water pump;
21-spray water pipeline, 22-heat pump, 23-heat pump cooling side water pump, 24-heat pump cooling side pipeline, 25-mixing ratio operation station, 26-filling operation station, 27-thermos bottle operation station, 28-packaging operation station, 29-water tank and 30-bypass electromagnetic valve.
Detailed Description
In order to make the technical problems, technical solutions and advantageous effects to be solved by the present invention more clearly apparent, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
In one embodiment provided by the present invention, as shown in fig. 1, the system for producing soda beverage based on heat pump comprises a raw material passage 1 connected with an inlet of a mixing cylinder 6 and a raw material water pipeline 5, wherein the raw material water pipeline 5 flows through hot side passages of a first heat exchanger 3 and a second heat exchanger 4;
Further, in the embodiment of the present invention, the outlet of the mixing cylinder 6 is connected to the filling and capping device 9 through a mixed liquid pipeline, wherein a cooler 7 is disposed on the mixed liquid pipeline; a thermos bottle machine 11 is arranged at the downstream of the filling and sealing device 9, the thermos bottle machine 11 comprises a spraying device 13 and a water tank 29 positioned below the spraying device 13, the spraying device 13 sprays atomized steam onto the beverage bottles to heat the beverage bottles, and water sprayed onto the beverage bottles is cooled and flows into the water tank 29.
The water tank 29 is connected with a spray water pipeline 21, the spray water pipeline 21 firstly flows through the cold side channel of the heat exchanger 3 from the water tank 29, then flows through the heater 10, and finally is connected with the spray device 13, so that the cyclic utilization of spray water is realized.
Furthermore, a third heat exchanger 12 is installed in the water tank 29, two sides of the third heat exchanger 12 are connected with a condenser side interface of the heat pump 22 through a pipeline 19, the third heat exchanger 12 heats water circulation in the water tank 29 through the heat pump 22, and an evaporator side of the heat pump 22 absorbs heat from the mixing operation station 25, the filling operation station 26, the thermos bottle operation station 27, a fan coil in the packaging operation station 28 and the second heat exchanger 4 through water circulation in a pipeline 23, and the heat is sent to the side connected with the heat exchanger of the water tank 29 through internal conversion of the heat pump, so that water in the water tank 29 is heated by the third heat exchanger 12. Preferably, in the embodiment of the present invention, a packaging machine 16 for packaging carbonated beverage products is further disposed downstream of the thermos bottle machine 11.
In a preferred embodiment of the present invention, the water intake line 18 is further connected to the water tank 29, and the water intake or emptying replacement can be performed from the water tank 29 by opening the electromagnetic valve 15 of the water intake line 18.
Further, in the embodiment of the present invention, a water level valve 14 is disposed in the water tank 29, and the water level valve 14 is connected to the water replenishing pipe 17; preferably, the water level valve 14 is a float valve.
When the water in the water tank 29 is lower than the preset level during the operation of the production line, the water level valve 14 is opened, and external water enters the water tank 29 through the water replenishing pipeline 17, so that the water in the water tank 29 is ensured to be enough to maintain the operation of the production line.
In addition, a first water pump 2 is arranged on the raw water pipeline 5, a second water pump 8 is arranged on the spray water pipeline 21, a third water pump 20 is arranged on a pipeline 19 at the side where the heat pump is connected with the third heat exchanger 12 in the water tank 29, and a fourth water pump 23 is arranged on a pipeline 24 where the heat pump is connected with the second heat exchanger 4 of the raw water pipeline 5 so as to provide pressure for the flow of water in the pipeline.
Further, the heater 10 employs a steam heater, which is preferably a coil type steam heater; the first heat exchanger 3 and the second heat exchanger 4 are preferably plate heat exchangers; the cooler 7 is a heat exchanger, preferably a plate heat exchanger, which is supplied with chilled water.
because the raw material water temperature is higher than the water temperature in the water tank 29, the temperature of the steam water is required to be reduced to a temperature far lower than that of the raw material water before filling, and the product is required to be heated to the dew point temperature by the thermos bottle machine 11 after filling, the raw material water pipeline 5 flows through the heat measuring channel of the heat exchanger 3, the spraying water pipeline 21 flows through the cold side channel of the heat exchanger 3, heat exchange is carried out between the cold side channel and the cold side channel, the water before entering the heater 10 can be preheated to a certain degree, the raw material water is cooled to a certain degree, and the purpose of energy saving is achieved.
In addition, the raw water is cooled to some extent by the first heat exchanger 3 and then further deeply cooled by the second heat exchanger 4.
An application embodiment of the production line of the present invention is provided as follows: raw material water with the temperature of about 28 ℃ flows through a hot side channel of a heat exchanger 3 through a raw material water pipeline 5, heat is transferred to water in a spray water pipeline 21 flowing through a cold side channel in the heat exchanger 1, the temperature of the raw material water is reduced by 5-24 ℃, the raw material water enters a hot side channel of a second heat exchanger to be further cooled by 5-19 ℃, then the raw material water enters a mixing cylinder 9, the raw material water also enters the mixing cylinder 6 through a raw material channel 1, the raw material water and the raw material are mixed in the mixing cylinder 6 to form mixed liquid, the mixed liquid flows through a cooler 7 from an outlet of the mixing cylinder 6 along the mixed liquid pipeline to be further cooled to reach the temperature of 7 ℃ meeting the filling requirement, and then the mixed liquid is filled into a beverage bottle through a filling and sealing device 9 to form a carbonated.
Meanwhile, the water in the water tank 29 enters the spray water pipeline 21, the water in the spray water pipeline 21 is heated by the first heat exchanger 3 and then is increased from 16 ℃ to 20 ℃, and then is heated by the heater 10 to the temperature of 38 ℃ or above required by the thermos bottle machine 11 and is sprayed out from the spraying device 13 to heat the carbonated drink product in the thermos bottle machine 11.
When the water in the water tank 29 exceeds 25 ℃, the bypass electromagnetic valve 30 is opened, the water in the pipeline 21 does not pass through the first heat exchanger 3 any more, and when the water in the water tank 29 exceeds 38 ℃, the water temperature meets the heating requirement of atomized spray, and the heater 10 stops supplying steam. The water vapor sprayed by the spraying device 13 can condense into water drops to enter the water tank 29, so that the water is recycled, and the water in the water tank 29 is partially supplemented through a water supplementing pipeline so as to keep the water balance.
the water in the pipeline 19 circulates in the third heat exchanger 12 and the condenser side of the heat pump, heat is carried to the third heat exchanger 12 from the heat pump, and the water in the water tank 29 is circularly heated to 38 ℃ by the third heat exchanger 12, so that the recycling of energy is realized. The evaporator side of the heat pump absorbs heat from the fan coils in the second heat exchanger 4, the mix operation station 25, the pour operation station 26, the thermos bottle operation station 27 and the pack operation station 28 by circulation of water in the line 23, and the heat is sent to the side connected to the third heat exchanger 12 of the water tank 29 by internal conversion of the heat pump, and the heat is finally absorbed by the water in the water tank 29 to raise the temperature.
In summary, in the embodiment of the present invention, the first heat exchanger 1 and the second heat exchanger 2, and the fan coils in the mixing operation station, the filling operation station, the thermos bottle operation station, and the packaging operation station are respectively used to absorb the heat of the raw material water and the heat of the air around each operation station, so as to heat the water in the water tank 29 for free, thereby reducing the usage amount of heating steam, reducing the chilled water consumption of the cooler 9, linking the cooling link and the heating link in the production line, and realizing the full utilization of energy, thereby realizing energy saving and emission reduction.
In the description of the present invention, unless otherwise expressly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
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 (7)

1. The system for producing the soda water beverage based on the heat pump is characterized by comprising a raw material passage (1) and a raw material water pipeline (5), wherein the raw material passage (1) is connected with an inlet of a mixing cylinder (6), and the raw material water pipeline (5) flows through a hot side passage of a first heat exchanger (3) and a second heat exchanger (4);
the outlet of the mixing cylinder (6) is connected with a filling and capping device (9) through a mixed liquid pipeline, and a cooler (7) is arranged on the mixed liquid pipeline; a thermos bottle machine (11) is arranged at the downstream of the filling and capping device (9), and the thermos bottle machine (11) comprises a spraying device (13) and a water tank (29) positioned below the spraying device (13);
The water tank (29) is connected with a spray water pipeline (21), the spray water pipeline (21) firstly flows through a cold side channel of the heat exchanger (3) from the water tank (29), then flows through a heater (10), and finally is connected with a spray device (13);
a third heat exchanger (12) is installed in the water tank (29), two sides of the third heat exchanger (12) are connected with a condenser side interface of the heat pump (22) through a pipeline (19), the third heat exchanger (12) circularly heats water in the water tank (29) through the heat pump (22), and an evaporator side of the heat pump (22) absorbs heat from the mixing ratio operation station (25), the filling operation station (26), the thermos bottle operation station (27), a fan coil in the packaging operation station (28) and the second heat exchanger (4) through water circulation in a pipeline (23);
the water tank (29) is also connected with a water taking pipeline (18); a water level valve (14) is arranged in the water tank (29), and the water level valve (14) is connected in the water replenishing pipeline (17); the water level valve (14) adopts a float valve, when the water in the water tank (29) is lower than a preset height in the working process of the production line, the water level valve (14) is opened, and external water enters the water tank (29) through the water replenishing pipeline (17).
2. A heat pump based beverage production system for carbonated water according to claim 1, wherein said raw water line (5) is provided with a first water pump (2); and a second water pump (8) is arranged on the spray water pipeline (21).
3. A beverage production system according to claim 2, characterized in that a third water pump (20) is provided on the pipe (19) on the side where the heat pump is connected to the third heat exchanger (12) in the water tank (29).
4. a heat pump based beverage production system for carbonated water according to claim 3, characterized in that a fourth water pump (23) is provided on the line (24) of the heat pump (22) connected to the second heat exchanger (4) of the raw water line (5).
5. The heat pump-based beverage production system according to any one of claims 2 to 4, wherein the heater (10) is a steam heater, and the steam heater is a coil steam heater.
6. A heat pump based beverage production system according to claim 5, characterized in that said first (3) and second (4) heat exchangers are plate heat exchangers.
7. Heat pump based beverage production system according to claim 6, characterized in that said cooler (7) is a heat exchanger, in particular a plate heat exchanger, with chilled water.
CN201910907424.9A 2019-09-24 2019-09-24 Soda water beverage production system based on heat pump Pending CN110562905A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910907424.9A CN110562905A (en) 2019-09-24 2019-09-24 Soda water beverage production system based on heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910907424.9A CN110562905A (en) 2019-09-24 2019-09-24 Soda water beverage production system based on heat pump

Publications (1)

Publication Number Publication Date
CN110562905A true CN110562905A (en) 2019-12-13

Family

ID=68782087

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910907424.9A Pending CN110562905A (en) 2019-09-24 2019-09-24 Soda water beverage production system based on heat pump

Country Status (1)

Country Link
CN (1) CN110562905A (en)

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Application publication date: 20191213