CN111559730A - Energy-saving beverage filling cold bottle system - Google Patents
Energy-saving beverage filling cold bottle system Download PDFInfo
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- CN111559730A CN111559730A CN202010378014.2A CN202010378014A CN111559730A CN 111559730 A CN111559730 A CN 111559730A CN 202010378014 A CN202010378014 A CN 202010378014A CN 111559730 A CN111559730 A CN 111559730A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
- B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
- B67C3/22—Details
- B67C3/26—Filling-heads; Means for engaging filling-heads with bottle necks
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
- B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
- B67C3/22—Details
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
- B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
- B67C3/22—Details
- B67C3/24—Devices for supporting or handling bottles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
- B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
- B67C3/22—Details
- B67C3/28—Flow-control devices, e.g. using valves
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
- B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
- B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
- B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
- B67C3/22—Details
- B67C2003/226—Additional process steps or apparatuses related to filling with hot liquids, e.g. after-treatment
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- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
Abstract
The invention discloses an energy-saving beverage filling and bottle cooling system which comprises a feeding pump, a high-temperature sterilization device, a filling device and a bottle cooling machine connected with the filling device through a conveying device, wherein a first heat exchanger, a heat storage water tank and a second heat exchanger are arranged between the high-temperature sterilization device and the bottle cooling machine, the first heat exchanger and the second heat exchanger comprise two flow passages, the inlet and the outlet of one flow passage of the first heat exchanger are respectively connected with the feeding pump and the high-temperature sterilization device, and the inlet and the outlet of the other flow passage are respectively connected with the inlets of one flow passage of the heat storage water tank and the second heat exchanger; an outlet of a flow channel connected with the first heat exchanger in the second heat exchanger is connected with the heat storage water tank, and an inlet and an outlet of the other flow channel of the second heat exchanger are respectively connected with a cooling water outlet and a cooling water inlet of the bottle cooling machine. The high-temperature sterilization device and the bottle cooling machine are connected through the heat recovery system to form a closed loop system, so that the heat self-balance is realized, and the energy is saved.
Description
Technical Field
The invention relates to the technical field of beverage production equipment, in particular to an energy-saving beverage filling cold bottle system.
Background
In the later stage of beverage production, the beverage is generally sterilized at high temperature by UHT ultrahigh temperature instantaneous sterilization process, then filled, and then the filled and sterilized filled bottles are cooled by a cold bottle machine to prevent bottle expansion. For example, a "bottle cooling water recycling device of a bottle cooling machine" disclosed in chinese patent document, publication No. CN201697426U, includes a water inlet pipeline communicated with a water inlet of the bottle cooling machine, the water inlet pipeline is provided with a heat exchanger for exchanging heat between the bottle cooling water and ice water; an overflow pipeline communicated with an overflow port of the bottle cooling machine; the cold bottle water cyclic utilization device still includes: the water inlet of the water storage tank is communicated with the overflow pipeline of the bottle cooling machine; the water circulation pipeline is arranged between the water outlet of the water storage tank and the water inlet of the bottle cooling machine; the high-order cooling tower is connected in series in the water circulation pipeline. This cold bottle water cyclic utilization device can carry out cycle recycle with the water that cold bottle machine overflows to reduce the make-up volume of cold bottle water, also reduced the steam quantity, practiced thrift water resources and electric power resource.
However, in the beverage filling and cooling process in the prior art, two opposite temperature adjusting processes exist, a UHT process needs to heat the beverage before filling, and needs to cool the filling bottle after filling, huge energy consumption exists in the two processes, energy waste is caused, the production cost is increased, and the development requirement of environmental protection and energy conservation is against the original requirement.
Disclosure of Invention
The invention aims to overcome the defects that in the beverage filling and cooling process in the prior art, the UHT process before filling needs to heat the beverage, the filling bottle needs to be cooled after being filled, the two temperature adjusting processes are mutually independent, huge energy consumption exists, energy waste is caused, and the production cost is improved, the energy-saving beverage filling cold bottle system is provided, the process characteristic that the temperature difference exists between the front process and the back process of the filling and cooling assembly line is utilized, the heat storage water tank is used as a heat transfer isolation medium, the heat exchange is carried out through the two heat exchangers, the heat which needs to be discharged originally is recycled to the working procedure which needs to be heated, meanwhile, the low-temperature beverage in the front passage is used as a refrigerant to cool cooling water needing cooling, so that the balance recycling of heat energy is realized, the external energy requirement of the production line is reduced, the energy cost of products is saved, and the carbon emission is reduced.
In order to achieve the purpose, the invention adopts the following technical scheme:
an energy-saving beverage filling cold bottle system comprises a feeding pump, a high-temperature sterilization device, a filling device and a bottle cooling machine, wherein the feeding pump, the high-temperature sterilization device and the filling device are sequentially connected through pipelines; an outlet of a flow passage connected with the first heat exchanger in the second heat exchanger is connected with the heat storage water tank through a pipeline, a cooling water inlet and a cooling water outlet are arranged on the bottle cooling machine, and an inlet and an outlet of the other flow passage of the second heat exchanger are respectively connected with the cooling water outlet and the cooling water inlet of the bottle cooling machine through pipelines.
The invention utilizes the characteristic of dynamic balance of heat carrier flow to connect the front high-temperature sterilization device and the rear bottle cooling machine through the heat recovery system to form a closed loop system, thereby realizing self-balance of heat and ensuring that the bottle cooling machine does not need to supply a refrigerant additionally. When in use, the beverage is sterilized by the high-temperature sterilization device and then enters the filling device to be filled into bottles, and then the filled bottles are sent into the bottle cooling machine by the conveying device and are cooled by cooling water.
In the subsequent cooling process, low-temperature cooling water enters from a cooling water inlet of the bottle cooling machine, cools filling bottles to become high-temperature outlet water, flows out from a cooling water outlet, flows into one flow channel of the second heat exchanger along a pipeline, and exchanges heat with low-temperature water flowing through the other flow channel of the second heat exchanger, so that the high-temperature outlet water of the bottle cooling machine is changed into low-temperature water again, and flows into the cooling water inlet of the bottle cooling machine from the second heat exchanger through the pipeline to be circularly cooled; and the low-temperature water in the other flow channel of the second heat exchanger is changed into high-temperature water after heat exchange, the high-temperature water enters the heat storage water tank, flows into one flow channel of the first heat exchanger from the heat storage water tank through a pipeline and exchanges heat with the low-temperature beverage to be sterilized in the other flow channel of the first heat exchanger through the feeding pump, the beverage is preheated, the beverage is changed into medium-temperature beverage and enters the high-temperature sterilization device for high-temperature sterilization, the high-temperature water after heat exchange with the low-temperature beverage is changed into low-temperature water again, the low-temperature water flows into the second heat exchanger from the first heat exchanger through a pipeline, and the heat exchange with the high-temperature water flowing out from a cooling water.
The invention takes the heat storage water tank as a heat transfer isolation medium, recycles the heat which is originally required to be discharged in the high-temperature outlet water of the bottle cooling machine through the heat exchange in the two heat exchangers, and is used for preheating the beverage to be sterilized in the process required to be heated; meanwhile, the low-temperature beverage to be sterilized is used as a refrigerant to cool cooling water to be cooled, so that the balance recycling of heat energy is realized, the external energy requirement of the production line is reduced, the energy cost of the product is saved, and the carbon emission is reduced.
Preferably, a plurality of cooling sections are arranged in the bottle cooling machine, a cooling water spraying device is arranged above each cooling section, a cooling water outlet is arranged below each cooling section, the cooling water spraying devices in the cooling sections are connected through cooling water pipes, the water inlet end of each cooling water pipe is positioned on the cooling section at one end, far away from the filling device, of the bottle cooling machine, the conveying device enters from the cooling section at one end, close to the filling device, of the bottle cooling machine and sequentially passes through the lower parts of the cooling sections, the inlet of one runner of the second heat exchanger is connected with the cooling water outlets on the two cooling sections at one end, close to the filling device, of the bottle cooling machine, and the outlet of the runner is connected with the water inlet end of each cooling water.
The bottle cooling machine is internally provided with a plurality of cooling sections, a product to be cooled is transmitted to one end far away from the filling device from one end of the bottle cooling machine close to the filling device along the conveyor belt, and cooling water flows to one end near the filling device from one end far away from the filling device of the bottle cooling machine along the cooling water pipe, and the direction of the cooling water is opposite to the transmission direction of the product, so that the cooling efficiency is improved; the product temperature in the cooling section which is closer to the filling device is higher, the cooled outlet water temperature is higher, and the heat exchange effect is better when the temperature difference between the cooled outlet water and the low-temperature water entering the second heat exchanger from the first heat exchanger is larger.
Preferably, the system is further provided with a standby cooling system connected with the heat recovery system in parallel, the standby cooling system comprises a cooling tower and a third heat exchanger comprising two mutually separated flow channels, an inlet of the cooling tower is connected with a cooling water outlet of the bottle cooling machine, an outlet of the cooling tower is connected with an inlet of one flow channel of the third heat exchanger, and an outlet of the flow channel connected with the cooling tower of the third heat exchanger is connected with a cooling water inlet of the bottle cooling machine. In order to ensure that the whole product cooling system can normally operate when the heat recovery system breaks down, the standby cooling system is arranged in the system and connected with the heat recovery system in parallel, and when the heat recovery system breaks down, high-temperature outlet water in the bottle cooling machine can be cooled through the standby cooling system. And the high-temperature outlet water enters a cooling tower in the standby cooling system for cooling, then enters one flow channel in the third heat exchanger, exchanges heat with ice water introduced into the other flow channel for sufficient cooling, and the cooled outlet water enters the bottle cooling machine from a cooling water inlet of the bottle cooling machine for circulating cooling.
Preferably, the top of the heat storage water tank is connected with a first water replenishing pipeline, the bottom of the heat storage water tank is connected with a water drainage pipeline, a water replenishing valve is arranged on the first water replenishing pipeline, and a discharge valve is arranged on the water drainage pipeline. When the water quantity participating in circulation in the heat recovery system is insufficient, water can be supplemented into the heat storage water tank through the first water supplementing pipe; when the water quantity is excessive, the redundant water can be discharged through the drainage pipeline, and the effective operation of the internal circulation of the heat recovery system is ensured.
Preferably, a cooling water inlet of the bottle cooling machine is connected with a second water replenishing pipeline, and a water replenishing valve is arranged on the second water replenishing pipeline. When the amount of cooling water in the bottle cooling machine is insufficient, the cooling water can be supplemented into the bottle cooling machine through the second water supplementing pipeline, and the cooling effect is ensured.
Preferably, each pipeline is provided with a control valve.
Preferably, centrifugal pumps are respectively arranged on a pipeline connecting the first heat exchanger and the heat storage water tank and a pipeline connecting the second heat exchanger and a cooling water outlet of the bottle cooling machine, and a flow meter is arranged in front of the pumps. The circulating water quantity in the heat recovery system is ensured to be kept stable.
Preferably, the first, second and third heat exchangers are plate heat exchangers or tube heat exchangers.
Preferably, the inlet and outlet directions of the two flow channels in the first, second and third heat exchangers are opposite. Two fluids with different temperatures in the heat exchanger flow reversely, so that the heat exchange effect can be improved.
Therefore, the beneficial effects of the invention are as follows:
(1) the heat storage water tank is used as a heat transfer isolation medium, heat which is originally required to be discharged in the high-temperature outlet water of the bottle cooling machine is recycled through heat exchange in the two heat exchangers, and the heat storage water tank is used for preheating the beverage to be sterilized in the previous process needing heating, so that the external energy requirement of the high-temperature sterilization device is reduced;
(2) the beverage to be sterilized at low temperature is used as a refrigerant to cool cooling water required to be cooled, so that the beverage is used for the subsequent bottle cooling process, the refrigerant is not required to be additionally supplied in the bottle cooling process, the balance recycling of heat energy is realized, the energy cost of products is saved, and the carbon emission is reduced.
Drawings
Fig. 1 is a schematic view of a connection structure of the present invention.
In the figure: the system comprises a feeding pump 1, a high-temperature sterilization device 2, a filling device 3, a conveying device 4, a bottle cooling machine 5, a cooling water inlet 501, a cooling water outlet 502, a cooling water spraying device 503, a second water supplementing pipeline 504, a first heat exchanger 6, a heat storage water tank 7, a first water supplementing pipeline 701, a water supplementing valve 702, a water discharging pipeline 703, a water discharging valve 704, a second heat exchanger 8, a cooling tower 9, a third heat exchanger 10, a centrifugal pump 11 and a flowmeter 12.
Detailed Description
The invention is further described with reference to the following detailed description and accompanying drawings.
Example (b):
as shown in fig. 1, an energy-saving beverage filling cold bottle system comprises a feed pump 1, a UHT high-temperature sterilization device 2, a filling device 3 and a cold bottle machine 5 connected with the filling device through a conveying device 4, wherein five cooling sections are arranged in the cold bottle machine, a cooling water inlet 501 is arranged on the leftmost cooling section, a cooling water spraying device 503 is arranged above each cooling section, a cooling water outlet 502 is arranged below each cooling section, the cooling water spraying devices in the cooling sections are connected through cooling water pipes, the water inlet ends of the cooling water pipes are communicated with the cooling water inlet, and the conveying device enters from the rightmost cooling section of the cold bottle machine and sequentially passes below each cooling section.
A heat recovery system is arranged between the UHT high-temperature sterilization device and the bottle cooling machine, the heat recovery system comprises a first heat exchanger 6, a heat storage water tank 7 and a second heat exchanger 8, the first heat exchanger and the second heat exchanger respectively comprise an upper runner and a lower runner which are mutually separated, the inlets of the upper runners of the first heat exchanger and the second heat exchanger are positioned at the right side of the heat exchangers, and the outlets of the upper runners of the first heat exchanger and the second heat exchanger are positioned at the left side of the heat; the lower channel inlets of the first and second heat exchangers are positioned at the left side of the heat exchangers, and the outlets are positioned at the right side of the heat exchangers. An upper runner inlet of the first heat exchanger is connected with a feeding pump through a pipeline, an upper runner outlet is connected with a UHT high-temperature sterilization device through a pipeline, a lower runner inlet of the first heat exchanger is connected with a heat storage water tank through a pipeline, and a lower runner outlet is connected with a lower runner inlet of the second heat exchanger; the lower runner outlet of the second heat exchanger is connected with the heat storage water tank through a pipeline, the upper runner inlet of the second heat exchanger is connected with the cooling water outlets of the two cooling sections on the rightmost side of the bottle cooling machine through a pipeline, the upper runner outlet is connected with the water inlet end of the cooling water pipe through a pipeline, each pipeline is provided with a control valve, centrifugal pumps 11 are respectively arranged on the pipeline connecting the first heat exchanger with the heat storage water tank and the pipeline connecting the second heat exchanger with the cooling water outlets of the bottle cooling machine, and a flow meter 12 is arranged in front of each pump.
The system is also provided with a standby cooling system which is connected with the heat recovery system in parallel, the standby cooling system comprises a cooling tower 9 and a third heat exchanger 10, the cooling tower adopts a closed cooling tower, the third heat exchanger comprises an upper runner and a lower runner which are mutually separated, the inlet of the upper runner is positioned on the left side of the heat exchanger, the outlet of the upper runner is positioned on the right side of the heat exchanger, and the outlet and inlet directions of the lower runner are opposite to those of the upper runner. The inlet of the cooling tower is connected with the outlets of the cooling water ports of the five cooling sections of the bottle cooling machine through a pipeline, the outlet of the cooling tower is connected with the inlet of the lower runner of the third heat exchanger, and the outlet of the lower runner of the third heat exchanger is connected with the water inlet end of the cooling water pipe in the bottle cooling machine.
The first heat exchanger, the second heat exchanger and the third heat exchanger adopt plate heat exchangers, the top of the heat storage water tank is connected with a first water supplementing pipeline 701, the bottom of the heat storage water tank is connected with a water drainage pipeline 703, the first water supplementing pipeline is provided with a water supplementing valve 702, and the water drainage pipeline is provided with a discharge valve 704; the cooling water pipe of bottle cooling machine is intake and is connected with second moisturizing pipeline 504, also is equipped with the moisturizing valve on the second moisturizing pipeline.
When the system works, the beverage is sterilized by the UHT high-temperature sterilization device and then enters the filling device to be filled into bottles, then the filled bottles enter from the rightmost cooling section of the bottle cooling machine through the conveying device and sequentially pass through the cooling sections leftwards, and are cooled by cooling water sprayed by the cooling water spraying devices above the cooling sections.
The high-temperature water in the two cooling sections on the right side flows into an upper flow channel of a second heat exchanger along a pipeline under the action of a centrifugal pump and exchanges heat with the low-temperature water flowing through a lower flow channel of the second heat exchanger, so that the high-temperature water in the bottle cooling machine is changed into low-temperature water again, flows out of an outlet of the upper flow channel of the second heat exchanger and flows into a water inlet end of the cooling water pipe of the bottle cooling machine through the pipeline, and the product is cooled in a circulating manner; and the low-temperature water in the lower runner of the second heat exchanger is changed into high-temperature water after heat exchange, the high-temperature water flows out from the outlet of the lower runner and enters the heat storage water tank, the high-temperature water in the heat storage water tank flows into the lower runner of the first heat exchanger through a pipeline under the action of a centrifugal pump and exchanges heat with the low-temperature beverage to be sterilized entering the upper runner of the first heat exchanger through a feed pump, the beverage is preheated, the beverage is changed into medium-temperature beverage and enters a UHT high-temperature sterilization device for high-temperature sterilization, the high-temperature water after heat exchange with the low-temperature beverage in the lower runner is changed into low-temperature water again, the high-temperature water flows out from the outlet of the lower runner of the first heat exchanger and flows into the inlet of the lower runner of the second heat exchanger through. In the circulation process, when the water quantity participating in circulation in the heat recovery system is insufficient, water can be supplemented into the heat storage water tank through the first water supplementing pipe; when the water amount is excessive, the redundant water can be discharged through the drainage pipeline, so that the effective operation of the internal circulation of the heat recovery system is ensured; when the amount of cooling water in the bottle cooling machine is insufficient, the cooling water can be supplemented into the bottle cooling machine through the second water supplementing pipeline, and the cooling effect is ensured.
When the heat recovery system operates normally, the standby cooling system is in a non-use state; when the heat recovery system breaks down, the standby cooling system can be started to cool the high-temperature outlet water in the bottle cooling machine. After the standby cooling system is started, high-temperature outlet water of each cooling section of the bottle cooling machine firstly enters a cooling tower for cooling under the action of a centrifugal pump and then enters a lower flow channel in a third heat exchanger, ice water is introduced into an upper flow channel of the third heat exchanger to further cool the outlet water of the cooling tower, and the cooled outlet water flows out of an outlet of the lower flow channel of the third heat exchanger and then enters a water inlet end of a cooling water pipe of the bottle cooling machine to circularly cool a product.
The invention utilizes the characteristic of dynamic balance of heat carrier flow to connect the front high-temperature sterilization device with the rear bottle cooling machine through the heat recovery system to form a closed loop system, thereby realizing self-balance of heat and effectively saving energy.
Claims (9)
1. An energy-saving beverage filling cold bottle system comprises a feeding pump (1), a high-temperature sterilization device (2), a filling device (3) and a bottle cooling machine (5) which is connected with the filling device through a conveying device (4) in sequence, and is characterized in that a heat recovery system is arranged between the high-temperature sterilization device and the bottle cooling machine, the heat recovery system comprises a first heat exchanger (6), a heat storage water tank (7) and a second heat exchanger (8), the first heat exchanger and the second heat exchanger respectively comprise two mutually separated runners, an inlet and an outlet of one runner of the first heat exchanger are respectively connected with the feeding pump and the high-temperature sterilization device through pipelines, and an inlet and an outlet of the other runner are respectively connected with inlets of one runner of the heat storage water tank and the second heat exchanger through pipelines; an outlet of a flow channel connected with the first heat exchanger in the second heat exchanger is connected with the heat storage water tank through a pipeline, a cooling water inlet (501) and a cooling water outlet (502) are arranged on the bottle cooling machine, and an inlet and an outlet of the other flow channel of the second heat exchanger are respectively connected with the cooling water outlet and the cooling water inlet of the bottle cooling machine through pipelines.
2. The energy-saving beverage filling cold bottle system according to claim 1, wherein a plurality of cooling sections are arranged in the cold bottle machine, a cooling water spraying device (503) is arranged above each cooling section, a cooling water outlet is arranged below each cooling section, the cooling water spraying devices in the cooling sections are connected through cooling water pipes, the water inlet ends of the cooling water pipes are located on the cooling section at the end, far away from the filling device, of the cold bottle machine, the conveying device enters from the cooling section at the end, close to the filling device, of the cold bottle machine and sequentially passes below each cooling section, the inlet of one of the flow passages of the second heat exchanger is connected with the cooling water outlets on the first two cooling sections at the end, close to the filling device, of the cold bottle machine, and the outlet of the flow passage is connected with the water inlet end of the cooling water pipe.
3. An energy-saving beverage filling and cold bottle system as claimed in claim 1, wherein a backup cooling system is further provided in parallel with the heat recovery system, the backup cooling system comprises a cooling tower (9) and a third heat exchanger (10) comprising two mutually separated flow passages, an inlet of the cooling tower is connected with a cooling water outlet of the bottle cooling machine, an outlet of the cooling tower is connected with an inlet of one flow passage of the third heat exchanger, and an outlet of the flow passage of the third heat exchanger connected with the cooling tower is connected with a cooling water inlet of the bottle cooling machine.
4. The energy-saving beverage filling cold bottle system according to claim 1, wherein a first water replenishing pipeline (701) is connected to the top of the hot water storage tank, a water draining pipeline (703) is connected to the bottom of the hot water storage tank, a water replenishing valve (702) is arranged on the first water replenishing pipeline, and a discharge valve (704) is arranged on the water draining pipeline.
5. The energy-saving beverage filling and cold bottle system according to claim 1, wherein a second water replenishing pipeline (504) is connected to a cooling water inlet of the bottle cooling machine, and a water replenishing valve is arranged on the second water replenishing pipeline.
6. The energy-saving beverage filling cold bottle system according to claim 1, wherein each pipeline is provided with a control valve.
7. An energy-saving beverage filling and bottle cooling system as claimed in claim 1 or 2, wherein the pipeline connecting the first heat exchanger and the hot water storage tank and the pipeline connecting the second heat exchanger and the cooling water outlet of the bottle cooling machine are respectively provided with a centrifugal pump (11), and a flow meter (12) is arranged behind the pump.
8. The energy-saving beverage filling cold bottle system according to claim 3, wherein the first, second and third heat exchangers are plate heat exchangers or tube heat exchangers.
9. The energy-saving beverage filling cold bottle system according to claim 3 or 8, wherein the inlet and outlet directions of the two flow passages in the first, second and third heat exchangers are opposite.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010378014.2A CN111559730B (en) | 2020-05-07 | 2020-05-07 | Energy-saving beverage filling cold bottle system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010378014.2A CN111559730B (en) | 2020-05-07 | 2020-05-07 | Energy-saving beverage filling cold bottle system |
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| CN111559730A true CN111559730A (en) | 2020-08-21 |
| CN111559730B CN111559730B (en) | 2022-05-24 |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2625652A1 (en) * | 1988-01-08 | 1989-07-13 | Biotech So | Method for obtaining fruit and/or vegetable concentrates and installation for implementing this method |
| JP3643172B2 (en) * | 1996-04-08 | 2005-04-27 | 大和製罐株式会社 | Method and apparatus for producing hot-packed beverages in containers |
| CN101774522A (en) * | 2010-02-09 | 2010-07-14 | 广州达意隆包装机械股份有限公司 | Spraying method for bottled drink spraying bottle cooler |
| CN201697426U (en) * | 2010-03-31 | 2011-01-05 | 潍坊娃哈哈饮料有限公司 | Bottle cooling water recycling device for bottle cooling machine |
| CN104068447A (en) * | 2014-06-12 | 2014-10-01 | 上海锦江电子技术工程有限公司 | Energy-saving high-temperature beverage sterilizing and cooling system |
| CN105658083A (en) * | 2013-11-12 | 2016-06-08 | Khs有限责任公司 | Method and system for pasteurization of products in containers |
| CN109900070A (en) * | 2019-04-09 | 2019-06-18 | 同方节能装备有限公司 | The Power Cycle of beverage production |
| CN212503939U (en) * | 2020-05-07 | 2021-02-09 | 杭州娃哈哈集团有限公司 | Energy-saving beverage filling cold bottle system |
-
2020
- 2020-05-07 CN CN202010378014.2A patent/CN111559730B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2625652A1 (en) * | 1988-01-08 | 1989-07-13 | Biotech So | Method for obtaining fruit and/or vegetable concentrates and installation for implementing this method |
| JP3643172B2 (en) * | 1996-04-08 | 2005-04-27 | 大和製罐株式会社 | Method and apparatus for producing hot-packed beverages in containers |
| CN101774522A (en) * | 2010-02-09 | 2010-07-14 | 广州达意隆包装机械股份有限公司 | Spraying method for bottled drink spraying bottle cooler |
| CN201697426U (en) * | 2010-03-31 | 2011-01-05 | 潍坊娃哈哈饮料有限公司 | Bottle cooling water recycling device for bottle cooling machine |
| CN105658083A (en) * | 2013-11-12 | 2016-06-08 | Khs有限责任公司 | Method and system for pasteurization of products in containers |
| CN104068447A (en) * | 2014-06-12 | 2014-10-01 | 上海锦江电子技术工程有限公司 | Energy-saving high-temperature beverage sterilizing and cooling system |
| CN109900070A (en) * | 2019-04-09 | 2019-06-18 | 同方节能装备有限公司 | The Power Cycle of beverage production |
| CN212503939U (en) * | 2020-05-07 | 2021-02-09 | 杭州娃哈哈集团有限公司 | Energy-saving beverage filling cold bottle system |
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