CN110562905A - Soda water beverage production system based on heat pump - Google Patents
Soda water beverage production system based on heat pump Download PDFInfo
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- 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
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- water tank
- heat pump
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 176
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 31
- 235000013361 beverage Nutrition 0.000 title claims abstract description 30
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 title claims abstract description 25
- 239000007921 spray Substances 0.000 claims abstract description 36
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 239000002994 raw material Substances 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000004806 packaging method and process Methods 0.000 claims description 11
- 238000001816 cooling Methods 0.000 abstract description 12
- 238000005507 spraying Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B63/00—Auxiliary devices, not otherwise provided for, for operating on articles or materials to be packaged
- B65B63/08—Auxiliary devices, not otherwise provided for, for operating on articles or materials to be packaged for heating or cooling articles or materials to facilitate packaging
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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
- B67C7/00—Concurrent cleaning, filling, and closing of bottles; Processes or devices for at least two of these operations
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-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
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient 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
Description
技术领域technical field
本发明涉及一种生产线，尤其涉及一种汽水饮料生产线，具体是一种基于热泵的汽水饮料生产系统。The invention relates to a production line, in particular to a soda drink production line, in particular to a heat pump-based soda drink production system.
背景技术Background technique
目前的汽水饮料生产过程通常包括混比/碳化、灌注封盖、暖瓶和包装这四个流程，其中，混比/碳化流程指的是将糖浆等原质（原汁）与原料水在混合缸中进行混合的过程，由于汽水在灌装前需要把混合缸从大约28℃降温至7℃，因此需要消耗冷冻机电能实现降温；暖瓶流程是指将灌装后或包装前的产品从8℃左右升温至露点温度，避免产品表面出现冷凝水，因此需用蒸汽加热暖瓶机水槽中的水至38℃-44℃，然后在移动的产品上空进行雾化喷淋来实现升温。The current soda beverage production process usually includes four processes: mixing/carbonization, filling and capping, thermos bottle and packaging. In the process of mixing, because the soda needs to cool down the mixing cylinder from about 28°C to 7°C before filling, it needs to consume the power of the refrigerator to cool down; the warming process refers to cooling the product after filling or before packaging from 8°C Raise the temperature to the dew point temperature around to avoid condensed water on the surface of the product. Therefore, it is necessary to use steam to heat the water in the water tank of the bottle warmer to 38°C-44°C, and then spray atomized spray over the moving product to achieve temperature rise.
由于现有的汽水饮料灌装生产线中，暖瓶加热系统与混比冷却系统及其连接管道是各自独立的，因此冷却和加热过程都需要消耗能量，整个生产线的能耗较大。因此，如何提供一种可以将生产线中的冷却环节和加热环节通过热泵技术和热交换装置相互联系，实现热量和冷量的有效传递，从而实现节能目的的汽水饮料生产线是亟需解决的技术问题。In the existing soda beverage filling production line, the thermos bottle heating system, the mixing cooling system and their connecting pipes are independent, so the cooling and heating processes require energy consumption, and the energy consumption of the entire production line is relatively large. Therefore, how to provide a soda beverage production line that can connect the cooling link and the heating link in the production line through heat pump technology and heat exchange devices to achieve effective transfer of heat and cold, thereby achieving the purpose of energy saving is a technical problem that needs to be solved urgently .
发明内容Contents of the invention
本发明实施例的目的在于提供一种基于热泵的汽水饮料生产系统，以解决上述背景技术中提出的问题。为实现上述目的，本发明实施例提供如下技术方案：The purpose of the embodiments of the present invention is to provide a heat pump-based soda beverage production system to solve the problems raised in the background art above. In order to achieve the above purpose, embodiments of the present invention provide the following technical solutions:
一种基于热泵的汽水饮料生产系统，包括与混合缸的入口相连接的原质通道和原料水管路，原料水管路流经第一换热器和第二换热器的热侧通道；A heat pump-based soda beverage production system, including a raw material channel and a raw material water pipeline connected to the inlet of the mixing cylinder, and the raw water pipeline flows through the hot side channels of the first heat exchanger and the second heat exchanger;
所述混合缸的出口则通过混合液管路与灌注封盖装置相连接，混合液管路上设有冷却器；在灌注封盖装置的下游设有暖瓶机，暖瓶机包括喷淋装置和位于喷淋装置下方的水槽，喷淋装置喷出雾化蒸汽到饮料瓶上，对饮料瓶进行加热，喷到饮料瓶上的水被冷却并流入水槽中；The outlet of the mixing cylinder is connected to the filling and capping device through the mixed liquid pipeline, and a cooler is arranged on the mixed liquid pipeline; The water tank under the shower device, the spray device sprays atomized steam onto the beverage bottle to heat the beverage bottle, and the water sprayed on the beverage bottle is cooled and flows into the water tank;
所述水槽连接有喷淋水管路，喷淋水管路先由水槽流经换热器的冷侧通道，再流经一个加热器，最终与喷淋装置相连接，实现喷淋水的循环利用；The water tank is connected with a spray water pipeline, and the spray water pipeline first flows through the cold side channel of the heat exchanger from the water tank, then flows through a heater, and finally connects with the spray device to realize the recycling of the spray water;
所述水槽内安装有第三换热器，第三换热器两侧通过管路与热泵的冷凝器侧接口相连，第三换热器通过热泵对水槽中的水循环加热，所述热泵的蒸发器侧通过管路中的水循环从混比操作工位、灌注操作工位、暖瓶操作工位、包装操作工位中的风机盘管以及第二换热器中吸收热量，通过热泵内部变换，把热量送到与水槽换热器相连一侧，被第三换热器加热给水槽中的水；A third heat exchanger is installed in the water tank, and both sides of the third heat exchanger are connected to the condenser side interface of the heat pump through pipelines. The third heat exchanger circulates and heats the water in the water tank through the heat pump, and the evaporation of the heat pump The side of the device absorbs heat from the mixing operation station, filling operation station, thermos bottle operation station, fan coil in the packaging operation station and the second heat exchanger through the water circulation in the pipeline, and converts it through the heat pump. The heat is sent to the side connected to the water tank heat exchanger, and is heated by the third heat exchanger to the water in the water tank;
所述水槽上还连接有取水管路；所述水槽中设有水位阀，水位阀连接在补水管路中；所述水位阀采用浮子阀，当水槽中的水在生产线工作过程中低于预设的高度时，水位阀打开，外部的水由补水管路进入水槽。The water tank is also connected with a water intake pipeline; the water tank is provided with a water level valve, and the water level valve is connected in the water replenishment pipeline; When the height is set, the water level valve is opened, and the external water enters the tank through the replenishment pipeline.
作为本发明进一步的方案：所述原料水管路上设有第一水泵；所述喷淋水管路上设有第二水泵。As a further solution of the present invention: the raw water pipeline is provided with a first water pump; the spray water pipeline is provided with a second water pump.
作为本发明进一步的方案：所述热泵与水槽中的第三换热器相连侧管路上设有第三水泵。As a further solution of the present invention: a third water pump is provided on the side pipeline where the heat pump is connected to the third heat exchanger in the water tank.
作为本发明进一步的方案：所述热泵与原料水管路的第二换热器相连的管路上设有第四水泵，以便为管路内水的流动提供压力。As a further solution of the present invention: a fourth water pump is provided on the pipeline connected between 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.
作为本发明进一步的方案：所述加热器采用蒸汽加热器，蒸汽加热器为盘管式蒸汽加热器。As a further solution of the present invention: the heater is a steam heater, and the steam heater is a coil type steam heater.
作为本发明进一步的方案：所述第一换热器和第二换热器采用板式换热器。As a further solution of the present invention: the first heat exchanger and the second heat exchanger adopt plate heat exchangers.
作为本发明进一步的方案：所述冷却器为通有冷冻水的热交换器，具体为板式热交换器。As a further solution of the present invention: the cooler is a heat exchanger through which chilled water passes, specifically a plate heat exchanger.
与现有技术相比，本发明实施例通过用换热器和水源热泵连接原料水管路和喷淋水管路，将生产线中的冷却环节和加热环节相互联系，把冷却环节中提取出的能量通过热泵和换热器，传递到加热环节，实现能量的充分利用，减少了生产线中的加热器和冷却器同时消耗的电能，从而实现节能目的的汽水饮料生产线，并进一步为现场各工位的操作员工免费提供冷却。Compared with the prior art, the embodiment of the present invention connects the raw material water pipeline and the spray water pipeline with a heat exchanger and a water source heat pump, interconnects the cooling link and the heating link in the production line, and passes the energy extracted from the cooling link through The heat pump and heat exchanger are transferred to the heating link to realize the full utilization of energy and reduce the electric energy consumed by the heater and cooler in the production line at the same time, so as to realize the energy-saving purpose of the soda beverage production line and further provide for the operation of each station on site Employees provide cooling for free.
附图说明Description of drawings
为了更清楚地说明本发明实施例中的技术方案，下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本发明的一些实施例。In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the following will briefly introduce the accompanying drawings that need to be used in the descriptions of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only of the present invention. some examples.
图1为本发明实施例提供的基于热泵的汽水饮料生产系统的结构示意图。Fig. 1 is a schematic structural diagram of a heat pump-based soda beverage production system provided by an embodiment of the present invention.
图中：1-原质通道，2-第一水泵，3-第一换热器，4-第二换热器，5-原料水管路，6-混合缸，7-冷却器，8-第二水泵，9-灌注封盖装置，10-加热器；In the figure: 1-protoplasm channel, 2-first water pump, 3-first heat exchanger, 4-second heat exchanger, 5-raw water pipeline, 6-mixing tank, 7-cooler, 8-the first Two water pumps, 9-perfusion capping device, 10-heater;
11-暖瓶机，12-第三换热器，13-喷淋装置，14-水位阀，15-电磁阀换热器，16-包装机，17-取水管路，18-补水管路，19-热泵加热侧管路，20-热泵加热侧水泵；11-Bottle warmer, 12-Third heat exchanger, 13-Spray device, 14-Water level valve, 15-Solenoid valve heat exchanger, 16-Packaging machine, 17-Water intake pipeline, 18-Water supply pipeline, 19 - heat pump heating side pipeline, 20 - heat pump heating side water pump;
21-喷淋水管路，22-热泵，23-热泵冷却侧水泵，24-热泵冷却侧管路，25-混比操作工位，26-灌注操作工位，27-暖瓶操作工位，28-包装操作工位，29-水槽，30-旁路电磁阀。21-spray water pipeline, 22-heat pump, 23-heat pump cooling side water pump, 24-heat pump cooling side pipeline, 25-mixing operation station, 26-perfusion operation station, 27-warm bottle operation station, 28- Packaging operation station, 29-water tank, 30-bypass solenoid valve.
具体实施方式Detailed ways
为了使本发明所要解决的技术问题、技术方案及有益效果更加清楚明白，以下结合附图及实施例，对本发明进行进一步详细说明。应当理解，此处所描述的具体实施例仅仅用以解释本发明，并不用于限定本发明。In order to make the technical problems, technical solutions and beneficial effects to be solved by the present invention clearer, the present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
如图1所示，在本发明实施例提供的一个实施例中，一种基于热泵的汽水饮料生产系统，包括与混合缸6的入口相连接的原质通道1和原料水管路5，其中，原料水管路5流经第一换热器3和第二换热器4的热侧通道；As shown in Figure 1, in an embodiment provided by the embodiment of the present invention, a heat pump-based soda beverage production system includes a raw material channel 1 and a raw water pipeline 5 connected to the inlet of the mixing cylinder 6, wherein, The raw water pipeline 5 flows through the hot side channels of the first heat exchanger 3 and the second heat exchanger 4;
进一步的，在本发明实施例中，所述混合缸6的出口则通过混合液管路与灌注封盖装置9相连接，其中，混合液管路上设有冷却器7；在灌注封盖装置9的下游设有暖瓶机11，暖瓶机11包括喷淋装置13和位于喷淋装置13下方的水槽29，喷淋装置13喷出雾化蒸汽到饮料瓶上，对饮料瓶进行加热，喷到饮料瓶上的水被冷却并流入水槽29中。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 the mixed liquid pipeline, wherein a cooler 7 is arranged on the mixed liquid pipeline; The downstream of the bottle warmer 11 is provided with a bottle warmer 11. The bottle warmer 11 includes a spray device 13 and a water tank 29 located below the spray device 13. The spray device 13 sprays atomized steam onto the beverage bottle to heat the beverage bottle and spray it onto the beverage bottle. The water on the bottle is cooled and flows into the water tank 29.
所述水槽29连接有喷淋水管路21，喷淋水管路21先由水槽29流经换热器3的冷侧通道，再流经一个加热器10，最终与喷淋装置13相连接，实现喷淋水的循环利用。The water tank 29 is connected with a spray water pipeline 21, and the spray water pipeline 21 first flows through the cold side channel of the heat exchanger 3 from the water tank 29, then flows through a heater 10, and finally connects with the spray device 13 to realize Recycling of spray water.
进一步的，所述水槽29内安装有第三换热器12，第三换热器12两侧通过管路19与热泵22的冷凝器侧接口相连，第三换热器12通过热泵22对水槽29中的水循环加热，所述热泵22的蒸发器侧通过管路23中的水循环从混比操作工位25、灌注操作工位26、暖瓶操作工位27、包装操作工位28中的风机盘管以及第二换热器4中吸收热量，通过热泵内部变换，把热量送到与水槽29换热器相连一侧，被第三换热器12加热给水槽29中的水。优选地，在本发明实施例中，所述暖瓶机11的下游还设有用于对汽水饮料产品进行包装包装机16。Further, the third heat exchanger 12 is installed in the water tank 29, and both sides of the third heat exchanger 12 are connected to the condenser side interface of the heat pump 22 through the pipeline 19, and the third heat exchanger 12 is connected to the water tank through the heat pump 22. 29, the evaporator side of the heat pump 22 passes through the water circulation in the pipeline 23 from the fan disc in the mixing operation station 25, the filling operation station 26, the thermos bottle operation station 27, and the packaging operation station 28. The heat is absorbed in the tube and the second heat exchanger 4, and the heat is transferred to the side connected to the heat exchanger of the water tank 29 through the internal transformation of the heat pump, and is heated by the third heat exchanger 12 to the water in the water tank 29. Preferably, in the embodiment of the present invention, a packaging machine 16 for packaging soda beverage products is further provided downstream of the bottle warming machine 11 .
在本发明的一个优选实施例中，所述水槽29上还连接有取水管路18，打开取水管路18上的电磁阀15，可以从水槽29中取水或排空更换。In a preferred embodiment of the present invention, the water tank 29 is also connected with a water intake pipeline 18, and the solenoid valve 15 on the water intake pipeline 18 can be opened to take water from the water tank 29 or empty it for replacement.
进一步的，在本发明实施例中，所述水槽29中设有水位阀14，水位阀14连接在补水管路17中；优选的，水位阀14采用浮子阀。Further, in the embodiment of the present invention, the water tank 29 is provided with a water level valve 14, and the water level valve 14 is connected to the water supply pipeline 17; preferably, the water level valve 14 is a float valve.
当水槽29中的水在生产线工作过程中低于预设的高度时，水位阀14打开，外部的水由补水管路17进入水槽29，确保水槽29中的水量足够维持生产线的运转。When the water in the water tank 29 is lower than the preset height during the production line operation, the water level valve 14 is opened, and the external water enters the water tank 29 by the replenishment pipeline 17 to ensure that the water quantity in the water tank 29 is enough to maintain the operation of the production line.
此外，原料水管路5上设有第一水泵2，喷淋水管路21上设有第二水泵8，热泵与水槽29中的第三换热器12相连侧管路19上设有第三水泵20，热泵与原料水管路5的第二换热器4相连的管路24上设有第四水泵23，以便为管路内水的流动提供压力。In addition, a first water pump 2 is provided on the raw water pipeline 5, a second water pump 8 is provided on the spray water pipeline 21, and a third water pump is provided on the side pipeline 19 where the heat pump is connected to the third heat exchanger 12 in the water tank 29. 20. The heat pump is provided with a fourth water pump 23 on the pipeline 24 connected to the second heat exchanger 4 of the raw water pipeline 5, so as to provide pressure for the flow of water in the pipeline.
进一步地，加热器10采用蒸汽加热器，蒸汽加热器优选地为盘管式蒸汽加热器；第一换热器3和第二换热器4优选地采用板式换热器；冷却器7为通有冷冻水的热交换器，优选地采用板式热交换器。Further, the heater 10 adopts a steam heater, and the steam heater is preferably a coiled steam heater; the first heat exchanger 3 and the second heat exchanger 4 are preferably plate heat exchangers; A heat exchanger with chilled water, preferably a plate heat exchanger.
由于原料水温度高于水槽29中的水温，且汽水在灌装前需要降温至远低于原料水的温度，灌装后又需要用暖瓶机11将产品升温至露点温度，因此通过使原料水管路5流经换热器3的热测通道，喷淋水管路21流经换热器3的冷侧通道，相互之间进行热交换，可以对进入加热器10前的水进行一定程度的预热，并对原料水进行一定程度的冷却，从而达到节能的目的。Because the raw water temperature is higher than the water temperature in the water tank 29, and the soda needs to be cooled to a temperature far lower than the raw water before filling, and the product needs to be warmed up to the dew point temperature with the bottle warmer 11 after filling, so by making the raw water pipe The channel 5 flows through the heat measuring channel of the heat exchanger 3, and the spray water pipeline 21 flows through the cold side channel of the heat exchanger 3, and they exchange heat with each other, which can pre-heat the water before entering the heater 10 to a certain extent. Heat, and cool the raw water to a certain extent, so as to achieve the purpose of energy saving.
另外，原料水在通过第一换热器3得到一定程度的冷却后，经过第二换热器4得到进一步深度冷却。In addition, after the raw material water is cooled to a certain extent by the first heat exchanger 3 , it is further deeply cooled by the second heat exchanger 4 .
以下提供一种本发明生产线的一种应用实施例：28℃左右的原料水由原料水管路5流经换热器3的热侧通道，在换热器1内部将热量传递给流经冷侧通道的喷淋水管路21中的水，原料水温度降低5℃-24℃，进入第二换热器的热侧通道进一步冷却5℃-19℃，然后进入混合缸9，原质也由原质通道1进入混合缸6，在混合缸6中原料水与原质混合形成混合液，混合液从混合缸6的出口沿混合液管路流经冷却器7进一步冷却，达到符合灌装要求的温度7℃，然后经过灌注封盖装置9灌入饮料瓶中，成为汽水饮料产品，汽水饮料产品然后进入暖瓶机11。An application example of a production line of the present invention is provided below: Raw water at about 28°C flows through the hot side channel of the heat exchanger 3 through the raw water pipeline 5, and transfers heat to the cold side in the heat exchanger 1. The water in the spray water pipeline 21 of the channel, the temperature of the raw material water is reduced by 5°C-24°C, and enters the hot side channel of the second heat exchanger to be further cooled by 5°C-19°C, and then enters the mixing tank 9, and the raw material is also obtained from the raw material. The substance channel 1 enters the mixing tank 6, where the raw material water and the original substance are mixed to form a mixed liquid, and the mixed liquid flows from the outlet of the mixing tank 6 along the mixed liquid pipeline through the cooler 7 for further cooling to meet the filling requirements. Temperature 7 ℃, pours in the beverage bottle through pouring and capping device 9 then, becomes soda beverage product, and soda beverage product enters warm bottle machine 11 then.
与此同时，水槽29中的水进入喷淋水管路21，喷淋水管路21中的水经第一换热器3加热后由16℃上升到20℃，然后又经过加热器10加热至暖瓶机11所需的温度38℃或以上，并从喷淋装置13喷出，对暖瓶机11中的汽水饮料产品进行升温。At the same time, the water in the water tank 29 enters the spray water pipeline 21, and the water in the spray water pipeline 21 rises from 16°C to 20°C after being heated by the first heat exchanger 3, and then is heated to the thermos bottle by the heater 10. Machine 11 required temperature 38 ℃ or above, and spray from spray device 13, the soda drink product in warm bottle machine 11 is heated up.
当水槽29中的水超过25℃时，打开旁通电磁阀30，管路21的水将不再经过第一换热器3，当水槽29中的水超过38℃时，水温符合雾化喷淋加热要求，加热器10停止供蒸汽。喷淋装置13喷淋出的水蒸汽再加热饮料瓶会凝结成水滴部分进入水槽29，实现水的循环利用，水槽29中的水部分通过补水管路补充，以保持水量平衡。When the water in the water tank 29 exceeds 25°C, open the bypass solenoid valve 30, and the water in the pipeline 21 will no longer pass through the first heat exchanger 3. Shower heating requirement, heater 10 stops supplying steam. The water vapor sprayed out by the spraying device 13 will condense into water droplets and enter the water tank 29 after reheating the beverage bottle, so as to realize the recycling of water.
管路19中的水在第三换热器12和热泵冷凝器侧中循环流动，把热量从热泵带至第三换热器12,水槽29中的水就被第三换热器12循环加热至38℃，实现能源的循环利用。热泵的蒸发器侧通过管路23中的水的循环从第二换热器4，混比操作工位25、灌注操作工位26、暖瓶操作工位27及包装操作工位28中的风机盘管吸收热量，通过热泵内部变换，把热量送到与水槽29第三换热器12相连一侧，热量最终被水槽29中的水吸收升温。The water in the pipeline 19 circulates in the third heat exchanger 12 and the condenser side of the heat pump, bringing heat from the heat pump to the third heat exchanger 12, and the water in the water tank 29 is circulated and heated by the third heat exchanger 12 To 38 ℃, to achieve energy recycling. The evaporator side of the heat pump passes through the circulation of water in the pipeline 23 from the second heat exchanger 4, the fan disc in the mixing operation station 25, the filling operation station 26, the thermos bottle operation station 27 and the packaging operation station 28. The tube absorbs heat, and through the internal conversion of the heat pump, the heat is sent to the side connected to the third heat exchanger 12 of the water tank 29, and the heat is finally absorbed by the water in the water tank 29 to raise the temperature.
综上所述，本发明实施例通过用第一换热器1和第二换热器2，以及混比操作工位、灌注操作工位、暖瓶操作工位及包装操作工位中的风机盘管分别吸取原料水的热量和各操作工位周围中的空气热量，对水槽29中的水进行免费加热，减少了加热蒸汽的使用量，减少了冷却器9的冷冻水消耗，将生产线中的冷却环节和加热环节相互联系并实现能量的充分利用，实现了节能减排。In summary, the embodiment of the present invention uses the first heat exchanger 1 and the second heat exchanger 2, and the fan disc in the mixing operation station, filling operation station, thermos bottle operation station and packaging operation station The pipe absorbs the heat of the raw material water and the heat of the air around each operating station to heat the water in the water tank 29 for free, reducing the use of heating steam, reducing the consumption of chilled water in the cooler 9, and reducing the consumption of the water in the production line. The cooling link and the heating link are connected with each other to realize the full utilization of energy and realize energy saving and emission reduction.
在本发明的描述中，除非另有明确的规定和限定，术语“安装”、“相连”、“连接”应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或一体地连接；可以是机械连接，也可以是电连接；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通。对于本领域的普通技术人员而言，可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, unless otherwise specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integrated Connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediary, and it can be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention in specific situations.
以上所述仅为本发明的较佳实施例而已，并不用以限制本发明，凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等，均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. within range.
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