Steam recycling system for plant beverage production
By designing a steam recycling system in plant beverage production, and recycling high-temperature water vapor using plate heat exchangers and steam condensate recycling tanks, the problems of high-temperature water vapor waste and environmental pollution are solved, and efficient utilization of water resources and energy are achieved. save.
Patent Information
- Application Number
- CN202420211504.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-01-29
- Publication Date
- 2024-12-27
- Estimated Expiration
- 2034-01-29
AI Technical Summary
During the production of plant beverages, high-temperature water vapor is only used once and then discharged directly into the sewer, resulting in waste of water resources and environmental pollution, while increasing production costs.
A steam recycling system was designed, including a plate heat exchanger, steam condensate recovery tank, water supply pipeline, spray water storage tank and boiler room water storage tank. The high-temperature steam condensate is sent into the plate heat exchange through a centrifugal pump. The device conducts heat to room temperature water, and sends the cooled steam water into the boiler room water storage tank for circulation and heating, realizing the recycling of high-temperature water vapor.
It realizes rapid recycling of high-temperature water vapor, saves production costs, makes full use of water resources, reduces energy consumption, and brings good energy saving effects and economic benefits.
Smart Images
Figure CN222256507U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of water recovery, in particular to a steam recovery and utilization system for plant beverage production. Background Art
[0002] In the production process of plant beverages, there are many processes that require the use of a large amount of high-temperature steam, such as heating the water for extraction tanks and ingredients, shrinking the labels of beverage packaging, and high-temperature sterilization and cleaning of metal beverage cans. Due to the liquefaction phenomenon, high-temperature steam will condense into condensed water after releasing heat. The condensed water has a relatively high temperature. Therefore, in the existing plant beverage production process, high-temperature steam is generally only used once and then directly discharged into the sewer, which will cause a waste of water resources. Since the factory uses a large amount of water in production, it will also increase the overall cost of beverage production. Moreover, since the water temperature after the steam is liquefied is relatively high, directly discharging it into the sewer will not only pollute the environment, but also waste a lot of heat energy. Utility Model Content
[0003] In order to solve the problems in the prior art, the utility model provides a steam recovery and utilization system for the production of plant beverages. By arranging a plate heat exchanger, a steam condensate recovery tank, a water supply pipeline, a spray water storage tank and a boiler room water storage tank that cooperate with each other in the steam recovery and utilization system for the production of plant beverages, a large amount of high-temperature water vapor used in the production process of plant beverages can be quickly, timely and fully recovered, thereby saving production costs. The high degree of automation can make more full use of water resources, reducing the cost of using water resources in the production process of plant beverages. In addition, the recovery of heat energy reduces energy consumption, brings good energy-saving effects and objective economic benefits, and solves the problem that a large amount of high-temperature water vapor in the existing plant beverage production process is directly discharged into the sewer after being used only once, wasting water resources, polluting the environment with heat, and increasing water production costs.
[0004] The utility model provides a steam recovery and utilization system for plant beverage production, comprising a plate heat exchanger, a steam condensate recovery tank, a water delivery pipeline, a spray water storage tank and a boiler room water storage tank, the plate heat exchanger is provided with a steam condensate water inlet, a normal temperature water inlet, a cooling steam water outlet and a spray water outlet, the steam condensate water recovery tank is connected with the steam condensate water inlet through the water delivery pipeline, a centrifugal pump is provided between the steam condensate water recovery tank and the steam condensate water inlet, the cooling steam water outlet is connected with the boiler room water storage tank through the water delivery pipeline, the spray water outlet is connected with the spray water storage tank through the water delivery pipeline, the centrifugal pump can send the high-temperature steam condensate in the steam condensate water recovery tank into the plate heat exchanger to transfer the heat to the normal temperature water to heat it into spray water for spraying thermos bottles, and the cooling steam water can be sent into the boiler room water storage tank to be circulated and heated into high-temperature water vapor for plant beverage production.
[0005] The utility model is further improved in that a circulation pump is provided between the cooling steam water outlet and the boiler room water storage tank.
[0006] The utility model is further improved in that a first pipeline valve is provided between the steam condensate recovery tank and the centrifugal pump.
[0007] The utility model is further improved in that a second pipeline valve is provided between the boiler room water storage tank and the circulation pump.
[0008] The utility model is further improved in that the top of the steam condensate recovery tank is provided with a first exhaust port connected to the external atmospheric environment.
[0009] The utility model is further improved in that the top of the spray water storage tank is provided with a second exhaust port which is communicated with the external atmospheric environment.
[0010] The utility model is further improved in that the steam condensate water recovery tank is also provided with a liquid level pressure sensing device for sensing the water level in the steam condensate water recovery tank.
[0011] The utility model is further improved in that a thermometer for sensing the water temperature in the steam condensate recovery tank is also provided in the steam condensate recovery tank.
[0012] Compared with the prior art, the beneficial effects of the utility model are as follows: the utility model provides a steam recovery and utilization system for plant beverage production. By arranging a plate heat exchanger, a steam condensate recovery tank, a water pipeline, a spray water storage tank and a boiler room water storage tank that cooperate with each other in the steam recovery and utilization system for plant beverage production, a centrifugal pump can send the high-temperature steam condensate in the steam condensate recovery tank into the plate heat exchanger to transfer the heat to the normal temperature water to heat it into spray water for spraying thermos bottles. The cooled steam water can be sent to the boiler room water storage tank for circulation and heating to high-temperature water vapor for plant beverage production. A large amount of high-temperature water vapor used in the production process of plant beverages can be quickly, timely and fully recovered, thereby saving production costs. The degree of automation is high, and water resources can be more fully utilized, reducing the cost of using water resources in the production process of plant beverages. Moreover, the recovery of heat energy reduces energy consumption, bringing good energy-saving effects and objective economic benefits, and solving the problems that a large amount of high-temperature water vapor in the existing plant beverage production process is directly discharged into the sewer after only being used once, wasting water resources, polluting the environment with heat, and increasing water production costs. BRIEF DESCRIPTION OF THE DRAWINGS
[0013] Figure 1 The utility model is a schematic diagram of the specific structure of the steam recovery and utilization system for plant beverage production.
[0014] In the figure, 1-plate heat exchanger, 2-steam condensate recovery tank, 21-centrifugal pump, 22-first pipeline valve, 3-water pipeline, 4-spray water storage tank, 5-boiler room water storage tank, 51-circulation pump, 52-second pipeline valve. DETAILED DESCRIPTION
[0015] The utility model is further described in detail below with reference to the accompanying drawings and embodiments.
[0016] like Figure 1As shown, the utility model provides a steam recovery and utilization system for plant beverage production, including a plate heat exchanger 1, a steam condensate recovery tank 2, a water supply pipeline 3, a spray water storage tank 4 and a boiler room water storage tank 5. The plate heat exchanger 1 is provided with a steam condensate water inlet, a normal temperature water inlet, a cooling steam water outlet and a spray water outlet. The steam condensate water recovery tank 2 is connected to the steam condensate water inlet through the water supply pipeline 3. A centrifugal pump 21 is provided between the steam condensate water recovery tank 2 and the steam condensate water inlet. The cooling steam water outlet is connected to the boiler room water storage tank 5 through the water supply pipeline, and the spray water outlet is connected to the spray water storage tank 4 through the water supply pipeline. In this embodiment, the centrifugal pump can send the high-temperature steam condensate in the steam condensate recovery tank into the plate heat exchanger to transfer the heat to the normal temperature water to heat it up to spray water for spraying thermos bottles. The cooled steam water can be sent to the boiler room water storage tank for circulation and heating to high-temperature water vapor for plant beverage production. The large amount of high-temperature water vapor used in the production process of plant beverages can be recovered quickly, timely and fully, thereby saving production costs. It has a high degree of automation and can make more full use of water resources, reducing the cost of using water resources in the production process of plant beverages. In addition, the recovery of heat energy reduces energy consumption, bringing good energy-saving effects and objective economic benefits.
[0017] like Figure 1 As shown, a circulating pump 51 is provided between the cooling steam water outlet and the boiler room water storage tank 5; a first pipeline valve 22 is provided between the steam condensate water recovery tank 2 and the centrifugal pump 21; a second pipeline valve 52 is provided between the boiler room water storage tank 5 and the circulating pump 51; a first exhaust port connected to the external atmospheric environment is provided on the top of the steam condensate water recovery tank 2; a second exhaust port connected to the external atmospheric environment is provided on the top of the spray water storage tank 4; a liquid level pressure sensing device for sensing the water level in the steam condensate water recovery tank 2 is also provided in the steam condensate water recovery tank 2; a thermometer for sensing the water temperature in the steam condensate water recovery tank 2 is also provided in the steam condensate water recovery tank 2. In this embodiment, the circulating pump is used to send the cooled steam condensate water into the boiler room water storage tank for circulation heating to high-temperature water vapor for plant beverage production; the first exhaust port and the second exhaust port are used to discharge the air and carbon dioxide in the tank to prevent the pressure in the steam condensate water recovery tank and the spray water storage tank from being too high; the liquid level pressure sensing device and the thermometer are both used to monitor the state of the high-temperature steam water in the steam condensate water recovery tank.
[0018] As can be seen from the above, the utility model provides a steam recovery and utilization system for the production of plant beverages. By arranging a plate heat exchanger, a steam condensate recovery tank, a water supply pipeline, a spray water storage tank and a boiler room water storage tank that cooperate with each other in the steam recovery and utilization system for the production of plant beverages, a centrifugal pump can send the high-temperature steam condensate in the steam condensate recovery tank into the plate heat exchanger to transfer the heat to the normal temperature water to heat it into spray water for spraying thermos bottles. The cooled steam water can be sent to the boiler room water storage tank for circulation and heating to high-temperature water vapor for the production of plant beverages. A large amount of high-temperature water vapor used in the production process of plant beverages can be recovered quickly, timely and fully, thereby saving production costs. It has a high degree of automation and can make more full use of water resources, reducing the cost of using water resources in the production process of plant beverages. Moreover, the recovery of heat energy reduces energy consumption, brings good energy-saving effects and objective economic benefits, and solves the problems that a large amount of high-temperature water vapor in the existing plant beverage production process is directly discharged into the sewer after only being used once, wasting water resources, polluting the environment with heat, and increasing water production costs.
[0019] The specific implementation methods described above are preferred implementation methods of the present utility model, and are not intended to limit the specific implementation scope of the present utility model. The scope of the present utility model includes but is not limited to the specific implementation methods. All equivalent changes made in accordance with the present utility model are within the protection scope of the present utility model.
Claims
1. A steam recovery system for plant beverage production, characterized in that: It includes a plate heat exchanger, a steam condensate recovery tank, a water supply pipeline, a spray water storage tank and a boiler room water storage tank. The plate heat exchanger is provided with a steam condensate water inlet, a normal temperature water inlet, a cooling steam water outlet and a spray water outlet. The steam condensate water recovery tank is connected with the steam condensate water inlet through the water supply pipeline. A centrifugal pump is provided between the steam condensate water recovery tank and the steam condensate water inlet. The cooling steam water outlet is connected with the boiler room water storage tank through the water supply pipeline. The spray water outlet is connected with the spray water storage tank through the water supply pipeline. The centrifugal pump can send the high-temperature steam condensate in the steam condensate water recovery tank into the plate heat exchanger to transfer the heat to the normal temperature water to heat it into spray water for spraying thermos bottles. The cooling steam water can be sent to the boiler room water storage tank for circulation and heating into high-temperature water vapor for the production of plant beverages.
2. The steam recovery system for producing plant beverages according to claim 1, characterized in that: A circulation pump is provided between the cooling steam water outlet and the boiler room water storage tank.
3. The steam recovery system for plant beverage production according to claim 2, characterized in that: A first pipeline valve is provided between the steam condensate recovery tank and the centrifugal pump.
4. The steam recovery and utilization system for producing plant beverages according to claim 3, characterized in that: A second pipeline valve is provided between the boiler room water storage tank and the circulating pump.
5. The steam recovery system for producing plant beverages according to claim 4, characterized in that: The top of the steam condensate recovery tank is provided with a first exhaust port which is connected to the external atmospheric environment.
6. The steam recovery system for producing plant beverages according to claim 5, characterized in that: A second exhaust port communicating with the external atmospheric environment is provided on the top of the spray water storage tank.
7. The steam recovery system for producing plant beverages according to claim 6, characterized in that: The steam condensate water recovery tank is also provided with a liquid level pressure sensing device for sensing the water level in the steam condensate water recovery tank.
8. The steam recovery system for producing plant beverages according to claim 7, characterized in that: The steam condensate recovery tank is also provided with a thermometer for sensing the water temperature in the steam condensate recovery tank.