CN218269029U - Condensate water recycling device of high-temperature high-pressure sterilizer - Google Patents
Condensate water recycling device of high-temperature high-pressure sterilizer Download PDFInfo
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- CN218269029U CN218269029U CN202222247623.1U CN202222247623U CN218269029U CN 218269029 U CN218269029 U CN 218269029U CN 202222247623 U CN202222247623 U CN 202222247623U CN 218269029 U CN218269029 U CN 218269029U
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Abstract
The utility model provides a condensate water recycling device of a high-temperature high-pressure sterilizer, belonging to the technical field of condensate water recycling. The utility model discloses a condensate water collector, the water level inductor, trap and heat energy exchange convection current jar, condensate water collector is equipped with the first comdenstion water inlet that links to each other with high temperature autoclave condensate water discharge port, the condensate water collector bottom is equipped with the first comdenstion water delivery port that is linked together with the water level inductor, the top is equipped with the second comdenstion water delivery port with the trap intercommunication, heat energy exchange convection current jar is equipped with the convection current jar comdenstion water inlet that is linked together with the water level inductor, RO water inlet, connect the convection current jar comdenstion water delivery port of boiler supply water jar and connect the RO water delivery port of dissolving sugar hot-water jar. The utility model has the advantages that: reducing the pollution to the environment and the waste of water resources.
Description
Technical Field
The utility model relates to a condensate recovery technical field, concretely relates to condensate recovery utilizes device of high temperature and high pressure sterilizer.
Background
UHT (Ultra-high temperature sterilization) is a sterilization process in the beverage industry, namely, ultra-high temperature instantaneous sterilization by a high-temperature and high-pressure sterilizer, the temperature is 135-140 ℃,4-10 seconds, the Ultra-high temperature instantaneous sterilization can be stored without refrigeration below 10 ℃, and the shelf life can reach 1-6 months.
In the production process of the existing industry, condensed water and steam generated by UHT sterilization are mostly discharged directly, and in the moment that the condensed water and the steam are discharged into the atmosphere from a steam using device, because the pressure is suddenly reduced, a large amount of secondary flash steam is generated, and the sprayed high-temperature condensed water carries the flash steam to easily scald field operators. In winter in the north, because the ambient temperature is lower, the fog curtain is easily formed, influences pedestrian's sight. In summer, the environment is helped by high temperature, and the environment is easily polluted.
Because the recovery of the condensed water is limited by specific production conditions and recovery technical conditions, the condensed water and the steam generated by UHT sterilization generally directly pass through a drain valve discharge device and enter a condensed water treatment and discharge system for direct discharge, the universal recovery rate is low, and the water resource waste degree is higher.
SUMMERY OF THE UTILITY MODEL
For solving the problem among the prior art, the utility model provides a condensate water recycle device of high temperature and high pressure sterilizer, condensate water collector and heat energy exchange convection jar through the setting of condensate water recycle device at high temperature and high pressure sterilizer mutually support, can be used for dissolving sugar behind the heat conduction of comdenstion water for normal atmospheric temperature RO water, the consumption of the energy has been reduced, good energy-conserving effect and objective economic benefits have been brought, the comdenstion water is as boiler make-up water after the heat energy exchange, because the total dissolved solid content of comdenstion water is lower, boiler blowdown number of times has been reduced, the heat loss of blowdown has been reduced, the recycle of comdenstion water has also reduced the pollution to the environment, produce good environmental benefit and social benefit, the problem of the current trade condensate water and the direct discharge easy polluted environment of steam in process of production has been solved, the low water waste degree that leads to the low rate of recovery is higher.
The utility model provides a pair of condensed water recycle device of high temperature autoclave sterilizer, including comdenstion water collector, water level inductor, trap and heat energy exchange convection tank, comdenstion water collector is equipped with the first comdenstion water inlet that links to each other with high temperature autoclave comdenstion water discharge port, comdenstion water collector bottom is equipped with first comdenstion water delivery port, comdenstion water collector top is equipped with second comdenstion water delivery port, first comdenstion water delivery port with the water level inductor is linked together, second comdenstion water delivery port with the trap intercommunication, the trap with the water level inductor is linked together, heat energy exchange convection tank is equipped with convection tank comdenstion water inlet, RO water inlet, convection tank comdenstion water delivery port and RO water delivery port, the water level inductor with convection tank comdenstion water inlet is linked together, convection tank comdenstion water delivery port connects the boiler to supply water tank, RO water delivery port connects and dissolves sugar hot-water tank.
The utility model discloses make further improvement, the condensate collector top still is equipped with the first exhaust port with outside atmospheric environment intercommunication.
The utility model discloses make further improvement, the trap top is equipped with the vapor water inlet, the vapor water inlet links to each other with high temperature autoclave vapor discharge port.
The utility model discloses make further improvement, first comdenstion water delivery port with be equipped with first pipeline valve between the water level sensor.
The utility model discloses make further improvement, the water level inductor with be equipped with second pipeline valve between the convection current jar comdenstion water inlet.
The utility model discloses make further improvement, water level sensor top is equipped with the second gas vent that communicates with outside atmospheric environment.
The utility model discloses make further improvement, be equipped with in the water level inductor and be used for the response the water level pressure sensing device of water level in the condensate water collector.
The utility model discloses make further improvement, be equipped with the convection current device that is used for condensate water and RO water convection current heat transfer in the heat energy exchange convection current jar.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model provides a condensate water recycle device of high temperature and high pressure sterilizer, condensate water collector and heat energy exchange convection jar of mutually supporting are set up through the condensate water recycle device at high temperature and high pressure sterilizer, can be used for dissolving sugar behind the heat conduction for normal atmospheric temperature RO water of comdenstion water, the consumption of the energy has been reduced, good energy-conserving effect and objective economic benefits have been brought, the comdenstion water is as boiler make-up water after the heat energy exchange, because the total dissolved solid content of comdenstion water is lower, boiler blowdown number of times has been reduced, the heat loss of taking away in the blowdown has been reduced, the recycle of comdenstion water has also reduced the pollution to the environment, produce good environmental benefits and social benefits, the easy polluted environment of condensate water and the direct emission of steam in the production process of having solved current trade, the low problem that leads to the water resource waste degree.
Drawings
Fig. 1 is a schematic view of the specific structure of the condensate water recycling device of the high-temperature and high-pressure sterilizer of the present invention.
In the figure, 1-a condensed water collector, 11-a first exhaust port, 12-a first pipeline valve, 2-a water level sensor, 21-a second pipeline valve, 22-a second exhaust port, 3-a drain valve, 4-a heat energy exchange convection tank, 5-a boiler make-up water tank and 6-a sugar dissolving hot water tank.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and examples.
As shown in FIG. 1, the utility model provides a pair of condensate recovery utilizes device of autoclave, including condensate collector 1, water level inductor 2, trap 3 and heat energy exchange convection tank 4, condensate collector 1 is equipped with the first comdenstion water inlet that links to each other with autoclave comdenstion water discharge port, condensate collector 1 bottom is equipped with first comdenstion water delivery port, 1 top of condensate collector is equipped with second comdenstion water delivery port, first comdenstion water delivery port is linked together with water level inductor 2, second comdenstion water delivery port and trap 3 intercommunication, trap 3 is linked together with water level inductor 2, heat energy exchange convection tank 4 is equipped with convection tank comdenstion water inlet, RO water inlet, convection tank comdenstion water delivery port and RO water delivery port, water level inductor 2 is linked together with convection tank comdenstion water inlet, convection tank comdenstion water delivery port connects boiler make-up water tank 5, RO water delivery port connects and dissolves sugar hot-water tank 6.
The principle of the membrane separation technology developed in sixties is that raw water passes through a reverse osmosis membrane under the action of high pressure, and a solvent in the water is diffused from low concentration to high concentration so as to achieve the purposes of separation, purification and concentration. Reverse osmosis can remove bacteria, viruses, colloids, organic matters and over 98 percent of soluble salts in water. The method has the characteristics of low operation cost, simple operation, high automation degree, stable effluent quality and the like. Compared with other traditional water treatment methods, the method has obvious advantages and is widely applied to water treatment related industries. In this embodiment, the RO water is heated by the condensed water and then stored in the hot water tank, and the heat energy is transferred to the sugar dissolving system for dissolving sugar, thereby reducing the heat energy required for heating the RO water at normal temperature.
As shown in fig. 1, the top of the condensate collector 1 is further provided with a first exhaust port 11 communicated with the external atmospheric environment, the top of the drain valve 3 is provided with a steam inlet, the steam inlet is connected with a steam exhaust port of the high-temperature high-pressure sterilizer, a first pipeline valve 12 is arranged between the first condensate water outlet and the water level sensor 2, a second pipeline valve 21 is arranged between the water level sensor 2 and the condensate water inlet of the convection tank, and the top of the water level sensor 2 is provided with a second exhaust port 22 communicated with the external atmospheric environment.
As shown in fig. 1, a water level pressure sensing device for sensing the water level in the condensate collector 1 is provided in the water level sensor 2, and a convection device for convection heat transfer of condensate and RO water is provided in the heat exchange convection tank 4.
The working principle is as follows: the utility model provides a comdenstion water recycle device during operation of high temperature autoclave sterilization ware, comdenstion water that has liquefied in the comdenstion water discharge port of high temperature autoclave sterilization ware gets into the comdenstion water collector from first comdenstion water inlet, pass through first pipeline valve again, in the inflow water level inductor, pass through second pipeline valve again and get into in the heat energy exchange convection current jar, give RO water with heat energy conduction in the heat energy exchange convection current jar, then flow in the boiler make-up water tank, RO water flows in after the comdenstion water heating and dissolves in the sugar hot-water tank. The top of the condensed water collector is provided with an exhaust port for exhausting air and carbon dioxide in the condensed water collector to prevent overhigh pressure in the condensed water collector; when the water level in the condensed water collector is too high, the condensed water flows into the drain valve from the second condensed water outlet, and the steam is input into the drain valve from the steam outlet of the high-temperature high-pressure sterilizer and flows into the water level sensor after being condensed; the open top of the water level sensor is provided with a second air outlet for discharging air and carbon dioxide.
According to the above, the utility model provides a condensate water recycle device of high temperature and high pressure sterilizer, condensate water collector and heat energy exchange convection jar through mutually supporting are set up to the condensate water recycle device at high temperature and high pressure sterilizer, can be used for dissolving sugar behind the heat conduction of comdenstion water for normal atmospheric temperature RO water, the consumption of the energy has been reduced, good energy-conserving effect and objective economic benefits have been brought, the comdenstion water is as boiler makeup water behind the heat energy exchange, because the total dissolved solid content of comdenstion water is lower, boiler blowdown number of times has been reduced, the heat loss of taking away the blowdown has been reduced, the recycle of comdenstion water has also reduced the pollution to the environment, produce good environmental benefit and social benefit, the problem of the high degree of water waste is led to the low rate of recovery condensate water in the production process of current trade condensate water and steam direct emission easy polluted environment is solved.
The above-mentioned embodiments are preferred embodiments of the present invention, and the scope of the present invention is not limited thereto, and the scope of the present invention includes but is not limited to the above-mentioned embodiments, and all equivalent changes made according to the present invention are within the protection scope of the present invention.
Claims (8)
1. The utility model provides a condensate water recycle device of high temperature and high pressure sterilizer which characterized in that: including condensate collector, water level inductor, trap and heat energy exchange convection current jar, condensate collector is equipped with the first comdenstion water inlet that links to each other with high temperature autoclave sterilizer comdenstion water discharge port, the condensate collector bottom is equipped with first comdenstion water delivery port, the condensate collector top is equipped with second comdenstion water delivery port, first comdenstion water delivery port with the water level inductor is linked together, second comdenstion water delivery port with the trap intercommunication, the trap with the water level inductor is linked together, heat energy exchange convection current jar is equipped with convection current jar comdenstion water inlet, RO water inlet, convection current jar comdenstion water delivery port and RO water delivery port, the water level inductor with convection current jar comdenstion water inlet is linked together, convection current jar comdenstion water delivery port connects the boiler to supply water jar, RO water delivery port connects and dissolves sugar hot-water jar.
2. The apparatus for recycling condensed water of a autoclave according to claim 1, wherein: the top of the condensed water collector is also provided with a first exhaust port communicated with the external atmospheric environment.
3. The apparatus for recycling condensed water of a autoclave as set forth in claim 2, wherein: the top of the drain valve is provided with a steam inlet which is connected with a steam outlet of the high-temperature high-pressure sterilizer.
4. The apparatus for recycling condensed water in a autoclave according to claim 3, wherein: and a first pipeline valve is arranged between the first condensate water outlet and the water level sensor.
5. The apparatus for recycling condensed water of a autoclave according to claim 4, wherein: and a second pipeline valve is arranged between the water level sensor and the condensate water inlet of the convection tank.
6. The apparatus for recycling condensed water of a autoclave according to claim 5, wherein: and a second exhaust port communicated with the external atmospheric environment is arranged at the top of the water level sensor.
7. The apparatus for recycling condensed water of a autoclave according to claim 6, wherein: and a water level pressure sensing device used for sensing the water level in the condensate water collector is arranged in the water level sensor.
8. The apparatus for recycling condensed water of a autoclave according to claim 7, wherein: and a convection device for convection heat conduction of condensed water and RO water is arranged in the heat energy exchange convection tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222247623.1U CN218269029U (en) | 2022-08-25 | 2022-08-25 | Condensate water recycling device of high-temperature high-pressure sterilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222247623.1U CN218269029U (en) | 2022-08-25 | 2022-08-25 | Condensate water recycling device of high-temperature high-pressure sterilizer |
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| Publication Number | Publication Date |
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| CN218269029U true CN218269029U (en) | 2023-01-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202222247623.1U Active CN218269029U (en) | 2022-08-25 | 2022-08-25 | Condensate water recycling device of high-temperature high-pressure sterilizer |
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| CN (1) | CN218269029U (en) |
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2022
- 2022-08-25 CN CN202222247623.1U patent/CN218269029U/en active Active
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