CN214537450U - White fog equipment is removed to comdenstion water - Google Patents
White fog equipment is removed to comdenstion water Download PDFInfo
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- CN214537450U CN214537450U CN202120603161.5U CN202120603161U CN214537450U CN 214537450 U CN214537450 U CN 214537450U CN 202120603161 U CN202120603161 U CN 202120603161U CN 214537450 U CN214537450 U CN 214537450U
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Abstract
The utility model discloses a white fog equipment is removed to comdenstion water, including condensate recovery unit, condensate recovery unit's input is equipped with high temperature comdenstion water import, condensate recovery unit's output is equipped with flash steam discharge port, condensate recovery unit's output fixedly connected with condensate discharge port, one side of condensate discharge port is equipped with power steam inlet, condensate discharge port's below is equipped with the overflow mouth, condensate recovery unit's top is equipped with steam-water heat exchanger, the last flash steam inlet that is equipped with of steam-water heat exchanger, flash steam inlet is connected with flash steam discharge port, steam-water heat exchanger's output is equipped with steam discharge port, steam-water heat exchanger's input is equipped with cold water inlet. The utility model discloses can retrieve the comdenstion water that steam system heat transfer produced effectively, reach water recovery and reduce the energy consumption, also can effectual reduction simultaneously because of the flash distillation vapour that the flash distillation of high temperature comdenstion water flash distillation produced, indirect has beautified the environment.
Description
Technical Field
The utility model relates to a comdenstion water processing apparatus technical field especially relates to white fog equipment is removed to comdenstion water.
Background
The steam can also be called as steam, but in actual conditions, the steam is classified according to pressure and temperature and is respectively saturated steam and superheated steam, the steam is mainly used for heating/humidifying and can also generate power and the like, and the condensed water is liquid water formed by reducing the temperature of the steam as the name implies, wherein the most common condensed water flows out from a water collecting tray below an evaporator of the indoor unit.
In practical situations, because of the great latent heat of evaporation carried by steam, steam is widely used as a heating medium in many heating applications, and after the steam heats the medium, a great amount of latent heat is released, so that the steam becomes high-temperature condensed water, and this part of the high-temperature condensed water contains great heat, if the high-temperature condensed water is directly discharged, the high-temperature condensed water can flash quickly after entering the atmosphere (after the flash evaporation is performed, high-pressure saturated liquid enters a relatively low-pressure container, and due to the sudden reduction of pressure, the saturated liquid becomes a part of saturated steam and saturated liquid under the container pressure), so that "cloud and fog winding" in the atmosphere is caused, and energy waste and the environment are caused.
Therefore, we propose a condensed water white fog removing apparatus to solve the above problems.
Disclosure of Invention
The utility model aims at solving the defects existing in the prior art, and providing a condensed water white fog removing device.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the white fog equipment is removed to comdenstion water, including condensate recovery unit, condensate recovery unit's input is equipped with high temperature comdenstion water import, condensate recovery unit's output is equipped with flash steam discharge port, condensate recovery unit's output fixedly connected with comdenstion water discharge port, one side of comdenstion water discharge port is equipped with power steam inlet, the below of comdenstion water discharge port is equipped with the overflow mouth, condensate recovery unit's top is equipped with the soda heat exchanger, be equipped with flash steam inlet on the soda heat exchanger, flash steam inlet is connected with flash steam discharge port, the output of soda heat exchanger is equipped with steam discharge port, the input of soda heat exchanger is equipped with cold water inlet, the output of soda heat exchanger is equipped with the hot water export.
Preferably, a condensate recovery pump is arranged on the condensate discharge port, and the condensate recovery pump is driven by using power steam.
Preferably, the overflow port comprises a storage tank, a transition pipe and a connecting pipe, the input end of the connecting pipe is connected with the output end of the condensate recovery device, the input end of the connecting pipe is located at the position, close to the middle of the condensate recovery device, of the middle of the condensate recovery device, and the transition pipe is connected with the flash steam discharge port.
Preferably, the cold water inlet is connected to an external cold water output source, and the hot water outlet is connected to an external hot water input source.
Preferably, the output end of the overflow port is connected with an external water source.
Preferably, the high-temperature condensed water inlet is connected with a condensed water outlet after heat exchange of the steam system.
Compared with the prior art, the beneficial effects of the utility model are that:
in this device, the comdenstion water is arranged to condensate recovery unit, gets into the soda heat exchanger behind the low temperature low pressure steam that flashes into through condensate recovery unit, and low temperature low pressure flash distillation steam becomes the comdenstion water after cold water cooling, and the comdenstion water leans on the dead weight to get back to in the condensate recovery unit again to can retrieve the comdenstion water that steam system heat transfer produced effectively, reach water recovery and reduce the energy consumption, also can effectually reduce simultaneously because of the flash distillation steam that high temperature comdenstion water flash distillation produced, the indirect environment that has beautified.
Drawings
Fig. 1 is a schematic structural view of the condensed water white fog removing device provided by the utility model.
In the figure: the system comprises a condensate water recovery device 1, a high-temperature condensate water inlet 2, a flash steam discharge port 3, a power steam inlet 4, an overflow port 5, a condensate water discharge port 6, a steam-water heat exchanger 7, a flash steam inlet 8, a steam discharge port 9, a cold water inlet 10 and a hot water outlet 11.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
Referring to fig. 1, white fog equipment is removed to comdenstion water, including condensate recovery unit 1, condensate recovery unit 1's input is equipped with high temperature comdenstion water import 2, condensate outlet after high temperature comdenstion water import 2 and the steam system heat transfer is connected, condensate recovery unit 1's output is equipped with flash steam discharge port 3, condensate recovery unit 1's output fixedly connected with comdenstion water discharge port 6, be equipped with the condensate recovery pump on comdenstion water discharge port 6, and the condensate recovery pump uses power steam to drive, one side of condensate discharge port 6 is equipped with power steam inlet 4.
The below of comdenstion water discharge port 6 is equipped with overflow mouth 5, and overflow mouth 5 is including persisting jar, excessive pipe and connecting pipe, and the input of connecting pipe is connected with condensate recovery unit 1's output, and the input of connecting pipe is in the position that the centre of condensate recovery unit 1 leaned on, and excessive pipe is connected with flash distillation steam discharge port 3, and the output of overflow mouth 5 is connected with outside water source.
A steam-water heat exchanger 7 is arranged above the condensate water recovery device 1, a flash steam inlet 8 is arranged on the steam-water heat exchanger 7, the flash steam inlet 8 is connected with a flash steam discharge port 3, a steam discharge port 9 is arranged at the output end of the steam-water heat exchanger 7, a cold water inlet 10 is arranged at the input end of the steam-water heat exchanger 7, the cold water inlet 10 is connected with an external cold water output source, a hot water outlet 11 is arranged at the output end of the steam-water heat exchanger 7, and the hot water outlet 11 is connected with an external hot water input source.
The utility model discloses in, the comdenstion water export after the steam system heat transfer is connected to comdenstion water recovery unit 1, and high temperature comdenstion water gets into comdenstion water recovery unit 1 from high temperature comdenstion water import 2, and 3 discharge flash steam in upper portion flash steam discharge port, lower part comdenstion water discharge port 6 get into the comdenstion water recovery pump, and the comdenstion water recovery pump sends the comdenstion water pump to the comdenstion water with the water spot under the power steam drive in power steam entry 4, realizes comdenstion water recovery and first order energy recuperation.
The flash steam inlet 8 on the steam-water heat exchanger 7 is connected with flash steam discharged by the condensate water recovery device 1, after cooling by cold water, low-temperature flash steam is discharged to the atmosphere through the steam discharge port 9 (basically no flash steam), the condensed flash steam is changed into water drops, the water drops are returned to the condensate water recovery device 1 through the flash steam discharge port 3 under the action of gravity, and the cold water is heated through the cold water inlet 10 and then discharged from the hot water outlet 11, so that the secondary energy recovery is realized.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (6)
1. The white fog removing device for the condensed water is characterized by comprising a condensed water recovery device (1), wherein a high-temperature condensed water inlet (2) is formed in the input end of the condensed water recovery device (1), a flash steam discharge port (3) is formed in the output end of the condensed water recovery device (1), a condensed water discharge port (6) is fixedly connected with the output end of the condensed water recovery device (1), a power steam inlet (4) is formed in one side of the condensed water discharge port (6), an overflow port (5) is formed below the condensed water discharge port (6), a steam-water heat exchanger (7) is arranged above the condensed water recovery device (1), a flash steam inlet (8) is formed in the steam-water heat exchanger (7), the flash steam inlet (8) is connected with the flash steam discharge port (3), and a steam discharge port (9) is formed in the output end of the steam-water heat exchanger (7), the input end of the steam-water heat exchanger (7) is provided with a cold water inlet (10), and the output end of the steam-water heat exchanger (7) is provided with a hot water outlet (11).
2. The condensed water white fog removing apparatus according to claim 1, wherein a condensed water recovery pump is provided on the condensed water discharge port (6), and the condensed water recovery pump is driven using power steam.
3. The condensed water white fog removing apparatus according to claim 1, wherein the overflow port (5) comprises a reserve tank, a transition pipe and a connecting pipe, and an input end of the connecting pipe is connected with an output end of the condensed water recovery device (1), an input end of the connecting pipe is located at a position above a middle of the condensed water recovery device (1), and the transition pipe is connected with the flash steam discharge port (3).
4. The condensed water white mist removing apparatus according to claim 1, wherein the cold water inlet (10) is connected to an external cold water output source, and the hot water outlet (11) is connected to an external hot water input source.
5. The condensed water white mist removing device according to claim 1, characterized in that the output end of the overflow port (5) is connected with an external water source.
6. The condensed water white fog removing device according to claim 1, wherein the high temperature condensed water inlet (2) is connected with a condensed water outlet after heat exchange of a steam system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202120603161.5U CN214537450U (en) | 2021-03-24 | 2021-03-24 | White fog equipment is removed to comdenstion water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN202120603161.5U CN214537450U (en) | 2021-03-24 | 2021-03-24 | White fog equipment is removed to comdenstion water |
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CN214537450U true CN214537450U (en) | 2021-10-29 |
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CN202120603161.5U Active CN214537450U (en) | 2021-03-24 | 2021-03-24 | White fog equipment is removed to comdenstion water |
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CN (1) | CN214537450U (en) |
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2021
- 2021-03-24 CN CN202120603161.5U patent/CN214537450U/en active Active
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