CN2826176Y - Flash evaporator capable of recovering steam condensed water - Google Patents
Flash evaporator capable of recovering steam condensed water Download PDFInfo
- Publication number
- CN2826176Y CN2826176Y CN 200520076337 CN200520076337U CN2826176Y CN 2826176 Y CN2826176 Y CN 2826176Y CN 200520076337 CN200520076337 CN 200520076337 CN 200520076337 U CN200520076337 U CN 200520076337U CN 2826176 Y CN2826176 Y CN 2826176Y
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- tank body
- steam
- separating plate
- carbonated drink
- tank
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Abstract
The utility model discloses a flash vaporizing device capable of recovering steam condensed water in a heating system. The utility model is provided with a flash vaporizing tank which comprises a tank body, a steam-water separating plate with discharge holes and a supporting element which is fixedly connected with the tank body, wherein a liquid inlet, a steam outlet and a liquid outlet are arranged on the tank body, and a liquid level adjusting device is arranged in the tank body, is positioned below the steam-water separating plate and is connected to the liquid outlet. Steam condensed water recovered by the utility model is free from pollution, and the utility model has high recovering efficiency, can automatically recover steam condensed water circularly without a water pump, thus saving cost.
Description
Technical field
The utility model relates to the water separator in a kind of heating system.
Background technology
In heating system, the indirect heating apparatus afterbody is installed steam trap, plays the block steam and drain water effect, and when steam condensate was discharged from steam trap, the heat of taking out of accounted for 25% of steam total amount of heat.Generally speaking, the steam condensate of discharge directly enters sewer, and this will waste a large amount of heat energy and cause thermal pollution.For effective use of energy sources, people begin steam condensate is reclaimed, and as boiler feedwater, the recovery gathering-device majority that is adopted is the steel storage tank or the brick cement pit of opening, with extraneous blow-by, the contaminated situation of condensate water is more serious, hardness wherein, basicity, iron ion, solid impurity, severe overweights such as suspension can not use after tending to cause recovery, even if can use, also having 1/3rd condensate water becomes steam and has wasted, organic efficiency is not high, carries recycle-water need use water pump in addition, has increased cost, and easy break-down, unmanageable.
Summary of the invention
It is not contaminated that the purpose of this utility model is to provide a kind of steam condensate to reclaim, and the efficient height is saved cost, and the steam condensate that reclaims condensate water automatically reclaims flash distillation plant.
In order to achieve the above object, the utility model is by the following technical solutions: a kind of steam condensate reclaims flash distillation plant, has flash tank, flash tank comprises tank body, the carbonated drink separating plate of band discharge orifice and the support that is connected with tank body, tank body is provided with inlet, venthole and liquid outlet, the below that is positioned at the carbonated drink separating plate in the tank body also is provided with liquid level regulation device, and liquid level regulation device is connected to liquid outlet.
After adopting said structure,, separate through carbonated drink because steam condensate enters flash tank from inlet, the water that reclaims discharges and flow to process such as boiler room again through liquid outlet all be to carry out under the state in totally-enclosed, do not contact, so recycle-water is not contaminated, can use repeatedly with the external world; And thermal loss is little, the organic efficiency height; Also be provided with liquid level regulation device owing to be positioned at carbonated drink separating plate below in the tank body, this liquid level regulation device is connected to liquid outlet, therefore utilize this liquid level regulation device, can control the water yield that flows out flash tank, thereby reach the function of regulating flash tank internal pressure and temperature, further improve the flash distillation organic efficiency, and need not water pump, utilize the flash tank internal pressure to reach the steam condensate recovery that circulates automatically, save cost, and be convenient to management.
Description of drawings
Fig. 1 is the structural representation that steam condensate of the present utility model reclaims flash distillation plant;
Fig. 2 is the cutaway view of Fig. 1 along the A-A line.
The specific embodiment
The embodiment that provides below in conjunction with accompanying drawing does explanation in further detail to the utility model.
As shown in Figure 1, 2, steam condensate of the present utility model reclaims flash distillation plant, has flash tank 1, flash tank 1 comprises tank body 1-1, the carbonated drink separating plate 1-5 of band discharge orifice 1-5-1 and the support 1-6 that is connected with tank body 1-1, tank body 1-1 is provided with inlet 1-1-1, venthole 1-1-2 and liquid outlet 1-1-3, the below that is positioned at carbonated drink separating plate 1-5 in the tank body 1-1 also is provided with liquid level regulation device 1-4, and liquid level regulation device 1-4 is connected to liquid outlet 1-1-3.
As shown in Figure 1, liquid level regulation device 1-4 is a float switch.Liquid level regulation device 1-4 also can be the electronic type liquid-level switch.
As shown in Figure 1, 2, in order to carry out carbonated drink separation more fully, be positioned at the carbonated drink separating plate 1-3 that carbonated drink separating plate 1-5 top also is provided with second band discharge orifice 1-3-1 in the tank body 1-1, this second carbonated drink separating plate 1-3 is connected by supporting 1-2 and tank body 1-1, and venthole 1-1-2 is positioned on the tank body 1-1 of second carbonated drink separating plate 1-3 top.
As shown in Figure 1, for flow and the pressure of controlling the steam condensate that enters flash tank 1, and be convenient to sending into of multichannel steam condensate, the inlet 1-1-1 of flash tank 1 links to each other with at least one steam trap 3 by pipeline 2.
As shown in Figure 1, be provided with the float switch 3-1 of control liquid outlet in the steam trap 3.Like this can strict control steam trap 3 interior liquid levels.
When the utility model uses, as shown in Figure 1, the steam condensate that comes out in the heater flows in the steam trap 3, float switch 3-1 control liquid level height, the steam condensate that will exceed a certain liquid level is delivered in the flash tank 1 continuously or discontinuously, the hurried step-down of steam condensate, pressure is reduced to 1.5～2.0kg/cm
2, the heat that exceeds more than 110 ℃ evaporates rapidly, and the low-pressure steam that is produced by venthole 1-1-2 output, is delivered to low pressure and is used with hot department after carbonated drink separating plate 1-5,1-3 separate.The condensate water of compiling under the carbonated drink separating plate 1-5 by liquid level regulation device 1-4 control, is delivered to the boiler deoxidizing method water tank through liquid outlet 1-1-3, the boiler of feeding feedwater.The different steam trap of a plurality of pressure 3 can be installed on the flash tank 1.Flash tank 1 also can be with steam trap 3 and use separately.
Claims (5)
1, a kind of steam condensate reclaims flash distillation plant, has flash tank (1), flash tank (1) comprises tank body (1-1), the carbonated drink separating plate (1-5) of band discharge orifice (1-5-1) and the support (1-6) that is connected with tank body (1-1), tank body (1-1) is provided with inlet (1-1-1), venthole (1-1-2) and liquid outlet (1-1-3), it is characterized in that: the below that is positioned at carbonated drink separating plate (1-5) in the tank body (1-1) also is provided with liquid level regulation device (1-4), and liquid level regulation device (1-4) is connected to liquid outlet (1-1-3).
2, steam condensate according to claim 1 reclaims flash distillation plant, and it is characterized in that: liquid level regulation device (1-4) is a float switch.
3, steam condensate according to claim 1 and 2 reclaims flash distillation plant, it is characterized in that: be positioned at the carbonated drink separating plate (1-3) that carbonated drink separating plate (1-5) top also is provided with second band discharge orifice (1-3-1) in the tank body (1-1), this second carbonated drink separating plate (1-3) is connected with tank body (1-1) by supporting (1-2), and venthole (1-1-2) is positioned on the tank body (1-1) of the second carbonated drink separating plate (1-3) top.
4, steam condensate according to claim 1 reclaims flash distillation plant, it is characterized in that: the inlet (1-1-1) of flash tank (1) links to each other with at least one steam trap (3) by pipeline (2).
5, steam condensate according to claim 4 reclaims flash distillation plant, it is characterized in that: the float switch (3-1) that is provided with the control liquid outlet in the steam trap (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520076337 CN2826176Y (en) | 2005-10-10 | 2005-10-10 | Flash evaporator capable of recovering steam condensed water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520076337 CN2826176Y (en) | 2005-10-10 | 2005-10-10 | Flash evaporator capable of recovering steam condensed water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2826176Y true CN2826176Y (en) | 2006-10-11 |
Family
ID=37066361
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520076337 Expired - Fee Related CN2826176Y (en) | 2005-10-10 | 2005-10-10 | Flash evaporator capable of recovering steam condensed water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2826176Y (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101290087B (en) * | 2007-04-20 | 2011-05-11 | 宝山钢铁股份有限公司 | Vapor condensation water and its secondary steam recovery method and equipment |
| CN101627276B (en) * | 2007-12-10 | 2012-01-04 | 株式会社东芝 | Steam condenser |
| CN102563609A (en) * | 2010-12-31 | 2012-07-11 | 贵州中烟工业有限责任公司 | Condensate-recycling system |
| CN102829460A (en) * | 2012-09-16 | 2012-12-19 | 北京工业大学 | Method for recovering surplus heat source energy by using flash evaporator |
| CN103185369A (en) * | 2012-08-20 | 2013-07-03 | 哈尔滨工大金涛科技股份有限公司 | Directly heating machine |
| CN103185362A (en) * | 2012-10-08 | 2013-07-03 | 哈尔滨工大金涛科技股份有限公司 | Low-position straight heating machine |
| CN104482524A (en) * | 2014-12-20 | 2015-04-01 | 桐梓县创兴自动化设备有限公司 | Textile steam recovery device |
-
2005
- 2005-10-10 CN CN 200520076337 patent/CN2826176Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101290087B (en) * | 2007-04-20 | 2011-05-11 | 宝山钢铁股份有限公司 | Vapor condensation water and its secondary steam recovery method and equipment |
| CN101627276B (en) * | 2007-12-10 | 2012-01-04 | 株式会社东芝 | Steam condenser |
| CN102563609A (en) * | 2010-12-31 | 2012-07-11 | 贵州中烟工业有限责任公司 | Condensate-recycling system |
| CN102563609B (en) * | 2010-12-31 | 2015-03-25 | 贵州中烟工业有限责任公司 | Condensate-recycling system |
| CN103185369A (en) * | 2012-08-20 | 2013-07-03 | 哈尔滨工大金涛科技股份有限公司 | Directly heating machine |
| CN102829460A (en) * | 2012-09-16 | 2012-12-19 | 北京工业大学 | Method for recovering surplus heat source energy by using flash evaporator |
| CN103185362A (en) * | 2012-10-08 | 2013-07-03 | 哈尔滨工大金涛科技股份有限公司 | Low-position straight heating machine |
| CN103185362B (en) * | 2012-10-08 | 2016-03-23 | 哈尔滨工大金涛科技股份有限公司 | Low level directly-heated machine |
| CN104482524A (en) * | 2014-12-20 | 2015-04-01 | 桐梓县创兴自动化设备有限公司 | Textile steam recovery device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061011 Termination date: 20111010 |