CN201906475U - Flash evaporator - Google Patents
Flash evaporator Download PDFInfo
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- CN201906475U CN201906475U CN2010206395492U CN201020639549U CN201906475U CN 201906475 U CN201906475 U CN 201906475U CN 2010206395492 U CN2010206395492 U CN 2010206395492U CN 201020639549 U CN201020639549 U CN 201020639549U CN 201906475 U CN201906475 U CN 201906475U
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- flash tank
- water
- liquid level
- flash
- outlet valve
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A flash evaporator comprises a flash tank, wherein a water inlet pipe for high-temperature condensate water, an air outlet pipe for discharging secondary steam and a water outlet pipe for discharging the high-temperature condensate water are arranged on the flash tank; a water inlet valve is arranged on the water inlet pipe; an air outlet valve is arranged on the air outlet pipe; a water outlet valve is arranged on the water outlet pipe; at least one layer of vapor-water separation plate is arranged inside the flash tank; a magnetic turning board liquid level meter for metering the liquid level of condensed water in the flash tank is arranged inside the flash tank; and a level control sensor is positioned at the upper part of the flash tank and electrically connected with the magnetic turning board liquid level meter, and used for controlling the opening and closing of the outlet valve through the variations in the liquid level. In the flash evaporator disclosed by the utility model, the level control sensor is arranged, so that the water feeding time and the water discharging time are effectively connected, and the work efficiency is improved.
Description
Technical field
The utility model relates to a kind of water separator in the condensation water recovery system, is specifically related to a kind of flash distillation plant.
Background technology
Flash tank is mainly used in the recovery system of Thermal Power Station's discharging of boiler, by with the indirect steam in the condensed water and moisture from, make indirect steam continue to be applied in the low-voltage equipment, condensed water is recycled, and improves the utilization ratio of condensed water.
Existing flash distillation plant is provided with float in flash tank inside, and when the condensed water of flash tank inside arrived the water inlet, float cut out water inlet, opens outlet valve afterwards condensed water is discharged, and there is following defective in existing flash distillation plant:
Life period was poor between float arrival water inlet and outlet valve were opened, and had increased the cycle of full flashing, had reduced the separative efficiency of flash distillation plant.
In addition, the liquid level lifting situation operating personnel of flash tank inside are difficult to observe, and can't determine whether the work of flash tank inside is normal.
The utility model content
The carbonated drink mixing the utility model discloses a kind of flash distillation plant to the influence of the device and the efficiency of heating surface in the recovery condensed water removal process in order to solve, to reach the purpose that carbonated drink is effectively separated.
The technical solution of the utility model is as follows:
A kind of flash distillation plant, comprise flash tank, described flash tank is provided with the water inlet pipe of high-temperature condensation water, be used to discharge the escape pipe of indirect steam, and the outlet pipe that is used to discharge high-temperature condensation water, described water inlet pipe is provided with water intaking valve, and described escape pipe is provided with air outlet valve, described drainpipe is provided with outlet valve, and the inside of described flash tank is provided with one deck carbonated drink separating plate at least;
The inside of described flash tank is provided with the magnetic turnover panel liquid level gauge that is used to measure condensed water liquid level in the described flash tank;
Be positioned at the top of described flash tank and be electrically connected with the liquid level control sensor of controlling described outlet valve keying by the variation of liquid level with described magnetic turnover panel liquid level gauge.
Preferably, described carbonated drink separating plate is 3 layers.
Preferably, be uniformly distributed with venthole on the described carbonated drink separating plate.
Preferably, also be provided with radiating fin on the described carbonated drink separating plate.
Preferably, also be provided with the drainpipe that is used for interim discharging on the described flash tank
The utility model discloses a kind of flash distillation plant, by orifice plate being set in flash tank inside, indirect steam is discharged from the gas outlet of flash tank top by orifice plate, condensed water drops on the bottom of flash tank, guaranteed effectively separating of condensed water and indirect steam, and the inside of flash tank is provided with magnetic turnover panel liquid level gauge, make the staff can observe the level condition of flash tank inside timely, the liquid level control sensor of the top of flash tank setting simultaneously is electrically connected with magnetic turnover panel liquid level gauge, liquid level by flash tank inside changes the keying of controlling outlet valve, has improved operating efficiency.
Description of drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, to do to introduce simply to the accompanying drawing of required use in embodiment or the description of the Prior Art below, apparently, accompanying drawing in describing below only is embodiment more of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of the disclosed a kind of flash distillation plant of the utility model;
Fig. 2 is the structural representation of the inner carbonated drink separating plate of the disclosed a kind of flash distillation plant of the utility model.
11, flash tank 12, carbonated drink separating plate 13, liquid level control sensor 14, magnetic turnover panel liquid level gauge 15, escape pipe 16, water inlet pipe 17, outlet pipe 18, drainpipe 151, air outlet valve 161, water intaking valve 171, outlet valve 181, draining valve 21, through hole
The specific embodiment
Below in conjunction with the accompanying drawing among the utility model embodiment, the technical scheme among the utility model embodiment is clearly and completely described, obviously, described embodiment only is the utility model part embodiment, rather than whole embodiment.Based on the embodiment in the utility model, those of ordinary skills are not making the every other embodiment that is obtained under the creative work prerequisite, all belong to the scope of the utility model protection.
As Fig. 1, shown in Figure 2, structural representation for the disclosed a kind of flash distillation plant of the utility model, this device comprises flash tank 11, flash tank 11 is provided with the water inlet pipe 16 of high-temperature condensation water, be used to discharge the escape pipe 15 of indirect steam, and the outlet pipe 17 that is used to discharge high-temperature condensation water, water inlet pipe 16 is provided with water intaking valve 161, escape pipe 15 is provided with air outlet valve 151, air outlet valve 151 is a normally open valve, outlet pipe 17 is provided with outlet valve 171, outlet valve 171 is a normally close valve, and outlet pipe 17 gos deep into the bottom of flash tank 11, guarantees that the condensed water of flash tank 11 inside reclaims completely, the bottom of flash tank 11 also is provided with drainpipe 18, guarantees to break down or internal condensation water is emitted effectively during other situation at device.
The inside of flash tank 11 is provided with carbonated drink separating plate 12, the inwall of the size of carbonated drink separating plate 12 and flash tank 11 is complementary, and be fixed on the described flash tank 11, carbonated drink separating plate 12 is three layers, three layers of carbonated drink separating plate 12 are thrown between water inlet pipe 16 and the outlet pipe 17 uniformly, the carbonated drink separating plate is provided with through hole 21, and the number of plies of carbonated drink separating plate 12 and the quantity of through hole 21 that is positioned at its top all are determined on a case-by-case basis, and do not limit at this.
Also be provided with the radiating fin (not shown) on the carbonated drink separating plate 12 uniformly, radiating fin is lowered the temperature high-temperature condensation water effectively, discharges indirect steam fully, guarantees the service efficiency of steam.
The top of flash tank 11 is provided with magnetic turnover panel liquid level gauge 14, and magnetic turnover panel liquid level gauge 14 shows the liquid level lifting situation of flash tank 11 inside timely, is convenient to staff's observation.
The top of flash tank 11 also is provided with liquid level control sensor 13, and liquid level control sensor 13 is electrically connected with magnetic turnover panel liquid level gauge 14, responds to the variation of inner liquid level, the keying of control outlet valve 171.
Operation principle of the present utility model is as follows:
When condensed water enters, water intaking valve 161 is opened automatically, high-temperature condensation water is imported in the flash tank 11, after 12 separation of carbonated drink separating plate, indirect steam is discharged from the air outlet valve 151 on the flash tank 11, and draining valve 151 is a normally open valve, when liquid level arrives the setting index, water intaking valve 161 is closed automatically, and the control outlet valve 171 of liquid level control sensor 13 reclaims condensed water.
The utility model discloses a kind of flash distillation plant, by orifice plate being set in flash tank inside, indirect steam is discharged from the gas outlet of flash tank top by orifice plate, condensed water drops on the bottom of flash tank, guaranteed effectively separating of condensed water and indirect steam, and the inside of flash tank is provided with magnetic turnover panel liquid level gauge, make the staff can observe the level condition of flash tank inside timely, the liquid level control sensor of the top of flash tank setting simultaneously is electrically connected with magnetic turnover panel liquid level gauge, keying by each valve on the liquid level variation control piper of flash tank inside has improved operating efficiency.
Simultaneously, in the flash tank bottom discharge outlet is set, when having guaranteed that device breaks down, condensed water can be discharged effectively.
More than be description,, make this area professional and technical personnel can realize or use the utility model by above-mentioned explanation to the disclosed embodiments to the utility model embodiment.Multiple modification to these embodiment will be conspicuous concerning those skilled in the art, and defined herein General Principle can realize under the situation that does not break away from spirit or scope of the present utility model in other embodiments.Therefore, the utility model will can not be restricted to these embodiment shown in this article, but will meet and principle disclosed herein and features of novelty the wideest corresponding to scope.
Claims (5)
1. flash distillation plant, comprise flash tank, described flash tank is provided with the water inlet pipe of high-temperature condensation water, be used to discharge the escape pipe of indirect steam, and the outlet pipe that is used to discharge high-temperature condensation water, described water inlet pipe is provided with water intaking valve, described escape pipe is provided with air outlet valve, described drainpipe is provided with outlet valve, it is characterized in that
The inside of described flash tank is provided with one deck carbonated drink separating plate at least;
The inside of described flash tank is provided with the magnetic turnover panel liquid level gauge that is used to measure condensed water liquid level in the described flash tank;
Be positioned at the top of described flash tank and be electrically connected with the liquid level control sensor of controlling described outlet valve keying by the variation of liquid level with described magnetic turnover panel liquid level gauge.
2. flash distillation plant according to claim 1 is characterized in that, described carbonated drink separating plate is 3 layers.
3. flash distillation plant according to claim 2 is characterized in that, is uniformly distributed with venthole on the described carbonated drink separating plate.
4. flash distillation plant according to claim 2 is characterized in that, also is provided with radiating fin on the described carbonated drink separating plate.
5. according to each described flash distillation plant of claim 1-4, it is characterized in that, also be provided with the drainpipe that is used for interim discharging on the described flash tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206395492U CN201906475U (en) | 2010-12-03 | 2010-12-03 | Flash evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206395492U CN201906475U (en) | 2010-12-03 | 2010-12-03 | Flash evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201906475U true CN201906475U (en) | 2011-07-27 |
Family
ID=44298685
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206395492U Expired - Fee Related CN201906475U (en) | 2010-12-03 | 2010-12-03 | Flash evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201906475U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527201A (en) * | 2011-12-31 | 2012-07-04 | 福建省建瓯市芝星活性炭有限公司 | Technical device for recycling tail gas and residual heat during production of active carbon with phosphoric acid method |
| CN102553279A (en) * | 2012-01-16 | 2012-07-11 | 哈尔滨工程大学 | High pressure flash drum |
| CN102921181A (en) * | 2012-11-12 | 2013-02-13 | 广西农垦思源酒业有限公司 | Recovery method and recovery equipment of distillation waste liquid latent heat of alcohol plant |
| CN104296124A (en) * | 2014-10-21 | 2015-01-21 | 佛山市佳利达环保科技股份有限公司 | Medium-temperature medium-pressure steam waste heat recovery device |
| CN104998431A (en) * | 2015-08-05 | 2015-10-28 | 太仓中化环保化工有限公司 | Comprehensive utilization device and method for steam condensate in fluorocarbon alkane production device |
| CN106287196A (en) * | 2016-09-29 | 2017-01-04 | 佛山市丰川节能科技有限公司 | A kind of steam condensate (SC) steam trap connection and control method thereof |
| CN108917372A (en) * | 2018-05-21 | 2018-11-30 | 亚太森博（山东）浆纸有限公司 | A kind of flash vapor system |
| CN112050176A (en) * | 2020-07-23 | 2020-12-08 | 东莞市福瑞斯环保设备有限公司 | Heat storage type enhanced heat pump steam unit |
-
2010
- 2010-12-03 CN CN2010206395492U patent/CN201906475U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527201A (en) * | 2011-12-31 | 2012-07-04 | 福建省建瓯市芝星活性炭有限公司 | Technical device for recycling tail gas and residual heat during production of active carbon with phosphoric acid method |
| CN102527201B (en) * | 2011-12-31 | 2016-04-20 | 福建省芝星炭业股份有限公司 | Phosphoric acid tail gas and waste heat recovery re-use device in activated carbon of phosphoric acid method production |
| CN102553279A (en) * | 2012-01-16 | 2012-07-11 | 哈尔滨工程大学 | High pressure flash drum |
| CN102553279B (en) * | 2012-01-16 | 2014-03-26 | 哈尔滨工程大学 | High pressure flash drum |
| CN102921181A (en) * | 2012-11-12 | 2013-02-13 | 广西农垦思源酒业有限公司 | Recovery method and recovery equipment of distillation waste liquid latent heat of alcohol plant |
| CN102921181B (en) * | 2012-11-12 | 2014-12-10 | 广西农垦思源酒业有限公司 | Recovery method and recovery equipment of distillation waste liquid latent heat of alcohol plant |
| CN104296124A (en) * | 2014-10-21 | 2015-01-21 | 佛山市佳利达环保科技股份有限公司 | Medium-temperature medium-pressure steam waste heat recovery device |
| CN104998431A (en) * | 2015-08-05 | 2015-10-28 | 太仓中化环保化工有限公司 | Comprehensive utilization device and method for steam condensate in fluorocarbon alkane production device |
| CN106287196A (en) * | 2016-09-29 | 2017-01-04 | 佛山市丰川节能科技有限公司 | A kind of steam condensate (SC) steam trap connection and control method thereof |
| CN108917372A (en) * | 2018-05-21 | 2018-11-30 | 亚太森博（山东）浆纸有限公司 | A kind of flash vapor system |
| CN112050176A (en) * | 2020-07-23 | 2020-12-08 | 东莞市福瑞斯环保设备有限公司 | Heat storage type enhanced heat pump steam unit |
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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: 20110727 Termination date: 20121203 |