CN206121203U - Meticulous atomizing flash tank - Google Patents
Meticulous atomizing flash tank Download PDFInfo
- Publication number
- CN206121203U CN206121203U CN201620393124.5U CN201620393124U CN206121203U CN 206121203 U CN206121203 U CN 206121203U CN 201620393124 U CN201620393124 U CN 201620393124U CN 206121203 U CN206121203 U CN 206121203U
- Authority
- CN
- China
- Prior art keywords
- flash tank
- vaporizer
- tank
- jar
- aerochamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
Abstract
The utility model provides a meticulous atomizing flash tank, is including the atomizer chamber and the vaporizer that are linked together, meticulous atomizing flash tank's inlet pipe is installed in the atomizer chamber to install a plurality of atomizers on the inlet pipe, meticulous atomizing flash tank's gas liquid separator installs in the vaporizer. Two cavities for being linked together are separated by the baffle by meticulous atomizing flash tank's the internal portion of jar, and the baffle top is the vaporizer, and the baffle below is the atomizer chamber. Perhaps, regard as atomizer chamber and vaporizer respectively by two jar bodies, two jar bodies are by intercommunication passageway intercommunication. Flash tank during operation, through -put atomizer spout with the little liquid drop form of dispersion goes into jar internally, and the little liquid drop suspension of dispersion is in jar internal space, and the surface area is huge, and under the internal low pressure condition of jar, the carburetion takes place on all little liquid drops surfaces, does not just have the static pressure effect, and liquid vaporization effect is better, has overcome traditional flash tank and has had static pressure effect and the little shortcoming of flash distillation vaporization surface area.
Description
Technical field
This utility model is related to a kind of finer atomization flash tank, belongs to field of chemical equipment.
Background technology
Flash tank plays pivotal role in the industries such as light industry, chemical industry, metallurgy, building materials.Due to its floor space it is little, energy
It is continuous to produce, good reliability, high degree of automation, environmentally safe.Flash distillation is that water is entered in flash tank, due to dashing forward for pressure
So reduce, the boiling point of water is decreased so that water rapid vaporization, water vapour are detached from flash tank.The boiling point of water is with pressure
Increase and raise, conversely, pressure is lower, boiling point is also lower.Flash principle is exactly to allow high pressure-temperature water in lower pressure environment, is made
Its boiling point is reduced, the boiling point under water temperature is higher than residing pressure, water rapid boiling vaporization in flash tank, and carries out biphase point
From.The effect of flash tank is to provide the space of water rapid vaporization and vapor-liquid separation, is that water seethes with excitement in flash tank, so as to realize water
Vaporization is separated.Traditional flash tank is generally single tank structure, and high-temperature water enters flash distillation along tank body tangential direction by water inlet
Tank, the steam that flash distillation is produced are discharged from tank body top, and unboiled water is discharged from tank body lower part.But, lead in traditional flash drum
Often maintain have certain height of water level, be inevitably present hydrostatic effects, vaporization occurs mainly in liquid level surface, liquid level
Below partially due to hydrostatic pressure affects, boiling vaporization capacity declines.Traditional flash drum does not emphasize that feed pipe upper nozzle sprays
Impact of the droplet size to flash tank flash evaporation effect, while tank inner chamber is divided into two functions not by no design entity part
Same chamber.
Utility model content
This utility model is directed to the deficiencies in the prior art, there is provided a kind of more preferable finer atomization flash distillation of flash of steam effect
Tank.
To achieve these goals, this utility model employs technical scheme below：
A kind of finer atomization flash tank, including the aerochamber and vaporizer that are connected, the finer atomization flash tank enters
Expects pipe is arranged in aerochamber, and multiple atomizers are provided with feed pipe, the vapour-liquid point of the finer atomization flash tank
It is arranged in vaporizer from device.
The tank interior of the finer atomization flash tank is divided into the two chambers being connected by dividing plate, is vapour above dividing plate
Change room, be aerochamber below dividing plate.
By two tank bodies respectively as aerochamber and vaporizer, two tank bodies are connected by communicating passage.
Vapour liquid separator is provided with multiple equally distributed ventholes.
Compared with prior art, the beneficial effect that this utility model possesses：
(1), when flash tank described in the utility model works, water sprays into tank with scattered droplet form by atomizer
In vivo, scattered droplet is suspended in the space in tank body, and surface area is huge, under lower pressure in tank body, vaporization
Occur on all droplet surfaces, water vapor effect more preferably, overcomes traditional flash drum flash of steam and mainly occurs at liquid level
Shortcoming.
(2) two chambers that tank interior is designed to be connected by this utility model, enable to water first with atomized drop
Form be introduced into aerochamber, enter back into vaporizer, although aerochamber is connected with vaporizer, but the environment bar of two chambers
Part is incomplete same, can extend the time of staying of the material of atomized drop in tank so that atomized drop is subject to low in tank body
The effect of super pressure-high temperature environment is more long, further increases vaporizing liquid efficiency.
Description of the drawings
Fig. 1 is the structural representation of the finer atomization flash tank that dividing plate described in the utility model separates configuration.
Fig. 2 is the structural representation of the finer atomization flash tank of two tank body configurations described in the utility model.
1. flange；2. venthole；3. deflector；4. tank body；5 dividing plates；7. feed pipe；8. atomizer；9. aerochamber；
10. discharge nozzle；11. mozzles；12. vaporizers；13. vapour liquid separators；14. Disengagement zone；15. escape pipes；16. communicating passages connect
It is logical.
Specific embodiment
The technical solution of the utility model is further elaborated below by embodiment.
Embodiment 1
A kind of finer atomization flash tank, including the aerochamber 9 and vaporizer 12 that are connected, the finer atomization flash tank
Feed pipe 7 is arranged in aerochamber 9, and multiple atomizers 8, the vapour-liquid of the finer atomization flash tank are provided with feed pipe 7
Separator 13 is arranged in vaporizer 12.
The tank interior of the finer atomization flash tank is divided into the two chambers being connected by dividing plate 5, above dividing plate 5 is
Vaporizer 12, is aerochamber 9 below dividing plate 5.
By two tank bodies respectively as aerochamber 9 and vaporizer 12, two tank bodies connect 16 by communicating passage.
Vapour liquid separator 13 is provided with multiple equally distributed ventholes 2.
Finer atomization flash tank described in the present embodiment on the basis of features described above structure, also including vapour liquid separator, vapour
Liquid/gas separator includes flange 1, venthole 2, deflector 3, mozzle 11, Disengagement zone 14 and escape pipe 15.Vapour liquid separator 13
Above tank body 4, vapour liquid separator 13 can adopt various conventional vapour liquid separators.Venthole 2 is arranged on Disengagement zone 14
On the wall of side and Disengagement zone 14 is connected with inside tank body 4 by venthole 2.Mozzle 11 is connected to the lower section of Disengagement zone 14, and
With communicate inside tank body 4, the liquid of Disengagement zone 14 can pass through the liquid that mozzle 11 is directly flow in 4 bottom of tank body and tank body
Body converges, prevent liquid be subject to air-flow disturbance again with gas mixing.In addition, mozzle 11 to realize liquid to Disengagement zone close
Seal to ensure separating effect；Escape pipe 15 is located at the top of tank body 4 and stretches in vapour liquid separator 13, by vapour liquid separator 13
Connect with the inside of tank body 4, escape pipe 15 is connected by flange 1 with tank body 4, as one end of escape pipe 15 is located at venthole 2
Lower section, so as to be easier to produce whirlpool in Disengagement zone 14, to provide bigger centrifugal force；Discharge nozzle 10 is located at the bottom of tank body 4
Portion.
Claims (2)
1. a kind of finer atomization flash tank, it is characterised in that including the aerochamber and vaporizer that are connected, the finer atomization is dodged
The feed pipe of steaming pot is arranged in aerochamber, and multiple atomizers, the vapour of the finer atomization flash tank are provided with feed pipe
Liquid/gas separator is arranged in vaporizer；
The tank interior of the finer atomization flash tank is divided into the two chambers being connected by dividing plate, is vaporization above dividing plate
Room, is aerochamber below dividing plate；Or, by two tank bodies respectively as aerochamber and vaporizer, two tank bodies are by communicating passage
Connection.
2. finer atomization flash tank as claimed in claim 1, it is characterised in that the vapour liquid separator is provided with multiple uniform
The venthole of distribution.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2016201396763 | 2016-02-24 | ||
| CN201620139676 | 2016-02-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206121203U true CN206121203U (en) | 2017-04-26 |
Family
ID=56288807
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620393124.5U Expired - Fee Related CN206121203U (en) | 2016-02-24 | 2016-05-04 | Meticulous atomizing flash tank |
| CN201610288554.5A Pending CN105727583A (en) | 2016-02-24 | 2016-05-04 | Fine atomization flash tank |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610288554.5A Pending CN105727583A (en) | 2016-02-24 | 2016-05-04 | Fine atomization flash tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN206121203U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930171A (en) * | 2017-12-20 | 2018-04-20 | 四川省银河化学股份有限公司 | Flash vessel for the discharging of high-temperature high-voltage reaction device |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BR112019003097B1 (en) * | 2016-09-21 | 2022-09-06 | Borealis Ag | FLASH SEPARATOR AND PROCESS FOR SEPARATING HYDROCARBONS FROM A REACTION SOLUTION CONTAINING A POLYMER AND SUCH HYDROCARBONS |
| CN107050906B (en) * | 2017-01-24 | 2022-06-10 | 曹海亮 | Pressure stabilizing protection spray head for corrosive fluid flash evaporation |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7628893B1 (en) * | 2005-08-01 | 2009-12-08 | Pure Energy Technology Co | Apparatus and method for separation |
| CN202410203U (en) * | 2012-02-04 | 2012-09-05 | 潍坊兴信技术服务有限公司 | Flash tank |
| CN202822825U (en) * | 2012-09-25 | 2013-03-27 | 安徽中粮生化燃料酒精有限公司 | Flash tank |
| CN203494189U (en) * | 2013-08-23 | 2014-03-26 | 天津聚贤达科技有限公司 | Flash tank |
| CN204973114U (en) * | 2015-09-22 | 2016-01-20 | 成都艾比科生物科技有限公司 | Flash tank for preparing dimethyl ether |
-
2016
- 2016-05-04 CN CN201620393124.5U patent/CN206121203U/en not_active Expired - Fee Related
- 2016-05-04 CN CN201610288554.5A patent/CN105727583A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107930171A (en) * | 2017-12-20 | 2018-04-20 | 四川省银河化学股份有限公司 | Flash vessel for the discharging of high-temperature high-voltage reaction device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105727583A (en) | 2016-07-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170426 Termination date: 20210504 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |