CN87210486U - Vaccum dewater and gas removing device - Google Patents
Vaccum dewater and gas removing device Download PDFInfo
- Publication number
- CN87210486U CN87210486U CN 87210486 CN87210486U CN87210486U CN 87210486 U CN87210486 U CN 87210486U CN 87210486 CN87210486 CN 87210486 CN 87210486 U CN87210486 U CN 87210486U CN 87210486 U CN87210486 U CN 87210486U
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- chamber
- valve
- vacuum
- utility
- filler
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- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model discloses a novel vacuum dewatering and gas removing device, belonging to a liquid depth dewatering and gas removing integral device by adopting the vacuum method; The utility model comprises a mixing-chamber, a filler chamber, a floating type rotary valve, a vacuum chamber, a plenum chamber, a casing, etc.; the utility model makes up for the insufficiency of the use function of the public known vacuum dewatering and gas removing device, and has the function of stirring, mixing, centrifugal separation, liquid level adjusting, etc. The utility model has the advantages of good tightness and small size.
Description
The utility model belongs to the comprehensive device of a kind of deep dehydration that adopts vacuum method to carry out liquid, degasification.
General known liquid vacuum dehydration, depassing unit, sealing property is relatively poor, easily sews, and liquid level is difficult for keeping, and system is more numerous and more jumbled, and cost is higher, brings many inconvenience to use.
The purpose of this utility model is to design a kind of novel vacuum dehydration, depassing unit, makes it good seal performance, and system is simple, and is easy to use, and cost is low.
Characteristics of the present utility model are:
1, designed the floating type multifunctional rotary rotary valve of self-regulated, had functions such as stirring, mixing, centrifugation and liquid level adjustment, helped the heat and the transmission of matter, be easy to the dehydration of degree of depth ground, degasification, kept liquid level, and can prevent that desire from removing gas and being wrapped up in suction by fluid.
2, adopt supercharge method in the booster, solved the leakage problems of the removal component of liquid outlet preferably.
3, adopt degasifier (as NH
3, N
2H
4, C
2H
5OH etc.), reduce to remove the gaseous phase partial pressure of component, can further reduce fluid temperature.
4, adopt back-off type outer cover, remove liquid and go into, export, remove outside component outlet and the pressure measurement external pipeline, do not have other external outlet, guaranteed sealing property.
5, compare with known vacuum dehydration, depassing unit, volume is little, and system is simplified greatly, and cost is lower.
Operation principle of the present utility model is:
Adopt vacuum method that the gaseous phase partial pressure of removing component is reduced, reduce this component concentration in liquid; The boiling point of liquid reduces under the vacuum state, and the corresponding increase of the dividing potential drop of liquid in gas phase has reduced to remove the dividing potential drop of component in gas phase; When one timing of gas phase stagnation pressure, remove the component dividing potential drop of any component in addition as long as increase, the concentration of removal component in liquid is reduced.
Below with reference to accompanying drawing the utility model is described in further detail.
Accompanying drawing 1 is the utility model general assembly structural representation.
With reference to Fig. 1, the utility model partly is made up of mixing chamber 1, filler chamber 2, floating type rotary valve 3, vacuum chamber 4, pumping chamber 5 and housing 6 etc.Mixing chamber 1 comprises inlet tube 7, upper flange 8, impeller 9, the shell 10 on top and the assemblies such as rotating shaft 13 that are bound up with impeller 9.Mixing chamber 1 inside is a cylindrical cavity.Filler chamber 2 is between mixing chamber 1 and floating type rotary valve 3, and inside also is a cylindrical cavity, is provided with filler 12, porous grid 11 and sleeve 25 in cavity.Sleeve 25 upper ends are fixed with mixing chamber 1 bottom and are communicated.Floating type rotary valve 3 comprises valve 16 and following valve 20 two parts, a back-off of this body image of last valve 16 round-ended cylinder arranged, the vacuum chamber 4 and filler chamber's 2 conductings that make floating type rotary valve 3 interior many communicating pipes 15 are arranged at an upper portion thereof.The last valve 16 top center nozzle 14 of ining succession, its inner chamber is turbination, bottom lock, rotating shaft 13 roots are fixed on it.Rotating shaft 13 passes sleeve 25, can drive floating type rotary valve 3 rotations.There are a tapered flanges 26 and nozzle 14 engagements in sleeve 25 lower ends.Following valve 20 comprises air guide shroud 17, sleeve pipe 18.One of this body image of following valve 20 is just being put round-ended cylinder.Last valve 16 sets with each other with following valve 20, forms inner vacuum chamber 4.Pumping chamber 5 comprises carrying cylinder 21, wireway 19, catheter 22, booster 23 and lower flange 24.By in the air guide shroud 17, the lower end is connected with the vacuum machine of system by lower flange 24 by sleeve pipe 18 in wireway 19 upper ends.Pumping chamber's 5 inner chambers are cylindrical.Housing 6 is thin-walled core structures.
The utility model course of work is as follows:
Process temperature adjustment or interpolation degasifier are (as NH
3, N
2H
4, C
2H
5OH etc.) liquid enters mixing chamber 1 by inlet tube 7, with impeller 9 red switch, by rotating shaft 13, drives floating type rotary valve 3 rotations, and rotary speed is decided by feed liquor amount size.Liquid in the mixing chamber 1 is turbination through sleeve 25 upward by nozzle 14 formation liquid films and is sprayed onto filler chamber 2.Because the rotation of floating type rotary valve 3, liquid is subjected to centrifugal action when flowing through nozzle 14, and liquid and removal component, degasifier are separated because of quality is different.When the liquid that is sprayed onto filler chamber 2 was flowed through corrugated filler 12, liquid film was by more than 12 high degree of dispersion of filler and tearing, and made to remove component and have enough chances to deviate from from liquid.The removal component that is separated sucks vacuum chamber 4 by communicating pipe 15, and the vacuum machine that is entered system by wireway 19 is excluded.Sloughed the space inflow pumping chamber 5 of liquid around floating type rotary valve 3 and between the housing 6 of removing component in the filler chamber 2.In pumping chamber 5, through the effect of booster 23, liquid becomes malleation by negative pressure, makes the liquid pump of system prevent that easily the packing leakage problem from taking place.
When system loading changed, load of the present utility model also changed thereupon.Load increases, and makes it flow and increases, and liquid level descends, and floating type rotary valve 3 descends thereupon, and the aperture of the nozzle 14 of last valve 16 strengthens, and is last, reaches liquid level and rises, and remains to certain altitude.If load reduces, just the opposite with above-mentioned situation, the aperture of nozzle 14 diminishes, and when the utility model fluid flow of coming in and going out equates, just reaches corresponding stable liquid level.When equipment is stopped transport, last valve 16 will be closed tight automatically.
Enter liquid of the present utility model and enter system through booster 23.
The utility model is applicable to the deoxygenation of industry and civil boiler moisturizing, the deoxygenation of flushing, the cation bed water deoxygenation of chemical water desalination hydrogen ion and carbon dioxide, the career fields such as the dehydration of oil and desalinization.
Claims (2)
1, a kind of employing vacuum method carries out the liquid dehydration, depassing unit, by mixing chamber 1, filler chamber 2, floating type rotary valve 3, vacuum chamber 4, pumping chamber 5 and housing 6 are formed, it is characterized in that, mixing chamber 1 comprises inlet tube 7, upper flange 8, impeller 9, shell 10 and rotating shaft 13, be provided with filler 12 in the filler chamber 2, porous grid 11 and sleeve 25, there are a tapered flanges 26 and nozzle 14 engagements in sleeve 25 lower ends, floating type rotary valve 3 comprises valve 16 and following valve 20 two parts, two valves set with each other up and down, form inner vacuum chamber 4, pumping chamber 5 comprises carrying cylinder 21, wireway 19, catheter 22, booster 23 and lower flange 24.
2, dehydration according to claim 1, depassing unit is characterized in that, the last valve 16 top center nozzle 14 of ining succession, and its inner chamber is turbination, bottom lock, rotating shaft 13 roots are fixed on it, and following valve 20 comprises air guide shroud 17, sleeve pipe 18.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 87210486 CN87210486U (en) | 1987-08-25 | 1987-08-25 | Vaccum dewater and gas removing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 87210486 CN87210486U (en) | 1987-08-25 | 1987-08-25 | Vaccum dewater and gas removing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN87210486U true CN87210486U (en) | 1988-03-23 |
Family
ID=4825411
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 87210486 Withdrawn CN87210486U (en) | 1987-08-25 | 1987-08-25 | Vaccum dewater and gas removing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN87210486U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1981907B (en) * | 2002-03-01 | 2010-12-08 | 庄臣及庄臣视力保护公司 | Degasser for liquid degassing in vacuum |
| CN103041621A (en) * | 2013-01-25 | 2013-04-17 | 李明忠 | Fluid kinetic energy type paddle driver |
| CN103284288A (en) * | 2013-06-07 | 2013-09-11 | 江苏南方机电股份有限公司 | Degassing main machine for jam type food materials |
| CN105854355A (en) * | 2016-05-10 | 2016-08-17 | 武汉工程大学 | Exogenetic force link gas-liquid separation device |
| CN108031166A (en) * | 2017-12-22 | 2018-05-15 | 苏州艾捷尔斯生物科技有限公司 | A kind of environment-friendly type centrifugal dewatering equipment |
| CN111512091A (en) * | 2017-12-22 | 2020-08-07 | 福瑞科有限公司 | Assembly for cleaning and/or protecting a liquid conduit system |
| CN117618989A (en) * | 2023-10-23 | 2024-03-01 | 山东明合地热能源开发有限公司 | Oil-gas-water three-phase separator |
-
1987
- 1987-08-25 CN CN 87210486 patent/CN87210486U/en not_active Withdrawn
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1981907B (en) * | 2002-03-01 | 2010-12-08 | 庄臣及庄臣视力保护公司 | Degasser for liquid degassing in vacuum |
| CN103041621A (en) * | 2013-01-25 | 2013-04-17 | 李明忠 | Fluid kinetic energy type paddle driver |
| CN103284288A (en) * | 2013-06-07 | 2013-09-11 | 江苏南方机电股份有限公司 | Degassing main machine for jam type food materials |
| CN105854355A (en) * | 2016-05-10 | 2016-08-17 | 武汉工程大学 | Exogenetic force link gas-liquid separation device |
| CN108031166A (en) * | 2017-12-22 | 2018-05-15 | 苏州艾捷尔斯生物科技有限公司 | A kind of environment-friendly type centrifugal dewatering equipment |
| CN111512091A (en) * | 2017-12-22 | 2020-08-07 | 福瑞科有限公司 | Assembly for cleaning and/or protecting a liquid conduit system |
| CN117618989A (en) * | 2023-10-23 | 2024-03-01 | 山东明合地热能源开发有限公司 | Oil-gas-water three-phase separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |