CN205570028U - Oxygenerator water separator - Google Patents
Oxygenerator water separator Download PDFInfo
- Publication number
- CN205570028U CN205570028U CN201620349974.5U CN201620349974U CN205570028U CN 205570028 U CN205570028 U CN 205570028U CN 201620349974 U CN201620349974 U CN 201620349974U CN 205570028 U CN205570028 U CN 205570028U
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- China
- Prior art keywords
- gas
- water
- steam
- cylinder
- oxygenerator
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- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to an oxygenerator water separator, including barrel, air inlet, heater, gas outlet, comdenstion water entry, condensate outlet, liquid outlet, central pivot, condensate return chamber, turbine blade, spiral aviation baffle, steam -water separation membrane, toper structure, gas flowmeter. It can the by heating ware and the condensate return chamber heat earlier condensation again with gas, improve moisture content liquefaction rate in the gas, through half -circular arc turbine blade, increase gaseous motive force, improve the gas conditioning volume, increase gaseous motive force in the barrel through the spiral aviation baffle, make gaseous cylinder side wall with through comdenstion water adequate cooling fully contact, improve the liquefaction rate, through the steam -water separation membrane of gas outlet and liquid outlet, strengthen the leakproofness of barrel.
Description
Technical field
This utility model belongs to steam-water separation technical field, concrete, relates to a kind of oxygenerator water separator.
Background technology
By in the gas of compressor with moisture content, such compressed gas enters after oxygenerator, can cause molecule
Sieve efflorescence, is substantially reduced molecular sieve surface and amasss, reduce gas percent of pass.Water separator for oxygenerator
It is dependent on the effects such as shock, deceleration, inertia, adhesive force and centrifugal force, makes moisture separate from steam,
Thus reduce steam moisture, it is dried gas, the molecular sieve of protection oxygenerator, extends the service life of oxygenerator.
Water separator of the prior art is primarily present following problem: 1. gas treatment amount is less,
The motive force that gas passes through is less.2. utilize centrifugal force, gas and liquid gravity difference to separate, separate effect
Rate is low.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, it is provided that a kind of increase gas push power, carries
The oxygenerator water separator of moisture content liquefied fraction in high gas.
This utility model solves it and technical problem is that and take techniques below scheme to realize:
A kind of oxygenerator water separator, including cylinder, described cylinder lateral wall top has air inlet, described
Air inlet is provided with heater, and described cylinder lateral wall bottom has gas outlet, and described cylinder shell is double-layer seal
Steel plate, and between double-layer seal steel plate, form condensate return chamber, the outer layer top of described double-layer seal steel plate
Being provided with condensation-water drain, the outer layer bottom of described double-layer seal steel plate is provided with condensing water inlet, described inner barrel
Center vertical is provided with central rotating shaft, and described central rotating shaft one end is fixing with described cylinder top to be connected, described center
Rotating shaft has been fixedly connected sequentially turbo blade and spiral aviation baffle from top to bottom, described cylinder lower taper structure,
The bottom of described pyramidal structure is provided with liquid outlet, is provided with steam-water separation film inside described liquid outlet.
Further, being provided with steam-water separation film inside described gas outlet, the outside of described steam-water separation film is provided with gas
Flowmeter body.
Further, described turbo blade is 4 semicircular arc blades, and angle is 90 degree two-by-two.
Compared with prior art, this utility model produces and provides the benefit that: 1. by heater and condensed water
Gas is first heated and condenses by back cavity, improves moisture content liquefied fraction in gas;2. by semicircular arc turbine leaf
Sheet, increases gas push power, improves gas treatment amount;3. increase gas in cylinder by spiral aviation baffle
Motive force, the cylinder lateral wall making gas sufficiently cool with condensed water is fully contacted, improve liquefied fraction.4. logical
Cross the steam-water separation film of gas outlet and liquid outlet, strengthen the sealing of cylinder.
Accompanying drawing explanation
Below in conjunction with the accompanying drawings this utility model is further illustrated:
Fig. 1 is brief configuration schematic diagram of the present utility model;
Fig. 2 is the top view of turbo blade.
Wherein: 1 cylinder, 2 air inlets, 3 gas outlets, 4 condensation-water drains, 5 condensing water inlets, 6 liquid
Outlet, 7 central rotating shafts, 8 condensate return chambeies, 9 turbo blades, 10 spiral aviation baffles, 11 steam-water separations
Film, 12 pyramidal structures, 13 gas flowmeters.
Detailed description of the invention
Below in conjunction with embodiment, this utility model is described further:
As depicted in figs. 1 and 2, a kind of oxygenerator water separator, including cylinder 1, described cylinder 1 side
Wall top has air inlet 2, and described air inlet 2 is provided with heater 13, and described cylinder 1 lower sidewall has
Gas outlet 3, described cylinder 1 shell is double-layer seal steel plate, and forms condensed water between double-layer seal steel plate
Back cavity 8, the outer layer top of described double-layer seal steel plate is provided with condensation-water drain 4, described double-layer seal steel plate
Outer layer bottom be provided with condensing water inlet 5, described cylinder 1 bosom is vertically provided with central rotating shaft 7, described
Central rotating shaft 7 one end is fixing with described cylinder 1 top to be connected, and described central rotating shaft 7 is fixed the most successively
Connecting and have turbo blade 9 and spiral aviation baffle 10, described cylinder 1 lower taper structure 12, described taper is tied
The bottom of structure 12 is provided with liquid outlet 6, and described liquid outlet 6 is internal is provided with steam-water separation film 11.
In above-mentioned oxygenerator water separator, it should be pointed out that described gas outlet 3 is internal is provided with vapour
Water separation film 11, the outside of described steam-water separation film 11 is provided with gas flowmeter 14.
In above-mentioned oxygenerator water separator, it should be pointed out that described turbo blade 9 is 4 half
Circular arc vane, angle is 90 degree two-by-two.
When compressed gas is by the air inlet 2 of cylinder 1 side wall upper part, after being heated by heater 13, enter cylinder
In body 1, in the pending gas after heating, moisture content fully merges with gas, beneficially later stage condensation process.Center
Rotating shaft 7 drives turbo blade 9 and spiral aviation baffle 10 to rotate successively, and rotation direction is turbo blade 9 semicircle
Arc convex direction, such shape and the direction of motion can reduce fluid resistance, increase fluid throughput.Added
Compressed gas high speed rotating under the drive of turbo blade 9 of heat, and centrifugal downwards along spiral aviation baffle 10
Tilting moves, and the biodiversity carried secretly in compressed gas is more than gas, therefore moisture content movement velocity is less and be detained
Get off, and be fully contacted with cylinder 1 sidewall of condensed water cooling and liquefy.Condensed water is double-deck from cylinder 1
The condensing water inlet 5 of the outer layer bottom sealing steel plate enters condensate return chamber 8, warp after cooling cylinder 1 sidewall
The outer layer top condensation-water drain 4 of cylinder 1 double-layer seal steel plate, the flow direction setting of condensed water can fully ensure that cold
Solidifying effect.Liquefy after the rotated separation of moisture content in compressed gas and condensation process, flow along pyramidal structure 12
To the bottom of cylinder 1, flowing out after liquid outlet 6, the dry gas after being processed is discharged through gas outlet 3,
The gas flowmeter 14 arranged on gas outlet 3 can measure processed compressed gas total amount.Gas outlet 3 and liquid
The steam-water separation film 11 being equipped with in body outlet 6, steam-water separation film 11 can strengthen the sealing of cylinder 1.
This oxygenerator water separator can increase gas push power, strengthens cylinder 1 sealing, improves at gas
Reason amount, improves gas liquid rate.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all
Within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. done, all should wrap
Within being contained in protection domain of the present utility model.
Claims (3)
1. an oxygenerator water separator, including cylinder (1), is characterized in that: on described cylinder (1) sidewall
Portion has air inlet (2), and described air inlet (2) is provided with heater (13), and described cylinder (1) lower sidewall has
Gas outlet (3), described cylinder (1) shell is double-layer seal steel plate, and forms condensation between double-layer seal steel plate
Water back cavity (8), the outer layer top of described double-layer seal steel plate is provided with condensation-water drain (4), described double-layer seal
The outer layer bottom of steel plate is provided with condensing water inlet (5), and described cylinder (1) bosom is vertically provided with central rotating shaft (7),
Described central rotating shaft (7) one end is fixing with described cylinder (1) top to be connected, and described central rotating shaft (7) depends on from top to bottom
Secondary it is fixedly connected with turbo blade (9) and spiral aviation baffle (10), described cylinder (1) lower taper structure (12), institute
The bottom stating pyramidal structure (12) is provided with liquid outlet (6), and described liquid outlet (6) is internal is provided with steam-water separation film
(11)。
Oxygenerator water separator the most according to claim 1, is characterized in that: described gas outlet (3)
Inside is provided with steam-water separation film (11), and the outside of described steam-water separation film (11) is provided with gas flowmeter (14).
Oxygenerator water separator the most according to claim 1, is characterized in that: described turbo blade (9)
Being 4 semicircular arc blades, angle is 90 degree two-by-two.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620349974.5U CN205570028U (en) | 2016-04-21 | 2016-04-21 | Oxygenerator water separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620349974.5U CN205570028U (en) | 2016-04-21 | 2016-04-21 | Oxygenerator water separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205570028U true CN205570028U (en) | 2016-09-14 |
Family
ID=56860288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620349974.5U Expired - Fee Related CN205570028U (en) | 2016-04-21 | 2016-04-21 | Oxygenerator water separator |
Country Status (1)
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CN (1) | CN205570028U (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765290A (en) * | 2016-12-14 | 2017-05-31 | 无锡市金武助剂厂有限公司 | A kind of efficient boiler blower unit |
CN109361003A (en) * | 2018-12-05 | 2019-02-19 | 江苏氢电新能源有限公司 | A kind of fuel cell control hygroscopic water hydrophone |
CN109482473A (en) * | 2018-11-26 | 2019-03-19 | 河北冠润药业股份有限公司 | The dry screening all-in-one machine of pelleted chemical product |
CN110860174A (en) * | 2018-08-27 | 2020-03-06 | 江苏中远环保科技有限公司 | Circulating oil-gas separation method |
CN112174095A (en) * | 2020-11-06 | 2021-01-05 | 中国人民解放军空军军医大学 | Hot blowing dehumidification mechanism of oxygenerator |
CN112360988A (en) * | 2020-11-24 | 2021-02-12 | 成都正升能源技术开发有限公司 | Condensate valve for rapidly recovering oilfield associated gas |
CN114849433A (en) * | 2022-06-16 | 2022-08-05 | 哈尔滨理工大学 | Novel condensation type water-vapor separation device |
-
2016
- 2016-04-21 CN CN201620349974.5U patent/CN205570028U/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106765290A (en) * | 2016-12-14 | 2017-05-31 | 无锡市金武助剂厂有限公司 | A kind of efficient boiler blower unit |
CN110860174A (en) * | 2018-08-27 | 2020-03-06 | 江苏中远环保科技有限公司 | Circulating oil-gas separation method |
CN109482473A (en) * | 2018-11-26 | 2019-03-19 | 河北冠润药业股份有限公司 | The dry screening all-in-one machine of pelleted chemical product |
CN109482473B (en) * | 2018-11-26 | 2024-06-04 | 河北畅瀚生物科技有限公司 | Drying and screening integrated machine for granular chemical products |
CN109361003A (en) * | 2018-12-05 | 2019-02-19 | 江苏氢电新能源有限公司 | A kind of fuel cell control hygroscopic water hydrophone |
CN112174095A (en) * | 2020-11-06 | 2021-01-05 | 中国人民解放军空军军医大学 | Hot blowing dehumidification mechanism of oxygenerator |
CN112174095B (en) * | 2020-11-06 | 2024-05-17 | 中国人民解放军空军军医大学 | Hot blowing dehumidification mechanism of oxygenerator |
CN112360988A (en) * | 2020-11-24 | 2021-02-12 | 成都正升能源技术开发有限公司 | Condensate valve for rapidly recovering oilfield associated gas |
CN112360988B (en) * | 2020-11-24 | 2022-05-17 | 成都正升能源技术开发有限公司 | Condensate valve for rapidly recovering oilfield associated gas |
CN114849433A (en) * | 2022-06-16 | 2022-08-05 | 哈尔滨理工大学 | Novel condensation type water-vapor separation device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160914 Termination date: 20170421 |
|
CF01 | Termination of patent right due to non-payment of annual fee |