CN201182921Y - Gas water separation device of ozonated water - Google Patents

Gas water separation device of ozonated water Download PDF

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Publication number
CN201182921Y
CN201182921Y CNU2008200217032U CN200820021703U CN201182921Y CN 201182921 Y CN201182921 Y CN 201182921Y CN U2008200217032 U CNU2008200217032 U CN U2008200217032U CN 200820021703 U CN200820021703 U CN 200820021703U CN 201182921 Y CN201182921 Y CN 201182921Y
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China
Prior art keywords
gas
water
aeration
bucket
ozone
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Expired - Fee Related
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CNU2008200217032U
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Chinese (zh)
Inventor
徐名勇
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Individual
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Individual
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Priority to CNU2008200217032U priority Critical patent/CN201182921Y/en
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Publication of CN201182921Y publication Critical patent/CN201182921Y/en
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Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a gas-water separating device used for ozone water. The gas-water separating device is provided with an aeration barrel (4), the lower end of the aeration barrel (4) is connected with an aeration barrel cover (6), and an air outlet (1) is arranged at the upper end of the aeration barrel (4). The gas-water separating device is characterized in that a gas-water separating sleeve (5) is arranged in the aeration barrel cover (6), a water inlet (8) and a water outlet (7) are arranged on the aeration barrel cover (6), the water inlet (8) is arranged on the aeration barrel cover (6) in the gas-water separating sleeve (5), the water outlet (7) is arranged on the aeration barrel cover (6) between the gas-water separating sleeve (5) and the aeration barrel (4), a floater barrel (3) is arranged at the upper part of the gas-water separating sleeve (5) in the aeration barrel (4), a sealing gasket (2) corresponding to the air outlet (1) is arranged at the upper end of the floater barrel (3). The gas-water separating device has the advantages of simplicity and practicality, security, reliability, long service life and low cost.

Description

The gas and water separator of Ozone Water
Technical field:
The utility model relates to a kind of gas and water separator, especially a kind of gas and water separator that is used for Ozone Water.
Background technology:
Water-fast ozone gas is arranged in Ozone Water manufacturing process, the ozone gas that exposes from Ozone Water is also arranged, be dispersed in the environment for use space, when ozone gas reaches certain concentration in the environment for use space, can damage the human body respiration organ.(referring to Fig. 1-Fig. 2), the gas and water separator of Ozone Water is fixed on the wall 6a by gas outlet 3a, when fluctuation in stage, float 5a can following water-level lifting for the gas and water separator of existing Ozone Water.When water level descended, float 5a descended, and spring 4a is elongated, and fly rod 1a separates with gas outlet 3a, and gas outlet 3a is opened, and ozone gas that exposes from Ozone Water or not water-soluble ozone gas can flow out from gas outlet 3a, as shown in Figure 1; When water level rose, float 5a was also along with rising, and spring 4a recovers, and fly rod 1a and gas outlet 3a are close to, and gas outlet 3a is closed, and flows out from the 3a of gas outlet to avoid Ozone Water, as shown in Figure 2.This aerator by spring 4a connection float 5a and gas outlet 3a is very strict to the requirement of spring material, and the material of spring requires very strong anti-ozone oxidation performance and very high anti-fatigue performance.Connect that in a single day spring gets rusty or powerful unstable inefficacy will cause the inefficacy of whole aerating system, influence the service life of gas and water separator.
The utility model content:
The purpose of this utility model is to overcome the deficiency of above-mentioned prior art and the low Ozone Water of a kind of safe, reliable, long service life, cost and the separator of ozone gas is provided.
The purpose of this utility model can realize by following measure: the gas and water separator of Ozone Water, it has the aeration bucket, the lower end of aeration bucket connects the aeration bung, the upper end of aeration bucket is provided with venthole, it is characterized in that being provided with in the aeration bung gas-water separation cover, the aeration bung is provided with water inlet, delivery port, water inlet is located on the interior aeration bung of gas-water separation cover, delivery port is located on the aeration bung between gas-water separation cover and the aeration bucket, the top of gas-water separation cover is provided with the float bucket in the aeration bucket, and the upper end of float bucket is provided with and the corresponding sealing gasket of venthole.
In order further to realize the purpose of this utility model, described float bucket is the polygon prism type.
In order further to realize the purpose of this utility model, described float bucket is the pentagonal prism type.
In order further to realize the purpose of this utility model being equipped with reinforcement in the loam cake of described float bucket and the lower cover.
In order further to realize the purpose of this utility model, described reinforcement is made of the annulus of centre and the bar muscle that links to each other with annulus.
In order further to realize the purpose of this utility model, the lower surface of described venthole is a circular arc.
The utility model can produce following good effect compared with the prior art: Ozone Water is carried ozone gas and is flowed into from water inlet 8, can effectively separate not water-soluble ozone gas through gas-water separation cover 5.Ozone gas moves upward, Ozone Water flows out from delivery port 7 after flowing through the top of gas-water separation cover 5, simultaneously because the liquid level rising, float bucket 3 moves upward, and when the sealing gasket 2 that moves to the upper end pushed up venthole 1, gas was sealed, can not discharge (referring to accompanying drawing 3), ozone gas is cumulative more than liquid level, and pressure increases, and presses down water level is descended, buoyancy reduces, when buoyancy during less than the gravity of float bucket 3, float bucket 3 descends with water level, and venthole 1 is opened, ozone gas is discharged (referring to accompanying drawing 4) from venthole 1, liquid level rises, and buoyancy increases, and float bucket 3 rises and seals venthole 1.Through rising, the decline of water level and float bucket 3, ozone gas is sealed, is discharged, and the discharge of gas-water separation and gas is continuously carried out in so repeating motion.The utility model is mainly used in separating of Ozone Water and ozone gas, and its manufactured materials all adopts ozone proof material.Sealing gasket adopts ozone proof fluorosioloxane rubber, and other parts all adopt hard PVC.Mold injection molding, ultrasonic bonding are firmly, reliably.Sealing gasket adopts the bright and clean plane and the R circular arc line of the aperture of giving vent to anger to seal, and has strengthened sealing effectiveness.The gas and water separator that the utility model has overcome existing Ozone Water is to high dependence and because the disadvantage of the aerator inefficacy that the unstability of spring causes of spring 4a (as Fig. 1).
Description of drawings:
Fig. 1 is a kind of user mode structural representation of the gas and water separator of existing Ozone Water;
Fig. 2 is the another kind of user mode structural representation of the gas and water separator of existing Ozone Water;
Fig. 3 is a kind of user mode structural representation of the present utility model;
Fig. 4 is an another kind of user mode structural representation of the present utility model;
Fig. 5 is the A-A profile of Fig. 3.
The specific embodiment:
Below in conjunction with accompanying drawing the specific embodiment of the present utility model is elaborated:
Embodiment: the gas and water separator of Ozone Water is (referring to Fig. 3-Fig. 5), it has aeration bucket 4, the upper end of aeration bucket 4 is provided with venthole 1, the lower surface of venthole 1 is a circular arc, the lower end of aeration bucket 4 connects aeration bung 6, be provided with gas-water separation cover 5 in the aeration bung 6, aeration bung 6 is provided with water inlet 8, delivery port 7, water inlet 8 is located on the aeration bung 6 in the gas-water separation cover 5, delivery port 7 is located on the aeration bung 6 between gas-water separation cover 5 and the aeration bucket 4, and gas-water separation are overlapped 5 top and are provided with float bucket 3 in the aeration bucket 4, and float bucket 3 is the polygon prism type, present embodiment float bucket 3 is the pentagonal prism type, cover on the float bucket 3 and be provided with sealing gasket 2, the position of sealing gasket 2 is corresponding with venthole 1, and five ribs of float bucket 3 are as guiding rib, so both alleviate weight, reached the effect of guiding and increasing gas flow space again.Be equipped with reinforcement 9 in the loam cake of float bucket 3 and the lower cover, reinforcement 9 is made of the annulus of centre and the bar muscle that links to each other with annulus, and float bucket 3 has been played the effect of reinforcing.
During use, Ozone Water is carried not water-soluble ozone gas and is entered aeration bucket 4 from water inlet 8, when overlapping 5 through gas-water separation, Ozone Water is effectively separated with ozone gas, and ozone gas moves upward, Ozone Water flows out from delivery port 7 after flowing through the top of gas-water separation cover 5, simultaneously because liquid level rises, and pentagonal prism float bucket 3 moves upward, when the sealing gasket 2 that moves to the upper end pushes up venthole 1, gas is sealed, can not discharge (referring to accompanying drawing 3), ozone gas is cumulative more than liquid level, when ozone gas is accumulated to a certain degree, pressure increases, press down water level is descended, buoyancy reduces, when buoyancy during less than the gravity of pentagonal prism float bucket 3, float bucket 3 descends with water level, venthole 1 is opened, and ozone gas is discharged (referring to accompanying drawing 4) from venthole, and liquid level rises, buoyancy increases, and float bucket 3 rises and seals venthole 1.Through rising, the decline of water level and float bucket 3, ozone gas is sealed, is discharged, and the discharge of gas-water separation and gas is continuously carried out in so repeating motion.

Claims (6)

1, the gas and water separator of Ozone Water, it has aeration bucket (4), the lower end of aeration bucket (4) connects aeration bung (6), the upper end of aeration bucket (4) is provided with venthole (1), it is characterized in that being provided with in the aeration bung (6) gas-water separation cover (5), aeration bung (6) is provided with water inlet (8), delivery port (7), water inlet (8) is located on the interior aeration bung (6) of gas-water separation cover (5), delivery port (7) is located on the aeration bung (6) between gas-water separation cover (5) and the aeration bucket (4), the top of the interior gas-water separation cover of aeration bucket (4) (5) is provided with float bucket (3), and the upper end of float bucket (3) is provided with and the corresponding sealing gasket of venthole (1) (2).
2, the gas and water separator of Ozone Water according to claim 1 is characterized in that described float bucket (3) is the polygon prism type.
3, the gas and water separator of Ozone Water according to claim 2 is characterized in that described float bucket (3) is the pentagonal prism type.
4,, it is characterized in that being equipped with reinforcement (9) in the loam cake of described float bucket (3) and the lower cover according to the gas and water separator of claim 1 or 2 or 3 described Ozone Water.
5, the gas and water separator of Ozone Water according to claim 4 is characterized in that described reinforcement (9) is made of the annulus of centre and the bar muscle that links to each other with annulus.
6, the gas and water separator of Ozone Water according to claim 1, the lower surface that it is characterized in that described venthole (1) is a circular arc.
CNU2008200217032U 2008-04-28 2008-04-28 Gas water separation device of ozonated water Expired - Fee Related CN201182921Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008200217032U CN201182921Y (en) 2008-04-28 2008-04-28 Gas water separation device of ozonated water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008200217032U CN201182921Y (en) 2008-04-28 2008-04-28 Gas water separation device of ozonated water

Publications (1)

Publication Number Publication Date
CN201182921Y true CN201182921Y (en) 2009-01-21

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008200217032U Expired - Fee Related CN201182921Y (en) 2008-04-28 2008-04-28 Gas water separation device of ozonated water

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102458667A (en) * 2009-04-06 2012-05-16 伊安·格雷 Gas-liquid-solid separator
CN102560525A (en) * 2011-04-12 2012-07-11 周美荣 Electrolytic ozone generating device for recycling cathode water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102458667A (en) * 2009-04-06 2012-05-16 伊安·格雷 Gas-liquid-solid separator
CN102560525A (en) * 2011-04-12 2012-07-11 周美荣 Electrolytic ozone generating device for recycling cathode water

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Baxter Environmental Technology (Yantai) Co., Ltd.

Assignor: Xu Mingyong

Contract record no.: 2012990000037

Denomination of utility model: Gas-water separation device of ozone water

Granted publication date: 20090121

License type: Common License

Record date: 20120130

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090121

Termination date: 20160428