CN203803316U - Three-stage gas-water separation device for compressed air - Google Patents

Three-stage gas-water separation device for compressed air Download PDF

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Publication number
CN203803316U
CN203803316U CN201420224552.6U CN201420224552U CN203803316U CN 203803316 U CN203803316 U CN 203803316U CN 201420224552 U CN201420224552 U CN 201420224552U CN 203803316 U CN203803316 U CN 203803316U
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CN
China
Prior art keywords
compressed air
water
separator
dividing plate
meticulous
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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
Application number
CN201420224552.6U
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Chinese (zh)
Inventor
何蓉
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Individual
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Individual
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Priority to CN201420224552.6U priority Critical patent/CN203803316U/en
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Publication of CN203803316U publication Critical patent/CN203803316U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separating Particles In Gases By Inertia (AREA)
  • Cyclones (AREA)

Abstract

The utility model provides a three-stage gas-water separation device for compressed air, which comprises a primary cyclone separator, wherein a secondary fine baffle separator is arranged on the upper part of the primary cyclone separator; a fine filtering and water catching net is arranged on the upper part of the secondary fine baffle separator. By adoption of the three-stage gas-water separation device, the compressed air rotates at a high speed at a cyclone separation section, passes through a barycenter separation section, and then is finely separated in a fine baffle separation section, so that dried compressed air is obtained. Due to the cyclone effect, a gas molecule is enlarged to release a water molecule, when high-density water molecules, oil molecules and dust particles are thrown out of the secondary fine baffle separator under the action of centrifugal force, the water molecules, the oil molecules and the dust particles can be intercepted through multiple layers of baffles in the secondary fine baffle separator, the working pressure of the fine filtering and water catching net is lightened, the service life is prolonged, meanwhile, high-efficiency operation is kept, the phenomena that oil corrodes pipe walls and other parts can be reduced, so that the condition is good for users.

Description

Three grades of gas and water separators of a kind of compressed air
Technical field
The utility model relates to compressed air processing technology field, is specifically related to three grades of gas and water separators of a kind of compressed air.
Background technology
Cooling driers separator in the market mainly contains following three kinds, one, cyclone type moisture trap, two, iris type moisture trap, three, filtering type moisture trap, conventionally there is following shortcoming: first, interception dividing plate is not set in filter separator passage or only arranges and tackle together dividing plate, so virtually increase the operating pressure of filter separator, be easy to allow filter separator saturated, when filter separator enters after saturation state, its aqueous vapor separating effect can reduce greatly, having the compressed air of part moisture content and greasy dirt takes out of, equipment is easy to be corroded.
Summary of the invention
For the deficiencies in the prior art, the purpose of this utility model is to provide three grades of gas and water separators of a kind of compressed air, and it has solved these above-mentioned problems.
The technical scheme that the utility model adopts is as follows: three grades of gas and water separators of a kind of compressed air, comprise primary cyclone, described primary cyclone top is provided with the meticulous dividing plate separator of secondary, and the meticulous dividing plate separator of described secondary top is provided with fine filtering and catches the network of rivers.
Preferably, the meticulous dividing plate separator of described secondary is sandwich construction.
Preferably, the meticulous dividing plate separator of described secondary is layer 2-4 structure, and every layer of front end is all provided with folding part, and described folding part is 30-70 ° with respect to horizontal line and folds.
Preferably, the channel diameter of the meticulous dividing plate separator of described secondary is less than the coverage rate diameter of primary cyclone.
The beneficial effects of the utility model comprise:
The utility model adopts tertiary effluent gas separating device, the present cyclonic separation section of compressed air is rotated rapidly, pass through again center of gravity segregation section, and then enter after the meticulous separation of meticulous dividing plate segregation section, obtain dry compressed air, owing to revolving wind action, gas molecule is extended and discharge hydrone, when the large hydrone of density, oil molecule and dust particulate get rid of to the meticulous dividing plate separator of secondary under the effect of centrifugal force, several layers of dividing plate in the meticulous dividing plate separator of secondary can be by hydrone, under oil molecule and the interception of dust particulate, alleviate fine filtering and catch the operating pressure in the network of rivers, when extending its life-span, keep efficient operation, reduce the moisture in compressed air simultaneously, the parts such as oil corrosion tube wall, be conducive to user.
Brief description of the drawings
Fig. 1 is the structural representation of three grades of gas and water separators of a kind of compressed air of the utility model.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the utility model is elaborated.
Three grades of gas and water separators of a kind of compressed air, as shown in Figure 1, comprise primary cyclone 1, and described primary cyclone 1 top is provided with the meticulous dividing plate separator 2 of secondary, and the meticulous dividing plate separator of described secondary 2 tops are provided with fine filtering and catch the network of rivers 3.
The meticulous dividing plate separator 2 of described secondary is sandwich construction.
The meticulous dividing plate separator 2 of described secondary is layer 2-4 structure, and every layer of front end is all provided with folding part 4, and described folding part 4 is 30-70 ° with respect to horizontal line and folds.
The channel diameter of the meticulous dividing plate separator 2 of described secondary is less than the coverage rate diameter of primary cyclone 1.
Above-mentioned embodiment is preferred embodiment of the present utility model; be not for limiting enforcement of the present utility model and interest field; all equivalences of making according to the content described in the utility model patent protection scope change and modify, and all should be included in the utility model claim.

Claims (4)

1. three grades of gas and water separators of compressed air, is characterized in that, comprise primary cyclone, and described primary cyclone top is provided with the meticulous dividing plate separator of secondary, and the meticulous dividing plate separator of described secondary top is provided with fine filtering and catches the network of rivers.
2. three grades of gas and water separators of a kind of compressed air according to claim 1, is characterized in that, the meticulous dividing plate separator of described secondary is sandwich construction.
3. three grades of gas and water separators of a kind of compressed air according to claim 1 and 2, is characterized in that, the meticulous dividing plate separator of described secondary is layer 2-4 structure, and every layer of front end is all provided with folding part, and described folding part is 30-70 ° with respect to horizontal line and folds.
4. three grades of gas and water separators of a kind of compressed air according to claim 1, is characterized in that, the channel diameter of the meticulous dividing plate separator of described secondary is less than the coverage rate diameter of primary cyclone.
CN201420224552.6U 2014-05-04 2014-05-04 Three-stage gas-water separation device for compressed air Expired - Fee Related CN203803316U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420224552.6U CN203803316U (en) 2014-05-04 2014-05-04 Three-stage gas-water separation device for compressed air

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420224552.6U CN203803316U (en) 2014-05-04 2014-05-04 Three-stage gas-water separation device for compressed air

Publications (1)

Publication Number Publication Date
CN203803316U true CN203803316U (en) 2014-09-03

Family

ID=51442128

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420224552.6U Expired - Fee Related CN203803316U (en) 2014-05-04 2014-05-04 Three-stage gas-water separation device for compressed air

Country Status (1)

Country Link
CN (1) CN203803316U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI825529B (en) * 2021-03-11 2023-12-11 日商日本空氣乾燥器銷售股份有限公司 Condensation device for compressed air

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI825529B (en) * 2021-03-11 2023-12-11 日商日本空氣乾燥器銷售股份有限公司 Condensation device for compressed air

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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: 20140903

Termination date: 20150504

EXPY Termination of patent right or utility model