CN106377950A - Gas-liquid separator - Google Patents

Gas-liquid separator Download PDF

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Publication number
CN106377950A
CN106377950A CN201611107220.XA CN201611107220A CN106377950A CN 106377950 A CN106377950 A CN 106377950A CN 201611107220 A CN201611107220 A CN 201611107220A CN 106377950 A CN106377950 A CN 106377950A
Authority
CN
China
Prior art keywords
gas
liquid separation
spinning disk
liquid
liquid separator
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.)
Pending
Application number
CN201611107220.XA
Other languages
Chinese (zh)
Inventor
宋大伟
薛少威
许峙彬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuxi Younaite Purification Equipment Co Ltd
Original Assignee
Wuxi Younaite Purification Equipment Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Wuxi Younaite Purification Equipment Co Ltd filed Critical Wuxi Younaite Purification Equipment Co Ltd
Priority to CN201611107220.XA priority Critical patent/CN106377950A/en
Publication of CN106377950A publication Critical patent/CN106377950A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/16Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Centrifugal Separators (AREA)

Abstract

The invention relates to a gas-liquid separator which comprises a gas-liquid separation shell and is characterized in that a gas inlet and a gas outlet are formed in the upper part of the gas-liquid separation shell; a sewage outfall is formed in the bottom of the gas-liquid separation shell; the gas outlet communicates with a gas outlet pipeline in the gas-liquid separation shell; the gas outlet pipeline extends to the lower part of the gas-liquid separation shell; the upper part of an inner cavity of the gas-liquid separation shell is provided with a first swirl sheet and a second swirl sheet sequentially; a certain distance exists between the first swirl sheet and the second swirl sheet; the second swirl sheet is arranged below the first swirl sheet; the diameter of the second swirl sheet is smaller than that of the first swirl sheet; the diameter of the first swirl sheet is consistent to the inside diameter of the gas-liquid separation shell; the gas-liquid separation shell comprises a barrel body; and an upper sealing heat and a lower sealing heat are arranged at the upper and lower parts of the barrel body respectively. According to the gas-liquid separator, the structure of the traditional centrifugal type gas-liquid separator is optimized and treated, and the efficiency of gas-liquid separation is improved.

Description

Gas-liquid separator
Technical field
The present invention relates to a kind of gas-liquid separator, especially a kind of gas for gases such as compressed air, natural gas, nitrogen Liquid/gas separator.
Background technology
The gateway that gas-liquid separator is typically mounted at gas compressor is used for gas-liquid separation, also apply be applicable to gas and removes Multiple industry such as dirt, oil-water separation and liquid removal impurity and civil applications occasion.The isolating construction that gas-liquid separator adopts is very Many, such as:1st, gravity sedimentation type isolating construction;2nd, baffle separation;3rd, centrifugal force separate;4th, silk screen separates;5th, ultra-filtration and separation;6th, fill out Material separation etc..Wherein, centrifugal gas-liquid separator is the separation realizing between gas phase and liquid phase according to centrifugation principle, has knot Structure is simple, energy consumption is low, light weight, application is the advantages of facilitate.Theoretical and experimentation shows, improves centrifugal gas-liquid separator Structure has important effect to improving its performance.
Content of the invention
The purpose of the present invention is to overcome the deficiencies in the prior art, provides a kind of gas-liquid separator, to existing from The structure of core type gas-liquid separator is optimized process, improves the efficiency of gas-liquid separation.
The technical scheme providing according to the present invention, described gas-liquid separator, including gas-liquid separation housing, it is characterized in that:? The top setting air inlet of described gas-liquid separation housing and gas outlet, arrange sewage draining exit in the bottom of gas-liquid separation housing, give vent to anger Mouth is connected with the outlet pipe being arranged in gas-liquid separation housing, and outlet pipe extends to the bottom of gas-liquid separation housing;Institute The top stating gas-liquid separation housing cavity sets gradually the first spinning disk and the second spinning disk, the first spinning disk and the second spinning disk Between deposit a determining deviation, the second spinning disk is located at the lower section of the first spinning disk, and the diameter of the second spinning disk is less than the first spinning disk Diameter, the diameter of the first spinning disk is consistent with the internal diameter of gas-liquid separation housing.
Further, described gas-liquid separation housing includes cylinder, and the top and the bottom of cylinder are respectively provided with upper cover and low head.
Further, baffle plate is set in the bottom of described gas-liquid separation housing cavity, the upper surface of baffle plate is to raise up Cambered surface.
Further, the intracavity sidewall in described gas-liquid separation housing is provided with drainage strip.
Further, described sewage outfalls setting is on low head.
Further, described outlet pipe is passed through by the center of the first spinning disk and the second spinning disk.
Gas-liquid separator of the present invention, by being optimized place to the structure of existing centrifugal gas-liquid separator Reason, improves the efficiency of gas-liquid separation.
Brief description
Fig. 1 is the structural representation of gas-liquid separator of the present invention.
Specific embodiment
With reference to concrete accompanying drawing, the invention will be further described.
As shown in Figure 1:Described gas-liquid separator includes sewage draining exit 1, low head 2, drainage strip 3, baffle plate 4, cylinder 5, gives vent to anger Pipeline 6, the first spinning disk 7, air inlet 8, gas outlet 9, upper cover 10, second spinning disk 11 etc..
As shown in figure 1, gas-liquid separator of the present invention, including cylinder 5, the top and the bottom of cylinder 5 are respectively provided with upper cover 10 and low head 2, form airtight gas-liquid separation housing;Air inlet 8 is set on the top of described gas-liquid separation housing and gives vent to anger Mouth 9, gas outlet 9 is connected with the outlet pipe 6 being arranged in gas-liquid separation housing, and outlet pipe 6 extends to gas-liquid separation housing Bottom;Set gradually the first spinning disk 7 and the second spinning disk 11, the first eddy flow on the top of described gas-liquid separation housing cavity A determining deviation is deposited, the second spinning disk 11 is located at the lower section of the first spinning disk 7, the second spinning disk between piece 7 and the second spinning disk 11 11 diameter is less than the diameter of the first spinning disk 7, and the diameter of the first spinning disk 7 is consistent with the internal diameter of gas-liquid separation housing;Described First spinning disk 7 and the second spinning disk 11 are the core components of gas-liquid separator, and the present invention passes through the eddy flow of two different-diameters The setting of piece, can play the effect improving separation efficiency.
Baffle plate 4 is set in the bottom of described gas-liquid separation housing cavity, the upper surface of baffle plate 4 is the cambered surface raising up, Collect to flow to by baffle plate 4 in order to liquid and conflux after surrounding in the bottom of gas-liquid separation housing.
The intracavity sidewall of described gas-liquid separation housing is provided with drainage strip 3, drainage strip 3 can help in centrifugal action Under throw to the liquid of side wall and guide downwards.
Sewage draining exit 1 is arranged on described low head 2, for emptying the liquid collecting in gas-liquid separation housing bottom.
In addition, described outlet pipe 6 is passed through by the center of the first spinning disk 7 and the second spinning disk 11.
The operation principle of the present invention is:The gas containing liquid in a large number flows into from air inlet 8, passes sequentially through the first spinning disk 7 He Second spinning disk 11 forms spiral flow, drips liquid under the influence of centrifugal force and throws to barrel, makes gas-liquid separation, subsequent liquid quilt Baffle plate 4 collects in bottom, discharges from sewage draining exit 1, and the gas of dried and clean flows into pipe network from gas outlet 9.The present invention processes flow Greatly, separation efficiency is high, high pressure resistant, convenient for installation and maintenance.

Claims (6)

1. a kind of gas-liquid separator, including gas-liquid separation housing, is characterized in that:The top of described gas-liquid separation housing arrange into QI KOU(8)And gas outlet(9), in the bottom of gas-liquid separation housing, sewage draining exit is set(1), gas outlet(9)Divide with being arranged on gas-liquid Outlet pipe in shrinking away from theshell body(6)Connection, outlet pipe(6)Extend to the bottom of gas-liquid separation housing;In described gas-liquid separation The top of housing cavity sets gradually the first spinning disk(7)With the second spinning disk(11), the first spinning disk(7)With the second spinning disk (11)Between deposit a determining deviation, the second spinning disk(11)Positioned at the first spinning disk(7)Lower section, the second spinning disk(11)Diameter Less than the first spinning disk(7)Diameter, the first spinning disk(7)Diameter consistent with the internal diameter of gas-liquid separation housing.
2. gas-liquid separator as claimed in claim 1, is characterized in that:Described gas-liquid separation housing includes cylinder(5), cylinder (5)Top and the bottom be respectively provided with upper cover(10)And low head(2).
3. gas-liquid separator as claimed in claim 1, is characterized in that:In the bottom of described gas-liquid separation housing cavity, gear is set Plate(4), baffle plate(4)Upper surface be the cambered surface raising up.
4. gas-liquid separator as claimed in claim 1, is characterized in that:It is provided with the intracavity sidewall of described gas-liquid separation housing Drainage strip(3).
5. gas-liquid separator as claimed in claim 2, is characterized in that:Described sewage draining exit(1)It is arranged on low head(2)On.
6. gas-liquid separator as claimed in claim 1, is characterized in that:Described outlet pipe(6)By the first spinning disk(7)With Two spinning disks(11)Center pass through.
CN201611107220.XA 2016-12-06 2016-12-06 Gas-liquid separator Pending CN106377950A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611107220.XA CN106377950A (en) 2016-12-06 2016-12-06 Gas-liquid separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611107220.XA CN106377950A (en) 2016-12-06 2016-12-06 Gas-liquid separator

Publications (1)

Publication Number Publication Date
CN106377950A true CN106377950A (en) 2017-02-08

Family

ID=57959415

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611107220.XA Pending CN106377950A (en) 2016-12-06 2016-12-06 Gas-liquid separator

Country Status (1)

Country Link
CN (1) CN106377950A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107469472A (en) * 2017-09-13 2017-12-15 江苏新凯晟机械设备有限公司 Gas-liquid separator
CN113144759A (en) * 2021-06-11 2021-07-23 重庆宗申通用动力机械有限公司 Air filtering device
CN113440988A (en) * 2021-07-22 2021-09-28 中汽创智科技有限公司 Gas-water separator

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3707068A (en) * 1970-02-25 1972-12-26 Worthington Corp Multistage liquid and gas separator
CN1876612A (en) * 2005-06-07 2006-12-13 浙江工业大学 Three methods combined highly effective methanol separator
CN1883763A (en) * 2006-05-20 2006-12-27 浙江诸暨九牛农牧机械有限公司 Vapour-water separator
CN202778101U (en) * 2012-06-20 2013-03-13 江阴宇博科技有限公司 Gas-liquid separator
CN103055612A (en) * 2013-01-30 2013-04-24 吴棕雁 Multi-stage vortex type gas-water separator
CN204911023U (en) * 2015-06-10 2015-12-30 青岛京润石化工程有限公司 Gaseous liquid knockout of multistage whirl
CN205598774U (en) * 2016-04-13 2016-09-28 卢秀清 High -efficient multicell whirl defroster
CN206229075U (en) * 2016-12-06 2017-06-09 无锡优耐特净化装备有限公司 Gas-liquid separator

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3707068A (en) * 1970-02-25 1972-12-26 Worthington Corp Multistage liquid and gas separator
CN1876612A (en) * 2005-06-07 2006-12-13 浙江工业大学 Three methods combined highly effective methanol separator
CN1883763A (en) * 2006-05-20 2006-12-27 浙江诸暨九牛农牧机械有限公司 Vapour-water separator
CN202778101U (en) * 2012-06-20 2013-03-13 江阴宇博科技有限公司 Gas-liquid separator
CN103055612A (en) * 2013-01-30 2013-04-24 吴棕雁 Multi-stage vortex type gas-water separator
CN204911023U (en) * 2015-06-10 2015-12-30 青岛京润石化工程有限公司 Gaseous liquid knockout of multistage whirl
CN205598774U (en) * 2016-04-13 2016-09-28 卢秀清 High -efficient multicell whirl defroster
CN206229075U (en) * 2016-12-06 2017-06-09 无锡优耐特净化装备有限公司 Gas-liquid separator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107469472A (en) * 2017-09-13 2017-12-15 江苏新凯晟机械设备有限公司 Gas-liquid separator
CN113144759A (en) * 2021-06-11 2021-07-23 重庆宗申通用动力机械有限公司 Air filtering device
CN113440988A (en) * 2021-07-22 2021-09-28 中汽创智科技有限公司 Gas-water separator

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Application publication date: 20170208