CN201461336U - Gas-water separator of cyclone-type air compressor - Google Patents

Gas-water separator of cyclone-type air compressor Download PDF

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Publication number
CN201461336U
CN201461336U CN2009200749452U CN200920074945U CN201461336U CN 201461336 U CN201461336 U CN 201461336U CN 2009200749452 U CN2009200749452 U CN 2009200749452U CN 200920074945 U CN200920074945 U CN 200920074945U CN 201461336 U CN201461336 U CN 201461336U
Authority
CN
China
Prior art keywords
valve body
valve
guide rod
thread
whirlwind
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.)
Expired - Fee Related
Application number
CN2009200749452U
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Chinese (zh)
Inventor
王桂荣
陈鹏高
陈奕良
周芳
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.)
Shanghai Screw Compressor Co Ltd
Original Assignee
Shanghai Screw Compressor 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 Shanghai Screw Compressor Co Ltd filed Critical Shanghai Screw Compressor Co Ltd
Priority to CN2009200749452U priority Critical patent/CN201461336U/en
Application granted granted Critical
Publication of CN201461336U publication Critical patent/CN201461336U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a gas-water separator of a cyclone-type air compressor, comprising an air inlet, an air outlet, a valve lid and a valve body. The air inlet and the air outlet are respectively arranged at the upper side of the gas-water separator; the valve lid and the valve body are connected by a bolt; a cyclone cylinder in the valve body adopts a reverse-horn shape and is spinned in the middle of the valve lid by a thread; a cyclone impeller comprises 8 blades forming 45 degrees with the horizontal direction, is provided with a hollow internal thread in the middle and is mounted on the external thread at the mid-upper part of the cyclone cylinder 8 by the internal thread; a knock plate is arranged in a position at the inner side of the valve lid opposite to the inlet and cast on the valve lid; an airflow passage is formed between the knock plate and the valve lid; a drain guide rod is spinned at the lower part of the valve body by a thread; a floating ball and a compression spring are sleeved on the drain guide rod which is sealed with the floating ball by an O-shaped ring; a manual relief ball valve is mounted at the downmost part of the valve body; and a draining joint is arranged at the right lower center of the valve body and connected with a drain guide pipe. The utility model improves the use efficiency of post-treatment equipment downstream against a pipeline.

Description

The moisture trap of vortex type air compressor
Technical field
The utility model relates to a kind of moisture trap of vortex type air compressor, relates in particular to the moisture trap in a kind of vortex type air compressor.
Background technique
The gas that air compressor is discharged is the saturated pressurized air that contains a large amount of water vapour, the moisture trap that uses in the compressor industry exists pressure loss big at present, separation effect is low, particularly can not effectively separate the impurity such as iron filings in the compressor air, and have a strong impact on the utilization efficiency of the equipment for after-treatment in pipeline downstream.
Summary of the invention
The utility model technical issues that need to address have provided a kind of moisture trap of vortex type air compressor, are intended to solve the above problems.
In order to solve the problems of the technologies described above, the utility model is achieved through the following technical solutions:
The utility model comprises: the top is respectively equipped with suction port and relief opening, and valve gap is connected by bolt with valve body; Whirlwind tube in the valve body adopts the shape of falling the horn mouth, and the whirlwind tube passes through the screw thread spinning at the valve gap middle part; The whirlwind impeller is made up of eight from the horizontal by 45 ° blade, is the internal thread of hollow in the middle of it, and the whirlwind impeller is installed on the outside thread of whirlwind tube 8 middle and upper parts by internal thread; Position in the face of import in the valve gap is provided with crash panel, and crash panel is cast on the valve gap, forms air-flow path at crash panel and valve cover chamber; Draining guide rod through threaded spinning is in valve body lower portion, and ball float and pressure spring are enclosed within on the draining guide rod, and ball float and draining guide rod are by the sealing of O type circle; Valve body below the ball valve of manually releasing is housed; The following centre of valve body is furnished with the blowdown interface, and interface connects a drainage duct.
Compared with prior art, the beneficial effects of the utility model are: pressure loss is little in the working procedure, separation effect height (can reach 99.9%) can effectively separate oil, moisture content and impurity in the compressor air, improves the utilization efficiency of the equipment for after-treatment in pipeline downstream.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail:
As seen from Figure 1: the utility model comprises: the top is respectively equipped with suction port A and relief opening B, and valve gap 1 is connected by bolt 2 with valve body 4; Whirlwind tube 8 in the valve body 4 adopts the shape of falling the horn mouth, and whirlwind tube 8 passes through the screw thread spinning at valve gap 1 middle part; Whirlwind impeller 7 is made up of eight from the horizontal by 45 ° blade, is the internal thread of hollow in the middle of it, and whirlwind impeller 7 is installed on the outside thread of whirlwind tube 8 middle and upper parts by internal thread; Position in the face of import in the valve gap 1 is provided with crash panel 3, and crash panel 3 is cast on the valve gap 1, forms air-flow path at crash panel 3 and 1 of valve gap; In valve body 4 bottoms, ball float 9 and pressure spring 10 are enclosed within on the draining guide rod 11 draining guide rod 11 by the screw thread spinning, and ball float 9 and draining guide rod 11 are by 12 sealings of O type circle; Guarantee that inner air water can not leak, the water level around ball float 9 reaches certain position, and buoyancy of water holds up ball float 9, and water after the separation and impurity can emit by draining guide rod 11; Valve body 4 below the ball valve 5 of manually releasing is housed; Supply the user to debug and use or manual blowdown usefulness, the following centre of valve body 4 is furnished with blowdown interface 13, and interface connects a drainage duct 14; Sewage and impurity are discharged in the container or zone of appointment;
A spare interface 6 also is set on valve gap 1.
All constitutional details of the utility model all adopt anticorrosion pressure-resistant material, and this device has scientific and reasonable for structure, and is easy to operate, durable, characteristics such as separating power strong, draining reliability height, nothing leakage, volume is little, cost is low and need not maintain.
The utility model is applied to often be placed in the front of compressor gas supplied pipe rear end or aftercooler in the after-treatment system of compressor and compressed air line.This moisture trap can be separated the oil in the pressurized air, moisture content and impurity from pressurized air, be the important mechanism of Bihend Processing Equipment of Compressed Air.
The utility model adopts six grades of separation methods-collision cohesion, break-in, whirlwind is centrifugal, gravity, reduction of speed, principles such as secondary collision, have the water separation that is mingled in the pressurized air is become liquid, have oil, moisture content and impurity are separated from pressurized air, and discharge automatically and guarantee the dead-tight effect of gas by self releasing system, remove liquid water smoke and impurity in the pressurized air effectively, the pressure loss of almost can ignoring, automatic pollution discharge is pressurized air high efficiency particulate air filter and freezing-type, the requisite pre-treater element of absorption compressed air dryer.
As shown in Figure 1: the pressurized air flow process is as follows: suction port → crash panel 3 → whirlwind impeller 7 → whirlwind tube 8 → air outlet;
The separated flow journey is as follows in the pressurized air: suction port → crash panel 3 → whirlwind impeller 7 → whirlwind tube 8 → valve body (inwall) 4 → ball float 9 → drainage duct 14.
Working principle of the present utility model is: when containing big gauging, after the pressurized air of steam and solid impurity enters moisture trap, pressurized gas at first impinges upon on the valve gap 1 inner impact plate 3, moisture major part in the gas is condensed into big water particle, fast then flow speed and direction cyclone leaf wheel 7, whirlwind impeller 7 is made up of eight from the horizontal by 45 ° blade, whirlwind impeller 7 changes the compressed-air actuated flow direction, guarantee that pressurized air is round 8 sedimentations while rotating of whirlwind tube, through cyclonic separation, make the further particle chap of airborne moisture, and increase gradually and become drop, gas in eddy flow is because the factors such as acting in conjunction of centrifugal force and gravity force particle water to adhere to valve body 4 inwalls flows down.Solid impurity in the gas in addition, density is bigger, also because the whirlwind action of centrifugal force, is pasting the inwall of valve body 4, along with the current after separating are washed into below the valve body 4, forms sewage with water after separating, is deposited to together bottom the moisture trap.
Gas after cyclonic separation arrives whirlwind tube 8 belows, because whirlwind tube 8 horn mouths are bigger, form bigger area of space between the horn mouth of whirlwind tube and the ball float 9, the pressurized air flow velocity is lower, pressurized gas rotates while colliding along whirlwind tube 8 inwalls simultaneously, water behind the pressurized air flow velocity secondary collision flows down along whirlwind tube 8 inwalls, when the water level of ball float 9 peripheries reaches certain water level, water overcomes the elastic force of ball float 9 internal compression springs 10 to the buoyancy of ball float 9, ball float 9 rises because of buoyancy, and sewage can flow out from the aperture of draining guide rod 11.Be discharged to the zone of appointment again by drainage duct 14.
When the valve body 4 inner water yields were less, because the elastic force of spring 10 and the pressure of internal compressed gas, the O type circle 12 of ball float 9 belows and the lower plane of valve body 4 formed sealing, ball float 9 is closed inner chamber, thereby weep hole closes, and inner and extraneous partition of moisture trap, guarantees that gas can not revealed.And in valve body 4, preserve a certain amount of water, and allow valve body 4 interior gases and atmosphere intercept, play the water seal effect, so this moisture trap sealability is higher.
The effect of ball valve 5 of manually releasing is no matter valve body 4 inside have or not pressure, or the water yield what, can sewage and impurity in the valve body 4 be emitted by manually releasing ball valve 5.
Whole process is finished six steps such as collision cohesion, break-in, whirlwind are centrifugal, gravity, reduction of speed, secondary collision.
Though more than described embodiment of the present utility model; but those skilled in the art is to be understood that; these only are to prove for example; under the prerequisite that does not deviate from principle of the present utility model and essence; can make numerous variations or modification to these mode of executions; therefore, protection domain of the present utility model is limited by appended claims.

Claims (2)

1. the moisture trap of a vortex type air compressor, comprising: the top is respectively equipped with suction port and relief opening, and valve gap is connected by bolt with valve body; It is characterized in that: the whirlwind tube in the valve body adopts the shape of falling the horn mouth, and the whirlwind tube passes through the screw thread spinning at the valve gap middle part; The whirlwind impeller is made up of eight from the horizontal by 45 ° blade, is the internal thread of hollow in the middle of it, and the whirlwind impeller is installed on the outside thread of whirlwind tube (8) middle and upper part by internal thread; Position in the face of import in the valve gap is provided with crash panel, and crash panel is cast on the valve gap, forms air-flow path at crash panel and valve cover chamber; Draining guide rod through threaded spinning is in valve body lower portion, and ball float and pressure spring are enclosed within on the draining guide rod, and ball float and draining guide rod are by the sealing of O type circle; Valve body below the ball valve of manually releasing is housed; The following centre of valve body is furnished with the blowdown interface, and interface connects a drainage duct.
2. the moisture trap of vortex type air compressor according to claim 1 is characterized in that: a spare interface also is set on valve gap.
CN2009200749452U 2009-07-21 2009-07-21 Gas-water separator of cyclone-type air compressor Expired - Fee Related CN201461336U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009200749452U CN201461336U (en) 2009-07-21 2009-07-21 Gas-water separator of cyclone-type air compressor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009200749452U CN201461336U (en) 2009-07-21 2009-07-21 Gas-water separator of cyclone-type air compressor

Publications (1)

Publication Number Publication Date
CN201461336U true CN201461336U (en) 2010-05-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009200749452U Expired - Fee Related CN201461336U (en) 2009-07-21 2009-07-21 Gas-water separator of cyclone-type air compressor

Country Status (1)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101961581A (en) * 2010-10-19 2011-02-02 张晓荣 Gas-water separator capable of discharging water automatically
WO2020061096A1 (en) * 2018-09-19 2020-03-26 Haven Technology Solutions Llc Method and device for separating a lighter density fluid from a heavier density fluid

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101961581A (en) * 2010-10-19 2011-02-02 张晓荣 Gas-water separator capable of discharging water automatically
WO2020061096A1 (en) * 2018-09-19 2020-03-26 Haven Technology Solutions Llc Method and device for separating a lighter density fluid from a heavier density fluid
CN113015569A (en) * 2018-09-19 2021-06-22 哈文技术解决方案有限公司 Method and apparatus for separating a lower density fluid from a higher density fluid
US11351479B2 (en) 2018-09-19 2022-06-07 Haven Technology Solutions Llc Method and device for separating a lighter density fluid from a heavier density fluid

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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: 20100512

Termination date: 20140721

EXPY Termination of patent right or utility model