CN107670338A - A kind of outer-flowing type air separator - Google Patents
A kind of outer-flowing type air separator Download PDFInfo
- Publication number
- CN107670338A CN107670338A CN201710856140.2A CN201710856140A CN107670338A CN 107670338 A CN107670338 A CN 107670338A CN 201710856140 A CN201710856140 A CN 201710856140A CN 107670338 A CN107670338 A CN 107670338A
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- China
- Prior art keywords
- cylinder body
- inner barrel
- outer cylinder
- phase outlet
- end socket
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0073—Degasification of liquids by a method not covered by groups B01D19/0005 - B01D19/0042
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
The invention discloses a kind of outer-flowing type air separator, is mainly made up of the middle cylinder and inner barrel that are set in vertical outer cylinder body of the both ends with end socket, outer cylinder body;Outer cylinder body, middle cylinder and inner barrel are sequentially coaxially set from outside to inside, and along the upper edge for being higher than middle cylinder on inner barrel, spin-ended fan plate is provided with the inner barrel inwall close to inner barrel bottom;Medium entrance is provided with outer cylinder body bottom end socket center, relevant position is provided with gaseous phase outlet on end socket at the top of outer cylinder body directly over outer layer annular space, ball-cock assembly is installed at gaseous phase outlet, the liquid-phase outlet communicated with outer annular space is provided with outer cylinder body bottom side wall.The present invention gradually to outer barrel overflow, is separated using spin-ended fan plate and the design of three cartridge types, inner cylinder to the minute bubbles or air mass carried in liquid phase, improves separating effect, and make it that air separator structure is simpler, and operation is more convenient and reliable.
Description
Technical field
The invention belongs to Oil-gas Separation and flow assurance technical field, specifically, is related to a kind of outer-flowing type air separator.
Background technology
Bubble, impurity etc. not only result in flowmeter metering into mass flowmenter is forbidden, more can be to flowmeter internal junction
It is configured to abrasion damage.The flow assurance such as air separator, filter equipment must be added before mass flowmenter with quality assurance flow
The steady accurate measurement of meter.
Air separator and separation equipment in general sense are essentially different, and gravity separator or cyclone separator are directed to
Object be mainly the higher oil gas of gas liquid ratio, gas-liquid is all continuous phase, the liquid phase in the presence of gravity, buoyancy or from power
Mutually separate;And the main function of air separator prevents small to eliminate minute bubbles or the small air mass in liquid phase as dispersed phase
Bubble or air mass enter inside mass flowmenter.
The difference of separation object causes air separator and is generally separated the difference of device separating mechanism emphasis, centrifugal force with again
The effect of power, buoyancy in air separator can not occupy most important status, on the contrary separating mechanism of the overflow separation in air separator
In be indispensable.Overflow separating mechanism is made full use of to optimize great significance for design to air separator internal structure.
CN102225252A discloses a kind of spiral-flow type air eliminator, fluid edge and air separator inner walls phase in the air separator
After the direction cut enters container, flowed in funnelform cylinder internal rotation, gas is assembled to hopper centre and moved upwards, gathers
Collect the top vent of air separator housing, liquid is descending to be discharged by drain pipe, realizes gas-liquid separation.CN202674694U is disclosed
A kind of crude oil pipeline air separator, mainly for separating of and give off the gas mixed in crude oil, its structure mainly includes master
Body structure and air bleeding valve.Above two air separator can discharge the gas in liquid to a certain extent, but degasifying effect is limited.
The content of the invention
It is bad in order to solve degasifying effect existing for prior art, it is difficult to ensure the technical problem of the accuracy of metering, this
Invention provides a kind of outer-flowing type air separator.
Outer-flowing type air separator provided by the invention in vertical outer cylinder body of the both ends with end socket, outer cylinder body mainly by setting
Middle cylinder and inner barrel composition;Outer cylinder body, middle cylinder and inner barrel are sequentially coaxially set from outside to inside, middle cylinder and
Inner barrel is installed on outer cylinder body bottom bulkhead, is formed at the top of bottom lock and opened between outer cylinder inboard wall and middle cylinder outer wall
The outer annular space opened, the internal layer annular opened wide at the top of bottom lock is formed between middle cylinder inwall and inner barrel outer wall
Space, along the upper edge for being higher than middle cylinder on inner barrel, it is provided with the inner barrel inwall close to inner barrel bottom by inner barrel
Cross section is divided into the spin-ended fan plate of several fan-shaped runners, and the region above middle cylinder, at the top of outer cylinder body below end socket is formed
Gas phase zone;Medium entrance is provided with outer cylinder body bottom end socket center, directly over outer layer annular space at the top of outer cylinder body on end socket
Relevant position is provided with gaseous phase outlet, and ball-cock assembly is provided with gaseous phase outlet, and ball-cock assembly is floated in gas phase zone and outer annular space
On the gas-liquid interface of liquid phase region, the liquid-phase outlet communicated with outer annular space is provided with outer cylinder body bottom side wall.
The angle of circumference formed beyond the liquid-phase outlet and gaseous phase outlet centered on tubular axis can be any angle, one
As be 0 °, 90 ° or 180 °.
The spin-ended fan plate mainly fans plate by 3~9 pieces of rectangles and a center stand column is formed, and rectangle fans plate with center stand column
For axle center, it is distributed uniformly and circumferentially and is welded in center stand column, overall is in impeller shape;Every piece of rectangle fan plate with center
The axially in parallel side of column is mutually welded with inner barrel inwall, and inner barrel cross section is divided into and is cut into 3~9 fan-shaped runners.Only
Liquid turns are stable axial movement to eliminate the tangential velocity of fluid in flow field by the main function of rotation fan plate.Spin-ended fan
The fan plate quantity of plate is no less than 3 fans, and very few fan plate quantity is difficult to play a part of eliminating tangential velocity.
Ball-cock assembly is mature equipment, is installed on gaseous phase outlet, and ball float is located on gas-liquid interface.Gas-liquid interface is located at outer layer ring
It is gas phase zone above gas-liquid interface, lower section is liquid phase region in shape space.Gas phase is assembled to a certain extent inside container, gas-liquid
Interface declines, and ball-cock assembly is opened under the drive of float, and gas phase is discharged into blowdown system through gaseous phase outlet.
The general principle of the present invention is that the liquid phase of carrying minute bubbles or small air mass first is set through outer cylinder body bottom bulkhead center
The medium entrance put enters inner barrel;Gas-liquid incoming is moved through spin-ended fan plate steady flow condition from bottom to top in inner barrel;Carry
The liquid phase of minute bubbles along overflow on inner barrel through entering inner barrel and the internal layer annular space of middle cylinder formation, in this process
Middle minute bubbles or air mass buoyance lift enters gas phase zone, is separated for first time overflow;The liquid phase of internal layer annular space is through on middle cylinder
Enter outer annular space along overflow, wherein remaining minute bubbles escape into gas phase zone, separated for second of overflow;Gas phase is gathered
Liquid level declines collection in outer annular space to a certain extent, and air separator ball-cock assembly is opened, and gas phase is discharged into emptying system through gaseous phase outlet
System;Liquid phase after cooling down enters metering system through liquid-phase outlet.
Advantages of the present invention with:Using spin-ended fan plate and the design of three cartridge types, inner cylinder is gradually to outer barrel overflow, in liquid phase
The minute bubbles or air mass of carrying are separated, and improve separating effect, and make it that air separator structure is simpler, and operation is more square
It can lean on.
Brief description of the drawings
Fig. 1 is the structural representation of the outer-flowing type air separator of the present invention;
Fig. 2 is the structural representation of spin-ended fan plate in Fig. 1.
In figure:1- medium entrances, 2- liquid-phase outlets, 3- gaseous phase outlets, 4- ball-cock assemblys, 5- inner barrels, 6- internal layers annular are empty
Between, 7- middle cylinders, 8- outer annulars space, 9- outer cylinder bodies, 10- gas phase zones, the spin-ended fan plates of 11-, 12- tops end socket, 13- bottoms
Portion's end socket, 14- center stand columns, 15- rectangles fan plate.
Embodiment
Below in conjunction with the drawings and specific embodiments, topology layout, operational process to the present invention are described further.
Referring to Fig. 1, outer-flowing type air separator provided by the invention is mainly by vertical outer cylinder body 9 of the both ends with end socket, outer
The middle cylinder 7 and inner barrel 5 set in cylinder 9 forms;Outer cylinder body 9, middle cylinder 7 and inner barrel 5 are same successively from outside to inside
Axle is set, and middle cylinder 7 and inner barrel 5 are installed on the bottom bulkhead 13 of outer cylinder body 9, outside the inwall of outer cylinder body 9 and middle cylinder 7
Outer annular space 8 unlimited at the top of bottom lock, the shape between the inwall of middle cylinder 7 and the outer wall of inner barrel 5 are formed between wall
Into unlimited internal layer annular space 6 at the top of bottom lock, along the upper edge for being higher than middle cylinder 7 on inner barrel 5, close to inner barrel
The inner barrel inwall of 5 bottoms is provided with the spin-ended fan plate 11 that inner barrel cross section is divided into several fan-shaped runners, middle cylinder 7
Top, the region of the lower section of 9 top end socket of outer cylinder body 12 form gas phase zone 10;Medium is provided with the center of 9 bottom bulkhead of outer cylinder body 13
Import 1, relevant position is provided with gaseous phase outlet 3, gaseous phase outlet 3 on end socket 12 at the top of the surface outer cylinder body of outer layer annular space 8
Place is provided with ball-cock assembly 4, and ball-cock assembly 4 is floated in gas phase zone 10 and outer annular space 8 on the gas-liquid interface of liquid phase region, in outer barrel
The bottom sidewall of body 9 is provided with the liquid-phase outlet 2 communicated with outer annular space 8.
The liquid-phase outlet 2 is 180 ° with the angle of circumference that gaseous phase outlet 3 is formed centered on the axis of outer cylinder body 5.
As shown in Fig. 2 spin-ended fan plate 11 mainly fans plate 15 by 4 pieces of rectangles and a center stand column 14 is formed, rectangle fan plate
15 with center stand column 14 be axle center, is distributed uniformly and circumferentially and is welded in center stand column 14, and overall is in impeller shape;Every piece of square
Shape fan plate 15 is mutually welded with the side axially in parallel with center stand column and inner barrel inwall, and inner barrel cross section is divided into and is cut into
4 fan-shaped runners.
As shown in Figure 1, the course of work of the invention is:The liquid phase of minute bubbles or small air mass is carried first through outer cylinder body bottom
End socket centrally disposed medium entrance 1 in portion's enters inside inner barrel 5;Gas-liquid incoming is moved through stopping from bottom to top in inner barrel 5
The rotation fan steady flow condition of plate 11;The liquid phase of minute bubbles is carried through entering on inner barrel 5 along overflow between inner barrel 5 and middle cylinder 7
Internal layer annular space 6 in, minute bubbles or air mass buoyance lift enter gas phase zone 10 in this course, for first time overflow separate;
Liquid phase in internal layer annular space 6 on middle cylinder 7 along overflow through entering in outer annular space 8, wherein remaining minute bubbles
Gas phase zone 10 is escaped into, is separated for second of overflow;Liquid level decline disappears in outer annular space 8 to a certain extent for gas phase aggregation
Gas device ball-cock assembly 4 is opened, and gas phase is discharged into blowdown system through gaseous phase outlet 3, and the liquid phase after cooling down enters through liquid-phase outlet 2
Metering system.
Claims (3)
- A kind of 1. outer-flowing type air separator, it is characterised in that:Mainly by being set in vertical outer cylinder body of the both ends with end socket, outer cylinder body Middle cylinder and the inner barrel composition put;Outer cylinder body, middle cylinder and inner barrel are sequentially coaxially set from outside to inside, middle cylinder It is installed on outer cylinder body bottom bulkhead with inner barrel, is formed between outer cylinder inboard wall and middle cylinder outer wall at the top of bottom lock Unlimited outer annular space, the inner layer ring opened wide at the top of bottom lock is formed between middle cylinder inwall and inner barrel outer wall Shape space, along the upper edge for being higher than middle cylinder on inner barrel, it is provided with the inner barrel inwall close to inner barrel bottom by inner cylinder Body cross section is divided into the spin-ended fan plate of several fan-shaped runners, the region shape above middle cylinder, at the top of outer cylinder body below end socket Into gas phase zone;Medium entrance is provided with outer cylinder body bottom end socket center, in end socket at the top of outer cylinder body directly over outer layer annular space Upper relevant position is provided with gaseous phase outlet, and ball-cock assembly is provided with gaseous phase outlet, and ball-cock assembly floats on gas phase zone and outer annular space On the gas-liquid interface of interior liquid phase region, the liquid-phase outlet communicated with outer annular space is provided with outer cylinder body bottom side wall.
- 2. air separator according to claim 1, it is characterised in that:The liquid-phase outlet and tubular axis beyond gaseous phase outlet Centered on the angle of circumference that is formed be 0 °, 90 ° or 180 °.
- 3. air separator according to claim 1, it is characterised in that:The spin-ended fan plate mainly by 3~9 pieces of rectangles fan plates and A piece center stand column is formed, and rectangle fans plate using center stand column as axle center, is distributed uniformly and circumferentially and is welded in center stand column, Overall is in impeller shape;Every block of rectangle fan plate is mutually welded with the side axially in parallel with center stand column and inner barrel inwall, by Cylinder cross section, which is divided into, is cut into 3~9 fan-shaped runners.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710856140.2A CN107670338B (en) | 2017-09-21 | 2017-09-21 | Outward flow type air eliminator |
Applications Claiming Priority (1)
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CN201710856140.2A CN107670338B (en) | 2017-09-21 | 2017-09-21 | Outward flow type air eliminator |
Publications (2)
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CN107670338A true CN107670338A (en) | 2018-02-09 |
CN107670338B CN107670338B (en) | 2020-04-14 |
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CN201710856140.2A Active CN107670338B (en) | 2017-09-21 | 2017-09-21 | Outward flow type air eliminator |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202674694U (en) * | 2011-11-17 | 2013-01-16 | 中国石油化工股份有限公司 | Gas eliminating device for crude oil pipeline |
CN203043639U (en) * | 2012-11-08 | 2013-07-10 | 广西华纳新材料科技有限公司 | Device for liquid defoaming |
CN203558884U (en) * | 2013-09-18 | 2014-04-23 | 宁波明泰流量设备有限公司 | High-flow liquid gas eliminator for container |
CN203678022U (en) * | 2013-12-02 | 2014-07-02 | 天津斯秘特精密仪表股份有限公司 | Air eliminator |
CN204656168U (en) * | 2015-05-21 | 2015-09-23 | 中国海洋石油总公司 | A kind of swirl flow gas-liquid separator |
CN205252613U (en) * | 2015-12-29 | 2016-05-25 | 南京天梯自动化设备股份有限公司 | Plumbing installation of cooling down |
-
2017
- 2017-09-21 CN CN201710856140.2A patent/CN107670338B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN202674694U (en) * | 2011-11-17 | 2013-01-16 | 中国石油化工股份有限公司 | Gas eliminating device for crude oil pipeline |
CN203043639U (en) * | 2012-11-08 | 2013-07-10 | 广西华纳新材料科技有限公司 | Device for liquid defoaming |
CN203558884U (en) * | 2013-09-18 | 2014-04-23 | 宁波明泰流量设备有限公司 | High-flow liquid gas eliminator for container |
CN203678022U (en) * | 2013-12-02 | 2014-07-02 | 天津斯秘特精密仪表股份有限公司 | Air eliminator |
CN204656168U (en) * | 2015-05-21 | 2015-09-23 | 中国海洋石油总公司 | A kind of swirl flow gas-liquid separator |
CN205252613U (en) * | 2015-12-29 | 2016-05-25 | 南京天梯自动化设备股份有限公司 | Plumbing installation of cooling down |
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CN107670338B (en) | 2020-04-14 |
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