CN206372606U - Spiral vortex gas-liquid separator device - Google Patents
Spiral vortex gas-liquid separator device Download PDFInfo
- Publication number
- CN206372606U CN206372606U CN201621388902.8U CN201621388902U CN206372606U CN 206372606 U CN206372606 U CN 206372606U CN 201621388902 U CN201621388902 U CN 201621388902U CN 206372606 U CN206372606 U CN 206372606U
- Authority
- CN
- China
- Prior art keywords
- tank body
- separating core
- core cylinder
- baffle plate
- gas
- 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
Links
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model is related to a kind of spiral vortex gas-liquid separator, including tank body, combination ring, spiral cyclone plate, separating core cylinder, wire mesh demister, baffle plate, it is characterized in that:Separating core cylinder is cylinder, and bottom is provided with end socket provided with latticed support, top, there is perforate on end socket, and wire mesh demister is mounted in separating core cylinder;Separating core cylinder is arranged on the centre position of tank body internal upper part, and combination ring is arranged on tank body internal upper part, is connected with tank body and separating core barrel soldering;Spiral cyclone plate is set around separating core cylinder;Baffle plate is circular slab, and equally spaced provided with connecting plate around circular slab edge, baffle plate setting is below separating core cylinder;Gas-liquid mixture import is arranged on the side wall on tank body top, and liquid outlet is arranged on the side wall of tank body lower part, and in tank base least significant end, its advantage is sewage outfalls setting:Secondary separation can be carried out to gas-liquid mixture, separated more thorough.
Description
Technical field
The utility model is related to a kind of spiral vortex gas-liquid separator, it is adaptable to chemical industry Separate System of Water-jet, category
In separator technical field.
Background technology
Gas-liquid separator used in current chemical industry has baffle plate type separator, filter separator;Baffle plate type separator is used
One kind of property separator.This separator constitutes " shutter " formula structure by polylith plate washer.Barrier material has good to liquid water droplets
Good immersional wetting, drop is and very thin one layer in its Surface Creation with after stop collision, can largely be attached on baffle plate
Flow down after liquid along baffle plate, the drop of larger particle be agglomerated into baffle edge, drop under the Action of Gravity Field of itself with
Air is separated, but this separate mode efficiency is very low, is separated not thorough.Filter gas-liquid separator is such as used, can be reached really
Because filter can reach 100% to the filter efficiency of the drop of certain particle diameter, but it is due to dimension to good separating effect
Filter core financial cost height is protected, the loss caused is big, so being industrially seldom used as gas-liquid separator with filter.
The content of the invention
The purpose of this utility model is that secondary separation can be carried out to gas-liquid mixture by providing one kind, be separated more thorough
Spiral vortex gas-liquid separator.
The purpose of this utility model is achieved in the following ways:
The utility model includes tank body, combination ring, spiral cyclone plate, separating core cylinder, wire mesh demister, baffle plate, its
It is characterized in:Separating core cylinder is cylinder, and bottom is provided with end socket, end socket provided with latticed support, top perforate, and silk screen is removed
Foam device is mounted in separating core cylinder;Separating core cylinder is arranged on the centre position of tank body internal upper part, and combination ring is arranged in tank body
Top, is connected with tank body and separating core barrel soldering;Spiral cyclone plate is set around separating core cylinder, inner edge and separating core cylinder
Body is fixed, and outside is fixed with inner tank wall;Baffle plate is circular slab, equally spaced provided with connecting plate, baffle plate around circular slab edge
It is arranged on below separating core cylinder;Gas-liquid mixture import is arranged on the side wall on tank body top, and liquid outlet is arranged under tank body
On the side wall in portion, sewage outfalls setting is in tank base least significant end.
The utility model has the advantages that:Secondary separation can be carried out to gas-liquid mixture, separated more thorough.
Brief description of the drawings
Fig. 1 is the utility model spiral vortex gas-liquid separator apparatus structure schematic diagram;
Fig. 2 is the structural representation of spiral cyclone plate;
Fig. 3 is Fig. 2 top view;
Fig. 4 is the structural representation of baffle plate.
Referring to the drawings, the utility model includes tank body, combination ring, spiral cyclone plate, separating core cylinder, silk screen foam removal
Device, baffle plate, it is characterized in that:Separating core cylinder is cylinder, and bottom is provided with end socket, end socket provided with latticed support, top to be had
Perforate, wire mesh demister is mounted in separating core cylinder;Separating core cylinder is arranged on the centre position of tank body internal upper part, and combination ring is set
Put in tank body internal upper part, be connected with tank body and separating core barrel soldering;Spiral cyclone plate is set around separating core cylinder, inner edge
Fixed with separating core cylinder, outside is fixed with inner tank wall;Baffle plate is circular slab, equally spaced provided with company around circular slab edge
Fishplate bar, baffle plate setting is below separating core cylinder;Gas-liquid mixture import is arranged on the side wall on tank body top, and liquid outlet is set
On the side wall of tank body lower part, sewage outfalls setting is in tank base least significant end.
The utility model has the advantages that:Secondary separation can be carried out to gas-liquid mixture, separated more thorough.
Embodiment
Referring to the drawings, the utility model is removed including tank body 2, combination ring 5, spiral cyclone plate 4, separating core cylinder 8, silk screen
Foam device 7, baffle plate 3, separating core cylinder are cylinder, and latticed support, top are made of band steel and is provided with end socket, end socket for bottom has
Perforate(I.e.:Gas outlet), wire mesh demister is in separating core cylinder;Separating core cylinder is arranged on the interposition of tank body internal upper part
Put, combination ring is arranged on tank body internal upper part, is connected with tank body and separating core barrel soldering;Spiral cyclone plate is two helical layer knots
Structure, spiral cyclone plate is set around separating core cylinder, and inner edge is fixed with separating core barrel soldering, and outside is welded with inner tank wall
It is fixed;Baffle plate is circular slab, equally spaced provided with connecting plate around circular slab edge, and baffle plate is divided into two layers and is arranged on separating core cylinder
Body lower section, i.e. upper strata baffle plate and lower floor's baffle plate;Gas-liquid mixture import 6 is arranged on the side wall on tank body top, and liquid outlet 9 is set
On the side wall of tank body lower part, sewage draining exit 1 is arranged on tank base least significant end.Spiral cyclone type gas-liquid separation of the present utility model
Device device is a kind of inertia separator, and its principle is that compressed air enters after separator tank body along tank body barrel tangential direction,
The inside produces rotation, and the drop being mixed in gas is and then rotated together due to centrifugal action, and quality is bigger, and centrifugal force is bigger, institute
Moved with big drop to outer wall, encounter and gather again after baffle plate for bigger drop and separated with gas, and the small drop of particle diameter
Moved under gas pressure effect in the central shaft of negative pressure state, final path grain drop entrained gas again.
Working method of the present utility model is:Gas-liquid mixture enters tank body along the tangential direction of import 6,(Equipment tank body with
Between separating core cylinder), air-flow produced strong rotation by the guide functions of spiral cyclone plate 4, and air-flow is in spiral shell along tank body
Revolve shape downwards, the big drop of density and grit are thrown toward tank wall under the influence of centrifugal force, and under gravity, along tank body
Tank base is dropped down onto under wall, first separation is realized;Gas-liquid mixture after first separation falls to running into after upper and lower layer baffle plate 3
Liquid is attached on baffle plate, is condensed into after big drop because gravity is settled downwards, remaining contains the gas-liquid mixed of small particle size droplets
Thing, to center flow, is upwardly formed secondary vortex flow and enters separating core cylinder, warp from separating core cylinder body bottom again in tank body contract
Cross wire mesh demister 7(By silk screen just as sieving, gas passes through, and liquid is intercepted and stays on silk screen, and in weight
Downstream to tank body lower part in the presence of power)Secondary separation is realized, gas is through the perforate stream on separating core cylinder end socket at the top of equipment
Go out, final gas-liquid mixture passes through secondary separation, separation is thorough;Liquid after separation is finally discharged by liquid outlet 9, and debris is by arranging
Dirty mouth 1 is discharged.
Claims (1)
1. a kind of spiral vortex gas-liquid separator, including tank body, combination ring, spiral cyclone plate, separating core cylinder, silk screen are removed
Foam device, baffle plate, it is characterized in that:Separating core cylinder is cylinder, and bottom is provided with end socket, end socket provided with latticed support, top
There is perforate, wire mesh demister is mounted in separating core cylinder;Separating core cylinder is arranged on the centre position of tank body internal upper part, combines ring
Tank body internal upper part is arranged on, is connected with tank body and separating core barrel soldering;Spiral cyclone plate is set around separating core cylinder, interior
Side is fixed with separating core cylinder, and outside is fixed with inner tank wall;Baffle plate is circular slab, is provided with around circular slab edge is equally spaced
Connecting plate, baffle plate setting is below separating core cylinder;Gas-liquid mixture import is arranged on the side wall on tank body top, and liquid outlet is set
Put on the side wall of tank body lower part, sewage outfalls setting is in tank base least significant end.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621388902.8U CN206372606U (en) | 2016-12-18 | 2016-12-18 | Spiral vortex gas-liquid separator device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621388902.8U CN206372606U (en) | 2016-12-18 | 2016-12-18 | Spiral vortex gas-liquid separator device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206372606U true CN206372606U (en) | 2017-08-04 |
Family
ID=59406271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621388902.8U Expired - Fee Related CN206372606U (en) | 2016-12-18 | 2016-12-18 | Spiral vortex gas-liquid separator device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206372606U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
-
2016
- 2016-12-18 CN CN201621388902.8U patent/CN206372606U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107557087A (en) * | 2017-09-05 | 2018-01-09 | 中石化广州工程有限公司 | A kind of spiral-flow type gas-liquid separation device and method |
CN107557087B (en) * | 2017-09-05 | 2020-06-23 | 中石化广州工程有限公司 | Spiral-flow type gas-liquid separation device and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4857350B2 (en) | Fiber bed assembly and fiber bed therefor | |
JP6279506B2 (en) | Cyclone equipment | |
US20060117725A1 (en) | Dust-separating apparatus for a vacuum cleaner and dust-separating method for the same | |
US3225523A (en) | Cyclone dust collector for removing particles from a fluid stream | |
CN206372606U (en) | Spiral vortex gas-liquid separator device | |
US8349059B2 (en) | Pocketed cyclonic separator | |
CN102921259B (en) | Self-circulation rotary liquid combined type gas filter and filtering method thereof | |
CN213492783U (en) | Water-gas separating device | |
CN103240193A (en) | Screen structure for cyclone separator | |
CN211463541U (en) | Cyclone separator | |
CN205164414U (en) | Wet -type whirlwind water curtain dust collector | |
CN202860347U (en) | Agglomerate cyclone separator | |
JP2000279739A (en) | Dust collecting device | |
CN2366191Y (en) | Vortex flow type layered sieving separator | |
JP5320514B1 (en) | Dust catcher for blast furnace gas | |
RU2256488C1 (en) | Droplet separator | |
CN102872668B (en) | Agglomerate cyclone separator | |
CN202921124U (en) | Self-circulation revolving liquid composite gas filter | |
RU2534634C2 (en) | Separator-lock trap and method of its application | |
CN201524510U (en) | Combined type filtering separator | |
CN202438421U (en) | Multi-stage efficient sand dust separator | |
CN214261037U (en) | Tail gas cyclone separator | |
CN201579191U (en) | Composite sand dust separator | |
JP2009112966A (en) | Dust recovery apparatus | |
CN209629575U (en) | Dust catcher |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address |
Address after: 014032, Baotou, the Inner Mongolia Autonomous Region two mailbox technology and Information Technology Department Patentee after: Inner Mongolia First Machinery Group Limited by Share Ltd Address before: 014030 the first functional district of rare earth hi tech Industrial Development Zone, the Inner Mongolia Autonomous Region, Baotou Patentee before: Baotou Beifang Venture Co., Ltd. |
|
CP03 | Change of name, title or address | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170804 Termination date: 20181218 |
|
CF01 | Termination of patent right due to non-payment of annual fee |