CN210278649U - Vacuum system buffering cyclone separation equipment - Google Patents
Vacuum system buffering cyclone separation equipment Download PDFInfo
- Publication number
- CN210278649U CN210278649U CN201920830617.4U CN201920830617U CN210278649U CN 210278649 U CN210278649 U CN 210278649U CN 201920830617 U CN201920830617 U CN 201920830617U CN 210278649 U CN210278649 U CN 210278649U
- Authority
- CN
- China
- Prior art keywords
- tank body
- gas
- separator tank
- separator
- flange
- 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.)
- Active
Links
Images
Landscapes
- Cyclones (AREA)
Abstract
A vacuum system buffering cyclone separation device relates to the technical field of chemical vacuum systems, and a lower end flange of a gas outlet pipeline is connected with an upper end flange of a separator tank body through bolts. The side surface of the separator tank body is provided with a gas inlet pipeline, a partition plate is arranged in the separator tank body and divides the separator tank body into an upper layer and a lower layer, the partition plate is arranged above the gas inlet pipeline, the upper layer of the separator tank body is provided with a fixed pore plate, a ceramic ring is arranged on the fixed pore plate, a movable pore plate is covered above the ceramic ring, a flange at the lower end of the gas outlet pipeline is connected with a flange at the upper end of the separator tank body through bolts, and a bottom inserting pipe is arranged at the lower layer and welded on the partition plate. The gas inlet pipeline is welded on the separator tank body in the tangential direction. The gas is firstly centrifugally separated and then filtered and adsorbed by a ceramic ring, so that the gas and the liquid are effectively separated. The load of the vacuum system on tail gas treatment is reduced, and the liquid can be collected and reused. Energy conservation and environmental protection, reduced material consumption, simple operation, convenient disassembly, replacement, cleaning and the like.
Description
Technical Field
The utility model relates to a chemical industry vacuum system's technical field, concretely relates to vacuum system buffering cyclone separation equipment.
Background
During vacuum rectification, a vacuum buffer tank is generally used for the purpose of stabilizing vacuum and gas-liquid separation. The actual use effect is not good, and gas-liquid does not obtain good separation after the gas gets into the vacuum buffer tank, directly gets into vacuum apparatus in the middle of from the exhaust pipe line, has increaseed the processing degree of difficulty for subsequent vacuum tail gas treatment, makes subsequent tail gas separation adsorption effect not good, and directly discharges to the atmosphere in, the polluted environment.
Disclosure of Invention
The utility model aims at providing a vacuum system buffering cyclone separation equipment. The gas-liquid separation problem among the evacuation process can be solved better to it, stabilizes the steady of vacuum pressure assurance vacuum in the system, and liquid in the gas is by effectual separation, can not bring into tail gas in, has reduced the degree of difficulty of tail gas treatment, can not discharge polluted environment in the atmosphere, and material liquid can collect and recycle, and is energy-concerving and environment-protective.
The purpose of the invention is realized by the following technical scheme:
the utility model provides a vacuum system buffering cyclone separation equipment, includes separator jar body 1, baffle 2, gas inlet pipeline 3, fixed orifice plate 4, porcelain ring 5, activity orifice plate 6, gas outlet pipeline 7, inserts bottom tube 8, drain hole 9, its characterized in that: the lower end flange of the gas outlet pipeline 7 is connected with the upper end flange of the separator tank body 1 through bolts. The gas inlet pipeline 3 is installed on the side face of the separator tank body 1, the partition plate 2 is arranged in the separator tank body 1, the separator tank body 1 is divided into an upper layer and a lower layer, the partition plate 2 is located above the gas inlet pipeline 3, the fixed pore plate 4 is arranged on the upper layer of the separator tank body 1, the ceramic ring 5 is placed on the fixed pore plate 4, the movable pore plate 6 is covered above the ceramic ring 5, the flange at the lower end of the gas outlet pipeline 3 is connected with the flange at the upper end of the separator tank body 1 through bolts, the bottom inserting pipe 8 is arranged on the lower layer and welded on the partition plate 2. The lower end flange of the gas outlet pipeline 3 is connected with the side flange of the separator tank body 1 through bolts, and the gas inlet pipeline 3 is welded on the separator tank body 1 in the tangential direction.
The gas inlet pipeline is connected to the separator tank body in the tangential direction, and the gas enables part of liquid to be thrown out to the tank bottom through the centrifugal action.
A partition board is arranged in the separator tank body to divide the tank body into two spaces, the lower layer is a cyclone separation space, and the upper layer is a gas filtering space.
After the gas enters the upper space from the bottom inserting bottom pipe, the space is enlarged, so that the gas speed is reduced.
And a ceramic ring is placed between the fixed pore plate and the movable pore plate in the upper space to be used as gas filtration, and the upper movable pore plate is convenient for filling and replacing the ceramic ring.
The utility model has the advantages that: the gas is not directly introduced into the vacuum system through the outlet of the gas pipeline, but is firstly separated by centrifugation and then filtered and adsorbed by the ceramic ring, so that the gas and the liquid are effectively separated. The load of the vacuum system on tail gas treatment is reduced, and the liquid can be collected and reused. Energy conservation and environmental protection, reduced material consumption, simple operation, convenient disassembly, replacement, cleaning and the like.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a sectional view a-a of fig. 1.
In the figure: 1. the separator comprises a separator tank body 2, a partition plate 3, a gas inlet pipeline 4, a fixed pore plate 5, a ceramic ring 6, a movable pore plate 7, a gas outlet pipeline 8, a bottom inserting pipe 9 and a discharge hole.
Detailed Description
The invention is further described with reference to the following figures and specific examples.
The lower end flange of the gas outlet pipeline 7 is connected with the upper end flange of the separator tank body 1 through bolts. The gas inlet line 3 is welded tangentially to the separator tank 1. The separator 2 is positioned above the gas inlet line 3 to divide the separator tank 1 into upper and lower layers. The bottom inserting pipe 8 is arranged on the lower layer, welded on the partition board 2 and used for communicating the upper layer space with the lower layer space. The discharging port is arranged at the lowest end of the separator tank body and used for discharging. The upper layer of the separator tank body 1 is provided with a fixed pore plate 4, a ceramic ring 5 is arranged on the fixed pore plate 4, and a movable pore plate 6 is covered above the ceramic ring 5.
The working process is as follows: the vacuum gas carrying a small amount of liquid firstly enters the lower layer of the separator tank body in a tangential direction through a gas inlet pipeline, part of the liquid is thrown to the bottom of the tank due to the centrifugal action, the gas enters the upper layer of the separator tank body from the lower part of the bottom inserting pipe, after the gas enters the gas, the space is enlarged, the gas speed is slowed down, the gas is filtered and adsorbed through the fixed pore plate, the ceramic ring and the movable pore plate, the liquid carried by the gas is completely separated, the clean gas enters the vacuum equipment through the gas outlet pipeline and is treated, finally the gas is discharged to the atmosphere, and the liquid is collected to the bottom of the separator tank for recycling.
Claims (2)
1. The utility model provides a vacuum system buffering cyclone separation equipment, includes separator jar body (1), baffle (2), gas inlet pipeline (3), fixed orifice plate (4), porcelain ring (5), activity orifice plate (6), gas outlet pipeline (7), inserts bottom tube (8), drain hole (9), its characterized in that: gas outlet pipeline (7) are connected with the separator jar body (1), separator jar body (1) side ann has gas inlet pipeline (3), there is baffle (2) in the separator jar body (1), divide into the separator jar body (1) upper and lower two-layer, baffle (2) position is in gas inlet pipeline (3) top, there is fixed orifice plate (4) on the upper strata of separator jar body (1), place ceramic ring (5) on fixed orifice plate (4), ceramic ring (5) top is covered with movable orifice plate (6), gas outlet pipeline (7) lower extreme flange is connected with separator jar body (1) upper end flange with the bolt, insert bottom tube (8) in the lower floor, the welding is on baffle (2).
2. A vacuum system buffer cyclonic separating apparatus as claimed in claim 1, wherein: the flange at the lower end of the gas outlet pipeline (7) is connected with the flange at the side surface of the separator tank body (1) by bolts, and the gas inlet pipeline (3) is welded on the separator tank body (1) in the tangential direction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920830617.4U CN210278649U (en) | 2019-06-04 | 2019-06-04 | Vacuum system buffering cyclone separation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201920830617.4U CN210278649U (en) | 2019-06-04 | 2019-06-04 | Vacuum system buffering cyclone separation equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210278649U true CN210278649U (en) | 2020-04-10 |
Family
ID=70072252
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201920830617.4U Active CN210278649U (en) | 2019-06-04 | 2019-06-04 | Vacuum system buffering cyclone separation equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210278649U (en) |
-
2019
- 2019-06-04 CN CN201920830617.4U patent/CN210278649U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2736436A1 (en) | Vortex waste separator apparatus | |
CN205199080U (en) | Solid -liquid separation device | |
CN100457227C (en) | Rotational flow microporous filter | |
CN210278649U (en) | Vacuum system buffering cyclone separation equipment | |
CN202379784U (en) | Two-stage rotational flow pressure type coagulation reactor | |
CN104353297A (en) | Bag dust collector with separation chambers of air tank | |
CN113431549A (en) | Automatic liquid-discharging sand-removing separator | |
CN201823432U (en) | High-efficiency gas-liquid separator | |
KR101352617B1 (en) | Complex dust collector for cutting apparatus of printed circuit board | |
CN201940139U (en) | Vacuum cyclone separation filter | |
CN208436470U (en) | A kind of filter separator being centrifuged dirt collection | |
CN202297196U (en) | Rotary flow flotation device for treating oily wastewater | |
CN211585846U (en) | Efficient dust removal device of Raymond mill | |
CN203890149U (en) | Three-phase separator of water system | |
JPS60129154A (en) | Cyclone separator | |
CN207792881U (en) | A kind of effluent treatment plant with deoiling function | |
CN213589933U (en) | Cyclone separator | |
CN213260747U (en) | Inhale material auxiliary device | |
CN111392815A (en) | Layered oil-water separation device based on high-flux high-efficiency oil-water separation membrane | |
CN212532371U (en) | Layered oil-water separation device based on high-flux high-efficiency oil-water separation membrane | |
CN201189433Y (en) | Combined purification device | |
CN216571676U (en) | Multistage liquid and foam removing device for shale gas | |
CN217868165U (en) | Water filtering device with built-in pressure cyclone | |
CN211537081U (en) | Solid filter element gas-liquid separator with cyclone | |
CN204034343U (en) | A kind of civil aviation jet fuel solid phase impurity removal means |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |