CN217961660U - Gas-liquid cyclone separator - Google Patents
Gas-liquid cyclone separator Download PDFInfo
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- CN217961660U CN217961660U CN202222023780.4U CN202222023780U CN217961660U CN 217961660 U CN217961660 U CN 217961660U CN 202222023780 U CN202222023780 U CN 202222023780U CN 217961660 U CN217961660 U CN 217961660U
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Abstract
The utility model relates to a cyclone technical field especially relates to a gas-liquid cyclone, including the separator body, the separator body includes: the cover body is arranged at the top of the separator body and used for outputting secondary steam; the manhole is arranged on the top surface of the cover body and used for maintenance; the conical cylinder is arranged at the bottom of the separator body and is used for separating secondary steam; the exhaust core pipe is arranged at the top of the conical cylinder; the wire mesh demister is arranged on the bottom surface of the cover body and used for filtering liquid foam; the spraying ball is used for cleaning; and the spiral blade is arranged on the periphery of the exhaust core pipe and extends to the bottom of the conical cylinder for guiding flow. The utility model adopts the helical blades, the secondary steam entering the separator body tangentially from the side surface is cyclone downwards to the bottom of the conical cylinder along the helical blades, so that the gas-liquid separation effect can be improved; utilize and spray the ball and connect outside gas, liquid source, regularly wash lid inner wall and silk screen demister, can prolong the silk screen change time, reduce the equipment maintenance cost.
Description
Technical Field
The utility model relates to a vapour and liquid separator technical field especially relates to a gas-liquid cyclone.
Background
The gas-liquid separator is a separation device for removing liquid by adopting the principles of centrifugal separation and wire mesh filtration, mainly comprises a cylinder, a cyclone separator, a high-efficiency foam breaking net, a blow-down valve and other main components, and is generally arranged in front of a drying device and can roughly filter and remove part of moisture in air so as to reduce the workload of the drying device.
A large amount of foams are often generated in the evaporation process of organic matters, namely, a large amount of foams are entrained in secondary steam, and the entrained foams are difficult to be completely separated by a conventional gas-liquid separator. The secondary steam carrying the foam enters a follow-up heater, and can deposit and scale on the wall of the heat exchange tube, so that the heat exchange effect is influenced, the stable operation of the whole system is influenced, and the manual cleaning difficulty is high. The existing treatment mode is to enlarge the diameter and the height of a front-end separator, and the treatment mode has high investment cost on equipment but has poor separation effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a gas-liquid cyclone to solve the problem that proposes in the above-mentioned background art.
The utility model discloses a realize through following technical scheme:
the utility model provides a gas-liquid cyclone, its structure includes the separator body, is provided with air inlet, gas outlet, row's cinder notch and the valve that corresponds on the separator body, the separator body includes:
the cover body is arranged at the top of the separator body and used for outputting secondary steam, and the air outlet is arranged at the top of the cover body;
the manhole is arranged on the top surface of the cover body and used for maintenance;
the conical cylinder is arranged at the bottom of the separator body and used for separating secondary steam, the air inlet is tangentially arranged on the side surface of the conical cylinder, the steam enters the separator body from the side surface of the conical cylinder through the air inlet in a tangential manner, the slag discharge port is arranged on the bottom surface of the conical cylinder, the water discharge port is arranged on the side surface of the bottom of the conical cylinder, and the height of the water discharge port is higher than that of the slag discharge port so as to prevent solid waste residues from blocking the water discharge port;
the exhaust core pipe is arranged at the top of the conical cylinder, the exhaust core pipe is communicated with the bottom surface of the cover body, steam rotates along the helical blade to be separated, and gas flows upwards through the exhaust core pipe;
the wire mesh demister is arranged on the bottom surface of the cover body and used for filtering liquid foam in the air flow output from the exhaust core pipe, and the wire mesh demister can be detached;
the top surface of the cover body is also provided with a flushing port, the spraying ball is arranged at the flushing port through a mounting assembly, and the spraying ball can be connected with external gas and liquid to flush the inner wall of the cover body and the screen demister;
the spiral blades are arranged on the periphery of the exhaust core pipe and extend to the bottom of the conical cylinder, steam entering from the side surface in a tangential manner is swirled downwards to the bottom of the conical cylinder along the spiral blades, gas is upwards output through the exhaust core pipe, and liquid or solid impurities with high density are respectively output out of the separator body through the water outlet and the slag discharge port.
Preferably, the cover body and the conical cylinder are integrally arranged.
Preferably, the top of the exhaust core pipe is funnel-shaped, so that secondary steam outside the exhaust core pipe can flow downwards conveniently, and meanwhile, the cover body can be communicated conveniently.
Preferably, the wire mesh demister is a wave-shaped wire mesh demister, so that the defoaming effect is better.
As a further scheme of the utility model, it sprays the ball for the telescopic rotation type, and the injection angle is 360, compares with traditional fixed ball that sprays, can form great liquid drop and evenly spray, and the cleaning performance is good, can save the quantity of water and cleaner simultaneously, spray the ball with the connection of lid sets up to dismantling the connection.
Preferably, the aperture of the manhole is set to be 500mm, and a sealing member is arranged at the manhole.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the utility model discloses a helical blade, the secondary steam that the side tangential got into the separator body can improve the gas-liquid separation effect along helical blade downward cyclone to cone bottom.
2. The utility model discloses the utilization sprays the ball and connects outside gas, liquid source, carries out the periodic flushing to lid inner wall and silk screen demister, can prolong the silk screen change time, reduces the plant maintenance cost.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without creative efforts.
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is an enlarged schematic view of the top of the present invention;
fig. 3 is a schematic top view of the wire mesh demister of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person of ordinary skill in the art without creative efforts belong to the protection scope of the present invention.
Example 1:
as shown in fig. 1-2, the present embodiment provides a gas-liquid cyclone separator, which structurally includes a separator body, where corresponding valves are disposed at an air inlet 1, an air outlet 2, a water outlet 3, and a slag discharge port 4, and the separator body includes a cover body 5 and a conical barrel 7 that are integrally disposed.
The cover body 5 is arranged at the top of the separator body and used for outputting secondary steam, and the top of the cover body 5 is provided with an air outlet 2. The top surface of lid 5 still is provided with the manhole 6 that is located the opposite side, and manhole 6 aperture sets up to 500mm, and manhole 6 department is provided with sealing member 13, and sealing member 13 is used for avoiding gas to spill over from manhole 6, and when the inside of separator body broke down, opens manhole 6, and the maintainer was through manhole 6 entering separator body in, overhauld internal instrument.
The bottom surface of lid 5 is provided with detachable silk screen demister 9, and silk screen demister 9 is used for filtering the liquid foam in the air current of exporting from exhaust core pipe 8. The top surface of lid 5 still is provided with washes the mouth, sprays ball 11 and installs in washing the mouth through installation component 12, sprays the ball and can connect two ways of outside gas, liquid and wash lid 5 inner wall and silk screen demister 9.
The conical cylinder 7 is arranged at the bottom of the separator body and used for separating secondary steam. The side of a conical cylinder 7 is tangentially provided with an air inlet 1, steam enters the separator body from the side of the conical cylinder 7 through the air inlet 1 in a tangential manner, a slag discharge port 4 is arranged on the bottom surface of the conical cylinder 7, a water outlet 3 is arranged on the side of the bottom of the conical cylinder 7, and the height of the water outlet 3 is higher than that of the slag discharge port 4, so that solid waste residues are prevented from blocking the water outlet 3. The conical barrel 7 is also internally provided with an exhaust core pipe 8 communicated with the bottom surface of the cover body 5, the helical blade 10 is arranged on the periphery of the exhaust core pipe 8 and extends to the bottom of the conical barrel 7, the steam entering tangentially from the side surface is swirled downwards to the bottom of the conical barrel 7 along the helical blade 10, after gas-liquid separation, the gas flows upwards through the exhaust core pipe 8, and liquid or solid impurities with higher density are respectively output out of the separator body through the water outlet 3 and the slag discharge port 4.
Example 2:
as shown in fig. 1 to 3, in a gas-liquid cyclone separator described in embodiment 1, the top of the exhaust core pipe 8 is provided in a funnel shape so as to communicate with the cover body 5, and the cover body 5 in the funnel shape so as to facilitate the secondary steam entering into the conical cylinder 7 to flow down along the spiral blades 10 outside the exhaust core pipe 8. Further, the wire mesh demister 9 was provided as a wave-type wire mesh demister having a better defoaming effect, and the rest was the same as in example 1.
Example 3:
as shown in fig. 1 to 3, the present embodiment provides a gas-liquid cyclone separator, and differs from embodiment 2 in that: spray ball 11 and spray the ball for the telescopic rotation type, the injection angle is 360, compare with traditional fixed ball that sprays, the rotation type sprays the ball and can form great liquid drop even injection, and the cleaning performance is good, can save the quantity of water and cleaner simultaneously, sprays ball 11 and the connection of washing the mouth and sets up to dismantling the connection, in time changes after being convenient for damage, all the other all the same with embodiment 2.
A specific working manner of this embodiment is as follows:
the valves arranged at the air inlet 1, the air outlet 2, the water outlet 3 and the slag discharge port 4 are respectively opened. The secondary steam generated in the organic matter evaporation process enters the interior of the separator body from the side surface of the conical barrel 7 in a tangential mode through the air inlet 1, and the secondary steam is swirled downwards to the bottom of the conical barrel 7 along the spiral blades 10. After the steam is rotated and separated, gas with lower density flows upwards from the bottom surface of the exhaust core pipe 8, liquid foam in the airflow is filtered by the wire mesh demister 9, and the separated gas enters the cover body and is finally discharged out of the separator body from the gas outlet 2; the liquid or the waste residue with higher density is discharged out of the separator body through the water outlet 3 and the slag discharge port 4 respectively, and the water outlet 3 is higher than the slag discharge port 4 in height, so that the water outlet 3 can be effectively prevented from being blocked by the solid waste residue.
After gas-liquid cyclone operated a period, utilize and spray ball 11 and connect outside gas, the liquid source, regularly wash 5 inner walls of lid and silk screen demister 9, can prolong the change time of silk screen, reduce the maintenance of equipment cost, spray ball 11 and can adopt the telescopic rotation type to spray the ball, the injection angle is 360, compare with traditional fixed ball that sprays, the rotation type sprays the ball and can form great liquid drop and evenly spray, the cleaning performance is good, can save the quantity of water and cleaner simultaneously. When the internal equipment of separator body abnormal operation or damage, open the sealing member 13 that manhole 6 department set up, the maintainer gets into the separator body through manhole 6 in, overhauls the internal instrument, or dismantles and changes the silk screen of silk screen demister 9.
The preferred embodiments of the present invention disclosed above are intended only to help illustrate the present invention. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and its practical applications, to thereby enable others skilled in the art to best understand the invention for and utilize the invention. The present invention is limited only by the claims and their full scope and equivalents.
Claims (6)
1. The utility model provides a gas-liquid cyclone, includes the separator body, is provided with air inlet, gas outlet, outlet and row's cinder notch on the separator body, its characterized in that: the separator body includes:
a cover body arranged on the top of the separator body, the air outlet is arranged at the top of the cover body;
the manhole is arranged on the top surface of the cover body and used for maintenance;
the conical cylinder is arranged at the bottom of the separator body and used for separating secondary steam, the air inlet is tangentially arranged on the side surface of the conical cylinder, and the water outlet and the slag discharge port are both positioned on the bottom surface of the conical cylinder;
the exhaust core pipe is arranged at the top of the conical cylinder and communicated with the bottom surface of the cover body;
the wire mesh demister is arranged on the bottom surface of the cover body and used for filtering liquid foam in the output airflow;
the spraying ball is arranged on the top surface of the cover body through a mounting assembly and is used for cleaning the inner wall of the cover body and the wire mesh demister;
and the spiral blade is arranged on the periphery of the exhaust core pipe, extends to the bottom of the conical cylinder and is used for guiding flow.
2. A gas-liquid cyclone separator according to claim 1, wherein: the cover body and the conical cylinder are integrally arranged.
3. A gas-liquid cyclone separator according to claim 1, wherein: the top of the exhaust core pipe is funnel-shaped.
4. A gas-liquid cyclone separator according to claim 1, wherein: the wire mesh demister is a wave-shaped wire mesh demister.
5. A gas-liquid cyclone separator according to claim 1, wherein: the spraying ball is a rotary spraying ball, and the spraying ball and the cover body are detachably connected.
6. A gas-liquid cyclone separator according to claim 1, wherein: the aperture of the manhole is set to be 500mm, and a sealing element is arranged at the manhole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222023780.4U CN217961660U (en) | 2022-08-01 | 2022-08-01 | Gas-liquid cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222023780.4U CN217961660U (en) | 2022-08-01 | 2022-08-01 | Gas-liquid cyclone separator |
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| Publication Number | Publication Date |
|---|---|
| CN217961660U true CN217961660U (en) | 2022-12-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222023780.4U Active CN217961660U (en) | 2022-08-01 | 2022-08-01 | Gas-liquid cyclone separator |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116983760A (en) * | 2023-09-26 | 2023-11-03 | 长沙恒宇节能环保科技有限公司 | Desulfurizing and dedusting device for tail gas of water glass kiln |
-
2022
- 2022-08-01 CN CN202222023780.4U patent/CN217961660U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116983760A (en) * | 2023-09-26 | 2023-11-03 | 长沙恒宇节能环保科技有限公司 | Desulfurizing and dedusting device for tail gas of water glass kiln |
| CN116983760B (en) * | 2023-09-26 | 2024-01-09 | 长沙恒宇节能环保科技有限公司 | Desulfurizing and dedusting device for tail gas of water glass kiln |
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