CN214764329U - Vertical gas-liquid separator - Google Patents
Vertical gas-liquid separator Download PDFInfo
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- CN214764329U CN214764329U CN202121086978.6U CN202121086978U CN214764329U CN 214764329 U CN214764329 U CN 214764329U CN 202121086978 U CN202121086978 U CN 202121086978U CN 214764329 U CN214764329 U CN 214764329U
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Abstract
The utility model discloses a vertical vapour and liquid separator, including the shell, its characterized in that is still including setting up gas-liquid separation barrel in the shell, the left side wall intercommunication of gas-liquid separation barrel inner chamber has the air inlet, the right side wall intercommunication of gas-liquid separation barrel inner chamber has the leakage fluid dram, gas-liquid separation barrel top intercommunication has the gas outlet, one side of gas outlet is equipped with the motor, the table wall from the top down of fixed column has bolted first gas-liquid separation mechanism and second gas-liquid separation mechanism, motor drive first gas-liquid separation mechanism with second gas-liquid separation mechanism rotates, first gas-liquid separation mechanism with second gas-liquid separation mechanism all is in gas-liquid separation barrel inner chamber. The gas-liquid separator can completely separate gas and liquid, improves the separation precision, saves resources and reduces the cost. The utility model has the advantages that: the gas-liquid separator is matched with each mechanism to sufficiently separate gas from liquid.
Description
Technical Field
The utility model relates to a separator technical field, in particular to vertical vapour and liquid separator.
Background
The gas-liquid separator can be arranged at an inlet and an outlet of a gas compressor for gas-liquid separation, gas phase demisting after a condensing cooler on the top of a fractionating tower, gas phase demisting of various gas washing towers, absorption towers and analysis towers, and the like, and can also be applied to various industrial and civil occasions such as gas dust removal, oil-water separation, liquid impurity removal and the like.
However, the conventional gas-liquid separator often cannot completely separate the liquid in the gas, and the unseparated gas carries the liquid to corrode equipment parts such as pipelines and instruments for a long time, so that the service life of the equipment parts is shortened, the separation accuracy is poor, the use of the gas in the next step is influenced, and the operating cost is increased.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a vertical vapour and liquid separator, it can separate the gas-liquid completely, improves the separation precision, resources are saved, reduce cost.
The embodiment of the utility model is realized like this:
the application provides a vertical gas-liquid separator, which comprises a shell and a gas-liquid separation barrel arranged in the shell, wherein sealing plates are arranged at two ends of the gas-liquid separation barrel, the edge of each sealing plate is connected with the inner cavity of the gas-liquid separation barrel, the left side wall of the inner cavity of the gas-liquid separation barrel is communicated with an air inlet, the right side wall of the inner cavity of the gas-liquid separation barrel is communicated with a liquid outlet, the top of the gas-liquid separation barrel is communicated with an air outlet, one side of the air outlet is provided with a motor, and the output end of the motor penetrates through the top of the shell and penetrates through the gas-liquid separation barrel; the inner cavity of the gas-liquid separation barrel comprises a fixed column connected with the top of the shell, a first gas-liquid separation mechanism and a second gas-liquid separation mechanism are bolted to the surface wall of the fixed column from top to bottom, the motor drives the first gas-liquid separation mechanism and the second gas-liquid separation mechanism to rotate, and the first gas-liquid separation mechanism and the second gas-liquid separation mechanism are both arranged in the inner cavity of the gas-liquid separation barrel.
In the prior art, separation methods such as gravity settling, centrifugal separation, filtering separation and electric power settling are mainly adopted, but liquid in gas cannot be completely separated, unseparated gas carries liquid to corrode equipment parts such as pipelines and instruments for a long time, the service life of the equipment parts can be shortened, the separation precision is poor, the use of next-step gas can be influenced, and the operating cost is increased.
In combination with the technical scheme provided by the above, in some possible implementation manners, the first gas-liquid separation mechanism comprises a diagonal flow plate and scattering blades, and the scattering blades are uniformly distributed on the fixed column on the circumference; the oblique flow plate is sequentially bolted to the tops of two sides of the inner cavity of the gas-liquid separation barrel from top to bottom, one end, far away from the inner cavity of the gas-liquid separation barrel, of the oblique flow plate and the outer side wall of the fixed column form a hole for gas-liquid circulation, and the hole and the scattering blades are arranged oppositely.
In the embodiment of the application, the scattering blades scatter water molecules in the air, the oblique flow plates can separate liquid in the air, so that the separated gas obliquely flows upwards, and the liquid is condensed and falls by the oblique flow plates; the falling liquid falls downwards due to the factor of gravity after the falling liquid passes through the scattering blades; the scattering blades can be selectively flood dragon blades.
In some possible implementation manners, the ends, close to each other, of the oblique flow plates are all inclined downwards, and the number of the oblique flow plates is not less than 2.
In embodiments of the present application, the oblique flow of gas as it rises provides sufficient gravity separation of the liquid entrained in the gas.
In some possible implementation manners, the second gas-liquid separation mechanism includes a rotating plate bolted to the fixed column, and in a working state, the rotating plate is driven by the motor to rotate in the inner cavity of the gas-liquid separation cylinder; the shape of the rotating plate is spiral.
In the embodiment of the application, when the motor is driven, the spiral rotating plate rotates, and when the gas entering upwards from the gas inlet is spirally lifted, gas-liquid separation is performed due to the action of gravity, so that the gas-liquid separation effect is enhanced.
In some possible implementation manners, a filter plate is arranged between the first gas-liquid separation mechanism and the second gas-liquid separation mechanism.
In the embodiment of the application, the filter plate can perform multiple adsorption coagulation sedimentation effects on the liquid in the gas.
By integrating the technical scheme, in some possible implementation modes, a cavity is arranged in the fixed column, and the outer wall of the cavity is provided with a plurality of through holes connected with the inner cavity of the gas-liquid separation cylinder.
In the embodiment of this application, the outer wall of cavity is equipped with the through-hole, the through-hole passes the outer wall of fixed column and links to each other with gas-liquid separation barrel inner chamber.
According to the technical scheme, in some possible implementation modes, an air pipe is communicated with the cavity, one end, far away from the cavity, of the air pipe is connected with a hot air pump, and hot air provided by the hot air pump is communicated to the inner cavity of the gas-liquid separation barrel through the air pipe.
In the embodiment of this application, provide hot gas when the heat pump and lead to the cavity through the trachea, and then dry the hydrone of gas-liquid separation barrel inner chamber with hot gas through the through-hole.
By integrating the technical scheme, in some possible implementation modes, the lower part of the second gas-liquid separation mechanism is provided with a wire mesh inclined plane, the included angle between the wire mesh inclined plane and the horizontal plane is 45 degrees, the gas inlet is right opposite to the wire mesh inclined plane, and the gas of the gas inlet is communicated with the inner cavity of the gas-liquid separation cylinder through the wire mesh inclined plane.
In the embodiment of the application, after the moisture sinks to the second gas-liquid separation mechanism, the moisture flows to the liquid discharge port along the 45-degree included angle between the inclined surface of the silk screen and the horizontal plane, and the redundant moisture is discharged.
In combination with the technical scheme provided above, in some possible implementation manners, a drain outlet is arranged at the lowest point of the bottom of the gas-liquid separation cylinder body.
In the embodiment of this application, gaseous back that passes through the air inlet, be mingled with liquid in the gas and can pass through the filter screen on the shrouding and discharge outside the barrel, retrieve.
In combination with the above technical solutions, in some possible implementations, an O-ring is disposed between the sealing plate and the housing.
In the embodiment of the present application, the O-ring may prevent leakage of gas.
Because of the extension, when the liquid and the gas flow together due to the density difference of the gas and the liquid, if the gas meets the barrier, the gas can be deflected away, and the liquid continues to have a forward speed due to the inertia, and the forward liquid is attached to the wall surface of the barrier, is gathered together downwards due to the gravity and is discharged through a discharge pipe. A large amount of water-containing steam enters the steam-water separator and moves downwards in a centrifugal inclined mode; the entrained water is separated out as a result of the reduction in velocity; the separated liquid flow is discharged through a liquid outlet, and the dry and clean gas is discharged from a separator outlet.
Compared with the prior art, the utility model, following advantage and beneficial effect have:
1. the utility model relates to a vertical vapour and liquid separator, the utility model discloses a first gas-liquid separation mechanism with mutually supporting of second gas-liquid separation mechanism, when can making the gas-liquid get into gas-liquid separation barrel inner chamber, carry out preliminary gravity to great liquid in the gas and subside the back, break up the liquid in the gas, the separation, make the gas oblique flow after the separation rise, break up through the separator on the fixed column again, it subsides to last centrifugation gas and liquid, liquid is condensed by oblique flow plate and falls down, liquid falls down the back, rethread second gas-liquid separation mechanism's rotor plate can break up the separation to the gas-liquid mixture that has not yet separated in the gas through rotary motion, receive the influence of gravity, separated liquid is discharged through the leakage fluid dram, gas after the separation upwards discharges through the gas outlet.
2. The utility model relates to a vertical vapour and liquid separator through establishing the cavity in the fixed column, and the cavity in-connection has the trachea, and trachea one end is connected with the heat pump, and the steam that the heat pump will provide passes through the trachea and accesss to gas-liquid separation barrel inner chamber, and the liquid in the air can be dried by the steam that produces through the heat pump, can last high-efficient stoving to the liquid that carries in the gas to reach and fully separate the liquid in the gas.
Drawings
The accompanying drawings, which are included to provide a further understanding of the embodiments of the invention and are incorporated in and constitute a part of this application, illustrate embodiment(s) of the invention and together with the description serve to explain the principles of the invention. In the drawings:
fig. 1 is a schematic view of the overall structure provided by the embodiment of the present invention.
Fig. 2 is a partially enlarged view of the area of fig. 1A.
Fig. 3 is a partially enlarged view of the area of fig. 1B.
1-air inlet, 2-air outlet, 3-liquid outlet, 4-sewage outlet, 5-fixed column, 6-outer shell, 7-silk screen inclined plane, 8-rotating plate, 9-sealing plate, 10-inclined flow plate, 11-motor, 12-separator, 13-scattering blade, 14-cavity, 15-through hole, 16-air pipe, 17-liquid collecting tank and 18-hot air pump.
Detailed Description
To make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail below with reference to the following examples and drawings, and the exemplary embodiments and descriptions thereof of the present invention are only used for explaining the present invention, and are not intended as limitations of the present invention.
Examples
Referring to fig. 1-3, an embodiment of the present application provides a vertical gas-liquid separator 12, including a housing 6, and further including a gas-liquid separation cylinder disposed in the housing 6, where two ends of the gas-liquid separation cylinder are provided with closing plates 9, an edge of the closing plates 9 is connected to an inner cavity of the gas-liquid separation cylinder, a left side wall of the inner cavity of the gas-liquid separation cylinder is communicated with an air inlet 1, a right side wall of the inner cavity of the gas-liquid separation cylinder is communicated with a liquid outlet 3, a top of the gas-liquid separation cylinder is communicated with an air outlet 2, one side of the air outlet 2 is provided with a motor 11, and an output end of the motor 11 penetrates through the top of the housing 6 and penetrates through the gas-liquid separation cylinder; the inner cavity of the gas-liquid separation barrel comprises a fixed column 5 connected with the top of the shell 6, a first gas-liquid separation mechanism and a second gas-liquid separation mechanism are bolted to the surface wall of the fixed column 5 from top to bottom, the motor 11 drives the first gas-liquid separation mechanism and the second gas-liquid separation mechanism to rotate, and the first gas-liquid separation mechanism and the second gas-liquid separation mechanism are both arranged in the inner cavity of the gas-liquid separation barrel.
Optionally, the first gas-liquid separation mechanism includes a diagonal flow plate 10 and scattering blades 13, and the scattering blades 13 are uniformly distributed on the fixed column 5 along the circumference; the inclined flow plate 10 is sequentially bolted to the tops of two sides of the inner cavity of the gas-liquid separation cylinder from top to bottom, one end of the inclined flow plate 10, far away from the inner cavity of the gas-liquid separation cylinder, and the outer side wall of the fixed column 5 form a hole for gas-liquid circulation, and the hole is opposite to the scattering blades 13; the scattering blades 13 scatter water molecules in the air, the inclined flow plate 10 can separate liquid in the air, so that the separated gas obliquely flows upwards, and the liquid is condensed and falls by the inclined flow plate 10; the falling liquid falls downwards due to the factor of gravity through the dispersing blades 13; the scattering blades 13 can be flood dragon blades.
Preferably, the top end of the fixed column 5 is provided with a separator 12, when part of the gas carries a little liquid to the position of the separator 12, the separator 12 will break up and separate the gas again, the water molecules will settle down due to gravity, and the gas thief will rise to the gas outlet 2.
Optionally, the ends, close to each other, of the oblique flow plates 10 are all inclined downwards, and the number of the oblique flow plates 10 is not less than 2; when the gas oblique flow rises, the liquid carried in the gas can be fully separated by gravity.
Optionally, the second gas-liquid separation mechanism includes a rotating plate 8 bolted to the fixed column 5, and in a working state, the rotating plate 8 is driven by the motor 11 to rotate in the inner cavity of the gas-liquid separation cylinder; the rotating plate 8 is spiral in shape; when driven by the motor 11, the spiral rotating plate 8 rotates to spirally lift the gas entering from the gas inlet 1 upwards, and the gas and the liquid are separated by gravity, so that the gas and liquid separation effect of the gas is enhanced.
Optionally, a filter plate is arranged between the first gas-liquid separation mechanism and the second gas-liquid separation mechanism; the filter plate can adsorb, condense and settle liquid in gas for many times.
Optionally, a cavity 14 is arranged in the fixed column 5, the outer wall of the cavity 14 is provided with a plurality of through holes 15 connected with the inner cavity of the gas-liquid separation barrel, the outer wall of the cavity 14 is provided with the through holes 15, and the through holes 15 penetrate through the outer wall of the fixed column 5 to be connected with the inner cavity of the gas-liquid separation barrel.
Optionally, an air pipe 16 is communicated in the cavity 14, a heat air pump 18 is connected to one end of the air pipe 16 away from the cavity 14, and the heat air pump 18 leads the provided hot air to the inner cavity of the gas-liquid separation cylinder through the air pipe 16; when the hot air pump 18 provides hot air to the cavity 14 through the air pipe 16, the hot air is further dried by the water molecules in the inner cavity of the gas-liquid separation cylinder through the through hole 15.
Preferably, the air pipe 16 is connected with the hot air pump 18 through a liquid collecting tank 17, the liquid collecting tank 17 is arranged on a pipe of the air pipe 16 leading to the hot air pump 18, when the moisture in the inner cavity of the gas-liquid separation cylinder falls down due to the action of gravity, fine water molecules can be dried, and the redundant moisture can be brought into the liquid collecting tank 17.
Optionally, a wire mesh inclined plane 7 is arranged at the lower part of the second gas-liquid separation mechanism, an included angle between the wire mesh inclined plane 7 and a horizontal plane is 45 degrees, the gas inlet 1 is over against the wire mesh inclined plane 7, and gas in the gas inlet 1 is communicated with an inner cavity of the gas-liquid separation cylinder through the wire mesh inclined plane 7; when the water is settled to the second gas-liquid separation mechanism, the water flows to the liquid discharge port 3 along the 45-degree included angle between the silk screen inclined plane 7 and the horizontal plane, and the redundant water is discharged, wherein the 45-degree included angle or the 60-degree included angle is applicable as long as the water can flow out along the silk screen inclined plane 7.
Optionally, a drain outlet 4 is arranged at the lowest point of the bottom of the gas-liquid separation barrel; after the gas passes through the gas inlet 1, the liquid mixed in the gas is discharged out of the cylinder body through the filter screen on the sealing plate 9 and is recovered.
Optionally, an O-ring seal is disposed between the sealing plate 9 and the housing 6; the O-shaped sealing ring can prevent gas leakage.
It should be noted that the common gas-water separator 12 has a partition type, a packing type, or a cyclone type, and the utility model is a vertical gas-liquid separator 12.
The working principle of the utility model is as follows: gas enters the barrel through the gas inlet 1 for primary separation, sewage is mixed and discharged from the sewage outlet 4 through the sealing plate 9 under the action of gravity, part of the gas can be filtered and ascended through the silk screen inclined plane 7 and firstly enters the second gas-liquid separation mechanism, after primary gravity sedimentation is carried out on larger liquid in the gas, the liquid in the gas is scattered and separated, so that the separated gas obliquely ascends, the gas and the liquid are continuously centrifugally settled and then enter the first gas-liquid separation mechanism, the scattering blades 13 scatter water molecules in the air, the oblique flow plate 10 can separate the liquid in the gas, the separated gas obliquely ascends, and the liquid is condensed and falls by the oblique flow plate 10; part of liquid rises to separator 12, and separator 12 can be continuously broken up gas-liquid, and the liquid that falls because of the factor of gravity through breaking up blade 13, and after the liquid fell down, the rotor plate 8 of rethread second gas-liquid separation mechanism can break up the separation to the gas-liquid mixture that has not separated in the gas through rotary motion, receives the influence of gravity, and the liquid that separates is discharged through leakage fluid dram 3, and the gas after the separation upwards discharges through gas outlet 2.
To sum up, the utility model discloses can separate the gas-liquid completely, improve the separation precision, resources are saved, reduce cost.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate the position or positional relationship based on the position or positional relationship shown in the drawings, or the position or positional relationship which is usually placed when the product of the present invention is used, and are only for convenience of description and simplification of the description, but do not indicate or imply that the device or element referred to must have a specific position, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," "third," and the like are used solely to distinguish one from another and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The above-mentioned embodiments, further detailed description of the objects, technical solutions and advantages of the present invention, it should be understood that the above description is only the embodiments of the present invention, and is not intended to limit the scope of the present invention, and any modifications, equivalent substitutions, improvements, etc. made within the spirit and principle of the present invention should be included in the scope of the present invention.
Claims (10)
1. The vertical gas-liquid separator comprises a shell (6) and is characterized by further comprising a gas-liquid separation barrel arranged in the shell (6), sealing plates (9) are arranged at two ends of the gas-liquid separation barrel, the edge of each sealing plate (9) is connected with the inner cavity of the gas-liquid separation barrel, the left side wall of the inner cavity of the gas-liquid separation barrel is communicated with an air inlet (1), the right side wall of the inner cavity of the gas-liquid separation barrel is communicated with a liquid outlet (3), the top of the gas-liquid separation barrel is communicated with an air outlet (2), a motor (11) is arranged on one side of the air outlet (2), and the output end of the motor (11) penetrates through the top of the shell (6) and penetrates through the gas-liquid separation barrel;
the inner cavity of the gas-liquid separation barrel comprises a fixing column (5) connected with the top of the shell (6), a first gas-liquid separation mechanism and a second gas-liquid separation mechanism are bolted to the surface wall of the fixing column (5) from top to bottom, the motor (11) drives the first gas-liquid separation mechanism and the second gas-liquid separation mechanism to rotate, and the first gas-liquid separation mechanism and the second gas-liquid separation mechanism are both arranged in the inner cavity of the gas-liquid separation barrel.
2. The vertical gas-liquid separator according to claim 1 wherein said first gas-liquid separating means comprises a diagonal flow plate (10) and dispersing blades (13), said dispersing blades (13) being circumferentially and uniformly distributed on said stationary column (5);
the inclined flow plate (10) is sequentially bolted to the tops of two sides of the inner cavity of the gas-liquid separation cylinder from top to bottom, one end, far away from the inner cavity of the gas-liquid separation cylinder, of the inclined flow plate (10) and the outer side wall of the fixed column (5) form a hole for gas-liquid circulation, and the hole and the scattering blades (13) are arranged oppositely.
3. The vertical gas-liquid separator according to claim 2 wherein the ends of said diagonal flow plates (10) adjacent to each other are inclined downward, and the number of said diagonal flow plates (10) is not less than 2.
4. The vertical gas-liquid separator as claimed in claim 1, wherein the second gas-liquid separation mechanism comprises a rotating plate (8) bolted to the fixed column (5), and in an operating state, the rotating plate (8) is driven by the motor (11) to rotate in the inner cavity of the gas-liquid separation cylinder; the shape of the rotating plate (8) is spiral.
5. The vertical gas-liquid separator according to claim 1 wherein a filter plate is disposed between said first gas-liquid separating means and said second gas-liquid separating means.
6. The vertical gas-liquid separator according to claim 1, wherein a cavity (14) is arranged in the fixed column (5), and a plurality of through holes (15) connected with the inner cavity of the gas-liquid separation cylinder are formed in the outer wall of the cavity (14).
7. The vertical gas-liquid separator according to claim 6, wherein an air pipe (16) is communicated with the cavity (14), a hot air pump (18) is connected to one end of the air pipe (16) far away from the cavity (14), and the hot air pump (18) is used for supplying hot air to the inner cavity of the gas-liquid separation cylinder through the air pipe (16).
8. The vertical gas-liquid separator according to claim 1, wherein the lower part of the second gas-liquid separation mechanism is provided with a wire mesh inclined plane (7), the wire mesh inclined plane (7) forms an angle of 45 degrees with the horizontal plane, the gas inlet (1) is opposite to the wire mesh inclined plane (7), and the gas in the gas inlet (1) is communicated with the inner cavity of the gas-liquid separation cylinder through the wire mesh inclined plane (7).
9. The vertical gas-liquid separator as claimed in claim 1, wherein the lowest point of the bottom of the gas-liquid separation cylinder is provided with a sewage draining outlet (4).
10. The vertical gas-liquid separator according to claim 1, wherein an O-ring seal is provided between said closure plate (9) and said housing (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121086978.6U CN214764329U (en) | 2021-05-20 | 2021-05-20 | Vertical gas-liquid separator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121086978.6U CN214764329U (en) | 2021-05-20 | 2021-05-20 | Vertical gas-liquid separator |
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| Publication Number | Publication Date |
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| CN214764329U true CN214764329U (en) | 2021-11-19 |
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| CN202121086978.6U Active CN214764329U (en) | 2021-05-20 | 2021-05-20 | Vertical gas-liquid separator |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116907133A (en) * | 2023-09-12 | 2023-10-20 | 扬州市华淼净化设备有限公司 | Gas-liquid separator |
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2021
- 2021-05-20 CN CN202121086978.6U patent/CN214764329U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116907133A (en) * | 2023-09-12 | 2023-10-20 | 扬州市华淼净化设备有限公司 | Gas-liquid separator |
| CN116907133B (en) * | 2023-09-12 | 2023-11-24 | 扬州市华淼净化设备有限公司 | Gas-liquid separator |
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