CN117654199B - Efficient two-stage cyclone tube bundle type gas-liquid separator and application method thereof - Google Patents
Efficient two-stage cyclone tube bundle type gas-liquid separator and application method thereof Download PDFInfo
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- CN117654199B CN117654199B CN202311811169.0A CN202311811169A CN117654199B CN 117654199 B CN117654199 B CN 117654199B CN 202311811169 A CN202311811169 A CN 202311811169A CN 117654199 B CN117654199 B CN 117654199B
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- 239000007788 liquid Substances 0.000 title claims abstract description 194
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000000926 separation method Methods 0.000 claims abstract description 79
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000000203 mixture Substances 0.000 claims abstract description 38
- 230000008569 process Effects 0.000 claims abstract description 15
- 238000004804 winding Methods 0.000 claims abstract description 15
- 230000009471 action Effects 0.000 claims abstract description 11
- 230000001105 regulatory effect Effects 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims description 14
- 239000006260 foam Substances 0.000 claims description 14
- 230000008859 change Effects 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 7
- 239000012535 impurity Substances 0.000 claims description 6
- 238000012423 maintenance Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000011148 porous material Substances 0.000 claims description 4
- 238000005096 rolling process Methods 0.000 claims description 4
- 241000883990 Flabellum Species 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 230000008595 infiltration Effects 0.000 claims description 2
- 238000001764 infiltration Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims description 2
- 230000001737 promoting effect Effects 0.000 claims description 2
- 239000003351 stiffener Substances 0.000 claims 3
- 239000007787 solid Substances 0.000 claims 2
- 108010066057 cabin-1 Proteins 0.000 description 18
- 230000003014 reinforcing effect Effects 0.000 description 6
- 230000000149 penetrating effect Effects 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000003750 conditioning effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/06—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums
- B01D33/11—Filters with filtering elements which move during the filtering operation with rotary cylindrical filtering surfaces, e.g. hollow drums arranged for outward flow filtration
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Abstract
The invention discloses a high-efficiency two-stage cyclone tube bundle type gas-liquid separator, which relates to the technical field of gas-liquid separation and comprises the following components: the separating cabin is fixedly embedded with a liquid inlet pipe at one side. According to the invention, the liquid pump is started, so that the gas-liquid mixture is pumped out by pressurizing the liquid pump and is discharged through the liquid inlet pipe, the water outlet speed of the liquid inlet pipe is controlled by pulling the current limiting net rack at the moment under the action of the elastic band, the phenomenon that the flushed water flows excessively due to the drop of the liquid inlet pipe is avoided, when the water flow needs to be regulated, only the electromagnetic valve is required to be started, so that a part of the gas-liquid mixture pumped out by the liquid pump enters the inside of the split pipe, the fan blade is impacted under the guidance of the guide plate, the rotary pipe rotates around the positioning rod, the pull rope is wound in the winding groove, the current limiting net rack is pulled in the winding process by the pull rope, the current limiting net rack is pulled into the split pipe, and the internal channel of the liquid inlet pipe is opened at the moment.
Description
Technical Field
The invention relates to the technical field of gas-liquid separation, in particular to a high-efficiency two-stage cyclone tube bundle type gas-liquid separator and a use method thereof.
Background
Gas-liquid separators are devices for separating gas and liquid, which are often mixed together in many industrial and process applications, and the function of the gas-liquid separator is to separate them effectively to ensure proper operation of the system and to prevent unnecessary loss of material, two-stage swirl tube bundle gas-liquid separators are a common type of gas-liquid separator consisting of two swirl tube bundles for effecting separation of gas and liquid.
In the prior art, when the liquid mixed with gas is separated in the separator, fluid directly rushes into the upper-stage cyclone tube bundle, so that high-speed fluid generates centrifugal force in rotation, but the water flow of the fluid rushes into the upper-stage cyclone tube bundle can not be controlled, the gas is brought out together by the excessively high initial water flow, the water flow can only be increased by pressurizing a pump when the initial water flow is excessively small, and the energy consumption is increased.
Therefore, we propose a high-efficiency two-stage cyclone tube bundle type gas-liquid separator and a use method thereof so as to solve the problems set forth above.
Disclosure of Invention
The invention aims to provide a high-efficiency two-stage cyclone tube bundle type gas-liquid separator and a use method thereof, so as to solve the problem that the existing gas-liquid separator provided by the background art cannot control water flow.
In order to achieve the above purpose, the present invention provides the following technical solutions: a high efficiency two stage cyclone tube bundle gas-liquid separator comprising: the liquid inlet pipe is fixedly embedded at one side of the separation cabin; the regulating assembly comprises a shunt tube, wherein two ends of the shunt tube are communicated with the outer surface of a liquid inlet tube, one end of the shunt tube penetrates through the separation cabin to the inside, an electromagnetic valve is arranged on the rear surface of the shunt tube, a guide plate is fixedly arranged on one side inner wall of the shunt tube, a positioning rod is fixedly connected between the opposite inner walls of the shunt tube, a rotating tube is sleeved on the outer surface of the positioning rod in a rotating mode, a plurality of fan blades are fixedly arranged on the outer surface of the rotating tube close to two ends, a winding groove is formed in the middle of the outer surface of the rotating tube, a pull rope is wound on the inner wall of the winding groove, a current-limiting net rack is fixedly arranged at one end of the pull rope, the outer surface of the current-limiting net rack is connected with the inner wall of the shunt tube in a sliding mode, a supporting rod is fixedly connected between the inner walls of the current-limiting net rack, and an elastic band is fixedly arranged on the inner wall of the liquid inlet tube and is sleeved outside the supporting rod.
Preferably, an auxiliary frame is fixedly arranged on one side of the separation cabin, a liquid pump is arranged at the top of the auxiliary frame, the output end of the liquid pump is fixedly communicated with one end of the liquid inlet pipe, and the outlet of the other end of the liquid inlet pipe is in a bevel connection.
Preferably, the inner wall of the separation cabin is fixedly connected with a cyclone plate, and the inner wall of the cyclone plate is fixedly connected with a liquid baffle plate.
Preferably, the inner wall of the separation cabin is fixedly connected with a separation hopper near the bottom of the cyclone plate, the bottom end of the separation hopper is fixedly communicated with a reinforcing ring, and the outer surface of the reinforcing ring is provided with a rotary groove.
Preferably, the outside of strengthening ring rotates the cover and is equipped with filtering component, filtering component is including filtering the box, the inner wall fixed mounting of filtering the box has the elasticity spacing ring, the surface of elasticity spacing ring rotates with the inner wall of change groove to be connected, a plurality of filtration pores have been seted up to the surface of filtering the box.
Preferably, the inner wall of the filter box is fixedly connected with a fixed ring, and a plurality of vortex blades are fixedly arranged on the inner wall of the fixed ring.
Preferably, the top of separation cabin is fixed to be inlayed and is equipped with exhaust assembly, exhaust assembly is including the venthole, the top fixed intercommunication of venthole has the blast pipe, the bottom fixedly connected with of venthole a plurality of dead levers, a plurality of fixed mounting has a plurality of umbrella boards between the surface of dead lever, every a plurality of ventholes have all been seted up to the surface of umbrella board, the inner wall of venthole is close to bottom department and installs the foam net.
Preferably, the bottom fixed intercommunication of separation cabin has the fluid-discharge tube, the one end fixed intercommunication of fluid-discharge tube has the drain pipe, the one end fixed mounting of drain pipe has the installation cover, the surface of drain pipe sets up the check valve.
Preferably, the outer surface of the separation cabin is close to the bottom and fixedly connected with a mounting ring, the bottom of the mounting ring is fixedly connected with a plurality of support columns, a plurality of bottom rings are fixedly connected between the bottom ends of the support columns, and a maintenance port is formed in the outer surface of the separation cabin.
The application method of the high-efficiency two-stage cyclone tube bundle type gas-liquid separator comprises the following steps:
S1, a liquid pump is started to pump out a gas-liquid mixture under pressure, and then the gas-liquid mixture is discharged through a liquid inlet pipe, so that the speed of water outlet of the liquid inlet pipe is controlled by pulling of an elastic belt by a current limiting net rack at the moment, the overflow of the flushed water caused by the drop of the liquid inlet pipe is avoided, when the water flow needs to be regulated, only an electromagnetic valve is required to be started, a part of the gas-liquid mixture pumped out by the liquid pump enters the inside of a shunt pipe, a fan blade is impacted under the guidance of a guide plate, the rotary pipe rotates around a positioning rod, a pull rope is wound in a winding groove, the current limiting net rack is pulled in the winding process by the pull rope, the current limiting net rack is pulled into the shunt pipe, the internal channel of the liquid inlet pipe is opened at the moment, and the flow speed of the liquid inlet pipe is improved;
s2, the gas-liquid mixture directly rushes to the cyclone plate, most of the gas-liquid mixture is blocked by the liquid blocking plate, so that the gas-liquid mixture is accelerated to flow downwards along the rotation direction of the cyclone plate, centrifugal force is generated in the downward flowing process, the gas-liquid mixture continuously rotates along the inner wall of the second-stage separation hopper under the action of the centrifugal force, gas and liquid are separated by the centrifugal force, the liquid is dragged to the vicinity of the inner wall of the separation hopper, the gas is concentrated in the center, and the fluid continuously flows downwards;
S3, separating out liquid and discharging the liquid through a liquid discharge pipe, wherein when the gas is discharged upwards, the gas passes through an umbrella plate, the water drops mixed in the gas are condensed into big water drops, the gas continues to move upwards through an air outlet, and finally the gas passes through a foam net, so that the foam net is denser and finer, the water vapor mixed in the gas is completely discharged, in addition, when the gas-liquid mixture is downwards flushed, part of the water vapor is splashed out of the liquid baffle plate, and then the water vapor is discharged under the action of the umbrella plate and the foam net;
S4, through promoting the filter cartridge, make elasticity spacing ring card go into the change inslot, then liquid when the separation that is fighting through the separation flows, just can dash vortex blade, constantly alternately strike vortex blade, can drive the filter cartridge and rotate, liquid after the separation can filter impurity particle when the through-hole, and pivoted filter cartridge can accelerate the speed of liquid infiltration filter hole, outwards pull out the filter cartridge can during the cleanness, through the switch check valve, can control the drainage situation of fluid-discharge tube.
Compared with the prior art, the invention has the beneficial effects that:
1. When the liquid pump is used, the liquid pump is started to pump the gas-liquid mixture under pressure, and then the gas-liquid mixture is discharged through the liquid inlet pipe, so that the speed of water outlet of the liquid inlet pipe is controlled by the pulling of the elastic band by the current limiting net rack at the moment, the overflow of the flushed water caused by the drop of the liquid inlet pipe is avoided, when the water flow needs to be regulated, only the electromagnetic valve is required to be started, so that a part of the gas-liquid mixture pumped by the liquid pump enters the shunt pipe, the fan blade is impacted under the guidance of the guide plate, the rotary pipe rotates around the positioning rod, the pull rope is wound in the winding groove, the current limiting net rack is pulled in the winding process by the pull rope, the internal channel of the liquid inlet pipe is opened at the moment, and the flow speed of the flow to the cyclone plate is improved;
2. When the cyclone separator is used, the liquid baffle can block most of gas-liquid mixture, so that the gas-liquid mixture can accelerate to flow downwards along the rotation direction of the cyclone plate, centrifugal force is generated in the process of flowing downwards, the gas-liquid mixture can continuously rotate along the inner wall of the second-stage separation hopper under the action of the centrifugal force, gas and liquid are separated by the centrifugal force, the liquid is dragged to the vicinity of the inner wall of the separation hopper, the gas is concentrated in the center, the gas light is upwards discharged from the gas outlet barrel under the action of the pressure in the separation chamber along with the continuous downward flow of the fluid, the liquid is separated and discharged through the liquid discharge pipe, when the gas upwards moves through the umbrella plate and the foam net, water drops mixed in the gas are condensed into big water drops to fall down, when the liquid flows out through the separation of the separation hopper, the vortex blades are continuously impacted, the vortex blades can be driven to rotate, the separated liquid can filter impurity particles when passing through the filter holes, and the rotating filter box can accelerate the speed of the liquid penetrating the filter holes;
3. When the support device is used, the mounting ring is fixedly arranged outside the separation cabin, so that the support of the support column to the separation cabin is reinforced, the support column supports the separation cabin, the height of the separation cabin is positioned at a position convenient to operate, the bottom ends of the support column are connected together through the fixed bottom ring, the stability of the support column can be enhanced, and the support column is effectively prevented from continuously shaking in the use process.
Drawings
FIG. 1 is a side perspective view of a high efficiency two stage swirl tube bundle gas-liquid separator of the present invention;
FIG. 2 is another angular side perspective view of a high efficiency two stage swirl tube bundle gas-liquid separator of the present invention;
FIG. 3 is a cross-sectional perspective view of a separation chamber of a high-efficiency two-stage cyclone tube bundle type gas-liquid separator of the present invention;
FIG. 4 is a perspective view, partially in section, of an exhaust assembly of a high efficiency two-stage swirl tube bundle gas-liquid separator of the present invention;
FIG. 5 is a partially expanded cross-sectional perspective view of a filter assembly of a high-efficiency two-stage cyclone tube bundle gas-liquid separator of the present invention;
FIG. 6 is another perspective view, partially in section, of the exhaust assembly of a high efficiency two-stage swirl tube bundle gas-liquid separator of the present invention;
FIG. 7 is a perspective view, partially in section, of a conditioning assembly of a high efficiency two stage swirl tube bundle gas-liquid separator of the present invention;
FIG. 8 is a partially expanded cross-sectional perspective view of the conditioning assembly of a high efficiency two-stage swirl tube bundle gas-liquid separator of the present invention.
In the figure:
1. A separation chamber; 2. an exhaust assembly; 201. an air outlet tube; 202. an exhaust pipe; 203. a foam net; 204. a fixed rod; 205. an umbrella plate; 206. an air outlet hole; 3. an adjustment assembly; 301. a shunt; 302. an electromagnetic valve; 303. a deflector; 304. a rotary pipe; 305. a pull rope; 306. a current limiting net rack; 307. an elastic band; 308. a support rod; 309. a positioning rod; 310. a fan blade; 311. a winding groove; 4. a filter assembly; 401. a filter box; 402. filtering holes; 403. an elastic limit ring; 404. a fixing ring; 405. a swirl vane; 5. a mounting ring; 6. a support column; 7. a liquid discharge pipe; 8. a check valve; 9. a mounting sleeve; 10. fixing the bottom ring; 11. an auxiliary frame; 12. a liquid pump; 13. a swirl plate; 14. a liquid baffle; 15. a separating hopper; 16. a liquid inlet pipe; 17. a liquid outlet pipe; 18. a reinforcing ring; 19. a rotary groove; 20. and (5) maintaining the port.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the invention. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Referring to fig. 1-8: a high efficiency two stage cyclone tube bundle gas-liquid separator comprising: the separation cabin 1, one side of the separation cabin 1 is fixedly embedded with a liquid inlet pipe 16; the adjusting component 3, the adjusting component 3 includes the shunt tubes 301, both ends of shunt tubes 301 all are fixed with the surface of feed liquor pipe 16 and communicate, one end of shunt tubes 301 runs through separation cabin 1 to inside, the rear surface of shunt tubes 301 sets up solenoid valve 302, one side inner wall fixed mounting of shunt tubes 301 has guide plate 303, fixedly connected with locating lever 309 between the relative inner wall of shunt tubes 301, the surface rotation cover of locating lever 309 is equipped with changeing pipe 304, the surface that changes pipe 304 is close to both ends department and all fixedly mounted has a plurality of flabellum 310, the rolling groove 311 has been seted up to the surface intermediate department of changeing pipe 304, the inner wall winding of rolling groove 311 has stay cord 305, the one end fixed mounting of stay cord 305 has current-limiting rack 306, the surface of current-limiting rack 306 and the inner wall sliding connection of shunt tubes 301, fixedly connected with bracing piece 308 between the inner wall of current-limiting rack 306, the inner wall of feed liquor pipe 16 is fixed with elastic band 307, the outside at bracing piece 308 is established to elastic band 307 cover.
As shown in fig. 1, 2 and 6, an auxiliary frame 11 is fixedly installed on one side of the separation cabin 1, a liquid pump 12 is arranged at the top of the auxiliary frame 11, the output end of the liquid pump 12 is fixedly communicated with one end of a liquid inlet pipe 16, the outlet of the other end of the liquid inlet pipe 16 is in an inclined opening, and the liquid pump 12 is started by connecting the input end of the liquid pump 12 with a container containing a gas-liquid mixture, so that the gas-liquid mixture is pumped out by pressurization of the liquid pump 12 and then discharged through the liquid inlet pipe 16.
As shown in fig. 3 and 6, the inner wall of the separation chamber 1 is fixedly connected with a cyclone plate 13, the inner wall of the cyclone plate 13 is fixedly connected with a liquid baffle plate 14, and the water outlet of the liquid inlet pipe 16 is inclined to the cyclone plate 13, so that the gas-liquid mixture directly rushes to the cyclone plate 13, and most of the gas-liquid mixture can be blocked by the liquid baffle plate 14, so that the gas-liquid mixture can flow downwards in an accelerating way along the rotation direction of the cyclone plate 13.
As shown in fig. 3 and 5, the inner wall of the separation chamber 1 is fixedly connected with a separation bucket 15 near the bottom of the cyclone plate 13, the bottom end of the separation bucket 15 is fixedly communicated with a reinforcing ring 18, the outer surface of the reinforcing ring 18 is provided with a rotating groove 19, under the action of centrifugal force, the gas-liquid mixture can continuously rotate along the inner wall of the separation bucket 15 of the second stage, the centrifugal force separates gas from liquid, the liquid is dragged to the vicinity of the inner wall of the separation bucket 15, the gas is concentrated in the center, and the filter box 401 can be installed through the rotating groove 19.
As shown in fig. 3 and 5, the outer rotating sleeve of the reinforcing ring 18 is provided with a filter assembly 4, the filter assembly 4 comprises a filter box 401, an elastic limiting ring 403 is fixedly arranged on the inner wall of the filter box 401, the outer surface of the elastic limiting ring 403 is rotationally connected with the inner wall of the rotary groove 19, a plurality of filter holes 402 are formed in the outer surface of the filter box 401, the filter box 401 is pushed, the elastic limiting ring 403 is clamped into the rotary groove 19, separated liquid can filter impurity particles when passing through the filter holes 402, and the filter box 401 is pulled out outwards when being cleaned.
As shown in fig. 3 and 5, the inner wall of the filter box 401 is fixedly connected with a fixing ring 404, the inner wall of the fixing ring 404 is fixedly provided with a plurality of vortex blades 405, when the liquid in the gas-liquid mixture flows out through the separation of the separation bucket 15, the liquid can be flushed into the vortex blades 405, the vortex blades 405 are continuously impacted alternately, the filter box 401 can be driven to rotate, and the rotating filter box 401 can accelerate the speed of the liquid penetrating the filter holes 402.
As shown in fig. 3 and fig. 4, the top of the separation cabin 1 is fixedly embedded with an exhaust component 2, the exhaust component 2 comprises an air outlet barrel 201, the top end of the air outlet barrel 201 is fixedly communicated with an exhaust pipe 202, the bottom of the air outlet barrel 201 is fixedly connected with a plurality of fixing rods 204, a plurality of umbrella plates 205 are fixedly installed between the outer surfaces of the plurality of fixing rods 204, a plurality of air outlet holes 206 are formed in the outer surface of each umbrella plate 205, a foam net 203 is installed on the inner wall of the air outlet barrel 201 close to the bottom end, a plurality of umbrella plates 205 are installed through the fixing rods 204, when the air moves upwards, water drops mixed in the air are condensed into big water drops, the air continues to move upwards through the air outlet holes 206, and finally the foam net 203 is more dense and fine, and water vapor mixed in the air is completely discharged.
As shown in fig. 1-3, the bottom end of the separation chamber 1 is fixedly connected with a liquid discharge pipe 7, one end of the liquid discharge pipe 7 is fixedly connected with a liquid discharge pipe 17, one end of the liquid discharge pipe 17 is fixedly provided with a mounting sleeve 9, the outer surface of the liquid discharge pipe 17 is provided with a check valve 8, the drainage condition of the liquid discharge pipe 7 can be controlled by opening and closing the check valve 8, and the mounting sleeve 9 is used for being connected with an external collecting container.
As shown in fig. 1-3, the outer surface of the separation cabin 1 is fixedly connected with a mounting ring 5 near the bottom, the bottom of the mounting ring 5 is fixedly connected with a plurality of support columns 6, a fixed bottom ring 10 is fixedly connected between the bottom ends of the plurality of support columns 6, the outer surface of the separation cabin 1 is provided with a maintenance opening 20, the maintenance opening 20 is closed in the process of gas-liquid separation, and is opened only when the inside of the separation cabin 1 is overhauled, the mounting ring 5 is fixedly arranged outside the separation cabin 1, so as to strengthen the support of the support columns 6 on the separation cabin 1, the support columns 6 support the separation cabin 1, the height of the separation cabin 1 is in a convenient operation position, the bottom ends of the support columns 6 are connected together through the fixed bottom ring 10, the stability of the support columns 6 can be enhanced, and the support columns 6 are effectively prevented from continuously shaking in the use process.
In the invention, when in use, the mounting ring 5 is fixedly arranged outside the separation cabin 1, in order to strengthen the support of the support column 6 on the separation cabin 1, the support column 6 supports the separation cabin 1, the height of the separation cabin 1 is in a convenient operation position, the bottom ends of the support column 6 are connected together through the fixed bottom ring 10, the stability of the support column 6 can be enhanced, the support column 6 is effectively prevented from continuously shaking in the use process, in the gas-liquid separation process, the input end of the liquid pump 12 is connected with a container containing a gas-liquid mixture, the liquid pump 12 is started, the gas-liquid mixture is pumped out by the pressurization of the liquid pump 12, and then discharged through the liquid inlet pipe 16, then the flow-limiting net rack 306 is pulled by the elastic band 307, the water outlet speed of the liquid inlet pipe 16 is controlled, the phenomenon that the water flowing out of the liquid inlet pipe 16 flows too much due to the drop of the liquid inlet pipe 16 is avoided, when the water flow needs to be regulated, only the electromagnetic valve 302 is required to be opened, so that a part of the gas-liquid mixture pumped by the liquid pump 12 enters the shunt pipe 301, the fan blade 310 is impacted under the guidance of the guide plate 303, the rotating pipe 304 rotates around the positioning rod 309, then the pull rope 305 is wound in the winding groove 311, the pull rope 305 pulls the flow-limiting net rack 306 in the winding process, the flow-limiting net rack 306 is pulled into the shunt pipe 301, at this time, the internal channel of the liquid inlet pipe 16 is opened, the flow velocity flowing to the cyclone plate 13 is increased, the water outlet port of the liquid inlet pipe 16 is inclined to the cyclone plate 13, so that the gas-liquid mixture directly rushes to the cyclone plate 13, most of the gas-liquid mixture is blocked by the liquid blocking plate 14 and flows downwards along the rotation direction of the cyclone plate 13 in an accelerating way, centrifugal force is generated in the downward flowing process, the gas-liquid mixture continuously rotates along the inner wall of the separating hopper 15 of the second stage under the action of the centrifugal force, the gas and the liquid are separated by the centrifugal force, the liquid is dragged to the vicinity of the inner wall of the separating hopper 15, the gas is concentrated in the center and flows downwards along with the continuous flow of the fluid, the gas is light and is discharged upwards from the air outlet barrel 201 under the action of the pressure in the separation cabin 1, the liquid is separated and discharged through the liquid discharge pipe 7, the caliber of the air discharge pipe 202 is small when the gas is discharged upwards, impurities can be prevented from entering the inside of the separation cabin 1 from the pipe orifice, a plurality of umbrella plates 205 are arranged through the fixing rods 204, when the gas moves upwards, water drops mixed in the gas are condensed into big water drops, the gas continues to move upwards through the air outlet holes 206, finally, the foam net 203 is denser and finer, water vapor mixed in the gas is completely discharged, in addition, when the gas-liquid mixture is downwards flushed, part of water drops are splashed out of the liquid baffle plate 14, then water vapor is discharged under the action of the umbrella plate 205 and the foam net 203, the filter box 401 is pushed to enable the elastic limiting ring 403 to be clamped into the rotary groove 19, then liquid is flushed into the vortex blades 405 when separated and discharged through the separating hopper 15, the vortex blades 405 are continuously impacted alternately, the filter box 401 can be driven to rotate, the separated liquid can filter out impurity particles when passing through the filter holes 402, the rotating filter box 401 can accelerate the speed of liquid penetrating through the filter holes 402, the filter box 401 is pulled outwards during cleaning, the drainage condition of the liquid discharge pipe 7 can be controlled by opening and closing the check valve 8, the maintenance port 20 is closed during the gas-liquid separation and is only opened when the interior of the separation chamber 1 is serviced.
The wiring diagrams of the solenoid valve 302 and the liquid pump 12 in the present invention are common knowledge in the art, and the working principle thereof is a known technology, and the model thereof is selected to be an appropriate model according to actual use, so that the control manner and wiring arrangement will not be explained in detail for the solenoid valve 302 and the liquid pump 12.
Although the present invention has been described with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements and changes may be made without departing from the spirit and principles of the present invention.
Claims (5)
1. A high efficiency two stage cyclone tube bundle gas-liquid separator, comprising:
The device comprises a separation cabin (1), wherein a liquid inlet pipe (16) is fixedly embedded at one side of the separation cabin (1);
The adjusting component (3), adjusting component (3) is including shunt tubes (301), the both ends of shunt tubes (301) all are fixed with the surface of feed liquor pipe (16) and communicate, wherein one end of shunt tubes (301) runs through separation cabin (1) to inside, the rear surface of shunt tubes (301) sets up solenoid valve (302), one side inner wall fixed mounting of shunt tubes (301) has guide plate (303), fixed connection has locating lever (309) between the relative inner wall of shunt tubes (301), the surface rotation cover of locating lever (309) is equipped with change pipe (304), change pipe (304) surface and all fixed mounting have a plurality of flabellum (310) near both ends department, change pipe (304) surface intermediate part has seted up rolling groove (311), the inner wall winding of rolling groove (311) has stay cord (305), the one end fixed mounting of stay cord (305) has rack (306), the surface of current limiting rack (306) and the inner wall sliding connection of shunt tubes (301), change between inner wall fixed connection of rack (306) has elastic force of support bar (308), change pipe (307) are fixed in the outside of support bar (307);
The top of the separation cabin (1) is fixedly embedded with an exhaust assembly (2), the exhaust assembly (2) comprises an air outlet cylinder (201), the top end of the air outlet cylinder (201) is fixedly communicated with an exhaust pipe (202), the bottom of the air outlet cylinder (201) is fixedly connected with a plurality of fixing rods (204), a plurality of umbrella plates (205) are fixedly arranged between the outer surfaces of the fixing rods (204), a plurality of air outlet holes (206) are formed in the outer surface of each umbrella plate (205), and a foam net (203) is arranged on the inner wall of the air outlet cylinder (201) close to the bottom end;
The inner wall fixedly connected with whirl board (13) of separation cabin (1), the inner wall fixedly connected with of whirl board (13) keeps off liquid board (14), the inner wall of separation cabin (1) is close to the bottom fixedly connected with separation fill (15) of whirl board (13), the bottom fixed intercommunication of separation fill (15) has stiffener ring (18), change groove (19) have been seted up to the surface of stiffener ring (18), the outside of stiffener ring (18) rotates the cover and is equipped with filter component (4), filter component (4) are including filtration box (401), the inner wall fixed mounting of filtration box (401) has elasticity spacing ring (403), the surface rotation of elasticity spacing ring (403) and change groove (19) is connected, a plurality of filtration pores (402) have been seted up to the surface of filtration box (401), the inner wall fixedly connected with solid fixed ring (404) of filtration box (401), the inner wall fixed mounting of solid fixed ring (404) has a plurality of vortex blades (405).
2. The high efficiency two stage cyclone tube bundle gas-liquid separator of claim 1, wherein: an auxiliary frame (11) is fixedly arranged on one side of the separation cabin (1), a liquid pump (12) is arranged at the top of the auxiliary frame (11), the output end of the liquid pump (12) is fixedly communicated with one end of a liquid inlet pipe (16), and the outlet of the other end of the liquid inlet pipe (16) is in a bevel connection.
3. The high efficiency two stage cyclone tube bundle gas-liquid separator of claim 2, wherein: the bottom fixed intercommunication of separation cabin (1) has fluid-discharge tube (7), the one end fixed intercommunication of fluid-discharge tube (7) has drain pipe (17), the one end fixed mounting of drain pipe (17) has installation cover (9), the surface of drain pipe (17) sets up check valve (8).
4. A high efficiency two stage swirl tube bundle gas-liquid separator according to claim 3 wherein: the outer surface of the separation cabin (1) is close to the bottom, a mounting ring (5) is fixedly connected to the outer surface of the separation cabin (1), a plurality of support columns (6) are fixedly connected to the bottom of the mounting ring (5), a plurality of bottom fixing rings (10) are fixedly connected between the bottom ends of the support columns (6), and a maintenance port (20) is formed in the outer surface of the separation cabin (1).
5. The method for using the high-efficiency two-stage cyclone tube bundle type gas-liquid separator is characterized by comprising the following steps of:
S1, the liquid pump (12) is started to pump out a gas-liquid mixture under pressure, and then the gas-liquid mixture is discharged through the liquid inlet pipe (16), then the current limiting net frame (306) is pulled by the elastic band (307), the water outlet speed of the liquid inlet pipe (16) is controlled, the drop of the liquid inlet pipe (16) is prevented from making the flushed water flow bigger, when the water flow needs to be regulated, only the electromagnetic valve (302) is started, so that a part of the gas-liquid mixture pumped out by the liquid pump (12) enters the shunt pipe (301), the fan blade (310) is impacted under the guide of the guide plate (303), the rotating pipe (304) rotates around the positioning rod (309), then the pull rope (305) is wound in the winding groove (311), the current limiting net frame (306) is pulled in the winding process, the current limiting net frame (306) is pulled into the shunt pipe (301), the internal channel of the liquid inlet pipe (16) is opened, and the flow speed of the swirl plate (13) is improved;
S2, the gas-liquid mixture directly rushes to the cyclone plate (13), the liquid baffle (14) can block most of the gas-liquid mixture, so that the gas-liquid mixture is accelerated to flow downwards along the rotation direction of the cyclone plate (13), centrifugal force is generated in the downward flowing process, the gas-liquid mixture can continuously rotate along the inner wall of the second-stage separation bucket (15) under the action of the centrifugal force, gas and liquid are separated by the centrifugal force, the liquid is dragged to the vicinity of the inner wall of the separation bucket (15), the gas is concentrated in the center, and the fluid continuously flows downwards;
S3, separating out liquid and discharging the liquid through a liquid discharge pipe (7), wherein when the gas is discharged upwards, the gas passes through an umbrella plate (205), water drops mixed in the gas are condensed into big water drops, the gas continuously moves upwards through an air outlet hole (206), finally, the gas passes through a foam net (203), the foam net (203) is denser and finer, water vapor mixed in the gas is completely discharged, in addition, when the gas-liquid mixture is downwards flushed, part of the water vapor is splashed out of a liquid baffle (14), and then the water vapor is discharged under the action of the umbrella plate (205) and the foam net (203);
S4, through promoting filter cartridge (401), make elasticity spacing ring (403) card go into in change groove (19), then liquid just can dash vortex blade (405) when the separation of process separation fill (15) flows, constantly alternately strike vortex blade (405), can drive filter cartridge (401) and rotate, impurity particle can be filtered out when filtration pore (402) to liquid after the separation, and the speed that pivoted filter cartridge (401) can accelerate liquid infiltration filtration pore (402), during the cleanness with filter cartridge (401) outwards pull out can, through switch check valve (8), can control the drainage situation of fluid-discharge tube (7).
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| CN118384651B (en) * | 2024-04-24 | 2025-03-14 | 江苏章鼓力魄锐动力科技有限公司 | Vertical gas-water separator with two-stage multitube cyclone demister |
| CN118718550B (en) * | 2024-09-03 | 2025-01-10 | 山东佑坤能源设备有限公司 | Intelligent gravity two-phase gas-liquid separator equipment |
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| CN210845764U (en) * | 2019-11-04 | 2020-06-26 | 延长油田股份有限公司志丹采油厂 | Spiral-flow type vapour and liquid separator |
| CN216798996U (en) * | 2021-12-23 | 2022-06-24 | 新奥科技发展有限公司 | Filter screen and hydraulic impactor |
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| KR20040050221A (en) * | 2002-12-09 | 2004-06-16 | 엘지전자 주식회사 | Cyclone type dust collector |
| JP2011083696A (en) * | 2009-10-15 | 2011-04-28 | Toshiba Corp | Solid-liquid separator |
| CN211613095U (en) * | 2019-12-31 | 2020-10-02 | 扬州日发生物设备有限公司 | Cyclone tube of cyclone separator |
| CN212237797U (en) * | 2020-05-18 | 2020-12-29 | 湖北龙之泉农业发展股份有限公司 | Starch production line swirler |
| CN218774482U (en) * | 2022-12-05 | 2023-03-31 | 太仓市双益化工防腐设备有限公司 | Waste gas treatment gas-liquid separator |
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| CN210845764U (en) * | 2019-11-04 | 2020-06-26 | 延长油田股份有限公司志丹采油厂 | Spiral-flow type vapour and liquid separator |
| CN216798996U (en) * | 2021-12-23 | 2022-06-24 | 新奥科技发展有限公司 | Filter screen and hydraulic impactor |
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