CN219232719U - High-efficiency cyclone separator - Google Patents
High-efficiency cyclone separator Download PDFInfo
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- CN219232719U CN219232719U CN202223530766.XU CN202223530766U CN219232719U CN 219232719 U CN219232719 U CN 219232719U CN 202223530766 U CN202223530766 U CN 202223530766U CN 219232719 U CN219232719 U CN 219232719U
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
The utility model relates to the technical field of gas-solid separation, and discloses a high-efficiency cyclone separator, which comprises a separation mechanism, wherein a discharging mechanism is arranged at the lower end of the separation mechanism; the separating mechanism comprises an upper cylinder body, an inlet through pipe is fixedly communicated with the side surface of the upper end of the upper cylinder body, a valve plate is movably connected inside the inlet through pipe, a valve rod is arranged inside the valve plate, an exhaust outlet is fixedly communicated with the upper end of the upper cylinder body, a lower cone is fixedly communicated with the lower end of the exhaust outlet, and a supporting frame is fixedly connected with the outer portion of the lower cone. This high-efficient cyclone, through the inside of the leading-in barrel of entry siphunculus with the gas-solid mixture, the gas-solid mixture tangential gets into inside the cylindrical barrel of going up, through the tangential rotary motion that leads to the fact of introducing of air current, make the solid particle that has great inertial centrifugal force get rid of to the outer wall face separate, the solid particle that separates falls into cone bottom down, this device is through rotatory valve rod to adjust the valve plate at the inside angle of entry siphunculus.
Description
Technical Field
The utility model relates to the technical field of gas-solid separation, in particular to a high-efficiency cyclone separator.
Background
Cyclone separators are a type of apparatus used for separation of gas-solid systems or liquid-solid systems. The working principle is that solid particles or liquid drops with larger inertial centrifugal force are thrown to the outer wall surface for separation by the rotary motion caused by tangential introduction of air flow.
Solid particles separated by the prior cyclone separator fall along the inner wall and enter the bottom of the cyclone separator, after a certain time of separation, the solid particles are deposited at the bottom of the cyclone separator, the deposited solid particles in the cyclone separator need to be cleaned and discharged outwards, and the cyclone separator needs to be closed when the solid particles are discharged outwards, so that the working continuity of the cyclone separator is influenced, and the working efficiency of the cyclone separator is low.
We therefore propose a high efficiency cyclone separator to solve the above problems in the background.
Disclosure of Invention
The present utility model is directed to a high-efficiency cyclone separator, which solves the problems set forth in the background art.
In order to solve the technical problems, the utility model provides the following technical scheme:
the high-efficiency cyclone separator comprises a separating mechanism, wherein a discharging mechanism is arranged at the lower end of the separating mechanism;
the separating mechanism comprises an upper cylinder body, an inlet through pipe is fixedly communicated with the side surface of the upper end of the upper cylinder body, a valve plate is movably connected inside the inlet through pipe, a valve rod is arranged inside the valve plate, an exhaust outlet is fixedly communicated with the upper end of the upper cylinder body, a lower cone is fixedly communicated with the lower end of the exhaust outlet, and a supporting frame is fixedly connected with the outer part of the lower cone;
the discharging mechanism comprises a discharging box, a rotary valve is movably connected inside the discharging box, a discharging groove is formed in the surface of the rotary valve, a motor is installed outside the rotary valve, the lower end of the discharging box is fixedly communicated with a conveying pipe, a motor is fixedly connected to the outer portion of one end of the conveying pipe, and a screw rod is installed at one end of the inner side of the motor.
According to the technical scheme, the gas-solid mixture is guided into the upper cylinder through the inlet through pipe, the gas-solid mixture tangentially enters the cylindrical upper cylinder, solid particles with larger inertial centrifugal force are thrown to the outer wall surface to be separated through rotary motion caused by tangential air flow introduction, the separated solid particles fall into the bottom of the lower cone, the valve rod is rotated, so that the angle of the valve plate in the inlet through pipe is adjusted, the feeding speed of the inlet through pipe to the upper cylinder is adjusted, the gas-solid mixture is effectively separated, the gas-solid mixture is obliquely and obliquely communicated with the inside of the upper cylinder through the inlet through pipe, the gas-solid mixture can enter the upper cylinder to be separated, the solid particles are prevented from precipitating and blocking in the inlet through pipe, and the continuous and efficient separation of the gas-solid mixture is ensured;
the solid particles separated by the upper cylinder and the lower cone are deposited at the bottom of the lower cone, the upper end of the rotary valve is communicated with the bottom of the lower cone, so that solid particle materials enter the discharge chute, the rotary valve is driven by the motor to rotate in the discharge chute of the discharge box, the rotary discharge chute drives the solid particle materials inside to rotate, when the rotary valve rotates to the lower end of the discharge box, the solid particle materials fall into the conveying pipe under the gravity and rotate by the motor, the spiral rod is driven to rotate, so that the entering solid particle materials are conveyed, and the lower cone is closed when the discharge chute rotates to convey the solid particle materials, so that the upper cylinder and the lower cone do not need to separate gas-solid mixed materials, the cyclone separator does not need to stop working, and the deposited solid particles at the bottom of the cyclone separator can be discharged outwards, so that the cyclone separator can continuously separate and work, and the high-efficiency separation is achieved, and the production efficiency is improved.
Preferably, a material conveying inlet is formed in the upper portion of one end of the conveying pipe, and a material conveying outlet is formed below the other end of the conveying pipe.
Through the defeated material import and the discharging case lower extreme intercommunication of conveyer pipe, rotatory blown down tank drives inside solid particle material and rotates, when rotating to the discharging case lower extreme, the solid particle material receives the gravity whereabouts to enter into the conveyer pipe inside, through the defeated material export of the conveyer pipe other end, makes things convenient for the solid material output.
Preferably, a discharge groove is formed in the discharge box, and the lower end of the lower cone is fixedly communicated with the upper end of the discharge box.
The solid particles separated by the upper cylinder and the lower cone are deposited at the bottom of the lower cone, and the upper end of the rotary valve is communicated with the bottom of the lower cone, so that solid particle materials enter the discharge chute, the rotary valve is driven by the motor to rotate in the discharge chute of the discharge box, and the rotary discharge chute drives the solid particle materials in the discharge chute to rotate.
Preferably, the lower end of the discharging box is fixedly communicated with the material conveying inlet of the conveying pipe, and two ends of the screw rod are movably connected inside the conveying pipe.
Preferably, one end of the inlet through pipe connected with the upper cylinder body is arranged in a downward inclined mode, and the valve rod is arranged at the bottom of the inlet through pipe.
Through rotatory valve rod to adjust valve plate at the inside angle of entry siphunculus, thereby adjust the inside feed rate of entry siphunculus to last barrel, be favorable to the gas-solid mixture at effective separation, through the inside of barrel is gone up in the oblique tangential intercommunication of entry siphunculus, thereby make the gas-solid mixture can get into the inside separation of last barrel, prevent that solid particles from depositing in the inside jam of entry siphunculus, guarantee the continuous high-efficient separation of gas-solid mixture.
Preferably, the discharging box is fixedly connected to the bottom of the supporting frame, and the motor is fixedly connected to the inside of the discharging box.
The discharging box is kept fixed through the supporting frame, the motor is fixedly connected inside the discharging box, and the motor drives the rotary valve to rotate.
Preferably, the rotary valve is arranged in a circular shape, and the discharge chute is arranged below the lower cone.
The rotary valve is arranged to be round, so that the rotary valve can rotate in the discharge box, and the round rotary valve and the discharge groove of the discharge box are tightly attached, so that when the discharge groove rotates to convey solid particle materials, the lower part of the lower cone is closed, the separation of the upper cylinder body and the lower cone from gas-solid mixed materials is not influenced, and the cyclone separator can work stably and efficiently.
Compared with the prior art, the utility model provides the efficient cyclone separator which has the following beneficial effects:
1. this high-efficient cyclone, the solid particle that separates through last barrel and lower cone deposits in lower cone bottom, the rotary valve upper end communicates with lower cone bottom, thereby make solid particle material get into the blown down tank inside, drive the internal rotation of blow down tank at the rotary valve through the motor, rotatory blown down tank drives inside solid particle material and rotates, when rotating to the blown down tank lower extreme, solid particle material is fallen into the conveyer pipe inside by gravity, drive the hob through the motor and rotate, thereby carry the solid particle material that gets into, because circular rotary valve and blow down tank are closely laminated, thereby when the blown down tank rotates and carries solid particle material, lower cone below is sealed, do not influence barrel and lower cone and separate gas-solid mixture material, need not stop cyclone work, can be to the solid particle of the deposit of cyclone bottom outwards arrange, make cyclone can continuous separation work, reach high-efficient separation, improve production efficiency.
2. This high-efficient cyclone, inside the cylinder was gone up in the leading-in cylinder of gas-solid mixture through the entry siphunculus, the gas-solid mixture tangential gets into cylindrical, through the tangential rotary motion that causes of introducing of air current, make the solid particle that has great inertial centrifugal force get rid of to the outer wall face separate, the solid particle that separates falls into lower cone bottom, this device is through rotatory valve rod, thereby adjust the valve plate at the inside angle of entry siphunculus, thereby adjust the inside feed rate of entry siphunculus to last cylinder, be favorable to the gas-solid mixture at effective separation, through the inside cylinder of entry siphunculus slope diagonal intercommunication, thereby make the gas-solid mixture can get into the inside separation of last cylinder, prevent that solid particle from depositing in the inside jam of entry siphunculus, guarantee the continuous high-efficient separation of gas-solid mixture.
Drawings
The accompanying drawings are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate the utility model and together with the embodiments of the utility model, serve to explain the utility model. In the drawings:
FIG. 1 is a schematic view of the external structure of the present utility model;
FIG. 2 is a schematic view of the internal structure of the present utility model;
FIG. 3 is a schematic top view of the present utility model;
fig. 4 is a schematic view of the bottom structure of the present utility model.
Wherein: 101. an upper cylinder; 102. an inlet tube; 103. a valve plate; 104. a valve stem; 105. an exhaust outlet; 106. a lower cone; 107. a support frame; 201. a discharging box; 202. a rotary valve; 203. a discharge chute; 204. a motor; 205. a delivery tube; 206. a motor; 207. a screw rod.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Please refer to fig. 1-4.
The high-efficiency cyclone separator comprises a separating mechanism, wherein a discharging mechanism is arranged at the lower end of the separating mechanism;
the separating mechanism comprises an upper cylinder 101, an inlet through pipe 102 is fixedly communicated with the side surface of the upper end of the upper cylinder 101, a valve plate 103 is movably connected inside the inlet through pipe 102, a valve rod 104 is arranged inside the valve plate 103, an exhaust outlet 105 is fixedly communicated with the upper end of the upper cylinder 101, a lower cone 106 is fixedly communicated with the lower end of the exhaust outlet 105, and a supporting frame 107 is fixedly connected with the outer part of the lower cone 106;
the discharging mechanism comprises a discharging box 201, a rotary valve 202 is movably connected inside the discharging box 201, a discharging groove 203 is formed in the surface of the rotary valve 202, a motor 204 is arranged on the outer side of the rotary valve 202, a conveying pipe 205 is fixedly communicated with the lower end of the discharging box 201, a motor 206 is fixedly connected to the outer portion of one end of the conveying pipe 205, and a screw rod 207 is arranged at one end of the inner side of the motor 206.
According to the technical scheme, the gas-solid mixture is guided into the upper cylinder 101 through the inlet through pipe 102, the gas-solid mixture tangentially enters the cylindrical upper cylinder 101, solid particles with larger inertial centrifugal force are thrown to the outer wall surface for separation through the rotation motion caused by the tangential introduction of the air flow, the separated solid particles fall into the bottom of the lower cone 106, the valve rod 104 is rotated, so that the angle of the valve plate 103 in the inlet through pipe 102 is adjusted, the feeding speed of the inlet through pipe 102 to the upper cylinder 101 is adjusted, the gas-solid mixture is effectively separated, the gas-solid mixture is obliquely and obliquely communicated into the upper cylinder 101 through the inlet through pipe 102, the gas-solid mixture can enter the upper cylinder 101 for separation, the solid particles are prevented from precipitating and blocking in the inlet through pipe 102, and the continuous and efficient separation of the gas-solid mixture is ensured;
the solid particles separated by the upper cylinder 101 and the lower cone 106 are deposited at the bottom of the lower cone 106, the upper end of the rotary valve 202 is communicated with the bottom of the lower cone 106, so that the solid particles enter the discharge chute 203, the rotary valve 202 is driven by the motor 204 to rotate in the discharge chute of the discharge box 201, the rotary discharge chute 203 drives the solid particles in the discharge chute to rotate, when the rotary valve rotates to the lower end of the discharge box 201, the solid particles fall into the conveying pipe 205 under the gravity and rotate by the motor 206, the entering solid particles are conveyed, and the circular rotary valve 202 is tightly attached to the discharge chute of the discharge box 201, so that when the discharge chute 203 rotates to convey the solid particles, the lower cone 106 is closed, the upper cylinder 101 and the lower cone 106 are not influenced to separate the gas-solid mixed materials, the cyclone separator is not required to stop working, and the deposited solid particles at the bottom of the cyclone separator can be discharged outwards, the cyclone separator can continuously separate, the cyclone separator can work, the high-efficiency separation is achieved, and the production efficiency is improved.
A material conveying inlet is formed in the upper portion of one end of the conveying pipe 205, and a material conveying outlet is formed below the other end of the conveying pipe 205.
Through the defeated material import and the discharging case 201 lower extreme intercommunication of conveyer pipe 205, rotatory blown down tank 203 drives inside solid particle material and rotates, when rotating to the discharging case 201 lower extreme, the solid particle material receives gravity whereabouts to get into inside the conveyer pipe 205, through the defeated material export of conveyer pipe 205 other end, makes things convenient for the solid material output.
A discharge groove is arranged in the discharge box 201, and the lower end of the lower cone 106 is fixedly communicated with the upper end of the discharge box 201.
The solid particles separated by the upper cylinder 101 and the lower cone 106 are deposited at the bottom of the lower cone 106, and the upper end of the rotary valve 202 is communicated with the bottom of the lower cone 106, so that solid particle materials enter the discharge chute 203, the rotary valve 202 is driven by the motor 204 to rotate in the discharge chute of the discharge box 201, and the rotary discharge chute 203 drives the solid particle materials in the discharge chute to rotate.
The lower end of the discharging box 201 is fixedly communicated with the material conveying inlet of the conveying pipe 205, and two ends of the spiral rod 207 are movably connected inside the conveying pipe 205.
The inlet pipe 102 is connected with the upper cylinder 101, one end of the inlet pipe is arranged obliquely downwards, and the valve rod 104 is arranged at the bottom of the inlet pipe 102.
Through the rotation valve rod 104 to adjust valve plate 103 at the inside angle of inlet siphunculus 102, thereby adjust the inside feed rate of inlet siphunculus 102 to last barrel 101, be favorable to the gas-solid mixture at effective separation, through the inside of inlet siphunculus 102 chamfer directional intercommunication last barrel 101, thereby make gas-solid mixture can get into the inside separation of last barrel 101, prevent that solid particle from depositing in inlet siphunculus 102 and blocking up, guarantee the continuous high-efficient separation of gas-solid mixture.
The discharging box 201 is fixedly connected to the bottom of the supporting frame 107, and the motor 204 is fixedly connected to the inside of the discharging box 201.
The discharge box 201 is kept fixed through the supporting frame 107, the motor 204 is fixedly connected to the inside of the discharge box 201, and the rotary valve 202 is driven to rotate through the motor 204.
The rotary valve 202 is arranged in a circular shape and the discharge chute 203 is arranged below the lower cone 106.
The rotary valve 202 is arranged to be circular, so that the rotary valve 202 can rotate in the discharge box 201, and the circular rotary valve 202 is tightly attached to the discharge groove of the discharge box 201, so that when the discharge groove 203 rotates to convey solid particle materials, the lower part of the lower cone 106 is closed, the separation of the gas-solid mixed materials by the upper cylinder 101 and the lower cone 106 is not influenced, and the cyclone separator can work stably and efficiently.
The working principle of the utility model is as follows: the gas-solid mixture is guided into the upper cylinder 101 through the inlet through pipe 102, the gas-solid mixture tangentially enters the cylindrical upper cylinder 101, solid particles with larger inertial centrifugal force are thrown to the outer wall surface to be separated through the rotation motion caused by the tangential introduction of the air flow, the separated solid particles fall into the bottom of the lower cone 106, the valve rod 104 is rotated, so that the angle of the valve plate 103 in the inlet through pipe 102 is adjusted, the feeding speed of the inlet through pipe 102 to the inside of the upper cylinder 101 is adjusted, the gas-solid mixture is effectively separated, the gas-solid mixture is obliquely and obliquely communicated into the upper cylinder 101 through the inlet through pipe 102, the gas-solid mixture can enter the upper cylinder 101 to be separated, the solid particles are prevented from precipitating and blocking in the inlet through pipe 102, and the gas-solid mixture is ensured to be continuously and efficiently separated;
the solid particles separated by the upper cylinder 101 and the lower cone 106 are deposited at the bottom of the lower cone 106, the upper end of the rotary valve 202 is communicated with the bottom of the lower cone 106, so that the solid particles enter the discharge chute 203, the rotary valve 202 is driven by the motor 204 to rotate in the discharge chute of the discharge box 201, the rotary discharge chute 203 drives the solid particles in the discharge chute to rotate, when the rotary valve rotates to the lower end of the discharge box 201, the solid particles fall into the conveying pipe 205 under the gravity and rotate by the motor 206, the entering solid particles are conveyed, and the circular rotary valve 202 is tightly attached to the discharge chute of the discharge box 201, so that when the discharge chute 203 rotates to convey the solid particles, the lower cone 106 is closed, the upper cylinder 101 and the lower cone 106 are not influenced to separate the gas-solid mixed materials, the cyclone separator is not required to stop working, and the deposited solid particles at the bottom of the cyclone separator can be discharged outwards, the cyclone separator can continuously separate, the cyclone separator can work, the high-efficiency separation is achieved, and the production efficiency is improved.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present utility model has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (7)
1. The utility model provides a high-efficient cyclone, includes separating mechanism, its characterized in that: the lower end of the separation mechanism is provided with a discharging mechanism;
the separating mechanism comprises an upper cylinder body (101), an inlet through pipe (102) is fixedly communicated with the side surface of the upper end of the upper cylinder body (101), a valve plate (103) is movably connected inside the inlet through pipe (102), a valve rod (104) is arranged inside the valve plate (103), an exhaust outlet (105) is fixedly communicated with the upper end of the upper cylinder body (101), a lower cone (106) is fixedly communicated with the lower end of the exhaust outlet (105), and a supporting frame (107) is fixedly connected with the outer part of the lower cone (106);
the discharging mechanism comprises a discharging box (201), a rotary valve (202) is movably connected inside the discharging box (201), a discharging groove (203) is formed in the surface of the rotary valve (202), a motor (204) is mounted on the outer side of the rotary valve (202), a conveying pipe (205) is fixedly communicated with the lower end of the discharging box (201), a motor (206) is fixedly connected to the outer portion of one end of the conveying pipe (205), and a screw rod (207) is mounted at the inner end of the motor (206).
2. A high efficiency cyclone separator as claimed in claim 1, wherein: the upper part of one end of the conveying pipe (205) is provided with a material conveying inlet, and the lower part of the other end of the conveying pipe (205) is provided with a material conveying outlet.
3. A high efficiency cyclone separator as claimed in claim 1, wherein: the discharging box (201) is internally provided with a discharging groove, and the lower end of the lower cone (106) is fixedly communicated with the upper end of the discharging box (201).
4. A high efficiency cyclone separator as claimed in claim 1, wherein: the lower end of the discharging box (201) is fixedly communicated with a material conveying inlet of the conveying pipe (205), and two ends of the spiral rod (207) are movably connected inside the conveying pipe (205).
5. A high efficiency cyclone separator as claimed in claim 1, wherein: the inlet through pipe (102) is arranged at one end connected with the upper cylinder body (101) in a downward inclined mode, and the valve rod (104) is arranged at the bottom of the inlet through pipe (102).
6. A high efficiency cyclone separator as claimed in claim 1, wherein: the discharging box (201) is fixedly connected to the bottom of the supporting frame (107), and the motor (204) is fixedly connected to the inside of the discharging box (201).
7. A high efficiency cyclone separator as claimed in claim 1, wherein: the rotary valve (202) is arranged in a round shape, and the discharge chute (203) is arranged below the lower cone (106).
Priority Applications (1)
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CN202223530766.XU CN219232719U (en) | 2022-12-28 | 2022-12-28 | High-efficiency cyclone separator |
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CN202223530766.XU CN219232719U (en) | 2022-12-28 | 2022-12-28 | High-efficiency cyclone separator |
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CN219232719U true CN219232719U (en) | 2023-06-23 |
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CN202223530766.XU Active CN219232719U (en) | 2022-12-28 | 2022-12-28 | High-efficiency cyclone separator |
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