CN111672641A - Built-in net barrel type oil-sewage separation swirler - Google Patents
Built-in net barrel type oil-sewage separation swirler Download PDFInfo
- Publication number
- CN111672641A CN111672641A CN202010520689.6A CN202010520689A CN111672641A CN 111672641 A CN111672641 A CN 111672641A CN 202010520689 A CN202010520689 A CN 202010520689A CN 111672641 A CN111672641 A CN 111672641A
- Authority
- CN
- China
- Prior art keywords
- built
- cylinder
- shell
- pipe
- cyclone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/08—Vortex chamber constructions
- B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Cyclones (AREA)
Abstract
The invention discloses a built-in screen cylinder type oil-sewage separation cyclone, which belongs to the technical field of fluid machinery and comprises an upper cylindrical shell and a lower conical cylindrical shell, wherein a liquid flow inlet is connected to the side wall of the upper end of the upper cylindrical shell in a tangential manner, a cyclone cavity is arranged inside the upper cylindrical shell, a lower fastening flange is welded to the top of the upper cylindrical shell, a built-in screen cylinder is inserted into the lower fastening flange in a penetrating manner, the top of the built-in screen cylinder is fixedly connected with a connecting ring, two thirds of the built-in screen cylinder is positioned in the cyclone cavity, grids of the built-in screen cylinder are changed from dense to sparse from bottom. The built-in mesh cylinder reduces the swing of the rotation center of the cyclone, stabilizes the interface between oil stains, effectively improves the quality of the separated oil product, and can accelerate the blowdown speed of the underflow pipe and prevent the blockage and abrasion of the underflow pipe.
Description
Technical Field
The invention belongs to the technical field of fluid machinery, and particularly relates to a built-in mesh cylinder type oil-sewage separation cyclone.
Background
The oil sewage contains oil substances such as natural petroleum, petroleum products, tar and fractionated substances thereof and solid particles such as sludge, rust, sand and stone. Three-phase separation is required before treatment. At present, gravity settling tanks are mainly used for three-phase separators. The gravity settling type equipment is large in size, assemblies such as a weir plate are usually arranged inside the gravity settling type equipment, and the structure is complex. In addition, since the separation process is performed by gravity, the process has disadvantages such as long process time, discontinuous work, and large floor space. However, it is difficult to separate oil from water. The cyclone has been used in China as a separation device, the separation principle of the three-phase separator is that centrifugal separation is performed by using density difference between media, and the larger the density difference is, the better the separation effect is. The cyclone can separate oil, water and slag for reuse. But due to the oscillating centre of rotation of the cyclone, the already separated particles, water and oil will again mix in the central zone, resulting in a reduced quality of the separated oil. Therefore, how to improve the structure of the cyclone and improve the separation effect of the cyclone becomes a problem to be solved urgently in the oil sewage treatment industry and the practice of the related industry.
Disclosure of Invention
The invention aims to provide an oil-sewage separation cyclone with a built-in net barrel, wherein the built-in net barrel reduces the swing of the rotation center of the cyclone, so that the interface between oil stains is stable, the quality of the separated oil product is effectively improved, the pollution discharge speed of a bottom flow pipe can be accelerated, and the blockage and the abrasion of the bottom flow pipe are prevented.
The technical scheme adopted by the invention for realizing the purpose is as follows: the utility model provides a built-in net section of thick bamboo formula oil sewage separation swirler, shell under the shell on the cylinder, conical barrel, the upper end lateral wall of shell has the liquid stream entry along the tangential access on the cylinder, the inside whirl chamber that is equipped with of shell on the cylinder, the welding of shell top has fastening flange down on the cylinder, the inside interlude of fastening flange has built-in net section of thick bamboo down, built-in net section of thick bamboo top rigid coupling go-between, two-thirds of built-in net section of thick bamboo is located the whirl intracavity, supreme being dredged by the density down of the net of built-in net. Compared with the prior common cyclone, the cyclone with the new structure has a built-in net barrel structure, and after mixed oil sewage enters from an inlet, a flow guide channel between the wall surface and the net barrel rotates and flows downwards along the wall surface to generate centrifugal force, so that an oil layer, a water layer and a water residue layer are rapidly formed in the rotating process. Due to the special hydraulic property of the cyclone, upward rotary flow is formed inside the cyclone. The swing of the rotation center is stabilized by the built-in mesh cylinder, so that an interface between an oil layer and a water layer is stable, and oil can enter an upflow more stably due to the existence of the meshes. The cyclone with the structure can be connected in series in multiple stages, and the diameter of each stage of net barrel is adjusted according to the proportion of oil, water and slag.
Preferably, an upper fastening flange is arranged above the connecting ring, threaded holes with the same positions are formed among the upper fastening flange, the connecting ring and the lower fastening flange, the upper fastening flange, the connecting ring and the lower fastening flange are connected through screws, an upper overflow pipe is inserted into the upper fastening flange, the bottom end of the upper overflow pipe is located in a built-in net barrel, and the diameter of the built-in net barrel is larger than that of an upper shell of a cylinder with the diameter of the upper overflow pipe being smaller than two. Through the connected mode of upper and lower flange, make the leakproofness of swirler have better guarantee, oil reservoir can spill over so that the separation through last overflow pipe in the separation process, and built-in net section of thick bamboo diameter is greater than the overflow pipe diameter and is less than two-thirds cylinder upper housing diameter, has ensured greasy dirt water separating's stability, and just the oily water that gets into the whirl chamber can be around the quick rotation of water conservancy diversion passageway between wall and net section of thick bamboo.
Preferably, the inner wall of the liquid inlet is attached with wear-resistant rubber, the liquid outlet end of the liquid inlet corresponds to the guide circular table, the guide circular table is sleeved outside the built-in net barrel, and the top of the guide circular table is connected with the top surface of the rotational flow cavity. The wear-resisting rubber that the liquid stream entry inner wall set up has strengthened the wear resistance of liquid stream entry, has prolonged the life of liquid stream entry, and oily water passes through the liquid stream entry, at first can be followed the spiral downstream of direction round platform inclined plane, and the round platform has the guide effect to oily water for oily water continuous motion has avoided the existence of short-circuit flow. Due to the existence of the guide round platform, the oily water does not directly move downwards, but the inclined surface of the guide round platform moves tangentially, the tangential speed of the separation liquid is increased under the action of pressure, and the oily water which moves continuously can be guided to the periphery of the built-in mesh cylinder to continuously perform downward spiral motion until the oily water rotates to the separation cavity to perform oil stain separation.
Preferably, the bottom of the upper shell of the cylinder is connected with an upper shell flange, the upper shell flange is connected with a lower shell flange at the top of the lower shell of the conical cylinder through a screw, a separation cavity is formed in the lower shell of the conical cylinder, and the tail end of the lower shell of the conical cylinder is fixedly connected with an underflow pipe. Because can dwindle gradually between the inside separation chamber that sets up of shell under the conical barrel, sediment layer, water layer have the trend of subsiding to separation intracavity wall under the effect of conic section centrifugal force, and sediment layer, water layer receive the effect of great centrifugal force, and the internal face of swirler moves and forms outer whirl and discharges from the underflow pipe, and the oil reservoir that is located the middle part can the upward movement and discharges through the overflow pipe and form the overflow.
The converter is arranged below the built-in screen cylinder and fixedly connected with the inner wall of the cyclone cavity, the converter can further accelerate the rotation kinetic energy of oily water and improve the separation effect of the oily water, the oily water drained by the built-in screen cylinder is divided to the space between adjacent cyclone blades by the guide ball head, the upper section of each cyclone blade is perpendicular to the cylindrical carrier to enable the oily water to better flow in, the middle section of each cyclone blade is bent towards one side, the bending radian can be calculated by a specific formula, the downward spiral speed of the oily water is accelerated by the middle section of each cyclone blade, oil stains can be separated in the separation cavity, the lower section of each cyclone blade extends to the bottom of the cylindrical carrier to guide the oily water to the tapered guide head, the thicknesses of the upper section, the middle section and the lower end of each cyclone blade are gradually decreased, the lower section of each cyclone blade is thinnest, and the distance between the lower sections, the speed of the oily water can also be accelerated, the oil stain separated from the oil stain flowing into the separation cavity can upwards overflow from the overflow pipe through the through hole in the middle of the converter, and the sewage and the water slag can flow out from the underflow pipe due to centrifugal gravity.
The conical wall of the separation cavity is annularly provided with rib plates, the inner sides of the rib plates are provided with inner cones, gaps are arranged between the opening of the top of each inner cone and the top of the separation cavity, sand discharge holes are formed in the opening of each inner cone, the side walls of the sand discharge holes are connected with flow blocking blocks, and the wall of the top of each inner cone is provided with a conical groove. The design of interior awl can make the particulate matter in the greasy dirt aquatic isolate, the loss that the long-term friction of the granule that has avoided oily water and inside to contain and separation intracavity wall caused, when rotatory oily water moves to interior awl, particulate matter is because gravity, centrifugal force can throw away through the sediment outflow hole, and the clearance that is equipped with between interior awl and the separation intracavity is to the whereabouts, remaining oily water is spiral motion down until the separation again, the inner wall at the sediment outflow hole is connected to the fender stream piece, can prevent effectively that the inside oily water of interior awl from getting into at first step disperses when rotatory, ensure subsequent separation of oily water, the tapered groove of seting up on the interior awl wall, can play certain water conservancy diversion effect, take place wearing and tearing regularly and take out the change after the interior awl uses, reduce the equipment maintenance cost.
As preferred, the underflow pipe inner wall is equipped with prevents stifled subassembly, prevent stifled subassembly includes semicircular roller, the roller is located the concave hole that the underflow pipe lateral wall was seted up, the shrinkage pool that the underflow pipe lateral wall was seted up has at least one, all be equipped with the roller in every concave hole, the roller middle part is connected with the roller bearing, and be equipped with the clearance between roller and the roller bearing, the roller bearing middle part is connected with the underflow pipe lateral wall, every shrinkage pool outside all is connected with the inlet branch pipe of slope, the L shape is admitted air and is responsible for in the inlet branch pipe connection, the inlet end that the L shape was admitted air and is responsible for is located the underflow pipe outside, the horizontal end interlude of the L shape is responsible for admitting air has stifled pole, the inside top surface of top cap is connected to the middle part of stifled pole, the top edge of elasticity rope other end is connected, the. The particle impurities and sewage separated in the separation cavity can flow out to the underflow pipe through self gravity and centrifugal force, the sewage and particles flowing out of the underflow pipe can generate impact force to the push plate in the underflow pipe, the push plate subjected to the impact force can drive the blocking rods connected with two ends to move downwards, the downward movement distance of the blocking rods is effectively limited due to the tension of the elastic rope and the arrangement of the limiting blocks, the gas communicated in the L-shaped air inlet main pipe can quickly flow into the air inlet branch pipe after the blocking rods are pulled open, and then the gas is blown to the surface of the roller from the obliquely arranged air inlet branch pipe, so that the roller can quickly rotate, the flowing speed of the sewage and the particle impurities is increased, the blockage caused by long-term accumulation of the particle impurities is reduced, meanwhile, the particle impurities are prevented from directly contacting with the inner wall of the underflow pipe, the abrasion of the inner wall of the underflow pipe is greatly reduced, the service life of the whole swirler, the elastic rope can pull the blocking rod and the push plate to reset again, and the L-shaped air inlet main pipe is blocked to prevent air from entering.
Preferably, the central axes of the lower shell of the conical cylinder, the underflow pipe, the built-in net cylinder and the upper overflow pipe are all coincided with the central axis of the upper shell of the cylinder. The central axes of the parts are overlapped to ensure the separation efficiency of the oil sewage, the separated sewage spirally goes downwards along the separation cavity, and the oil stain upwards overflows through the overflow pipe.
Compared with the prior art, the invention has the beneficial effects that: the internal mesh cylinder is arranged in the cyclone separator, so that the swing of a rotating center is stabilized, the interface between an oil layer and a water layer is stabilized, oil can enter an upward flow more stably due to the existence of the mesh, the downward spiral flow velocity of oil sewage after passing through the converter can be further accelerated, the separation of the oil sewage in the separation cavity is facilitated, the separated oil stain overflows through the overflow pipe, the sewage and impurities flow out through the underflow pipe, the blockage prevention assembly in the underflow pipe can reduce the blockage caused by the long-term accumulation of particulate matters, meanwhile, the particulate matters can be prevented from directly contacting with the inside of the underflow pipe, and the service life of the whole cyclone is prolonged.
Description of reference numerals: 1, cylinder upper shell; 2 a liquid stream inlet; 3, mounting a shell flange; 4, fastening a flange; 5, a lower shell of the conical cylinder body; 6 lower housing flange; 7 an underflow pipe; 8, a net cylinder is arranged in the cylinder; 9 connecting rings; 10, an overflow pipe; 11, fastening a flange; 12, guiding the circular truncated cone; 13 a current transformer; 131 flow guiding ball heads; a 132 cylindrical support; 133 a conical flow directing head; 134 swirl vanes; 14 a rotational flow cavity; 15 wear-resistant rubber; 16 a separation chamber; 17 an anti-clogging assembly; 171 a roller; 172 rollers; 173 inlet manifold; 174L-shaped main intake pipe; 175 a push plate; 176 blocking the rod; 177 a top cover; 178 an elastic cord; 179 a stopper; 18 rib plates; 19 inner cone; 20, arranging sand holes; 21 flow blocking block; 22 tapered grooves.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a schematic diagram showing the separation of components of a built-in mesh tubular oil-sewage separation cyclone according to the present invention;
FIG. 2 is a schematic diagram of an internal structure of a built-in mesh tubular oil-sewage separation cyclone according to the present invention;
FIG. 3 is a schematic structural diagram of a built-in mesh drum according to the present invention;
FIG. 4 is a top view of the lower housing of the conical barrel of the present invention;
FIG. 5 is a schematic structural diagram of a current transformer according to the present invention;
FIG. 6 is a schematic structural view of a guide circular table according to the present invention;
FIG. 7 is a schematic view of the inner cone of the present invention;
FIG. 8 is an enlarged view of the invention at A;
FIG. 9 is a schematic view of the push plate of the present invention with no force applied and the elastic cord not stretched;
FIG. 10 is a schematic view of the push plate of the present invention being stressed and the elastic cord being stretched;
FIG. 11 is a graph of experimental data for the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1:
referring to fig. 1-10, a built-in net cylinder type oil-sewage separation cyclone comprises an upper shell 1 of a cylinder body and a lower shell 5 of a conical cylinder body, wherein a liquid flow inlet 2 is connected to the side wall of the upper end of the upper shell 1 of the cylinder body in a tangential manner, a rotational flow cavity 14 is arranged inside the upper shell 1 of the cylinder body, a lower fastening flange 4 is welded to the top of the upper shell 1 of the cylinder body, a built-in net cylinder 8 is inserted into the lower fastening flange 4 in a penetrating manner, a connecting ring 9 is fixedly connected to the top of the built-in net cylinder 8, two thirds of the built-in net cylinder 8 is located in the rotational flow cavity 14, grids of the built-in. Compared with the prior common cyclone, the cyclone with the new structure has a built-in net barrel structure, and after mixed oil sewage enters from an inlet, a flow guide channel between the wall surface and the net barrel rotates and flows downwards along the wall surface to generate centrifugal force, so that an oil layer, a water layer and a water residue layer are rapidly formed in the rotating process. Due to the special hydraulic property of the cyclone, upward rotary flow is formed inside the cyclone. The swing of the rotation center is stabilized by the built-in mesh cylinder, so that an interface between an oil layer and a water layer is stable, and oil can enter an upflow more stably due to the existence of the meshes. The cyclone with the structure can be connected in series in multiple stages, and the diameter of each stage of net barrel is adjusted according to the proportion of oil, water and slag.
Go up fastening flange 11 above the go-between 9, go up fastening flange 11, go-between 9 and set up the screw hole that the position is the same between the fastening flange 4 down, it passes through the screw connection, goes up inside the pegging graft of fastening flange 11 and has last overflow pipe 10, goes up overflow pipe 10 bottom and is located built-in net section of thick bamboo 8, and built-in net section of thick bamboo 8 diameter is greater than the overflow pipe 10 diameter and is less than two-thirds cylinder on the shell 1 diameter. Through the connected mode of upper and lower flange, make the leakproofness of swirler have better guarantee, oil reservoir can spill over so that the separation through last overflow pipe in the separation process, and built-in net section of thick bamboo diameter is greater than the overflow pipe diameter and is less than two-thirds cylinder upper housing diameter, has ensured greasy dirt water separating's stability, and just the oily water that gets into the whirl chamber can be around the quick rotation of water conservancy diversion passageway between wall and net section of thick bamboo.
The inner wall of the liquid flow inlet 2 is attached with wear-resistant rubber 15, the liquid outlet end of the liquid flow inlet 2 corresponds to the guide circular truncated cone 12, the guide circular truncated cone 12 is sleeved outside the built-in net barrel 8, and the top of the guide circular truncated cone 12 is connected with the top surface of the swirling flow cavity 14. The wear-resisting rubber that the liquid stream entry inner wall set up has strengthened the wear resistance of liquid stream entry, has prolonged the life of liquid stream entry, and oily water passes through the liquid stream entry, at first can be followed the spiral downstream of direction round platform inclined plane, and the round platform has the guide effect to oily water for oily water continuous motion has avoided the existence of lid short-circuit flow. Due to the existence of the guide round platform, the oily water does not directly move downwards, but the inclined surface of the guide round platform moves tangentially, the tangential speed of the separation liquid is increased under the action of pressure, and the oily water which moves continuously can be guided to the periphery of the built-in mesh cylinder to continuously perform downward spiral motion until the oily water rotates to the separation cavity to perform oil stain separation.
The upper shell flange 3 is connected to 1 bottom of shell on the cylinder, goes up shell flange 3 and passes through the lower shell flange 6 connection at 5 tops of shell under screw and the conical barrel, and separation chamber 16 has been seted up to 5 inside shells under the conical barrel, and 5 ends of shell link firmly underflow pipes 7 under the conical barrel. Because can dwindle gradually between the inside separation chamber that sets up of shell under the conical barrel, sediment layer, water layer have the trend of subsiding to separation intracavity wall under the effect of conic section centrifugal force, and sediment layer, water layer receive the effect of great centrifugal force, and the internal face of swirler moves and forms outer whirl and discharges from the underflow pipe, and the oil reservoir that is located the middle part can the upward movement and discharges through the overflow pipe and form the overflow.
The bottom of the built-in net barrel 8 is provided with a converter 13, the middle of the converter 13 is provided with a through hole, the converter 13 comprises a flow guide ball head 131, a cylindrical carrier 132 is connected below the flow guide ball head 131, a conical flow guide head 133 is connected below the cylindrical carrier 132, swirl blades 134 are annularly distributed on the surface of the cylindrical carrier 132, the swirl blades 134 are divided into three sections, the upper section of the swirl blades 134 is perpendicular to the cylindrical carrier 132, the middle section is bent towards one side, and the lower section extends to the bottom of the cylindrical carrier 132 along the bottom of the middle section. The converter is arranged below the built-in screen cylinder and fixedly connected with the inner wall of the cyclone cavity, the converter can further accelerate the rotation kinetic energy of oily water and improve the separation effect of the oily water, the oily water drained by the built-in screen cylinder is divided to the space between adjacent cyclone blades by the guide ball head, the upper section of each cyclone blade is perpendicular to the cylindrical carrier to enable the oily water to better flow in, the middle section of each cyclone blade is bent towards one side, the bending radian can be calculated by a specific formula, the downward spiral speed of the oily water is accelerated by the middle section of each cyclone blade, oil stains can be separated in the separation cavity, the lower section of each cyclone blade extends to the bottom of the cylindrical carrier to guide the oily water to the tapered guide head, the thicknesses of the upper section, the middle section and the lower end of each cyclone blade are gradually decreased, the lower section of each cyclone blade is thinnest, and the distance between the lower sections, the speed of the oily water can also be accelerated, the oil stain separated from the oil stain flowing into the separation cavity can upwards overflow from the overflow pipe through the through hole in the middle of the converter, and the sewage and the water slag can flow out from the underflow pipe due to centrifugal gravity.
The inner wall of the underflow pipe 7 is provided with an anti-blocking assembly 17, the anti-blocking assembly 17 comprises a semicircular roller 172, the roller 172 is positioned in a concave hole formed in the side wall of the underflow pipe 7, at least 4 concave holes formed in the side wall of the underflow pipe 7 are provided, a roller 172 is arranged in each concave hole, the middle part of the roller 172 is connected with a roller 171, a gap is arranged between the roller 172 and the roller 171, the middle part of the roller 171 is connected with the side wall of the underflow pipe 7, the outer side of each concave hole is connected with an inclined air inlet branch pipe 173, the air inlet branch pipe 173 is connected with an L-shaped air inlet main pipe 174, the air inlet end of the L-shaped air inlet main pipe 174 is positioned outside the underflow pipe 7, a blocking rod 176 is inserted into the transverse end of the L-shaped air inlet main pipe 174, the middle part of the blocking rod 176 is connected with one end of an elastic rope 178, the other end, the bottom of the stem 176 is connected to a transversely disposed pusher plate 175. The particle impurities and sewage separated in the separation cavity can flow out to the underflow pipe through self gravity and centrifugal force, the sewage and particles flowing out of the underflow pipe can generate impact force to the push plate in the underflow pipe, the push plate subjected to the impact force can drive the blocking rods connected with two ends to move downwards, the downward movement distance of the blocking rods is effectively limited due to the tension of the elastic rope and the arrangement of the limiting blocks, the gas communicated in the L-shaped air inlet main pipe can quickly flow into the air inlet branch pipe after the blocking rods are pulled open, and then the gas is blown to the surface of the roller from the obliquely arranged air inlet branch pipe, so that the roller can quickly rotate, the flowing speed of the sewage and the particle impurities is increased, the blockage caused by long-term accumulation of the particle impurities is reduced, meanwhile, the particle impurities are prevented from directly contacting with the inner wall of the underflow pipe, the abrasion of the inner wall of the underflow pipe is greatly reduced, the service life of the whole swirler, the elastic rope can pull the blocking rod and the push plate to reset again, and the L-shaped air inlet main pipe is blocked to prevent air from entering.
The central axes of the conical barrel lower shell 5, the underflow pipe 7, the built-in net barrel 8 and the upper overflow pipe 10 are coincided with the central axis of the barrel upper shell 1. The central axes of the parts are overlapped to ensure the separation efficiency of the oil sewage, the separated sewage spirally goes downwards along the separation cavity, and the oil stain upwards overflows through the overflow pipe.
Example 2:
the invention discloses a built-in net cylinder type oil-sewage separation cyclone, which is characterized in that in the actual operation process: when the device works, an external water pump provides enough pressure, oily water enters a rotational flow cavity 14 in an upper shell 1 of a cylinder body from the tangential direction of a liquid flow inlet 2, the oily water spirally moves downwards along the inclined surface of a guide circular truncated cone 12, the oily water moving downwards passes through a flow guide channel and a current transformer 13 between the wall surface of the upper shell 1 of the cylinder body and a built-in mesh cylinder 8 and then enters a separation cavity 16 in a lower shell 5 of a conical cylinder body, the rotational speed of the oily water in the separation cavity 16 is further accelerated, the radial pressure is unequal, the pressure near the axis is lowest, the side wall pressure of the separation cavity is highest, the oily water moves upwards while rotating, the sewage and granular substances move downwards and are discharged through a bottom flow pipe 7, in the process of discharging the sewage, the anti-blocking sewage can generate downward pressure on an assembly 17 in the bottom flow pipe 7, and the anti-blocking assembly 17 operates, the bottom flow pipe 7 of the cyclone is prevented from being blocked and abraded in a long-term working state.
Example 3:
the inventive cyclone (experimental group) and the common cyclone (control group) are selected, and the rated treatment capacity of the two groups of cyclones is 6
The flow-dividing ratio is 12 percent, the oil concentration of the oil-water mixed medium to be treated is controlled to be 2000mg/L, the engine oil of GL-4-80W/90 is selected, and the kinematic viscosity is 14.5-23m
Mixing the oil medium with water in a certain proportion to obtain an oil-water mixed medium, then statically mixing the oil-water mixed medium with an oil pump, respectively injecting the oil-water mixed medium into an experimental group and a control group, and testing the separation efficiency of the two groups of cyclones; as shown in FIG. 11, the separation efficiency of the cyclone of the present invention (experimental group) was about 95%, while that of the conventional cyclone (control group) was about 87%, which was 8% lower than that of the cyclone of the present invention (experimental group), and it can be seen that the cyclone of the present invention was divided into two partsThe separation efficiency is superior to that of the common cyclone.
The above disclosure is only for the purpose of illustrating the preferred embodiments of the present invention, and it is therefore to be understood that the invention is not limited by the scope of the appended claims.
Claims (8)
1. The utility model provides a built-in net section of thick bamboo formula oil sewage separation swirler, shell (5) under shell (1), the conical barrel on the cylinder, the upper end lateral wall of shell (1) has liquid stream inlet (2) along the tangential access on the cylinder, and shell (1) is inside to be equipped with whirl chamber (14) on the cylinder, and shell (1) top welding has fastening flange (4) down, its characterized in that on the cylinder: the built-in net barrel is inserted into the lower fastening flange (4), the top of the built-in net barrel (8) is fixedly connected with a connecting ring (9), two thirds of the built-in net barrel (8) are located in a rotational flow cavity (14), grids of the built-in net barrel (8) are thinned from top to bottom, and the meshes are gradually enlarged.
2. The cylinder type oil-sewage separation cyclone of claim 1, wherein: fastening flange (11) are equipped with above go up fastening flange (9), set up the screw hole that the position is the same between fastening flange (4) down, it passes through the screw connection, go up inside grafting of fastening flange (11) and have last overflow pipe (10), it is located built-in net section of thick bamboo (8) to go up overflow pipe (10) bottom, built-in net section of thick bamboo (8) diameter is greater than overflow pipe (10) diameter and is less than shell (1) diameter on the two-thirds cylinder.
3. The cylinder type oil-sewage separation cyclone of claim 1, wherein: the inner wall of the liquid flow inlet (2) is attached with wear-resistant rubber (15), the liquid outlet end of the liquid flow inlet (2) corresponds to the guide circular table (12), the guide circular table (12) is sleeved on the outer side of the built-in screen cylinder (8), and the top of the guide circular table (12) is connected with the top surface of the rotational flow cavity (14).
4. The cylinder type oil-sewage separation cyclone of claim 1, wherein: the cylinder is gone up shell flange (3) in shell (1) bottom connection, go up shell flange (3) and be connected through lower shell flange (6) at shell (5) top under screw and the conical barrel, separation chamber (16) have been seted up to shell (5) inside under the conical barrel, shell (5) end links firmly underflow pipe (7) under the conical barrel.
5. The cylinder type oil-sewage separation cyclone of claim 1, wherein: built-in net section of thick bamboo (8) bottom is equipped with converter (13), converter (13) middle part is equipped with the through-hole that link up, converter (13) are including water conservancy diversion bulb (131), cylinder carrier (132) are connected to water conservancy diversion bulb (131) below, toper drainage head (133) are connected to cylinder carrier (132) below, cylinder carrier (132) surface ring cloth has whirl blade (134), whirl blade (134) divide into the three-section, the upper segment and cylinder carrier (132) of whirl blade (134) are perpendicular, and the middle section is to one side bending, and the hypomere extends to cylinder carrier (132) bottom along the middle section bottom.
6. The cylinder type oil-sewage separation cyclone of claim 4, wherein: the conical wall of separation chamber (16) has rib plate (18) of encircleing, rib plate (18) inboard is equipped with interior awl (19), the opening part at interior awl (19) top is equipped with the clearance with the top of separation chamber (16), and the opening part of interior awl (19) has seted up sediment outflow hole (20), sediment outflow hole (20) lateral wall is connected with and keeps off stream block (21), conical groove (22) have been seted up on the wall at interior awl (19) top.
7. The cylinder type oil-sewage separation cyclone of claim 4, wherein: the underflow pipe (7) inner wall is equipped with prevents stifled subassembly (17), prevent stifled subassembly (17) including semicircular roller (172), roller (172) are located the concave hole that the underflow pipe (7) lateral wall was seted up, the concave hole that the underflow pipe (7) lateral wall was seted up has 4 at least, every the concave hole in all be equipped with roller (172), roller (172) middle part is connected with roller (171), and is equipped with the clearance between roller (172) and roller (171), roller (171) middle part is connected with underflow pipe (7) lateral wall, every the concave hole outside all be connected with air intake branch pipe (173) of slope, air intake branch pipe (173) are connected L shape and are admitted air and be responsible for (174), the air inlet end that L shape was admitted air and is responsible for (174) is located underflow pipe (7) outside, the horizontal end interlude of L shape air intake is responsible for (174) has stifled pole (176), the middle part of stifled pole (176) is connected elasticity rope (178) one end, the inside top surface of top cap (177) is connected to elasticity rope (178) other end, top cap (177) are located the outside of the horizontal end of L shape air intake main pipe (174), the top edge of stifled pole (176) is connected with stopper (179), the push pedal (175) of horizontal setting is connected to stifled pole (176) bottom.
8. The cylinder type oil-sewage separation cyclone of claim 1, wherein: the central axes of the lower conical barrel shell (5), the underflow pipe (7), the built-in net barrel (8) and the upper overflow pipe (10) are all coincided with the central axis of the upper cylindrical barrel shell (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010520689.6A CN111672641B (en) | 2020-06-10 | 2020-06-10 | Built-in net barrel type oil-sewage separation swirler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010520689.6A CN111672641B (en) | 2020-06-10 | 2020-06-10 | Built-in net barrel type oil-sewage separation swirler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111672641A true CN111672641A (en) | 2020-09-18 |
| CN111672641B CN111672641B (en) | 2021-10-12 |
Family
ID=72454408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010520689.6A Expired - Fee Related CN111672641B (en) | 2020-06-10 | 2020-06-10 | Built-in net barrel type oil-sewage separation swirler |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111672641B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112480958A (en) * | 2020-11-05 | 2021-03-12 | 中国石油大学(华东) | Axial-flow type oil-water separation device and method |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2238534A1 (en) * | 1973-07-24 | 1975-02-21 | Boise Cascade Corp | |
| CN2226496Y (en) * | 1994-11-04 | 1996-05-08 | 东北电力学院 | Fines separator |
| CN201940117U (en) * | 2010-11-29 | 2011-08-24 | 新疆旭日环保股份有限公司 | Whirling liquid pollutant removal device |
| CN102225382A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Pitting oil collecting curved cyclone of overflow pipe |
| CN103240193A (en) * | 2013-05-21 | 2013-08-14 | 天津曌宇环保科技发展有限公司 | Screen structure for cyclone separator |
| CN103286010A (en) * | 2013-05-22 | 2013-09-11 | 江苏新中环保股份有限公司 | Isolation device in cyclone dust remover |
| CN105536297A (en) * | 2016-02-26 | 2016-05-04 | 北京石油化工学院 | Tubular oil-water cyclone separation equipment |
| CN106111358A (en) * | 2016-06-30 | 2016-11-16 | 东北石油大学 | A kind of wear-resisting solid-liquid separating cyclone |
| CN209438828U (en) * | 2018-12-27 | 2019-09-27 | 吉水金诚新材料加工有限公司 | A kind of cyclone |
-
2020
- 2020-06-10 CN CN202010520689.6A patent/CN111672641B/en not_active Expired - Fee Related
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2238534A1 (en) * | 1973-07-24 | 1975-02-21 | Boise Cascade Corp | |
| CN2226496Y (en) * | 1994-11-04 | 1996-05-08 | 东北电力学院 | Fines separator |
| CN201940117U (en) * | 2010-11-29 | 2011-08-24 | 新疆旭日环保股份有限公司 | Whirling liquid pollutant removal device |
| CN102225382A (en) * | 2011-04-11 | 2011-10-26 | 东北石油大学 | Pitting oil collecting curved cyclone of overflow pipe |
| CN103240193A (en) * | 2013-05-21 | 2013-08-14 | 天津曌宇环保科技发展有限公司 | Screen structure for cyclone separator |
| CN103286010A (en) * | 2013-05-22 | 2013-09-11 | 江苏新中环保股份有限公司 | Isolation device in cyclone dust remover |
| CN105536297A (en) * | 2016-02-26 | 2016-05-04 | 北京石油化工学院 | Tubular oil-water cyclone separation equipment |
| CN106111358A (en) * | 2016-06-30 | 2016-11-16 | 东北石油大学 | A kind of wear-resisting solid-liquid separating cyclone |
| CN209438828U (en) * | 2018-12-27 | 2019-09-27 | 吉水金诚新材料加工有限公司 | A kind of cyclone |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112480958A (en) * | 2020-11-05 | 2021-03-12 | 中国石油大学(华东) | Axial-flow type oil-water separation device and method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111672641B (en) | 2021-10-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR890000527B1 (en) | Cyclone separators | |
| US6599422B2 (en) | Separator for liquids containing impurities | |
| CN105779022B (en) | Cyclone separator and gas-liquid solid separation system | |
| US9101869B2 (en) | Swirl helical elements for a viscous impingement particle collection and hydraulic removal system | |
| CN110735626B (en) | Pipeline type natural gas desanding device | |
| CN111672642B (en) | Built-in cone net type oil-sewage separation swirler | |
| US20150306528A1 (en) | Swirl helical elements for a viscous impingement particle collection and hydraulic removal system | |
| CN111672641B (en) | Built-in net barrel type oil-sewage separation swirler | |
| CN201140115Y (en) | Rotation increasing mesh screen hydraulic swirling-flow separator | |
| CN111001500A (en) | Inner flow passage of one-way centrifugal pump centrifuge | |
| RU2452579C2 (en) | Centrifugal concentrator | |
| CN211275038U (en) | Disc type separator | |
| KR20180022758A (en) | Dual cyclone type processing apparatus of suspened solids | |
| CN116986669A (en) | Vertical double-stage cyclone dirt remover | |
| CN108311295B (en) | Composite force field step reinforced centrifugal ore separator | |
| CN103201042A (en) | Bottom diluter structure in a vortex cleaner, and method in a bottom diluter structure in a vortex cleaner | |
| CN115957544A (en) | Rotational flow sand setting device for sewage treatment | |
| CN113559619B (en) | Two-stage separation dust removing equipment and method thereof | |
| CN109647239A (en) | A kind of waterpower mixing arrangement | |
| CN111632439B (en) | Enhanced separation type raw gas coalescence separator | |
| CN212576575U (en) | Static sludge cyclone | |
| CN1286571C (en) | A device for a cyclone scrubber | |
| CN109107786B (en) | High-temperature belt-pressure high-efficiency cyclone separator | |
| CN218048435U (en) | Cyclone classifying screen | |
| CN110585801A (en) | Pipeline type filter adopting cyclone separation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20211012 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |