WO2015051745A1 - Séparateur - Google Patents

Séparateur Download PDF

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Publication number
WO2015051745A1
WO2015051745A1 PCT/CN2014/088195 CN2014088195W WO2015051745A1 WO 2015051745 A1 WO2015051745 A1 WO 2015051745A1 CN 2014088195 W CN2014088195 W CN 2014088195W WO 2015051745 A1 WO2015051745 A1 WO 2015051745A1
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WO
WIPO (PCT)
Prior art keywords
vortex
chamber
separation chamber
vortex separation
separator
Prior art date
Application number
PCT/CN2014/088195
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English (en)
Chinese (zh)
Inventor
陈久斌
Original Assignee
陈久斌
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 陈久斌 filed Critical 陈久斌
Publication of WO2015051745A1 publication Critical patent/WO2015051745A1/fr

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B3/00—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering

Definitions

  • the utility model relates to a separator machine, a centrifuge device, a sewage treatment device, a seawater desalination device, a marine chemical equipment, a mineral processing equipment, a garbage disposal equipment, an odor eliminating equipment, an oil and gas recovery equipment, an air purification equipment, a dust removal equipment, a vacuuming equipment,
  • the field of range hoods, oxygen production equipment, oil refining equipment, etc. is specifically a separator.
  • Environmental pollution has seriously affected the Earth's ecological circle.
  • the existing sewage treatment equipment is complicated, the cost is too high, the sewage treatment cost is too high, the treatment effect is general, and sewage treatment has become the top priority of environmental treatment.
  • the existing water purifiers mainly adopt methods such as filtration and water purifying agents, and there are generally defects such as failure to reach higher drinking water standards and high water purification costs.
  • the existing air purification equipment has a general purification effect and cannot completely treat the dust.
  • the existing dust removal equipment has cyclone dust removal, electric dust removal, bag dust removal, etc., and there are generally defects such as unsatisfactory dust removal effect and high energy consumption. Dust pollution has become the most important. Source of pollution.
  • the existing odor removal equipment has a general purification effect, and has no ideal treatment method for many chemical odors, and odor gas pollution has become an important pollution source.
  • the existing oil and gas recovery equipment is too expensive, the energy consumption is too high, and the recycling effect is general.
  • the existing oxygen production equipment is too expensive, the oxygen production cost is too high, and the universal application cannot be realized, so that pure oxygen combustion cannot be achieved, and a large amount of nitrogen oxides are discharged to form an important pollution source.
  • the dust collection effect of the existing vacuuming equipment is not ideal, the noise is large, the dust particles are polluted, and the dust is troublesome after dust removal.
  • the existing range hoods are unable to separate the soot, causing troubles in the cleaning of the range hood, causing the soot particles to pollute the environment, and the soot particles have become another important source of pollution for urban air pollution.
  • the existing separation equipment mainly including centrifuges, generally has the defects of general separation effect and large energy consumption.
  • the existing seawater desalination equipment is complicated, the cost is too high, the seawater desalination cost is too high, and the energy consumption is too large.
  • the existing marine chemical equipment is complex, the cost is too high, and the utilization of marine resources is not satisfactory.
  • the existing beneficiation equipment has a general ore dressing effect and cannot achieve finer sorting, resulting in waste of resources and environmental pollution.
  • the existing refinery equipment generally adopts high-temperature distillation cracking method, which has high refining cost and high energy consumption.
  • the high temperature damages the macromolecules in the crude oil, and generates a large amount of petroleum gas and petroleum slag, which greatly reduces the oil yield and reduces the high-quality oil output.
  • the utility model provides a separator, adopts a new separation method, adopts a new vortex separation principle, fully utilizes fluid motion, utilizes mutual friction between fluid particles, utilizes eddy currents, causes fluid to be affected by eddy currents, and centrifugal force in circular motion Under the action, the eddy current is used to achieve separation.
  • the eddy current is formed by the mutual friction between the fluid particles and the acceleration of the motion, and the centrifugal force generated in the vortex is used to separate the particles of different volumes and specific gravity from each other. Particles of different volumes and specific gravity move at different speeds toward the periphery of the vortex, and the particles move faster toward the periphery of the eddy current than the larger particles.
  • the particles with larger specific gravity will move to the periphery of the vortex earlier, and the particles with smaller specific gravity will move to the periphery of the vortex later, and use this to realize the sorting of different substances.
  • Each point in the eddy current field has a relative motion with each other. The motion causes each point to interact with each other, and friction and collision occur between them.
  • the glued and dissolved molecules can be separated, and each particle, atom and other particles in the eddy current can form different moving speeds, and different particle sizes can be made by eddy current and centrifugal force and gravity. Different proportions of substances enter different areas.
  • the solute in the solution can be completely separated from the solvent, the different solute can be separated, the different suspended particles can be separated, and the gas components in the solution can be separated.
  • the separator can achieve cleaner dust removal, cleaner air purification, cleaner purifying soot, cleaner sewage treatment, cheaper seawater desalination, more efficient use of water resources, more complete extraction of marine resources, and more Efficient beneficiation, cleaner waste disposal, and more efficient refining.
  • the separator of the utility model can be widely applied to various fields of separation equipment. It can be used as a new type of centrifuge and separator. It has better separation effect, can separate, sort, extract and purify various components, and can also decompose various gaseous compounds. It can be separated and sorted out. Multiple elements. It can also be used to remove bubbles from the glass melt, which can completely separate the gas in the glass melt.
  • This separator can be used as an air purification device and can be used as a new indoor air purifier. It can be used as an odor-eliminating device to remove odorous gases. It can be used as a dust collector and can exceed the dust removal effect of any type of dust collector.
  • the separator can be used as an oil and gas recovery device to recover a variety of oil vapors.
  • the separator can also be used as a range hood to separate soot and make the flue gas emissions more environmentally friendly.
  • the separator can be used as a vacuum cleaner, and a filter screen can be arranged at the suction nozzle to filter the long fiber material in the filter screen separately.
  • the separator has convenient dust cleaning, low noise, good dust collecting effect, low cost and more energy saving, and is used as a vacuum cleaner without dust pollution, which is more sanitary and environmentally friendly.
  • the separator can be used as a sewage treatment device to extract a variety of useful components from sewage to realize resource recycling. Pure water can be directly supplied to meet drinking water standards, which can completely solve water pollution and solve water shortage problems.
  • the separator can be used as a water purification device to completely separate harmful elements in tap water to achieve higher drinking water standards, allowing people to drink more pure and healthy drinking water.
  • the separator can be used as a garbage disposal device. After the garbage is pulverized into granules, the granules are transported by water to carry out wet selection, the useful components are separated and sorted, and the useless components and the organic components are combined to be pressed into granule organic fertilizer, which can be thoroughly Eliminate environmental pollution and achieve resource recycling.
  • the separator can separate oxygen from the air, and the oxygen production cost is extremely low, so that the boiler, the kiln, the engine, the heat engine and the like can realize the cheap and economical pure oxygen combustion, can reduce the energy consumption, improve the heat work efficiency, and completely eliminate the nitrogen oxidation. Emissions, reducing engine volume, weight, displacement, and torque. Exhaust gas recirculation can also be used for engines, heat engines, kilns, boilers, etc., which can reduce combustion temperatures and reduce equipment material requirements.
  • the separator can be used as a new air purifier to remove dust and soot particles from the room.
  • the separator can be used as a beneficiation equipment to separate and extract a variety of minerals and raw materials, to remove impurities, and even to screen a variety of useful minerals from lean ore.
  • the ore can be pulverized into granules, and the granules are transported by water to carry out wet selection.
  • high-purity raw materials can be obtained, which can reduce the cost of raw material processing.
  • the separator can be used as seawater desalination equipment and marine chemical equipment, which can greatly reduce equipment cost, reduce seawater desalination cost, greatly reduce energy consumption, improve seawater desalination efficiency, and increase fresh water production. Simultaneously extract various useful ingredients from seawater, and at the same time realize separation, extraction and sorting and purification of various useful ingredients, which can be used as salt extraction equipment and marine chemical equipment, which can greatly reduce equipment cost.
  • various minerals can be extracted from the rivers and lakes, which can better protect the environment and resources. The water quality of rivers, lakes and seas will be better, and the earth's ecological environment can be better protected.
  • the separator When the separator is used as an oil refining equipment, it can realize low temperature cracking of crude oil, reduce the destruction of macromolecular components in crude oil, reduce the output of petroleum gas and petroleum slag, increase the oil yield, and improve the output of high quality oil.
  • the oil can be completely lead-free and free of radioactive elements.
  • the whole production process is free from pollution, and there is no waste water or exhaust gas.
  • the refining process is completely environmentally friendly, and the resources are completely utilized, which can greatly reduce the cost of refining.
  • the separator comprises a casing and a transmission device, a transmission device is arranged on the casing, a casing cavity is arranged in the casing, a vortex separation wheel is arranged in the casing cavity, a transmission device is connected with the vortex separation wheel, a vortex separation chamber is arranged in the vortex separation wheel, and the vortex separation is performed.
  • One end of the chamber is provided with an inlet of the vortex separation chamber, and the other end of the vortex separation chamber is provided with a shaft end outlet of the vortex separation chamber, and a plurality of vortex separation chamber peripheral outlets are arranged at the outer periphery of the vortex separation chamber, and a casing cavity inlet is provided on the casing corresponding to the inlet of the vortex separation chamber, and the casing is provided.
  • a stator stirring body is arranged, the stator stirring body penetrates into the vortex separating chamber, and a pressure increasing device is arranged outside the shaft end outlet of the vortex separating chamber, and at least one surrounding separator is arranged on the inner wall of the housing cavity, and at least two out of the housing cavity are arranged Feed port.
  • the discharge port is provided with an active sealing and unloading device.
  • the eddy current separation chamber is provided with a reinforcing card at the inlet.
  • the supercharging device is provided with at least one surrounding separation ring corresponding to the shaft end outlet of the vortex separating chamber, and the separating device is provided with a separating body corresponding to the surrounding separating ring, and the corresponding partition body on the inner wall of the housing chamber is provided with a surrounding separator, and the housing chamber is provided with a plurality of discharging ports.
  • a transmission is provided in the stator stirrer.
  • a liquid supply device is disposed on the housing corresponding to the housing cavity.
  • the outer diameter of the supercharging device is larger than the outer diameter of the vortex separation.
  • a flow guiding channel is arranged in the stator stirring body, and the outlet of the guiding flow channel is connected to the inlet of the vortex separating chamber, and the vortex separating chamber is arranged near the end of the transmission device to set the inlet of the eddy current separation chamber.
  • At least one surrounding partitioning plate is disposed in the supercharging device, and the inner wall of the casing cavity is disposed around the partitioning plate corresponding to the surrounding partitioning plate, and the casing cavity is provided with a plurality of discharging openings.
  • a plurality of surrounding partitions are disposed on the inner wall of the casing cavity surrounding the vortex separating chamber, and the casing cavity is provided with a plurality of discharging ports.
  • the utility model has the advantages that the circular motion and the fluid motion are fully utilized, the eddy current is fully utilized, and the fluid is separated by the eddy current, and the effect is synchronously improved with the increase of the rotational speed.
  • the utility model has the advantages of simple manufacture, low manufacturing cost, low use cost, low maintenance cost and long service life.
  • Figure 1 is a schematic view showing the structure of the main body of the separator of the present invention.
  • Figure 2 is a front view showing the structure of one of the embodiments of the separator of the present invention.
  • Figure 3 is a front view showing the structure of the second embodiment of the separator of the present invention.
  • Figure 4 is a front view showing the structure of the third embodiment of the separator of the present invention.
  • Figure 5 is a front view showing the structure of the fourth embodiment of the separator of the present invention.
  • Figure 6 is a front view showing the structure of the fifth embodiment of the separator of the present invention.
  • Figure 7 is a front view showing the structure of the sixth embodiment of the separator of the present invention.
  • Figure 8 is a front view showing the structure of the seventh embodiment of the separator of the present invention.
  • Figure 9 is a front view showing the structure of the eighth embodiment of the separator of the present invention.
  • Figure 10 is a schematic front view showing the structure of the ninth embodiment of the separator of the present invention.
  • the main structure of the separator of the utility model comprises a casing 1 and a transmission device 2, wherein the casing 1 is provided with a transmission device 2, and a casing cavity 3 is arranged in the casing 1, a vortex separating wheel 4 is arranged in the casing cavity 3, the transmission device 2 and the eddy current
  • the separation wheel 4 is connected, and the vortex separation wheel 4 is provided with a vortex separation chamber 5.
  • One end of the vortex separation chamber 5 is provided with a vortex separation chamber inlet 6, and the other end of the vortex separation chamber 5 is provided with a vortex separation chamber shaft end outlet 7, and the vortex separation chamber 5 is disposed at the outer periphery.
  • the vortex is separated from the outdoor peripheral outlet 8, and the casing 1 is provided with a casing cavity inlet 9 corresponding to the vortex separation chamber inlet 6.
  • the casing 1 is provided with a stator agitating body 10 corresponding to the vortex separation chamber 5, and the stator agitating body 10 is inserted into the vortex separation chamber.
  • a pressure increasing device 11 is arranged outside the shaft end outlet 7 of the vortex separating chamber, and at least one surrounding wall 12 is arranged on the inner wall of the housing chamber 3.
  • the housing chamber 3 is provided with at least two discharging ports 13.
  • the scope of the housing 1 includes a base, a casing, a pipe, and a power unit, and each part may be collectively referred to as a casing.
  • the housing may also be integral with the power unit to form a unitary housing.
  • an insulating material or a heat sink may be disposed outside the casing.
  • the separator can be made of different materials according to needs, and can be made of materials such as metal, alloy, ceramic, glass, glass steel, carbon fiber, graphite, plastic, nylon, foam, and the like.
  • the transmission device 2 includes a transmission shaft, a bearing or a bearing bush, a shaft seat, a sealing device, etc., and the transmission device 2 is provided with a transmission
  • the shaft uses the drive shaft to realize the power input and drives the separator to work.
  • the transmission device 2 is connected to the power device to realize the power input, and drives the separator to work.
  • the power unit can use a motor or an engine.
  • the power unit can be directly connected to the transmission unit 2, or can be powered by a coupling drive, a belt drive, a chain drive, a gear drive or a magnetic drive.
  • the power device and the housing can also be directly integrated, and the rotating shaft of the power device can be directly used as the transmission device 2, and the rotation of the transmission device 2 can be realized by using the bearing of the power device.
  • High-speed motors can be used to increase the speed of the transmission, and other high-speed power units can be used.
  • the speed can also be adjusted by using frequency conversion technology, etc., and the separation effect can be adjusted.
  • Bearings and seals can be manufactured with graphite bearings or graphite seals when the separator is operated at high temperatures.
  • a rotary sealing device may be disposed between the transmission device 2 and the casing 1, and a rotation may be provided between the transmission shaft of the transmission device 2 and the casing 1.
  • rotary sealing device can adopt graphite seal, graphite bearing, sealing ring, sealing packing, sealing packing, mechanical seal, magnetic sealing, magnetic fluid sealing and other devices.
  • the rotary seal prevents fluid from leaking out of the interior of the housing cavity 3.
  • the separator can also be used as a submersible separator.
  • the desalinated fresh water can be directly transported ashore to leave the separated salt in the ocean.
  • a high-speed motor can be used, which can reduce the volume of the equipment.
  • the high-speed motor can be cooled by the engine cooling system, and water cooling can be adopted.
  • a high-speed motor can also be used. The high-speed motor can directly use the treated water to cool, and the pressure generated by the separator can be used to cool the water through the high-speed motor.
  • a transmission 2 is arranged on the housing 1.
  • the separator can be arranged outside the housing 1 or the transmission 2 can be arranged in the housing 1. When the separator is installed upright, gravity and buoyancy can be better utilized, and the transmission 2 can be placed on the upper part of the casing to simplify the installation.
  • the splitter drive shaft can also be mounted horizontally or diagonally to allow the splitter to adapt to more operating conditions.
  • a housing cavity 3 is provided in the housing 1.
  • the cross section of the cavity of the housing cavity 3 can be arranged in various shapes such as a volute shape, a circular shape, a square shape or a polygonal shape.
  • the housing cavity 3 can be formed as an axially split open body or a horizontally open open body.
  • the opening position and the number of open bodies can be arbitrarily set according to requirements, and can be connected together during installation. Misalignments, seals or gaskets can be placed at the joint to better avoid leakage.
  • the inner wall of the housing cavity 3 can also be provided with a layer of wear resistant material, a bushing or a corrosion resistant layer to increase the service life or increase the range of use.
  • the housing cavity 3 can be made of a high temperature resistant material, and an insulating material or a heat dissipating device can be disposed outside the housing cavity 3.
  • a vortex separating wheel 4 is disposed in the housing chamber 3.
  • the cavity area can be used to realize the separation, collection, sorting and collecting of the separated objects.
  • the outside of the vortex separating wheel 4 can be arranged in a cylindrical or staggered cylindrical structure, and the staggered cylindrical shape can better coordinate the pressure in different regions of the housing cavity 3.
  • the vortex separating wheel 4 is disposed on the central axis of the housing chamber 3. The axial length of the vortex separating wheel 4 is appropriately lengthened to improve the separation effect, and the larger the diameter of the vortex separating wheel 4, the larger the flow rate.
  • the ratio of the axial length of the vortex separating wheel 4 to the diameter of the vortex separating wheel 4 can be arbitrarily set as needed.
  • the experiment proves that the ratio of the axial length of the vortex wheel 4 to the diameter of the vortex wheel 4 is preferably 0.382-0.618:1, which can better coordinate the dynamic balance of the vortex wheel 4.
  • the separation accuracy can be improved.
  • the vortex separating wheel 4 is usually provided as a single unit, and the vortex separating wheel 4 can be arranged in a hollow structure.
  • the vortex separating wheel 4 can be made of different materials according to requirements, and can be made of materials such as metal, alloy, ceramic, glass, glass steel, carbon fiber, graphite, plastic, nylon, refractory material, foam material and the like.
  • a labyrinth seal structure may also be provided on the end surface of the vortex separating wheel 4 corresponding to the inner wall of the housing chamber 3, so that leakage of fluid between the transmission shaft and the housing 1 can be better avoided.
  • the end face of the vortex separating wheel 4 can also be brought close to the inner wall of the casing cavity 3. The smaller the gap, the better, and the leakage of fluid between the transmission shaft and the casing 1 can be better avoided.
  • the transmission 2 is connected to the vortex separating wheel 4.
  • the transmission shaft of the transmission device 2 is to be connected and fixed in the axial center region of the vortex separation wheel 4 to ensure smooth rotation of the vortex separation wheel 4, and a connecting body such as a wheel disc and a wheel body can be arranged in the axial center region of the vortex separation wheel 4, which is more convenient.
  • the drive shaft is fixedly connected to the vortex separating wheel 4 and is detached. When the splitter drive shaft is mounted upright, the transmission 2 can be coupled to the upper end of the vortex separating wheel 4.
  • a vortex separation chamber 5 is provided in the vortex separating wheel 4.
  • the vortex separating wheel 4 can be disposed as a cavity, and the vortex separating chamber 5 can be formed by the cavity.
  • the vortex separation chamber 5 may be provided as a cavity having a circular cross section to better maintain the dynamic balance of the vortex separating wheel 4, so that a vortex flow having an increasing rotational speed from the center to the periphery is formed in the vortex separation chamber 5.
  • the vortex separation chamber inlet 6 is provided when the vortex separation chamber 5 is away from one end of the transmission device 2, so that fluid can enter the vortex separation chamber 5 from the opposite side of the transmission device 2, which simplifies the structure.
  • the vortex separation chamber inlet 6 may also be disposed at one end of the vortex separation chamber 5 near the transmission device 2, and the fluid may be introduced into the vortex separation chamber 5 through the vortex separation chamber 5 by using the flow guiding tube.
  • the disadvantage is that the energy consumption is relatively higher, and the advantages are It is available for special function structures.
  • the ratio of the inner diameter of the vortex separation chamber inlet 6 to the maximum inner diameter of the vortex separation chamber 5 can be arbitrarily set as needed, so that the inner diameter of the vortex separation chamber inlet 6 can be equal to the maximum inner diameter of the vortex separation chamber 5, which can be more Coordinating the peripheral pressure of the vortex separation chamber 5 well can improve the separation effect. It is also possible to provide a reinforcing ring at the inlet 6 of the vortex separation chamber, and the reinforcing ring can thicken the edge of the inlet 6 of the vortex separation chamber, thereby improving the structural strength of the vortex separation chamber 5.
  • the other end of the vortex separation chamber 5 is provided with a vortex separation chamber shaft end outlet 7.
  • the vortex separation chamber shaft end outlet 7 is opened at one end of the vortex separation chamber 5 close to the transmission 2, and the fluid can be axially passed through the vortex separation chamber 5.
  • the inner diameter of the vortex separation chamber shaft end outlet 7 is less than or equal to the maximum inner diameter of the vortex separation chamber 5, and the inner diameter of the vortex separation chamber shaft end outlet 7 is smaller than the inner diameter of the vortex separation chamber 5, which can slow the axial movement speed of the fluid and prolong the fluid in the vortex separation chamber.
  • the residence time in 5 can improve the separation effect.
  • the inner cavity of the vortex separation chamber 5 can be arranged in a cylindrical structure to improve the separation effect.
  • the inner cavity of the vortex separation chamber 5 may also be arranged to gradually expand or gradually contract toward the end of the shaft end 7 of the vortex separation chamber, so as to better prevent the deposition of particulate matter on the inner wall of the vortex separation chamber 5, and the inner cavity of the vortex separation chamber 5
  • the expansion angle can be arbitrarily selected, and can be specifically determined according to working conditions. When the particles are easily deposited on the inner wall of the vortex separation chamber 5, the expansion angle can be increased, and the maximum is not more than 30 degrees, and the expansion angle is too large, which easily affects the separation effect.
  • a plurality of eddy current separation outdoor peripheral outlets 8 are provided on the outer circumference of the vortex separation chamber 5.
  • the vortex separation outdoor circumferential outlet 8 may be disposed on the circumference of the vortex separation chamber 5, and may be directly drilled in the vortex separation outdoor peripheral wall as the vortex separation outdoor peripheral outlet 8, and a plurality of eddy current separation may be disposed on the outer periphery of the vortex separation chamber 5.
  • the outdoor circumferential outlet 8 allows a plurality of different separations to be leaked by the plurality of vortex separation outdoor peripheral outlets 8.
  • the arrangement of a plurality of closely arranged vortex separation outdoor peripheral outlets 8 in the vortex separation outdoor circumference can better prevent the separation of the separation objects on the inner wall of the vortex separation chamber 5, and the outer peripheral wall of the vortex separation chamber 5 can be made into a sieve in which the holes are axially staggered.
  • the stencil can simplify the structure and can smoothly select 1-10mm holes.
  • the number of vortex separation outdoor circumferential outlets 8 can be appropriately increased, and the area of the vortex separation outdoor circumferential outlet 8 can be appropriately increased, so that dust or the like can be better prevented from being deposited on the inner wall of the vortex separation chamber 5.
  • the ratio of the total area of the vortex separation outdoor peripheral outlet 8 to the total area of the inner wall of the vortex separation chamber 5 should not be too large, and it is sufficient, and the ratio should not exceed 0.5:1, which may affect the separation effect.
  • a housing cavity inlet 9 is provided in the housing 1 corresponding to the vortex separation chamber inlet 6.
  • a casing cavity inlet 9 may be provided on the casing 1 corresponding to the vortex separation chamber inlet 6, and the fluid to be separated may be sent into the separator through the casing cavity inlet 9.
  • the casing cavity inlet 9 is smaller than or equal to the vortex separation chamber inlet. 6 calibers can be.
  • a housing chamber inlet 9 can be provided at the lower end of the housing chamber 3 to allow fluid to move from bottom to top within the separator.
  • the housing cavity inlet 9 can be provided opposite the transmission 2, which simplifies the structure.
  • the flow regulating device can be provided with a valve, a damper and the like, and the flow regulating device can adjust the flow rate, the pressure in the casing cavity 3 and the separation effect.
  • a stator agitating body 10 is disposed on the casing 1 corresponding to the vortex separating chamber 5, and the stator agitating body 10 penetrates into the vortex separating chamber 5.
  • the axial center of the stator agitating body 10 can be closed, and the axial flow region of the stator agitating body 10 can also be provided with a flow guiding channel.
  • the outer circumference of the stator stirring body 10 is circular, and the outer portion of the stator stirring body 10 can be arranged in a cylindrical shape with the same thickness at both ends, and the outer portion of the stator stirring body 10 can also be arranged in a plurality of cylindrical cylinders having different outer diameters.
  • the outer portion of the stator agitating body 10 may be disposed to gradually expand or taper from the end of the vortex separation chamber inlet 6 to the outer diameter of the other end.
  • the outer wall of the stator stirring body 10 can be arranged corresponding to the inner wall of the vortex separation chamber 5, and can be arranged in parallel, which can better improve the separation effect.
  • the stator stirring body 10 is fixedly connected with the casing 1 to keep the stator stirring body 10 stationary as a stator, and a fixed supporting device may be disposed at one end of the stator stirring body 10 to weld or connect the fixed supporting device to the stator.
  • the inner wall of the casing 1 or the edge of the casing cavity inlet 9 keeps the stator agitating body 10 fixed, and the fixed supporting means leaves a gap, a cavity or a void to form a flow path, so that fluid can enter the casing cavity 3 through the flow path.
  • the stator agitating body 10 may be axially penetrated through the vortex separation chamber 5, and the other end of the stator agitating body 10 may be kept at a certain distance from the vortex separation chamber shaft end outlet 7.
  • the outer diameter of the stator agitating body 10 may be smaller than the inner diameter of the vortex separating chamber 5, and the flow passage area formed by the gap between the outer portion of the stator agitating body 10 and the inner wall of the vortex separating chamber 5 may be ensured.
  • the stator stirring body 10 can also be made into a tubular shape, and a baffle can be arranged in the tube to close the pipe, and the pipe is probed into the vortex separating chamber 5, and one end of the pipe is perforated to form a fixed supporting device and fixed at the edge of the casing cavity inlet 9.
  • the structure can be simplified.
  • the surface of the stator stirrer 10 can be made into a smooth or coarse surface, and the smooth surface can be used to better utilize the boundary layer effect, thereby improving the separation effect. It is also possible to provide shallow grooves or pits on the surface of the stator stirrer 10 to increase the surface friction coefficient of the stator stirrer 10, which can better improve the relative motion speed of the particles in the vortex and improve the separation effect.
  • stator stirring body 10 can increase the acceleration of the eddy current from the center to the peripheral speed, which can greatly improve the separation effect of the eddy current.
  • the outer wall of the stator stirring body 10 is stationary, and the inner wall of the vortex separating chamber 5 is rotated. There is relative movement between the two, and the relative friction between the two is present between the outer wall of the stator stirring body 10 and the inner wall of the vortex separating chamber 5. Room The smaller the gap, the more intense the relative motion, the more intense the relative friction of the fluid existing between the two, and the more intense the eddy current.
  • the stator stirring body 10 can block the axial flow of the fluid along the axial center of the vortex separation chamber 5, so that the fluid can be better separated during the axial movement of the circular cylindrical vortex, and the separation effect of the eddy current can be greatly improved.
  • the fluid particles can form a larger frictional force with each other, which can better improve the separation. ability.
  • the surface layer effect of the surface of the stationary stator stirrer 10 can adsorb the lighter weight separation, and the centrifugal force generated by the inner wall of the rotating vortex separation chamber 5 can attract the heavier specific gravity, from the center to the periphery.
  • the annular vortex with increasing rotational speed causes the separations of different specific gravity to move to the center of the vortex and the periphery of the vortex respectively, and finally realize the separation of the separations of different specific gravity.
  • stator stirrer 10 If there is no stator stirrer 10, the separators of different specific gravity move to the inner wall of the vortex separation chamber 5 under the action of centrifugal force, and finally it is difficult to achieve separation, and at the same time, due to the lack of friction of the surface of the stator stirrer 10, the final result is
  • the ring-shaped eddy current with increasing speed from the center to the periphery disappears, and becomes a rotating body with the center and the peripheral rotation speed, which greatly reduces the separation effect, which is the root cause of the poor separation effect of the existing centrifuge technology
  • the stator stirring body 10 is a key component for forming eddy currents and improving the eddy current separation effect. It is also possible to arrange the transmission 2 in the stator agitating body 10 to reduce the volume of the apparatus.
  • a supercharging device 11 is disposed outside the shaft end outlet 7 of the vortex separating chamber.
  • a supercharged impeller or a pressurized chamber may be disposed outside the outlet end of the vortex separation chamber as a supercharging device 11.
  • the supercharged impeller may adopt a centrifugal impeller structure, which may be a closed impeller or an open impeller structure;
  • the cavity having an outer diameter larger than the outer diameter of the vortex separation chamber 5 may be provided with a plurality of outlets on the outer circumference of the plenum chamber.
  • the outer diameter of the supercharging device 11 is greater than or equal to the outer diameter of the vortex separating chamber 5.
  • the peripheral pressure of the supercharging device 11 can be further increased.
  • the disadvantage is that the structure is complicated and increased.
  • the outer diameter of the supercharging device 11 is usually equal to the outer diameter of the vortex separation chamber 5.
  • the pressurizing device 11 pressurizes the fluid from the shaft end outlet 7 of the vortex separating chamber to increase the fluid pressure, which is advantageous for the fluid to be transported out of the casing chamber 3, and at the same time, the fluid discharged from the outdoor outlet 8 of the vortex separating chamber is prevented from leaking into the vortex.
  • the outer region of the shaft end outlet 7 of the separation chamber causes secondary separation of the separator.
  • the length of the boosting blade of the supercharging device 11, the number of blades or the outer diameter of the supercharging device 11 can be set according to the required conveying pressure. Generally, the pressure should not be too high, and the pressure is too high to increase the energy consumption. The axial thickness of the supercharging device 11 should not be too large, and the energy consumption can be increased by the assembly, and the flow rate can be sufficient.
  • At least one surrounding surround 12 is disposed on the inner wall of the housing cavity 3.
  • One or more surrounding separators 12 may be axially disposed on the inner wall of the housing chamber 3, and one or more surrounding surfaces may be disposed on the inner wall of the housing chamber 3 on the periphery of the vortex separating chamber 5.
  • the separator 12 can also be provided with one or more surrounding separators 12 on the inner wall of the housing chamber 3 on the periphery of the pressurizing device 11.
  • the outer edge of the surrounding body 12 is connected and fixed on the inner wall of the housing cavity 3, and is integrally sealed with the inner wall of the housing cavity 3.
  • the surrounding body 12 can axially divide the housing cavity 3 into a plurality of areas, which can separate the separated objects. Open, finally achieving separation of different isolates.
  • the surrounding separator 12 can be adjacent to the supercharging device 11, and a portion of the vortex separating chamber 5 near the shaft end outlet 7 of the vortex separating chamber is not provided with the vortex separating outdoor peripheral outlet 8 so that Surrounding the partition 12 at the periphery between the supercharging device 11 and the vortex separating outdoor peripheral outlet 8, it is possible to better prevent the separation of the effluent separation outdoor outlet 8 from leaking to the outer portion of the vortex separating chamber shaft end outlet 7 to cause separation Secondary mixing of the material can improve the separation effect.
  • At least two discharge openings 13 are provided in the housing chamber 3.
  • Two or more discharge ports 13 may be axially disposed in the housing cavity 3, and when the two discharge ports 13 are axially disposed in the housing cavity 3, the separations of different specific gravity may be respectively discharged from the two discharge ports 13
  • the body cavity 3 is provided with a plurality of discharge ports 13 in the axial direction, the separators of different specific gravity can be discharged from the respective discharge ports 13 respectively.
  • the discharge port 13 can be arbitrarily arranged, and can be arbitrarily disposed in the upper part, the lower part or the periphery of the housing cavity 3.
  • the discharge opening 13 can also be arranged in the tangential direction of the cross section of the housing cavity, and the outlet is directed forward in the direction of rotation of the vortex separating wheel 4, and can be utilized.
  • the centrifugal force and the inertia of the fluid are better to allow the separation to be smoothly discharged from the housing chamber 3.
  • the lower part of the housing cavity 3 can be arranged in a funnel shape, the funnel can be arranged in the tangential direction of the cross section of the housing cavity, and the discharge opening 13 is arranged in the lower part of the housing cavity 3, so that the granular separation can be better
  • the object is discharged after being settled in the lower portion of the casing chamber 3.
  • the discharge port 13 can be set to a fixed flow rate as needed, or a flow regulating device can be provided, which is set to an adjustable flow rate.
  • the pressure in different regions of the housing chamber 3 can be adjusted by adjusting the flow rate of the discharge port 13, and the separation effect can be improved.
  • the separation effect can be improved.
  • the housing cavity 3 is axially disposed in a plurality of regions, a plurality of discharge ports 13 are axially disposed at the same time, and at least one discharge port 13 is correspondingly disposed in each of the housing cavity regions, so that the separation can be further sorted.
  • a plurality of discharge ports 13 may be provided on the circumference of the casing chamber 3 to increase the flow rate.
  • the discharge port 13 can also be provided with a movable sealing and unloading device, which can be provided with a valve, a damper, a screw conveyor and the like.
  • the movable sealing and discharging device can adjust the flow rate, can adjust the separation effect, and can make the separation object in the casing according to the separation amount. Under the action of pressure, gravity and centrifugal force, it can be discharged from the casing, and the movable sealing and discharging device can be intermittently opened to discharge the separated matter.
  • a vacuum cleaner When used as a vacuum cleaner, a dust remover, a water purifier, etc., a ash box, a ash chamber, a sedimentation chamber, etc. may be provided in the lower part of the housing chamber 3, and the discharge port 13 may be provided in the lower part of the housing chamber 3.
  • one or more discharge ports 13 When the separator is installed transversely, one or more discharge ports 13 may be provided in the lower portion of the casing chamber 3 to facilitate the discharge of the separator.
  • Separator vertical When installed, a plurality of discharge ports 13 may be provided on the circumference around the housing chamber 3 to facilitate the discharge of the separator.
  • the separator of the main structure can be used as a dust collector, a vacuum cleaner, an oxygen generator, a seawater desalination device, a plasma separator, a cream separator, a glass melt defoaming machine, a tail gas processor, an odor removing device, an oil and gas recovery device, and an engine exhaust.
  • the purifier or the like can be used to simultaneously deliver the fluid. The higher the separator speed, the better the separation.
  • the separator drive shaft is installed vertically, the casing cavity inlet 9 can be arranged at the lower end of the separator; when the separator drive shaft is horizontally or obliquely installed, a plurality of discharge ports 13 can be arranged at the lower portion of the casing cavity 3, which is advantageous for solid separation.
  • the material is discharged, and one or more discharge ports 13 may be disposed at the upper portion of the casing chamber 3 to facilitate the discharge of gas components.
  • the separator When used as a dust removal device or a vacuum cleaner, the separator can be installed upright, diagonally or transversely. Gas can be drawn into the separator from the inlet 9 of the housing chamber, and the dust-free gas can be discharged from the discharge port 13 remote from the inlet 9 of the housing chamber, and the dust is discharged from the discharge port 13 near the inlet 9 of the housing chamber, near the inlet 9 of the housing chamber.
  • the discharge port 13 is provided with a movable sealing and discharging device, and the dust can be discharged intermittently or at a fixed flow rate.
  • a filter When used as a vacuum cleaner, a filter can be installed outside the inlet 9 of the casing cavity to filter long fibers. The dust is cleaned easily, the noise is low, the dust suction effect is good, the cost is cheap, the energy is saved, there is no dust pollution, and it is more sanitary and environmentally friendly.
  • the separator When used as a range hood, the separator can be mounted upright, diagonally or transversely.
  • the flue gas can be sucked into the separator from the inlet 9 of the casing cavity, the soot can be separated, the flue gas discharge is completely environmentally friendly, and the treated smokeless gas is discharged from the discharge port 13 away from the inlet 9 of the casing cavity, and the waste oil is close to the shell.
  • the discharge port 13 of the body cavity inlet 9 is discharged.
  • the hood can be cleaned all year round. When the diameter of the vortex separating wheel 4 is small, a high speed motor can be used.
  • air When used as an oxygen generating apparatus, air can be supplied to the separator, and nitrogen gas or the like can be separated from the discharge port 13 remote from the inlet 9 of the casing chamber, and oxygen can be separated from the discharge port 13 near the inlet 9 of the casing chamber. It can separate oxygen from the air, and the cost of oxygen production is extremely low, which can achieve pure oxygen combustion in boilers, furnaces, engines, etc., which can reduce energy consumption, improve thermal efficiency, completely eliminate nitrogen oxide emissions, and reduce engine volume, weight and row. Quantity, increase torque. Exhaust gas recirculation can also be used for engines, heat engines, kilns, boilers, etc., which can reduce combustion temperatures and reduce equipment material requirements.
  • Clean air can be separated from the discharge port 13 remote from the inlet 9 of the casing chamber, and dust particles, sulfur dioxide, carbon dioxide, coal tar, and the like are separated from the discharge port 13 near the inlet 9 of the casing chamber.
  • the odor gas When used as an odor-eliminating device, the odor gas can be removed, the clean air can be separated from the discharge port 13 away from the inlet 9 of the casing chamber, and dust particles, odor components and the like can be separated from the discharge port 13 near the inlet 9 of the casing chamber.
  • a plurality of oil vapors can be recovered, and clean air can be separated from the discharge port 13 away from the inlet 9 of the casing chamber, and oil, gas and the like can be separated from the discharge port 13 near the inlet 9 of the casing cavity.
  • the separated oil and gas components can be recovered by spraying, flux absorption, etc., and the recovered residual gas can be re-introduced into the shell cavity inlet 9 to participate in the separation again, forming a closed cycle, and finally achieving complete recovery.
  • fresh water When used as a seawater desalination apparatus, fresh water can be separated from the discharge port 13 remote from the inlet 9 of the casing chamber, and the salt is separated from the discharge port 13 near the inlet 9 of the casing chamber.
  • One of the embodiments of the present invention is such that, on the basis of the main structure, the discharge port 13 is provided with a movable sealing and unloading device 14.
  • the movable sealing and unloading device 14 can be provided with a valve, a damper, a screw conveyor and the like.
  • the movable sealing and discharging device 14 can adjust the flow rate, can adjust the separation effect, and can make the separation object act under the pressure, gravity and centrifugal force in the casing according to the separation amount. Then, it is discharged from the casing, and the movable sealing and discharging device 14 can be intermittently opened to discharge the separated matter.
  • the movable seal discharge device 14 disposed near the discharge port 13 of the inlet end 9 of the casing chamber can be made into a gray box, a ash chamber or the like.
  • the separator of this embodiment can better improve the separation effect.
  • the structure of the second embodiment of the present invention is: on the basis of the above structure, the eddy current separation chamber inlet 6 is provided with a reinforcing card 15.
  • the reinforcing card 15 can thicken the edge of the vortex separation chamber inlet 6, which can improve the structural strength of the vortex separation chamber 5.
  • the reinforcing card 15 can be placed close to the inner wall of the housing cavity 3 to better prevent the separation from re-entering the vortex separation chamber 5 to cause repeated separation.
  • the reinforcing card 15 can be integrally formed with the vortex separating wheel 4, or can be provided with a component body structure, and can be assembled together during installation. Increasing the radial width of the reinforcing card 15 can better prevent the separation from re-entering the vortex separation chamber 5 causing repeated separation.
  • the separator of the embodiment can improve the structural strength, improve the separation effect, and reduce the energy consumption.
  • the structure of the third embodiment of the present invention is: based on the above structure, the supercharging device 11 is provided with at least one surrounding separation ring 15 corresponding to the shaft end outlet 7 of the vortex separation chamber, and the separator is disposed corresponding to the surrounding separation ring 15 in the supercharging device 11 16.
  • the corresponding partition 16 on the inner wall of the housing chamber 3 is disposed around the partition 12, and the housing chamber 3 is provided with a plurality of discharge ports 13.
  • One or more surrounding separation rings 15 may be disposed on the supercharging device 11 corresponding to the vortex separation chamber shaft end outlets 7, The edge of the surrounding separation ring 15 can be adjacent to the vortex separation chamber shaft end outlet 7, and the edge of the surrounding separation ring 15 can also be introduced into the vortex separation chamber shaft end outlet 7.
  • the other end of the surrounding separation ring 15 is connected to the supercharging device 11.
  • a separator 16 is disposed in the supercharging device 11 corresponding to the surrounding separation ring 15, and a partition 16 can be disposed in each of the surrounding separation rings 15 in the supercharging device 11, and the partition 16 can be formed as an axial partition plate.
  • the pressing device 11 is axially divided into a plurality of regions. It is also possible to increase the diameter of the supercharging device 11 near the side of the transmission device 2 or increase the number of pressurized blades, thereby increasing the peripheral pressure of the region, thereby better avoiding the secondary mixing of the separation material and improving the separation effect.
  • the corresponding partition 16 on the inner wall of the housing cavity 3 is disposed around the partition 12, and the surrounding separator 12 can be adjacent to the partition 16, so that the secondary mixing of the separator can be better avoided, and the separation effect can be improved.
  • the housing chamber 3 is provided with a plurality of discharge ports 13 respectively, and one or more discharge ports 13 may be provided for each of the partition bodies 16, so that different fluids separated by the separation separation ring 15 can be discharged through different discharge ports 13 respectively.
  • the surrounding separation ring 15 forms a plurality of annular flow passages at the shaft end outlet 7 of the vortex separation chamber, so that the fluid flowing out from the center of the shaft end outlet 7 of the vortex separation chamber and the periphery can enter different flow passages.
  • the separation moves to the periphery of the vortex separation chamber 5 under the action of the rotating centrifugal force, so that different separations move into different annular flow passages from different discharge ports 13 discharge.
  • the surrounding separation ring 15 having the smallest inner diameter separates the gas components.
  • the separator of this embodiment can be used as sewage treatment, seawater desalination, water purification equipment, and the like.
  • the sewage is treated, the water purification is purified or the seawater is desalinated, the standard purified water is discharged from the central discharge port 13, and the organic component and the gas component are discharged from the discharge port 13 corresponding to the separation ring 15, and the gas component is from the inlet farthest from the casing cavity.
  • the discharge port 13 is discharged, and heavy elements, metal elements, sand dust, salty heavy water or a salt water mixture are discharged from the discharge port 13 near the inlet 9 of the casing chamber.
  • the mother-child separator is arranged, and each of the salt-containing heavy water, the organic component, the gas component and the like are subjected to secondary treatment and multi-stage treatment by using the respective sub-separators to further separate a plurality of salt, organic components and gas components.
  • a flow regulating valve can be separately provided at each discharge port 13 to separate harmful elements such as heavy elements and chlorine gas, and the separator can be directly installed on the tap water pipe, and a water valve switch is provided, and the separator is provided. In operation, the water valve switch is opened, and after the water passes through the separator, the separated heavy elements are discharged from the discharge port 13 near the inlet 9 of the casing chamber.
  • the harmful gas components and organic components such as chlorine gas in the tap water are discharged from the discharge port 13 which is connected to the separation ring 15.
  • the treated tap water flows out from the middle discharge port 13.
  • the beneficial elements in tap water have a small specific gravity, and the set speed keeps the beneficial elements in the tap water in the water, making the tap water more in line with drinking standards.
  • the structure of the fourth embodiment of the present invention is: based on the above structure, the transmission is arranged in the stator stirring body 10 Device 2.
  • the transmission 2 can be disposed in the stator agitating body 10, which can reduce the volume of the device, reduce the noise of the device, and avoid fluid leakage.
  • the transmission 2 can also be provided with a cooling system, which can be a water or oil cooled system.
  • the separator of this embodiment can reduce the volume of the device and enable the device to be leak-free.
  • the structure of the fifth embodiment of the present invention is that, on the basis of the above structure, the liquid supply device 18 is disposed on the casing 1 corresponding to the casing cavity 3.
  • the liquid supply device 18 may be a device such as a pump, a pipe, a flow control valve, a nozzle, a spray head, a sedimentation tank or a water tank, and may be continuously flowed into the casing chamber 3 by a liquid supply device 18 by various means such as pipe inflow, injection or spraying. Intermittently deliver a certain amount of water, oil, alkaline water or ammonia water, and control the flow rate.
  • the liquid supply device 18 can be disposed in the direction of the inner wall of the housing chamber 3 or in the tangential direction of the cross section of the housing chamber 3, so that the liquid can flow into the housing chamber 3 against the inner wall of the housing chamber 3, forming a layer on the inner wall of the housing chamber 3.
  • the rotating liquid membrane causes the separation to enter the liquid and exit the separator along with the liquid.
  • the liquid supply device 18 can be provided with nozzles of various structures, and the existing K-series or P-series wide-angle or narrow-angle fan-shaped nozzles can be provided, which can simplify the installation structure and better make the liquid adhere to the housing cavity 3
  • the inner wall is sprayed into the housing cavity 3.
  • the nozzle can also be arranged as a flat mouth, so that the nozzle can be close to the inner wall of the housing cavity 3, or a plurality of flat nozzles can be arranged together, or can be arranged together as a flat nozzle by the plate.
  • the liquid can be recycled and can be circulated through the liquid supply unit 18 into the separator by a pump.
  • the separator can be adapted to higher working temperature conditions.
  • the liquid supply device 18 inputs alkaline liquid, ammonia water, etc. into the housing chamber 3, it can be used in the fields of flue gas desulfurization, denitration, etc., which can improve the operation efficiency of the equipment, reduce the cost and operation cost, and can simultaneously complete the dust removal and realize the dust removal of the flue gas.
  • the desulfurization and denitration are completed in one step, and the discharged liquid can be used to make acid or other compounds.
  • the separator of the present embodiment can smoothly discharge dust, viscous separation, etc. from the separator, and can more conveniently collect the separation of dust and the like, and the separator is better for dust removal.
  • the separator is used for chemical odor removal, which can better collect odor components, and can also react odor components with acid and alkali to better remove odor.
  • oil, solvent or water can be used as absorption. liquid.
  • the structure of the sixth embodiment of the present invention is: based on the above structure, the outer diameter of the supercharging device 11 is larger than the outer diameter of the vortex separating chamber 5.
  • the outer diameter of the supercharging device 11 is larger than the outer diameter of the vortex separating chamber 5 to further increase the fluid pressure around the supercharging device 11, and the secondary mixing of the separated fluid can be better avoided.
  • the disadvantage is to increase energy consumption.
  • the separator of this embodiment can increase the fluid pressure around the supercharging device 11, and can better avoid secondary mixing of the separated fluid.
  • the structure of the seventh embodiment of the present invention is: based on the above structure, the stator choke body 10 is provided with a flow guiding channel 19, the diversion flow channel outlet 20 is connected to the vortex separating chamber inlet 6, and the vortex separating chamber 5 is close to the transmission device.
  • the vortex separation chamber inlet 6 is provided at the 2nd end.
  • a stator flow path 19 is provided in the stator agitating body 10, and the stator agitating body 10 can be made into a pipe structure, and a flow guiding channel 19 is formed inside the pipe.
  • the flow guiding channel outlet 20 is connected to the vortex separating chamber inlet 6.
  • the guiding flow channel 19 is inserted into one end of the vortex separating chamber to provide a guiding flow channel outlet 20, and the guiding flow channel outlet 20 communicates with the vortex separating chamber inlet 6 to make the fluid Through the flow guiding channel 19, it enters the vortex separation chamber 5 through the flow guiding channel outlet 20.
  • the vortex separation chamber 5 is provided with a vortex separation chamber inlet 6 near the end of the transmission 2, so that the fluid can move from the end close to the transmission 2 to the end away from the transmission 2.
  • the pressurizing device 11 can be close to the inner wall of the shaft end of the housing chamber 3, which can better prevent the re-entry of the separator into the pressurizing device 11 to cause repeated pressurization.
  • the use of the open impeller of the supercharging device 11 can better prevent the fluid from repeatedly entering the supercharging device 11 to increase energy consumption.
  • the separator of the present embodiment allows the fluid to enter the vortex separation chamber through the flow guiding passage and moves away from the transmission 2 end, thereby realizing special functional requirements.
  • the structure of the eighth embodiment of the present invention is: on the basis of the above structure, at least one surrounding partitioning plate 21 is disposed in the supercharging device 11, and the inner wall of the casing cavity 3 is disposed around the partitioning plate 21 to surround the partitioning body 12, and the casing cavity 3 is disposed.
  • a plurality of discharge ports 13 are provided.
  • One or more surrounding separators 21 may be disposed in the pressurizing device 11, and the surrounding separators 21 may be formed as an axial dividing plate to axially divide the pressurizing device 11 into a plurality of regions, or may be away from the vortex separating chamber.
  • the pressure-increasing device 11 on the 5 side has an increased diameter and an increased number of blades, which can increase the peripheral pressure of the region, and can better avoid secondary mixing of the separated materials, thereby improving the separation effect.
  • the supercharging device 11 near the side of the vortex separating chamber 5 can be disposed at the periphery of the shaft end outlet 7 of the vortex separating chamber, so that the eddy current in the vortex separating chamber 5 near the shaft end outlet 7 of the vortex separating chamber can be kept stable and stable.
  • the separation of the lighter weight is prevented from entering the periphery of the shaft end outlet 7 of the vortex separation chamber, so that the secondary mixing of the separation material can be better avoided, and the separation effect can be improved.
  • the inner wall of the housing cavity 3 is provided with a surrounding partition 12 corresponding to the surrounding partitioning plate 10, and the surrounding partitioning body 12 may also be adjacent to the surrounding partitioning plate 21, or the surrounding partitioning body 12 may be provided. It is arranged on the periphery of the surrounding separator 21 to better avoid secondary mixing of the separator, and the separation effect can be improved.
  • the housing chamber 3 is provided with a plurality of discharge ports 13 respectively, and one or more discharge ports 13 are provided corresponding to each of the surrounding separation plates 21, so that different fluids separated by the separation cards 21 can pass through different discharge ports 13 respectively. discharge.
  • a plurality of flow passages are formed in the axial direction of the supercharging device 11 around the partitioning plate 21, and the separation weights are different in specific gravity, particle size, etc., and the moving speed of the separating objects to the periphery of the vortex separating chamber 5 is different under the action of the rotating centrifugal force, so that the difference is different.
  • the separators move into different flow channels and are discharged from different discharge ports 13.
  • the surrounding separator 21 closest to the inlet 9 of the casing chamber separates the gas.
  • the surrounding separator 21 closest to the housing cavity inlet 9 separates the lightest gas components.
  • the separator of this embodiment can be used as sewage treatment, seawater desalination, water purification equipment, and the like.
  • the sewage is treated, the water purification is purified or the seawater is desalinated, the standard purified water is discharged from the central discharge port 13, and the organic component and the gas component are discharged from the discharge port 13 corresponding to the partition card 21 closest to the inlet of the casing cavity, and the heavy element Metal elements, sand dust, salty heavy water or brine mixture are discharged from the discharge port 13 away from the inlet 9 of the casing chamber.
  • the mother-child separator is arranged, and each of the salt-containing heavy water, the organic component, the gas component and the like are subjected to secondary treatment and multi-stage treatment by using the respective sub-separators to further separate a plurality of salt, organic components and gas components.
  • a plurality of surrounding partitions 12 are disposed on the inner wall of the casing chamber 3 around the periphery of the vortex separating chamber 5, and the casing chamber 3 is provided with a plurality of discharging ports 13.
  • a plurality of surrounding partitions 12 may be axially disposed around the inner wall of the housing chamber 3 so as to surround the periphery of the vortex separating chamber 5, and the housing chamber 3 surrounding the periphery of the vortex separating chamber 5 is axially isolated into a plurality of regions, one or more corresponding to each region.
  • One discharge port 13 is provided on the inner wall of the casing chamber 3 around the periphery of the vortex separating chamber 5, and the casing chamber 3 is provided with a plurality of discharging ports 13.
  • the separation speed of the separation object to the periphery of the vortex separation chamber 5 is different, so that different separation bodies are respectively moved to the axially different housing chamber 3 regions, so that a plurality of separations can be better separated. Things. Increasing the axial length of the vortex separation chamber 5 can better separate a plurality of separators.
  • the separator of this embodiment can further sort the isolate. It can be used as a classifier, air separation, sewage treatment, seawater desalination, marine chemical, oil refining equipment, etc., and the axial length of the vortex separation chamber 5 can be appropriately lengthened during use.
  • the crude oil When used as an oil refining equipment, the crude oil can be directly sucked into the separator, and the crude oil is affected by the vortex fluid movement, the centrifugal force generated by the vortex, and the gravity, thereby achieving low temperature cracking and realizing separation of various components.
  • Heavy elements, metals, sulfur, asphalt, paraffin, heavy oil, lubricating oil, diesel oil, kerosene, gasoline, and the like may be sequentially discharged from the respective discharge ports 13 near the inlet 9 of the casing chamber. Set the mother and child separators, and use the various sub-separators to discharge the various components.
  • the second separation and multi-stage separation can achieve ultra-high purity of various components, and can extract high-purity gasoline, diesel oil, lubricating oil, wax, various petroleum products, sulfur, heavy metals, metals, lead, and radioactivity. Elements, etc., can make the oil completely lead-free and free of radioactive elements.
  • the whole production process is non-polluting, there is no waste water and exhaust gas emission, and the refining process can be completely environmentally friendly, and the resources can be completely utilized, which can greatly reduce the refining cost.
  • Low-temperature cracking of petroleum greatly reduces the damage of macromolecular structure in crude oil by high temperature, reduces the production of LPG, and reduces the production of asphalt and wax, which can greatly improve the oil yield and greatly improve the output of high-quality gasoline. Oil rate.
  • the separation speeds of the separators with different specific gravity to the periphery of the vortex are different.
  • the separators with different specific gravity enter the different discharge ports 13 in the axial direction respectively, so that different separations can be sorted.
  • it can extract and sort various useful components from sewage and waste gas. It can also extract acid from sulfur dioxide, nitrogen oxides, etc. by using kiln exhaust gas to extract carbon dioxide and coal tar to realize resource utilization. Dust removal, desulfurization and denitrification can be completed simultaneously; when the exhaust gas is dusted, a variety of useful components can be selected from the dust.
  • various components of dust particles and various components can be separated from each discharge port 13.
  • the gas, dust removal and gas separation can also be completed simultaneously, and a mother-child separator can be arranged to further separate the various gases to obtain a high-purity gas, and the harmful gas can be subjected to secondary treatment, for example, carbon can be used.
  • the hydrogen compound is re-introduced into the kiln for secondary combustion, and the sulfur dioxide can be further treated twice.
  • an oxygen generator When used as an air separation device, an oxygen generator, a nitrogen generator, or a rare gas preparation device, air can be input to the separator, and various gases such as oxygen, nitrogen, and inert gas can be separated from each discharge port 13 directly. Collect and use various gases. When special needs are required, the various gases are secondarily sorted to obtain a high purity gas.
  • the separator of the embodiment When the separator of the embodiment is used as a beneficiation equipment or a garbage disposal equipment, the mineral or garbage can be pulverized into granules, and the granules are sent to the separator by water or gas for wet selection or dry selection: the water can be recycled, and the useful ingredients can be used. A variety of minerals and useless components are separated from the respective discharge ports 13. When the garbage is disposed, the useless components can be landfilled, and the organic components are fermented and pressed into granular organic fertilizers, which can completely eliminate environmental pollution and realize resource recycling. When coal is selected, a variety of minerals and sulfides in the raw coal can be selected to realize resource utilization, and high-purity coal water slurry can be produced.
  • the coal water slurry can achieve thorough clean combustion, and the combustion purity can be comparable to that of natural gas.
  • Exhaust gas can be used without desulfurization and dedusting; low-temperature combustion can be achieved, nitrogen oxides can be produced, and denitrification can be eliminated.
  • the standard water, organic components, gas components, heavy elements, metal elements, sand dust, salt heavy water or brine mixture can be discharged from the different discharge ports 13.
  • Set mother The sub-separator performs secondary treatment and multi-stage treatment on the discharged salt-containing heavy water, organic components, gas components and the like by using each sub-separator to further separate a plurality of salt, organic components and gas components.
  • the separator drive shaft can be installed horizontally or vertically.
  • the separator can simultaneously deliver the fluid, and the separator can automatically draw the fluid to be separated into the inlet of the casing chamber 9, or can send the fluid into the separator through other devices, and the fluid is separated in the separator.
  • the inner wall of the vortex separating chamber 5 drives the fluid to rotate, and the outer wall of the stator stirring body 10 is stationary, so that the fluid can be formed into a vortex.
  • the eddy current advances spirally along the axial direction, and the eddy current causes the movement speed of each particle in the fluid to be different, so that each particle in the fluid forms an individual moving individual.

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Abstract

L'invention concerne un séparateur qui comprend un boîtier et un appareil de transmission. L'appareil de transmission est prévu sur le boîtier. Une cavité de boîtier est prévue dans le boîtier. Une roue de séparation de tourbillon est prévue dans la cavité de boîtier. L'appareil de transmission est raccordé à la roue de séparation de tourbillon. Une chambre de séparation de tourbillon est prévue dans la roue de séparation de tourbillon. Une entrée de la chambre de séparation de tourbillon est prévue au niveau d'une extrémité de la chambre de séparation de tourbillon. Une sortie d'extrémité axiale de la chambre de séparation de tourbillon est prévue au niveau de l'autre extrémité de la chambre de séparation de tourbillon. De multiples sorties circonférentielles de la chambre de séparation de tourbillon sont prévues au niveau d'une circonférence de la chambre de séparation de tourbillon. Une entrée de la cavité de boîtier est prévue sur le boîtier, correspondant à l'entrée de la chambre de séparation de tourbillon. Un corps d'agitation à stator est prévu sur le boîtier, correspondant à la chambre de séparation de tourbillon. Le corps d'agitation à stator passe dans la chambre de séparation de tourbillon. Un appareil chargeur est prévu à l'extérieur de la sortie d'extrémité axiale de la chambre de séparation de tourbillon. Au moins un corps de séparation d'encerclement est prévu sur une paroi interne de la cavité de boîtier. Au moins deux orifices de décharge sont prévus sur la cavité de boîtier. Le séparateur peut être utilisé dans des domaines tels que le traitement des eaux résiduaires, la purification de l'eau, l'épuration de l'air, le traitement des odeurs, la récupération de vapeur d'huile, le dépoussiérage, l'élimination des déchets, la classification des poudres, le traitement des minerais, le dessalement d'eau de mer, le génie chimique en mer, le raffinage des huiles, la préparation de l'oxygène et il peut réduire la pollution environnementale.
PCT/CN2014/088195 2013-10-11 2014-10-09 Séparateur WO2015051745A1 (fr)

Applications Claiming Priority (12)

Application Number Priority Date Filing Date Title
CN201310474090.3 2013-10-11
CN201310474090 2013-10-11
CN201310647436.5 2013-12-04
CN201310647436 2013-12-04
CN201310690302 2013-12-16
CN201310690302.1 2013-12-16
CN201410481574 2014-09-21
CN201410481574.5 2014-09-21
CN201410518227.5 2014-10-01
CN201410518227 2014-10-01
CN201410519211.6A CN104841574A (zh) 2013-10-11 2014-10-07 分离器
CN201410519211.6 2014-10-07

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CN107638963A (zh) * 2016-11-04 2018-01-30 陈久斌 分离反应粉磨机
CN106801966A (zh) * 2017-02-27 2017-06-06 深圳沃海森科技有限公司 Pm2.5分解过滤回收式新风机
CN109569902A (zh) * 2017-07-15 2019-04-05 陈久斌 涡机
CN108837647B (zh) * 2018-05-31 2023-06-20 江苏润宇环境工程有限公司 一种油气回收除尘装置
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