WO2022007740A1 - 旋流机 - Google Patents

旋流机 Download PDF

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Publication number
WO2022007740A1
WO2022007740A1 PCT/CN2021/104468 CN2021104468W WO2022007740A1 WO 2022007740 A1 WO2022007740 A1 WO 2022007740A1 CN 2021104468 W CN2021104468 W CN 2021104468W WO 2022007740 A1 WO2022007740 A1 WO 2022007740A1
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Prior art keywords
swirl
chamber
cyclone
wheel
swirl chamber
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PCT/CN2021/104468
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English (en)
French (fr)
Inventor
陈久斌
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陈久斌
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Publication of WO2022007740A1 publication Critical patent/WO2022007740A1/zh

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C11/00Accessories, e.g. safety or control devices, not otherwise provided for, e.g. regulators, valves in inlet or overflow ducting
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/081Shapes or dimensions

Definitions

  • the invention relates to sewage treatment, water purification, seawater desalination, marine chemical industry, mineral processing, coal preparation, nuclear waste treatment, oil refining, oil and gas recovery, garbage treatment, air purification, dust removal, desulfurization, denitration, oil fume purification, tail gas treatment, and black removal.
  • the existing sewage treatment equipment is complicated, the cost is too high, the cost of sewage treatment is too high, and the treatment effect is mediocre.
  • the existing seawater desalination equipment is complex, the cost is too high, the cost of seawater desalination is too high, and the energy consumption is too high.
  • the existing marine chemical equipment is complex, the cost is too high, and the effect on the utilization of marine resources is not ideal.
  • the existing separation equipment mainly includes centrifuges, etc., which generally have defects such as general separation effect and high energy consumption.
  • the existing beneficiation equipment has a general beneficiation effect and cannot achieve finer separation, resulting in waste of resources and environmental pollution.
  • the current nuclear fuel is mainly selected by centrifuges, and the cost is too high and the selection is not clean, resulting in environmental pollution and waste of resources.
  • Nuclear waste and nuclear sewage are basically impossible to handle, posing a serious environmental threat.
  • Existing kilns include shaft kilns, rotary kilns, incinerators, reaction furnaces, etc., which generally have defects such as insufficient combustion, high energy consumption, low efficiency, and large volume.
  • Existing grinding equipment includes pulverizers, Raymond mills, air-swept mills, etc., which generally have high energy consumption, low powder grinding efficiency, and difficulty in preparing ultra-fine powder and nano-powder.
  • the glued and dissolved molecules can be separated, so that each molecule, atom and other particles in the swirl flow can form different moving speeds.
  • It uses swirl motion, centrifugal force and gravity to make substances with different particle sizes and different specific gravity enter different areas and finally achieve separation.
  • the solutes in the solution can be separated from the solvent, and the different solutes can be separated.
  • the particulate matter in the flue gas can enter the water to realize flue gas purification. and other fields.
  • the use of swirl to make molecules collide and rub against each other can greatly promote chemical reactions, and can be used as denitration equipment, chemical reactors, etc.
  • the swirl flow is used to make the materials collide and rub against each other in the swirl flow and are continuously dissociated, and the swirl flow is used to open the particle agglomeration, so that the materials are continuously ground into fine powder, ultrafine powder or nano powder.
  • the use of swirl combustion and swirl grinding can make the fuel fully burn, especially when burning coal, the coal can be continuously peeled and ground to be fully burned, and the temperature of the combustion zone can be kept stable and uniform, which can be more accurate.
  • the controlled furnace temperature can realize low-temperature combustion and greatly reduce the production of nitrogen oxides.
  • the high-speed swirl is used to decompose the molecules by continuous friction and collision in the swirl, and the molecular chain is opened by the high-speed swirl to achieve molecular decomposition. Solve energy, CO2 decomposition to solve greenhouse gas emissions, organic molecule decomposition to solve air pollution, metal oxide molecular decomposition metallurgy, etc.
  • This cyclone can achieve cleaner dust removal, air purification, oil fume purification, sewage treatment, cheaper seawater desalination, more adequate use of water resources, extraction of marine resources, higher efficiency of mineral processing, waste treatment, oil refining, etc.
  • the cyclone can be widely used in various separation fields, and can realize the separation, sorting, extraction and purification of various material components.
  • the cyclone can be used as a dust collector. It can use dry dust removal or wet dust removal to achieve dust-free discharge. It can achieve the same dust content as the excellent atmospheric environment, and does not contain harmful substances such as heavy elements. Be completely dust-free. It can remove black smoke, effectively remove odor components in flue gas, and remove dioxins and heavy element particles in flue gas. It can be used in flue gas desulfurization, denitration and other fields to realize wet dust removal and wet desulfurization. Completed in one step, the operation efficiency of the equipment can be greatly improved.
  • It can be used as sewage treatment equipment, and can extract various useful components from sewage to realize the recycling of water resources. It can directly provide pure water, can reach the drinking water standard, can completely solve the water pollution and solve the problem of water shortage.
  • It can be used as water purification equipment, can completely separate the harmful elements in tap water, can separate heavy water (deuterium water, heavy oxygen water), can reach higher drinking water standards, can extract heavy water from water for industrial use .
  • It can be used as a waste treatment equipment, dry or wet, to separate and sort the useful components, press the organic components into granular organic fertilizers, and landfill the useless components, which can completely eliminate environmental pollution and realize resource recycling. It can also be used for flue gas treatment after waste incineration, and the flue gas can be thoroughly cleaned.
  • Oxygen can be separated from the air, and various gases in the air can also be separated, and a variety of rare gases can be extracted.
  • the cost of oxygen production is extremely low, which enables boilers, kilns, engines, heat engines, etc. to achieve cheap and economical pure oxygen combustion, which can reduce energy consumption, improve thermal power efficiency, and completely eliminate nitrogen oxide emissions.
  • Engines, heat engines, kilns, boilers, etc. can also use exhaust gas recirculation, which can reduce the combustion temperature and reduce equipment material requirements.
  • the carbon dioxide produced after the combustion of pure oxygen can also be collected centrally.
  • It can be used as beneficiation equipment, which can realize the separation, extraction and purification of various minerals and raw materials, and can screen out a variety of useful minerals from poor ores. It can be used for all mineral sorting, and can be selected while grinding, and all kinds of useful components in minerals can be selected, which can greatly improve the economic benefits of mineral processing. When used in rare earth industry, various elements can be selected; when used in precious metal beneficiation, precious elements can be fully extracted.
  • seawater desalination equipment can be used as seawater desalination equipment and marine chemical equipment, which can greatly reduce equipment cost, greatly reduce energy consumption and improve seawater desalination efficiency.
  • Various useful components can be simultaneously extracted from seawater, and at the same time, the separation, extraction, sorting and purification of various useful components can be realized. It can be used as a marine chemical equipment, and seawater desalination can be realized without cost.
  • coal preparation equipment can be used as coal preparation equipment, and can be dry or wet. It can separate the sulfides, metal elements, precious elements, radioactive elements, common minerals, etc. in the coal for resource utilization. High-purity coal-water slurry can achieve clean combustion of coal.
  • the high radioactive elements in the nuclear waste can be extracted, and after reaching a certain concentration, they can be put back into the nuclear reactor to undergo nuclear transmutation and become low-level substances, which can make the tailings into low-level radioactive substances. , that is, vitrified landfill, so that nuclear waste has no safety hazard.
  • swirl flow can be used to make molecules collide and rub against each other, which can greatly promote chemical reactions and achieve catalytic reaction effects. It can be used in various chemical reactors, and can also be used as catalytic reaction equipment for denitration equipment.
  • any fuel can be used, the temperature of the combustion zone can be kept stable and uniform, the furnace temperature can be accurately controlled, low-temperature combustion can be achieved, and the temperature can be greatly reduced. Nitrogen oxides are produced.
  • the coal When burning coal, the coal can be continuously peeled and broken while burning continuously.
  • Simultaneous addition of calcium carbonate stone chips can realize dry desulfurization in the furnace, and can realize the integration of dust removal, desulfurization and denitrification of burners and boilers.
  • It can be used as a kiln, etc., and can replace the shaft kiln, rotary kiln, incinerator, reaction furnace, blast furnace, horseshoe furnace, etc., which can make full combustion, can quickly burn materials, can save energy, high output, and improve production efficiency. It can burn cement, lime, magnesium oxide, mineral powder, garbage, etc., and can burn high-activity lime ultrafine powder. It can be used for iron smelting, copper smelting, production of glass, frit, caustic soda, etc.
  • the grinding powder can be dry or wet. Dry grinding can be achieved by using air as the working medium, and wet grinding can be achieved by using water as the working medium. Ultrafine powder, nano-powder, monoatomic particles, etc. Solve the raw material of nanomaterials, can grind carbonene, can solve the raw material of graphene. It can also be used as a coal grinding pulverizer, which can dry-grind raw coal and spray pulverized coal into kilns for combustion.
  • It can be used as a molecular decomposition device, which can decompose molecules, and can break molecular chains such as H2O, SO2, CO2, NO, HS, and hydrocarbons to achieve molecular decomposition. It can decompose water molecules, and can use water or steam to produce hydrogen ions, which can solve energy; can process SO2, CO2, NO, HS, etc., can decompose SO2 to produce sulfur ions, can decompose CO2 to solve carbon emissions, and can use waste gas to produce S, C, etc.; can treat organic waste gas, decompose organic molecules, and treat organic waste gas odor, etc.
  • molecular decomposition device which can decompose molecules, and can break molecular chains such as H2O, SO2, CO2, NO, HS, and hydrocarbons to achieve molecular decomposition. It can decompose water molecules, and can use water or steam to produce hydrogen ions, which can solve energy; can process SO2, CO2, NO, HS, etc., can de
  • the swirl machine includes a casing and a transmission device, a transmission device is arranged on the casing, a swirl cavity is arranged in the casing, the cross section of the swirl cavity is circular, and a swirl wheel is arranged in the axial center area of one end of the swirl cavity.
  • the transmission device is connected with the swirl wheel.
  • the swirl chamber is provided with at least one swirl cavity inlet corresponding to the swirl wheel, and the other end of the swirl cavity is provided with a swirl cavity outlet.
  • the swirl flow between the flow wheel and the outlet of the swirl chamber is provided with a stator vortex rectifier with a circular cross section, at least one retaining ring is arranged around the outer wall of the stator vortex rectifier, and at least one discharge port is arranged on the periphery of the swirl chamber.
  • the cyclone wheel is provided with a cyclone separation chamber, one end of the cyclone separation chamber is provided with an outlet of the cyclone separation chamber, and the other end of the cyclone separation chamber is provided with an inlet of the cyclone separation chamber, and at least one cyclone chamber is set corresponding to the inlet of the cyclone separation chamber.
  • a section of the stator vortex rectifier penetrates the outlet of the cyclone separation chamber and probes into the cyclone separation chamber.
  • At least one surrounding partition is arranged on the inner wall of the swirl chamber, and at least one discharge port is arranged on the periphery of the swirl chamber corresponding to the surrounding partition.
  • the inner wall of the swirl chamber around the swirl wheel is close to the outer edge of the swirl wheel.
  • the axis of the swirl chamber is vertical, and the lower part of the swirl chamber is provided with surrounding water.
  • the swirl chamber is provided with a spray device corresponding to the swirl wheel.
  • a feeding device is provided in the swirl chamber near the inlet end of the swirl chamber.
  • the swirl chamber near the inlet end of the swirl chamber is provided with a feeding device and a combustion supply device.
  • the swirl chamber near the inlet end of the swirl chamber is provided with a combustion supply device, the swirl chamber is provided with a feeding device, the lower part of the swirl chamber is provided with a molten pool, and the molten pool is provided with at least one discharge port.
  • a combustion supply device is arranged in the swirl chamber close to the inlet end of the swirl chamber, and a heat recovery device is arranged on the inner wall of the swirl chamber.
  • the advantages of the swirl machine are that the circular motion and fluid motion are fully utilized, and the swirl flow is fully utilized, so that the fluid is gradually separated, and the effect increases synchronously with the increase of the linear speed, and the fluid moves spirally along the axial direction. Gradually separated, a variety of substances can be separated from the working medium.
  • the use of swirl to make molecules collide and rub against each other can generate a large number of free radicals, which can greatly promote chemical reactions, achieve catalytic effects, and can be used as catalytic reaction equipment.
  • the particles are gradually ground by cyclone grinding.
  • swirl combustion and swirl grinding can fully burn the fuel, and at the same time keep the temperature of the combustion zone stable and uniform, which can control the furnace temperature more accurately, realize low-temperature combustion, and greatly reduce the production of nitrogen oxides.
  • Using swirl combustion and swirl grinding a variety of materials can be fired, and the materials can be simultaneously ground into fine powder or ultra-fine powder.
  • the high-speed swirl is used to decompose the molecules by continuous friction and collision in the swirl, and the molecular chain is opened by the high-speed swirl to achieve molecular decomposition.
  • Solve energy solve greenhouse gas emissions, metal oxide molecular decomposition metallurgy, organic molecular decomposition to solve air pollution, etc.
  • the cyclone has the advantages of simple manufacture, large or small equipment, wide application fields, low manufacturing cost, low use cost, long service life and the like.
  • Fig. 8 is the front view structure schematic diagram of the seventh embodiment of the cyclone
  • Figure 10 is a schematic front view of the structure of the ninth embodiment of the cyclone.
  • the main structure of the swirl machine includes a swirl machine, including a casing 1 and a transmission device 2, a transmission device 2 is arranged on the casing, a swirl flow 3 is arranged in the casing 1, the cross-section of the swirl flow 3 is circular, and the swirl cavity 3 A swirl wheel 4 is arranged in the axial area of the inner end.
  • the swirl wheel 4 and the swirl chamber 3 are on the same axis.
  • the transmission device 2 is connected with the swirl wheel 4.
  • the swirl cavity corresponds to the swirl wheel 4.
  • At least one swirl cavity is set
  • the inlet 5, the other end of the swirl chamber 3 is provided with the swirl chamber outlet 6, and the swirl chamber 3 between the swirl wheel 4 and the swirl chamber outlet 6 is provided on the casing 1 with a circular stator scroll with a circular cross section.
  • at least one retaining ring 9 is arranged around the outer circumference of the stator scroll rectifier 7, and at least one discharge port 8 is arranged at the outer circumference of the swirl chamber 3.
  • the scope of the casing 1 includes the machine base, the bracket, the pipeline, the casing and the power unit, etc., and each part can be collectively referred to as the casing.
  • the casing 1 can also be integrated with the power unit to form an integral casing.
  • the cyclone can be made of different materials according to the needs, and can be made of metals, alloys, ceramics, glass, plastics, nylon, foam materials and other materials.
  • the transmission device 2 includes a transmission shaft, a transmission shaft sealing device, a bearing or a bearing bush, a shaft seat, etc.
  • the transmission device 2 is provided with a transmission shaft, and the transmission shaft is used to realize power input and drive the cyclone to work.
  • the transmission device 2 is connected with the power device to realize power input, and drives the cyclone to work.
  • the power device can use a motor or an engine, etc.
  • the power device can be directly connected to the transmission device 2, or it can realize power input through coupling drive, belt drive, chain drive, gear drive, etc., or through pulleys, reducers, etc. Change the axial direction of the drive shaft, and the large vertical mill can use the reducer as the transmission device.
  • the power device and the housing 1 can also be directly made into one body, or the power device can be directly used as the transmission device 2 .
  • the transmission device 2 can be arranged at one end to form a cantilever structure, or the other end of the rotating shaft of the transmission device 2 can be connected to a rotation stabilization device, and the rotation stabilization device can be provided with a bracket, a shaft seat, a bearing, a bearing bush or a sealing device.
  • the drive shaft sealing device can adopt various structures such as packing seal, oil cylinder seal and labyrinth seal according to specific working conditions.
  • a transmission device 2 is arranged on the casing 1 .
  • the transmission device 2 can adopt the setting scheme of a fan or a water pump transmission device.
  • a swirl chamber 3 is arranged in the casing 1 .
  • the swirl chamber 3 can be made into an integrated or open body structure, and can be assembled together during installation.
  • the swirl chamber 3 can also be opened arbitrarily according to needs, which can be easily assembled.
  • the inner wall of the swirl chamber 3 can also be provided with a wear-resistant material layer, a corrosion-resistant layer or a catalyst material layer, etc. as required, and wear-resistant sheets or wear-resistant bricks can also be attached to the surface in the areas prone to wear.
  • anti-corrosion or anti-corrosion wear-resistant layers, catalyst layers, etc. can be provided on the inner wall of the swirl chamber 3 according to specific working conditions.
  • a refractory thermal insulation layer can be provided on the inner wall of the swirl chamber 3 .
  • An electric heating device can also be arranged on the inner wall of the swirl chamber 3, so that the swirl machine can be turned into an electric heating furnace, which can burn various materials.
  • the cross section of the swirl chamber 3 is circular.
  • the cross section of the inner cavity of the swirl chamber 3 is set to be circular, which can better form a swirl flow in the swirl chamber 3.
  • the swirl chamber 3 can usually be set to a cylindrical structure, which can simplify the structure.
  • the swirl chamber 3 can also be set into a multi-section cylindrical structure with unequal inner diameters.
  • the swirl chamber 3 can also be set in a truncated cone-shaped structure or a multi-section truncated cone-shaped structure, which can be specifically set according to different needs.
  • the outlet end of the radial swirl cavity in the swirl chamber 3 is gradually expanded, which can make the fluid move smoothly in the axial direction.
  • the radial outlet end of the swirl chamber in the swirl chamber 3 is gradually reduced, so that the substances with heavier specific gravity can move to the inlet 5 of the swirl chamber, which can improve the separation effect.
  • a swirl wheel 4 is arranged in the axial center region of one end of the swirl chamber 3 , and the swirl wheel 4 and the swirl chamber 3 are on the same axis.
  • the swirl wheel 4 can adopt centrifugal impellers, axial flow impellers, mixed flow impellers or axial flow centrifugal combined impellers, rotating rollers, etc. of any structure according to specific working conditions, and all impellers of various structures can be used.
  • Arbitrary auxiliary devices can also be set on the swirl wheel 4, such as grinding hammers, round rollers, blades, etc.
  • a round roll device with the same diameter as the swirl wheel 4 can be set on the side of the swirl wheel 4, and the round roll device can be used.
  • the round roller device Adopting a cylindrical structure, the round roller device can better drive the fluid to rotate, which can improve the effects of grinding, reaction and mixing. Blades or hammers can also be set on the periphery of the round roller device, which can improve the effect of grinding or atomization.
  • the surface of the swirl wheel 4 can also be provided with a wear-resistant layer, a rubber lining or an anti-corrosion layer as required.
  • the swirl wheel 4 may be arranged on the central axis of one end area in the swirl chamber 3 .
  • the swirl wheel 4 transports fluid and drives the fluid to rotate and flow in the swirl chamber 3 to form a swirl flow.
  • the distance between the outer edge of the swirl wheel 4 and the inner wall of the swirl chamber 3 can be arbitrarily set according to the needs. , which can make the swirl friction more intense. When used as a reactor, it can improve the reaction effect. When used as a grinding equipment, it can improve the grinding strength and produce finer powders.
  • the transmission device 2 is connected with the swirl wheel 4 .
  • the transmission shaft of the transmission device 2 should be connected and fixed in the axial center area of the swirl wheel 4 to ensure that the swirl wheel 4 rotates smoothly.
  • the motor of the transmission device 2 and the swirl wheel 4 can also be made into one body, which can save space and reduce the cost.
  • the transmission shaft of the transmission device 2 can be passed through the swirl wheel 4, and both ends of the transmission shaft are provided with rotational stabilization devices.
  • the transmission shaft can also be a hollow shaft, and can also be welded with the swirl wheel 4 as a whole.
  • the swirl chamber 3 is provided with at least one swirl chamber inlet 5 corresponding to the swirl wheel 4 .
  • One or more swirl chamber inlets 5 can be arranged at one end or side wall of the swirl chamber 3 corresponding to the swirl wheel 4. Refer to the setting scheme of the inlet of the fan or the water pump shell.
  • the swirl chamber inlet 5 can be arranged in the swirl chamber 3. Axial area, which can realize the axial input of fluid.
  • a diversion cavity can also be provided on the inlet 5 of the swirl cavity, and opening an inlet on the side wall of the diversion cavity can change the fluid to radial input. It is also possible to set the swirl cavity inlet 5 on the side wall of the swirl cavity 3 and use the feeding device to feed the material into the swirl cavity 3.
  • the swirl cavity inlet 5 can be used to feed the swirl cavity 3 to feed different materials.
  • a flow regulating device such as a damper or a valve can also be set at the inlet 5 of the swirl chamber, which can adjust the flow and the separation reaction effect.
  • the other end of the swirl chamber 3 is provided with an outlet 6 of the swirl chamber.
  • One or more swirl chamber outlets 6 can be arbitrarily arranged at the other end of the swirl chamber 3, and the swirl chamber outlet 6 can be arranged at the other end of the swirl chamber 3 in the axial center area or on the side wall, so that the fluid can be output axially or radially. output.
  • the outlet 6 of the swirl chamber is arranged in the axial center area of the swirl chamber 3 to be circular, which can improve the separation effect. It is also possible to set a diversion cavity outside the outlet 6 of the swirl cavity, and an outlet on the side wall of the diversion cavity can change the fluid into Tangential or radial output, the guide cavity can also be made into a volute type, which can make the material discharge more smoothly.
  • the substances with larger specific gravity separated by the swirl formed in the swirl chamber 3 can be left in the swirl chamber 3 .
  • the inner diameter of the swirl chamber outlet 6 is larger than the maximum diameter of the swirl wheel 4, the fluid resistance can be reduced, and when the inner diameter of the swirl chamber outlet 6 is smaller than the maximum diameter of the swirl wheel 4, the fluid resistance can be increased, and the separation effect can be improved.
  • the inner diameter of the outlet 6 of the swirl chamber is equal to or greater than the maximum inner diameter of the swirl chamber 3, the fluid can flow out from the outlet 6 of the swirl chamber more smoothly.
  • the ratio of the outlet 6 of the swirl chamber to the maximum inner diameter of the swirl chamber 3 can be specifically set as required.
  • a circle of cylindrical baffles or pulling cylinders are arranged in the swirl chamber 3 at the outlet 6 of the swirl chamber to improve the separation effect.
  • the barrel can further improve the separation effect.
  • the rotation of the swirl wheel 4 drives the working medium to rotate to form a swirl flow, and the centrifugal force generated by the rotation makes many particles in the swirl flow move to the periphery of the swirl flow, and finally touch the inner wall of the swirl cavity 3, and the swirl cavity 3 is made into an inner radial swirl cavity.
  • the structure of the gradually narrowing end of the outlet 6 can make the inner wall of the swirl chamber 3 form an inclination angle with the axis, so that the particles touching the inner wall of the swirl chamber 3 can rebound to the side of the inlet 5 of the swirl chamber, so that the separated material with a large specific gravity can flow to the swirl chamber.
  • the movement of the 5 ends of the cavity inlet can improve the separation effect.
  • a flow regulating device can also be provided on the outlet 6 of the swirl chamber, and various valves, dampers, etc. can be used to adjust the fluid flow, adjust the pressure in the swirl chamber 3, and adjust the functional effect.
  • a stator scroll rectifier 7 with a circular cross-section is disposed on the casing 1 through the swirl chamber 3 from the swirl wheel 4 to the swirl chamber outlet 6 .
  • a circular stator scroll rectifier 7 is arranged on the casing 1 , which runs through the swirl chamber 3 from the swirl wheel 4 to the swirl chamber outlet 6 , and the stator scroll rectifier 7 can be used as the casing 1 .
  • the outer circumference of the stator scroll rectifier 7 is made into a circle, the shape of the stator scroll rectifier 7 can be made into a cylinder or a truncated cone, and the inside of the stator scroll rectifier 7 can be made into a cavity, and the cavity can be used as a pipeline.
  • a pipeline can be arranged in the swirl rectifier 7, and the pipeline is connected to the swirl chamber inlet 5, so that the fluid can enter the swirl chamber inlet 5 through the pipeline, and the vortex rectifier 7 can be used to realize the fluid input, which can simplify the structure and can use the existing centrifugal Fans and centrifugal pumps are made into cyclones.
  • the transmission device 2 can also be installed in the vortex rectifier 7, and the swirl wheel 4 can adopt a centrifugal impeller of any structure, so that the fluid can enter through one end of the swirl chamber 3, The other end of the swirl chamber 3 is output, which can be used in the fields of range hood purification of oil fume, air purification, etc., and the structure can be simplified.
  • the stator scroll rectifier 7 is located in the swirl chamber 3 from the swirl wheel 4 to the swirl chamber outlet 6.
  • the stator scroll rectifier 7 and the swirl chamber 3 are located on the same axis, which can be better formed. Swirl flow, the stator vortex rectifier 7 is fixed, and the outer peripheral wall of the stator vortex rectifier 7 has a boundary layer effect on the fluid, so that the material with a smaller specific gravity is closer to the outer circumference of the stator vortex rectifier 7 under the action of the centrifugal force of the circular motion. Under the action of the centrifugal force of the circular motion, the substances with larger specific gravity are further away from the outer peripheral wall of the stator scroll rectifier 7.
  • the stator scroll rectifier 7 enables the fluid to form a swirl flow with increasing rotational speed from the center to the periphery in the swirl chamber 3 around the stator scroll rectifier 7, which can better improve the separation effect.
  • the stator scroll rectifier 7 can be set into a cylindrical shape, a truncated cone shape or a trumpet shape according to the needs, and it is usually set to a cylindrical shape. Wheel 4 diameter is sufficient.
  • a plurality of supports can be arranged on the stator scroll rectifier 7 near the end of the swirl wheel 4. resistance, which promotes fluid rotation.
  • the guide vanes can be used as the supporting device for the stator vortex rectifier 7.
  • the approximate axial flow impeller blade structure is adopted, and a plurality of radially arranged guide vanes form an approximate axial flow impeller-like structure, which can promote the rotation of the swirl flow in the swirl chamber 3 and prolong the axial length of the swirl chamber 3 to improve the separation effect.
  • the rotation of the swirl wheel 4 drives the working medium to rotate and flow in the swirl cavity 3 around the stator vortex rectifier 7 to the outlet 6 of the swirl cavity.
  • the rotation of the swirl wheel 4 drives the working medium to rotate to form a swirl flow.
  • the working medium is gas or Liquids and other fluids, the working medium of this cyclone machine is different when used in different application fields.
  • the cyclone wheel 4 rotates, the cyclone wheel 4 transports the working medium and drives the working medium in the cyclone cavity around the stator vortex rectifier 7 3 inner rotating flow, forming a swirl flow propelled by the rotating flow towards the 6 end of the swirl chamber outlet.
  • At least one retaining ring 9 is arranged around the outer wall of the stator scroll rectifier 7 .
  • One or more retaining rings 9 can be arranged around the outer wall of the stator scroll rectifier 7. Affected by the boundary layer of the outer wall of the stator scroll rectifier 7, the rotational speed of the fluid close to the outer wall of the scroll rectifier 7 is low, resulting in a reduced separation effect.
  • the retaining ring 9 can block the axial flow of the fluid along the area close to the outer wall of the vortex rectifier 7, which can greatly improve the separation effect. Properly increasing the radial width of the retaining ring 9 can improve the separation effect.
  • the axial flow of the water containing pollutants adsorbed by the outer wall of the stator vortex rectifier 7 can also be blocked, so that the water can move to the periphery along the retaining ring 9, and the water can be separated from the outer wall of the vortex rectifier 7. Preventing the water from flowing out of the outlet 6 of the swirl chamber can improve the purification effect of the flue gas.
  • At least one discharge port 8 is arranged on the periphery of the swirl chamber 3 .
  • One or more discharge ports 8 can be arranged on the outer periphery or bottom of the swirl chamber 3 according to needs, which can separate out the separation material with a larger specific gravity. Drain the isolate.
  • multiple discharge ports 8 can also be arranged on the circumference, which can better discharge the separated material.
  • the axial length of the discharge port 8 can also be increased, and the maximum axially penetrating discharge port 8 can be set on the inner wall of the swirl chamber 3, which can better discharge solid separations such as dust;
  • a plurality of discharge ports 8 are arranged in the axial direction on the inner wall, and a variety of separated substances with different specific gravity can be sorted out.
  • the structure of the gradually narrowing end of the radial swirl cavity outlet 6 in the multi-section swirl cavity 3 can axially divide the swirl cavity 3 into multiple regions.
  • the feed port 8 separates out a variety of separates. It is also possible to set up movable sealing discharge devices such as valves, dampers, screw conveyors, etc.
  • a discharge port 8 can adjust the flow rate and the separation effect, so that the separated material can be released from the cyclone under the action of pressure, gravity and centrifugal force in the cyclone chamber 3. It is discharged from the flow chamber 3, and the discharge port 8 can also be opened intermittently to discharge the separated material.
  • a storage bin or ash collection box can also be set up at the discharge port 8, and the material or ash can be discharged intermittently or continuously from the discharge port 8. It is also possible to select the separated material with a larger specific gravity from the discharge port 8.
  • a discharge port 8 can also be set on the lower bottom or side wall of the periphery of the swirl chamber 3, and the discharge port 8 can be used.
  • a stirring cage or an unloader can also be installed on the discharge port 8 to realize automatic ash discharge, which can reduce equipment wear and tear, and can reduce grinding when used in coal mills, coal mills, etc.
  • the extra energy consumption caused by the ash and slag can produce high-purity pulverized coal, which can reduce the entry of sulfide and ash into the furnace, and can better dedust and desulfurize.
  • it can realize while grinding and beneficiation, and the minerals with larger specific gravity and more difficult to grind can be discharged from the lower part or bottom of the periphery of the swirl chamber 3 through the discharge port 8, and the minerals with lighter specific gravity and easier grinding can be discharged.
  • a discharge port 8 can be provided on the lower bottom or side wall of the swirl chamber 3, so that the material with a larger specific gravity in the garbage can be discharged from the discharge port 8, and the smaller specific gravity can be discharged from the discharge port 8.
  • the waste material is blown out from the outlet 6 of the swirl chamber, and can be directly blown into the incinerator. After removing the non-combustible materials with a large specific gravity that are not suitable for combustion, the waste incineration can be better carried out.
  • a discharge port 8 can also be set on the upper part of the swirl chamber 3, which can collect the finer materials after grinding, and add the inner diameter of the upper part of the swirl chamber 3 to the upper part of the swirl chamber 3.
  • the material can be separated better.
  • the lower side of the swirl wheel 4 is provided with a plurality of blades, which can enter the air or water from the lower swirl chamber inlet 5, and feed naturally from the upper swirl chamber inlet 5 or the side wall swirl chamber inlet 5 with a stirring cage.
  • the fineness of the powder can be adjusted by adjusting the air intake or water intake.
  • the pulverized material can be separated from the upper discharge port 8, and the air connection pipe blown out from the outlet 6 of the swirl chamber can be reintroduced into the inlet 5 of the lower swirl chamber to realize closed-circuit circulation. Circulating air can be cooled.
  • the material with larger specific gravity or difficult to grind can be separated from the lower discharge port 8, and the beneficiation can be realized while grinding.
  • the central axis of the swirl chamber 3 of the main structure can be installed horizontally, vertically or obliquely as required.
  • the main structure has the functions of grinding, separation, reaction, etc., and can transport the fluid at the same time, and can be used as separation equipment, grinding equipment, burners, kilns, reactors, etc.
  • the central axis of the cyclone chamber 3 can be installed vertically, which can better discharge the separated gas and avoid affecting the separation effect.
  • the central axis of the cyclone chamber 3 When the central axis of the cyclone chamber 3 is installed horizontally or obliquely, it can be The upper part of the swirl chamber 3 is provided with an exhaust valve, which can be stopped regularly to exhaust. When used in grinding equipment, burners, kilns, etc., the central axis of the swirl chamber 3 can also be installed vertically, so that the large particles can continue to be ground around the swirl wheel 4, which can improve the efficiency.
  • the separation device When used as a separation device, it can be used in various fields that require separation, and can separate substances with different specific gravity. It can be used as dust collector, vacuum cleaner, oxygen production equipment, plasma separator, cream separator, deodorant equipment, air purifier, sewage treatment equipment, water purification equipment, seawater desalination equipment, mineral processing equipment, garbage sorting equipment, coal preparation It can be used in equipment, etc., and the fluid can be transported out at the same time.
  • dust removal and dust suction equipment the gas can be sucked into the cyclone machine from the inlet 5 of the swirl chamber, the dust-free gas can be discharged from the outlet 6 of the swirl chamber, the dust can be discharged from the discharge port 8, and the activity can be set at the discharge port 8.
  • the unloading device open it intermittently or discharge the dust at a fixed flow rate.
  • the dust removal equipment can be thickened in front of the cyclone, which can reduce the wear and sticking of dust to the cyclone wheel.
  • an air outlet can also be set at the discharge port 8.
  • the air outlet is connected to the ash storage bin, and a return air pipe can be set. Dust airflow can be achieved. It can handle high temperature flue gas and realize dry dust removal.
  • the gradual expansion of the radial swirl cavity outlet 6 end of the swirl cavity 3 on the periphery of the swirl wheel 4 can promote the axial movement of the fluid, and can better prevent dust and the like from sticking.
  • a filter screen When used as a vacuum cleaner, a filter screen can be set at the inlet 5 of the swirl chamber to isolate large objects, the dust cleaning is convenient, the cost is low, there is no dust pollution, and it is more environmentally friendly.
  • the flue gas When used as a range hood, the flue gas can be sucked into the cyclone from the inlet 5 of the swirl chamber, and the fumes can be separated, so that the emission of the flue gas is completely environmentally friendly, and the treated smokeless gas is discharged from the outlet 6 of the swirl chamber.
  • the waste oil is discharged from the discharge port 8 .
  • air purification equipment it can be used as an indoor air purifier, and clean air can be separated from the outlet 6 of the swirl chamber, and dust particles can be separated from the discharge outlet 8.
  • air can be sucked into the cyclone, nitrogen can be separated from the outlet 6 of the cyclone chamber, and oxygen can be separated from the outlet 8.
  • the cost of oxygen production is extremely low, which can make boilers, kilns, and engines. To achieve pure oxygen combustion, it can reduce energy consumption, improve thermal efficiency, and eliminate nitrogen oxide emissions. Exhaust gas recirculation can also be used to reduce combustion temperature and reduce equipment material requirements.
  • the lighter gas When used as a deodorant device, the lighter gas can be separated from the outlet 6 of the swirl chamber, and the heavier gas can be separated from the discharge port 8, which can be treated by incineration, collection or chemical reaction for different odor gases. That's it.
  • various oil vapors can be recovered, clean air can be separated from the outlet 6 of the swirl chamber, and oil and gas can be separated from the outlet 8. The separated oil and gas can be condensed, sprayed, and solvent absorbed. After recovery, the recovered residual gas can be sent back to the inlet 5 of the swirl chamber to participate in the separation again, forming a closed cycle, and finally realizing complete recovery.
  • seawater desalination equipment fresh water can be separated from the outlet 6 of the swirl chamber, high-concentration brine can be separated from the discharge outlet 8, and salt can be obtained by evaporation and precipitation.
  • minerals When used as mineral processing equipment, minerals can be sent to the cyclone for grinding and sorting, wet or dry sorting, wet grinding and wet sorting are more effective, and water can be recycled. Heavy elements are separated from the discharge port 8 , and air or water and substances with lighter specific gravity are separated from the outlet 6 of the swirl chamber.
  • coal When used as coal preparation equipment, coal can be made into pulverized coal, which can be dry or wet, and the sulfides, metal elements, precious elements, radioactive elements, common minerals, etc. in the coal can be separated from the discharge port.
  • the selected resources can be used to separate air or water and high-purity coal powder from the outlet 6 of the swirl chamber to produce high-purity coal powder, briquettes or high-purity coal-water slurry.
  • the grinding powder can be dry or wet. Dry grinding can be achieved by using air as a carrier, and wet grinding can be achieved by using water as a carrier.
  • the raw materials to be ground and air or water can be fed separately, and an automatic feeding device can also be set up, which can make feeding more convenient.
  • the grinding continues in the flow chamber 3, and the finer powder is outputted through the outlet 6 of the swirl chamber along with the air or water, and the powder can be recovered by the recovery equipment.
  • the air or water after the recovered powder can also be re-inhaled into the swirl flow.
  • the cavity inlet 5 can realize closed-circuit circulation, which can be more environmentally friendly.
  • an air cooling and cooling device can be installed.
  • the fluid flow in the swirl chamber 3 can be adjusted, and the grinding fineness of the powder can be adjusted. The smaller the fluid flow rate, the finer the grinding fineness of the powder.
  • Adjusting the flow area of the inlet 5 of the swirl chamber can adjust the grinding fineness and the pressure in the swirl chamber 3 .
  • the swirl wheel 4 can also use a round roller, and the inlet 5 of the swirl chamber can be set corresponding to the area of the axis of the round roller.
  • the surface of the round roller can be used to drive the fluid movement, and the flow rate is smaller.
  • Increasing the axial height of the swirl chamber 3 can better select the powder, which is more conducive to the uniformity of the powder fineness.
  • the cyclone can completely solve the common particle agglomeration in the grinding process. Grinding carbene can grind graphene raw materials. It can also be used as a pulverizer for coal grinding, dry grinding of raw coal, and direct injection into kilns and boilers for combustion.
  • the swirl flow can be used to make molecules collide and rub against each other, which can promote chemical reactions and achieve catalytic reaction effects, and can be widely used in the chemical industry.
  • the catalyst layer can also be set on the inner wall of the swirl chamber 3 by spraying, smearing, patching, building blocks, etc., which can further improve the effect of chemical catalytic reaction.
  • the corresponding catalyst can be selected according to the specific working conditions. The flow can make all particles come into contact with the catalyst layer, which can greatly improve the effect of chemical catalytic reaction, and at the same time, it can avoid the adhesion of pollutants on the surface of the catalyst layer, and can improve the service life of the catalyst layer.
  • a denitration catalyst layer When used for flue gas denitration, a denitration catalyst layer can be set up according to specific working conditions to realize SCR denitration.
  • As denitration equipment hydrogen, unsaturated hydrocarbons, etc. can also be used as denitration agents, and hydrocarbons and hydrogen in flue gas can also be used as denitration agents.
  • the drive shaft When used as a burner device, the drive shaft can be placed horizontally or vertically. When large particle fuel is used, the vertical drive shaft is better, and gravity can be used to make the large particle fuel better swirl in the peripheral area of the swirl wheel 4 Grinding in flow chamber 3. It can directly provide hot gas to boilers, kilns, etc., which can reduce boiler renovation costs, and can use any fuel.
  • the swirl flow can be used to achieve fuel separation, so that the fuel with larger particles can always be burned near the area where the swirl wheel 4 is located, so that the burnt ash can leave the area where the swirl wheel 4 is located with the airflow, so that the fuel can be swirled.
  • Uniform swirl combustion is realized in the flow chamber 3, and the swirl combustion and swirl crushing can be used to fully burn the fuel, especially when burning coal or garbage, etc.
  • the mill burns fully.
  • Precisely supplying fuel and adjusting the air volume can keep the temperature of the combustion zone stable and uniform, accurately control the furnace temperature, realize low-temperature combustion, and reduce the production of nitrogen oxides.
  • Simultaneous addition of calcium carbonate chips can achieve dry desulfurization in the furnace.
  • a temperature measuring device can be installed on the inner wall of the swirl chamber 3.
  • the temperature measuring device can use thermocouples, temperature control instruments and other devices.
  • the temperature measuring device can automatically control the automatic feeding device. When the temperature in the furnace reaches the set temperature upper limit, it will automatically cut off. Turn on the power supply of the automatic feeding device, and when the temperature in the furnace reaches the lower limit of the set temperature, automatically turn on the power of the automatic feeding device.
  • Feeding materials into the swirl chamber 3 can make the swirl machine a new type of kiln or incinerator, which can burn cement, lime, magnesia, minerals, garbage, etc.
  • the drive shaft When the drive shaft is used vertically, it can be synchronized Grinding materials, can be fired ultra-high activity ultra-fine lime powder or mineral powder. Adding mineral powder, reducing agent or reactant, etc. can be used as a reaction furnace, which can be used for iron smelting, copper smelting, etc., and can also produce caustic soda, glass, frit, etc. When the transmission shaft is used vertically, the mineral powder and reducing agent, etc.
  • a molten pool is set in the peripheral area of the lower part of the swirl chamber 3 to separate the slag water, and the upper part of the molten pool is provided with a discharge port to discharge the slag , set the discharge port at the bottom of the molten pool to discharge molten iron or copper water, etc.; when the drive shaft is used horizontally, add mineral powder and reducing agent in the swirl chamber 3 close to the 5 section of the swirl chamber inlet, and in the swirl chamber 3 A molten pool is set in the middle area to separate the slag and water, a discharge port is set in the upper part of the molten pool to discharge slag, and a discharge port is set in the lower part of the molten pool to discharge molten iron or copper water.
  • the swirl wheel 4 can be cooled by the incoming air, and can be made of high-temperature-resistant stainless steel, and the swirl
  • the cyclone wheel 4 is provided with a cyclone separation chamber 10
  • one end of the cyclone separation chamber 10 is provided with an outlet 11 of the cyclone separation chamber
  • the other side of the cyclone separation chamber 10 is provided.
  • One end is provided with the cyclone separation chamber inlet 12
  • the cyclone chamber 3 is provided with at least one cyclone chamber inlet 5 corresponding to the cyclone separation chamber inlet 12
  • the stator vortex rectifier 7 section passes through the cyclone separation chamber outlet 11 and penetrates into the cyclone separation chamber 10 Inside.
  • the cyclone separation wheel 4 is provided with a cyclone separation chamber 10 .
  • a cyclone separation chamber 10 may be provided in the cyclone wheel 4 , a cavity may be provided in the cyclone wheel 4 , and the cyclone separation chamber 10 may be formed by using the cavity.
  • the cyclone separation chamber 10 can be set as a cavity with a circular cross section, which can better maintain the dynamic balance of the cyclone wheel 4, so that an annular cylindrical cyclone with increasing rotational speed from the center to the periphery is formed in the cyclone separation chamber 10. flow.
  • the peripheral inner wall of the cyclone separation chamber 10 can be set to be smooth or rough, and the smooth surface can make better use of the boundary layer effect and improve the separation effect.
  • a supercharging device can also be installed in the axial center area of the swirling separation wheel 4 in the swirling flow separation chamber 10, and the supercharging device can be made into a supercharging vane, an axial flow impeller, a centrifugal impeller or a mixed flow impeller structure, which can improve the swirling flow separation.
  • the structural strength of the wheel 4 can also improve the fluid flow and pressure.
  • One end of the cyclone separation chamber 10 is provided with an outlet 11 of the cyclone separation chamber.
  • the outlet 11 of the cyclone separation chamber can be set at one end of the cyclone separation chamber 10, the center of the outlet 11 of the cyclone separation chamber can be set on the central axis of the cyclone separation chamber 10, and the diameter of the outlet 11 of the cyclone separation chamber is the largest with the diameter of the cyclone separation chamber 10. diameters are equal.
  • the inner cavity of the cyclone separation chamber 10 can be set to a structure that gradually expands toward the outlet 11 of the cyclone separation chamber, which can better prevent the particles from depositing on the inner wall of the cyclone separation chamber 10, and can make the separation material move along the cyclone separation chamber 10.
  • the advancement of the inner wall can greatly improve the separation effect.
  • the expansion angle of the inner cavity of the cyclone separation chamber 10 can be selected arbitrarily, as long as the separation material is not deposited on the inner wall of the cyclone separation chamber 10. The smaller the expansion angle of the inner cavity of the cyclone separation chamber 10, the better the separation efficiency can be improved.
  • the inner cavity of the cyclone separation chamber 10 can also be set as a cylindrical structure, but the disadvantage is that it is easy to cause the separation material to be deposited on the inner wall of the cyclone separation chamber 10 .
  • the other end of the cyclone separation chamber 10 is provided with an inlet 12 of the cyclone separation chamber.
  • the cyclone separation chamber inlet 12 can be provided at the other end of the cyclone separation chamber 10, and the cyclone separation chamber inlet 12 can be arranged either in the cyclone separation chamber 10 or on the cyclone separation wheel 4, and the cyclone separation chamber inlet 12
  • the fluid can be sent into the cyclone separation chamber 10 by means of a guide tube.
  • the inlet 12 of the cyclone separation chamber is arranged on the cyclone separation wheel 4
  • the inlet 12 of the cyclone separation chamber can be arranged on the end of the cyclone separation wheel 4 connected to the transmission device 2, and a plurality of cyclone separation chamber inlets 12 can be arranged.
  • the support body can be connected with the transmission device 2, so that the working medium can flow into the cyclone separation chamber 10 from the inlet 12 of the cyclone separation chamber, and the axial flow of the working medium can be realized, and it can also realize various functions, such as being used for Better separation of materials can be achieved during grinding and beneficiation.
  • the swirl chamber 3 is provided with at least one swirl chamber inlet 5 corresponding to the inlet 12 of the swirl separation chamber.
  • One or more swirl chamber inlets 5 may be provided at one end of the swirl chamber 3 corresponding to the inlet 12 of the swirl separation chamber.
  • a section of the stator vortex rectifier 7 penetrates the outlet 11 of the cyclone separation chamber and penetrates into the cyclone separation chamber 10, so that the fluid can be directly sent into the cyclone separation chamber 10, so that the fluid flows along the cyclone separation chamber under the action of the rotating centrifugal force.
  • the inner wall of 10 rotates forward, and is finally thrown out from the outlet 11 of the cyclone separation chamber.
  • the outer wall of the stator scroll rectifier 7 can be parallel to the inner wall of the swirl separation chamber 10, which can better improve the effect of swirl movement.
  • the flow rate can be reduced, both of which will reduce the effect of the cyclone motion.
  • the outer wall of the stator scroll rectifier 7 is stationary, and the inner wall of the swirl separation chamber 10 rotates, and there is relative motion between the two.
  • the outer wall of the stator scroll rectifier 7 and the swirl separation chamber 10. The smaller the gap between the inner walls, the more severe the relative motion, the more severe the relative friction to the fluid existing between the two, and the more severe the swirl motion, and the outer wall of the stator vortex rectifier 7 conforms to the inner wall of the swirl separation chamber 10. Improve the separation effect well.
  • the outer wall of the stator vortex rectifier 7 can be set to be smooth or rough, and the smooth surface can make better use of the boundary layer effect and can improve the separation effect.
  • the effect of the boundary layer on the outer wall of the stationary stator vortex rectifier 7 can absorb the light-gravity separator, and the centrifugal force generated by the inner wall of the rotating cyclone separation chamber 10 can attract the heavier-gravity separator, and the rotating speed increases from the center to the periphery.
  • the swirling flow makes the separated substances with different specific gravity move to the center of the swirling flow and the periphery of the swirling flow respectively, and finally realizes the separation of the separated substances with different specific gravities.
  • stator scroll rectifier 7 If there is no stator scroll rectifier 7, the separated materials with different specific gravity will move to the inner wall of the cyclone separation chamber 10 under the action of centrifugal force, and it is difficult to achieve separation in the end, and the friction effect on the surface of the stator scroll rectifier 7 is missing, resulting in The swirl center with increasing rotational speed from the center to the periphery is similar to the peripheral rotational speed, which greatly reduces the separation effect. This is the fundamental reason for the poor separation effect of the existing centrifuge technology.
  • the outer wall of the stator vortex rectifier 7 is to improve the cyclone separation. The key component of the effect.
  • the rotation of the fluid is greatly accelerated, the attractive force between particles is opened, and the separation effect can be greatly improved.
  • the structure of the second embodiment of this cyclone is: on the basis of the above structure, at least one surrounding partition body 13 is provided on the inner wall of the cyclone cavity 3, and at least one discharge port 8 is provided on the periphery of the cyclone cavity 3 corresponding to the surrounding partition body 13.
  • Surrounding the partition body 13 can adopt a flange plate or a cylinder body, and one or more flange plates can be arranged on the inner wall of the swirl chamber 3 in parallel with the cross section of the swirl chamber 3 to divide the swirl chamber 3 into multiple sections, and the swirl chamber 3 can be divided into multiple sections.
  • the flow chamber 3 is axially isolated into a plurality of regions, and the flange can block the axial flow of the fluid along the periphery of the swirl chamber 3 to achieve the separation effect. It is also possible to set a surrounding retaining ring on the inner port of the flange near the inlet 5 of the swirl chamber.
  • the surrounding retaining ring can be made into a cylindrical shape or a pull-out shape.
  • the support function can make the flange flat, and can block the flow of the separator to the 6 end of the outlet of the swirl chamber, which can improve the separation effect.
  • the pulling cylinders can be set in the straight cylindrical swirl chamber 3, and connect the thicker end of the pulling cylinder to the inner wall of the swirl chamber 3, which can simplify the structure, and the pulling cylinder is relatively large.
  • the thin end can be facing the inlet 5 of the swirl chamber or the outlet 6 of the swirl chamber.
  • the thinner end of the cylinder is facing the inlet 5 of the swirl chamber, it can better block the separation from the outlet 6 of the swirl chamber. flow, which can improve the separation effect. Due to the difference in specific gravity and particle size, the moving speed of the separated objects to the outer periphery of the swirl chamber 3 is different during the axial movement process, and different separated materials move to different regions in the axial direction.
  • the outer periphery of the swirl chamber 3 is provided with a discharge port 8 corresponding to the surrounding separator 13 , and one or more discharge ports 8 can be set on the periphery of the swirl chamber 3 corresponding to the surrounding separator 13 according to the needs.
  • the discharge port 8 When the discharge port 8 is arranged on the side of the surrounding separator 13 close to the inlet 5 of the swirl chamber, it can discharge the separator with a larger specific gravity. It can block the separator with larger specific gravity and discharge the separator with smaller specific gravity. In use, the flow rate of each discharge port 8 can also be adjusted, which can better separate various separated substances.
  • this embodiment When this embodiment is used as sewage and waste gas treatment equipment, various useful components can be extracted and sorted from sewage and waste gas, and dust removal, desulfurization, and denitrification can be simultaneously completed;
  • dust removal equipment and dust suction equipment When used as dust removal equipment and dust suction equipment, the gas can be sucked into the cyclone machine from the inlet 5 of the cyclone chamber, the dust-free gas can be discharged from the outlet 6 of the cyclone chamber, the dust can be discharged from each discharge port 8, and the dust can be discharged from each outlet port 8.
  • the material port 8 separates dust particles of various components and gases of various components, and dust removal and gas separation can also be completed simultaneously.
  • air separation equipment When used as air separation equipment, oxygen production equipment, nitrogen production equipment, and rare gas production equipment, air can be sucked into the cyclone, and various gases such as oxygen, nitrogen, and inert gas can be separated from each discharge port 8. , all kinds of gases can be directly collected and utilized. When special needs are required, high-purity gas can be obtained by secondary separation of various gases.
  • minerals, etc. When used as ore dressing or coal dressing equipment, minerals, etc. can be sent to the cyclone for grinding and sorting, wet or dry sorting, wet grinding and wet sorting are better, the water can be recycled, and the specific gravity can be reduced. Large metal elements and heavy elements are separated from the discharge port 8 respectively, and air or water and substances with lighter specific gravity are separated from the cyclone chamber outlet 6, and useful minerals can be separated from each discharge port 8 respectively.
  • the sewage When treating sewage and purifying water, the sewage can be biochemically treated first, and then the reclaimed water can be treated with this cyclone.
  • the material port 8 is discharged, so that the purified water that reaches the standard is separated from the outlet 6 of the cyclone chamber, and the mother and child cyclones are set up, and each child cyclone is used to perform secondary treatment on the discharged high-concentration brine, and multi-stage treatment can further separate various types of salt, etc.
  • the salt and heavy metals in the reclaimed water can be removed.
  • water purification treatment equipment referring to seawater desalination, the heavy elements in the water can be separated, the beneficial elements can be retained, and the organic components, chlorine, microorganisms, insect eggs, etc. in the water and part of the water can be separated from the outlet 6 of the cyclone cavity and discharged.
  • the purified water up to the standard is discharged from the discharge port 8 near the outlet 6 of the swirl chamber.
  • the cyclone can also
  • the crude oil When used as oil refining equipment, the crude oil can be directly sucked into the cyclone, and the crude oil is affected by the movement of the cyclone fluid and the centrifugal force and gravity generated by the cyclone, so as to realize the separation of various components. Heavy elements, metals, sulfur, asphalt, paraffin, heavy oil, lubricating oil, diesel oil, kerosene, gasoline, etc. can be discharged from each discharge port 8 near the inlet 5 of the swirl chamber in sequence.
  • the intermediates of the two oils can be re-introduced into the crude oil for re-separation, or a mother-child cyclone can be set up, and each sub-cyclone can be used to carry out secondary separation and multi-stage separation of various components discharged, which can realize various components.
  • the ultra-high purity can be extracted into high-purity gasoline, diesel oil, lubricating oil, various petroleum products, sulfur, heavy metals, lead, radioactive elements, etc., so that the oil can be completely lead-free and free of radioactive element pollution.
  • the whole production process is pollution-free, and there is no waste water and waste gas discharge.
  • the refining process is completely environmentally friendly, and the resources are fully recovered and utilized, which can greatly reduce the cost of refining.
  • Low temperature cracking reduces the damage to the macromolecular structure of crude oil at high temperature, reduces the production of petroleum gas, petroleum residue, asphalt, wax, etc., and can improve the oil yield.
  • powders of various particle sizes When used as a grinding device, powders of various particle sizes can be sorted, and the powders selected are finer as they are closer to the discharge port 8 of the outlet 6 of the swirl chamber.
  • the raw coal can also be dry-ground and dry-selection, and various minerals in the coal can be selected from each discharge port 8, and the pulverized coal can be ejected from the outlet 6 of the swirl chamber, which can be directly injected into the kiln, boiler, etc. for combustion.
  • the useful elements with smaller specific gravity and larger specific gravity can be separated from each discharge port 8 respectively. Improving the selection effect can make the tailings more environmentally friendly.
  • the highly radioactive elements in the nuclear waste can be extracted and put back into the nuclear reactor for nuclear transmutation into low-level elements, and the low-level materials can be vitrified and landfilled.
  • the structure of the third embodiment of the swirl machine is as follows: on the basis of the above structure, the inner wall of the swirl chamber 3 around the swirl wheel 4 is close to the outer edge of the swirl wheel 4 .
  • the swirl wheel 4 can adopt a swirl wheel of any structure, and the axial thickness of the swirl wheel 4 can be increased as much as possible, which can improve the effect.
  • a cylinder or a round roller can be arranged on the side of the swirl wheel 4 near the outlet 6 of the swirl chamber, so that the outer circumference of the swirl wheel 4 and the inner wall of the swirl chamber 3 can be close to each other, and the swirl friction can be better formed.
  • the length of the swirl wheel blade can be shortened, and a groove with an oblique angle to the cross section can be arranged on one or the entire section of the round roller, which can replace the swirl wheel blade and increase the outer peripheral surface area of the swirl wheel;
  • a cylinder or a round roller can be arranged on the side of the swirl wheel 4 close to the outlet 6 of the swirl chamber, or an open centrifugal impeller can be used, and a plurality of blades can be arranged on the side of the swirl wheel 4, which can simplify the structure.
  • the inner wall of the swirl chamber 3 around the swirl wheel 4 is close to the outer edge of the swirl wheel 4, which can make the swirl friction more intense.
  • the reaction effect When used as a reactor, the reaction effect can be improved; when used as a grinding device, the grinding effect can be improved. , can be ground into finer powder; when used as mineral processing equipment, it can better realize mineral grinding and dissociation, and can improve the mineral processing effect.
  • the reaction effect When used as a wet-type flue gas purification equipment, super-atomization cleaning of the flue gas can be formed on the periphery of the swirl wheel 4, which can improve the flue gas purification effect.
  • the transmission shaft can be installed horizontally or vertically.
  • the rotational speed of the swirl wheel 4 reaches a certain height, when the inner wall of the swirl cavity 3 around the swirl wheel 4 is in close contact with the outer edge of the swirl wheel 4, the swirl friction increases. Violently, it can decompose molecules, and can break molecular chains such as H2O, SO2, CO2, NO, HS, O2, and hydrocarbons to achieve molecular decomposition.
  • Water molecules can be decomposed, hydrogen ions can be produced by water or water vapor, hydrogen ions can be separated from the outlet 6 of the swirl chamber, and oxygen ions can be separated from the outlet 8. The hydrogen ions can react and burn with oxygen in nature, which can completely solve the problem.
  • Oxygen ions can react with many substances in nature to form a variety of completely new compounds. It can process SO2, CO2, NO, HS, etc., can decompose SO2 to produce sulfur ions, can decompose CO2 to solve carbon emissions, can use waste gas to produce S, C plasma, can separate S, C plasma from the discharge port 8, and use them Manufactures many new compounds; can treat organic waste gas, decompose organic molecules, and can be used to treat waste gas odor, etc.
  • oxygen ions can be used as oxidants.
  • the oxygen ions can form polyatomic oxygen such as O3, O4, O5, O6, O7, O8, etc., which can be used to manufacture a variety of brand-new oxides.
  • a variety of gases can be decomposed into ionic states, which can be used to create a variety of completely new compounds.
  • This embodiment can be used as a reactor, grinding equipment, flue gas purification equipment, etc., and can improve the effects of grinding, reaction, atomization cleaning, and the like.
  • the structure of the fourth embodiment of the cyclone is as follows: on the basis of the above structure, the axis of the cyclone chamber 3 is placed vertically, and the lower part of the cyclone chamber 3 is provided with a surrounding pool 14 .
  • the axis of the swirl cavity 3 is placed vertically, and a surrounding pool 14 is arranged at the lower part of the swirl cavity 3.
  • a ring of retaining rings can be set on the inlet 5 of the swirl cavity 3, so that the lower part of the swirl cavity 3 forms a surrounding pool 14, and the surrounding pool 14 can be connected with
  • the swirl chamber 3 is connected into one body or separately arranged, and the casing at the lower part of the swirl chamber 3 can be submerged into the surrounding pool 14, and the water in the pool can be used to realize the sealing of the casing.
  • the small cyclone machine for household products When the small cyclone machine for household products is used for air purification , can be set as a separate structure, after the cyclone can be taken out of the surrounding pool 14, the water in the surrounding pool 14 can be added regularly or manually dumped and replaced; when used in the field of oil fume purification, the surrounding pool 14 and the cyclone
  • the cavity 3 can be connected into a whole, and the discharge port 8 can be set at the lower part of the surrounding pool 14, and a valve can be set on the discharge port 8 to connect to the sewer.
  • all the water can be drained. Automatically add water.
  • the transmission device 2 can be installed in the stator scroll rectifier 7, which can simplify the structure.
  • the inner wall of the swirl chamber 3 on the periphery of the swirl wheel 4 can be close to the periphery of the swirl wheel 4, which can improve the purification effect.
  • the inner wall of the swirl chamber 3 can be integrated with the surrounding pool 14, and a gap is arranged at the bottom to keep the pool connected. .
  • the swirl wheel 4 rotates, it drives the water in the surrounding pool 14 to flow to the outer circumference of the swirl chamber 3, and at the same time, a small amount of water mist can be sucked into the swirl wheel 4.
  • the flow chamber 3 moves upward, the water mist condenses on the inner wall of the swirl chamber 3 to form a water film, and the water film maintains a certain thickness, which can improve the contact between water and air, and can absorb dust, formaldehyde, etc. That's it.
  • the water level can be kept slightly lower than the inlet level of the swirl wheel 4.
  • This embodiment can be used in the fields of household air purification, cooking fume purification, etc., and can absorb dust, formaldehyde, cooking fume, etc. in the air into water. It can absorb the oil into the water when it is used to smoke oil fume, which can make it easier to discharge the oil.
  • the structure of the fifth embodiment of the swirl machine is: on the basis of the above structure, the swirl chamber 3 is provided with a spray device 15 corresponding to the swirl wheel 4 .
  • a spray device 15 can be provided near the inlet 5 of the swirl chamber or on the stator vortex rectifier 7 corresponding to the inlet of the swirl wheel 4.
  • the spray device 15 can be provided with various forms of atomizing nozzles, and the atomizing nozzles are connected to the infusion pipeline. Yes, just adjust the distance between the atomizing nozzle and the swirl wheel 4 during installation.
  • the spray device 15 continuously provides spray and atomized water to the swirl wheel 4, which can continuously wash the swirl wheel 4, and can prevent the impeller from sticking when it is used to deal with viscous and oily smoke.
  • the water liquid comes out of the swirl wheel 4, it is rapidly decomposed into finer water mist by the swirl flow in the swirl cavity 3 around the swirl wheel 4, so that the flue gas can interact with the water in the swirl cavity 3 around the swirl wheel 4.
  • the mist is quickly and fully contacted and washed to realize the ultra-atomization cleaning of the flue gas, so that various pollutants in the flue gas enter the water mist.
  • the mixture of flue gas and water mist leaves the peripheral area of the swirl wheel 4 and enters the peripheral area of the stator vortex rectifier 7. Under the action of the swirling flow in this area, demisting is realized, so that the flue gas and water mist are gradually separated, and the water is finally removed.
  • the misted flue gas is discharged from the outlet 6 of the swirl chamber, and the removed water mist is collected into water and discharged from the discharge port 8 .
  • a drain port can be opened at the lower part of the pipeline inlet to discharge the water liquid.
  • the atomizing nozzle of the spray device 9 can also be arranged on the back of the swirl chamber 3 corresponding to the centrifugal swirl wheel 4, and the water mist can be further cut and separated by the rotation of the swirl wheel 4, which can improve the atomization. It can improve the effect of flue gas purification.
  • a plurality of nozzles can also be arranged around the periphery of the swirl wheel 4, which can improve the effect of water mist atomization, and can improve the effect of atomization, washing and purification of flue gas.
  • the water inlet pipe can also be set on the periphery of the swirl wheel 4 along the tangential direction of the cross section of the swirl cavity 3 to comply with the rotation direction of the swirl wheel 4.
  • the rotation of the swirl wheel 4 can make the water on the inner wall of the swirl cavity 3 rotate, so that the separation It is pumped into the water and discharged together with the water, and a water film can be formed on the inner wall of the swirl chamber 3 that spirally moves toward the 6 end of the swirl chamber outlet, so that the separated material can enter the water film and follow the water to the swirl chamber outlet 6.
  • the swirl chamber 3 on the periphery of the swirl wheel 4 is made into a structure that slightly expands to the 6 end of the swirl chamber outlet, so that the water can flow to the 6 end of the swirl chamber outlet more smoothly; the swirl wheel 4 adopts an axial flow impeller
  • a guide vane can be arranged near the swirl wheel 4
  • a water inlet pipe can be arranged near the guide vane, which can improve the purification effect.
  • the vortex rectifier 7 can also be made into an empty pipe structure.
  • a pipe cavity can be arranged inside the vortex rectifier 7, and a spray device of any structure can be set in the pipe cavity, so that the pipe cavity forms a spray chamber, and the pipe cavity can be formed into a spray chamber.
  • a water outlet is provided at the lower part of the periphery of the inlet area to discharge the spray water, and the flue gas can be subjected to a first-level spray purification treatment before the inlet 5 of the swirl chamber, which can improve the flue gas purification effect.
  • a circle of rollers is arranged on the periphery of the inlet side of the swirl wheel 4 to improve the effect of flue gas purification.
  • the inner wall of the swirl chamber 3 on the periphery of the swirl wheel 4 can be close to the outer edge of the swirl wheel 4.
  • the swirl wheel 4 can adopt an impeller of any structure, and the axial thickness of the swirl wheel 4 can be increased as much as possible.
  • a cylinder or a round roller is arranged on the side of the outlet 6 of the swirl chamber, which can make the outer circumference of the swirl wheel 4 and the inner wall of the swirl chamber 3 close to each other, which can better form swirl friction, and can greatly improve the cleaning effect of flue gas atomization.
  • the drive shaft of this embodiment can be installed horizontally, obliquely, or vertically. It can replace existing dust collectors, desulfurization towers, etc., and can be widely used in all exhaust gas treatment fields such as various kilns, boilers, and incinerators. in all areas where flue gas is handled.
  • this embodiment is used for chemical odor removal, the odor components can be better collected, and the odor components can also be reacted with acid and alkali, which can better remove the odor.
  • wet dust removal can be performed, which can remove dust and harmful substances more efficiently, and can make the flue gas more environmentally friendly.
  • the cyclone can also be installed at the end of the flue gas purification.
  • spraying clean water can improve the flue gas purification effect.
  • the clean water can be supplemented by desulfurization and evaporation, which can completely eliminate wet electricity, and can simultaneously remove fine dust, deamination, and degassing.
  • Sol, removal of various pollutants, secondary desulfurization by adding alkali in water, etc., can achieve near zero emission of flue gas.
  • the structure of the sixth embodiment of the cyclone is as follows: on the basis of the above structure, a feeding device 16 is provided in the cyclone 3 near the inlet 5 of the cyclone.
  • a feeding device 16 can be provided on the outer peripheral wall of the swirl chamber 3 near the inlet 5 of the swirl chamber.
  • the material is evenly fed into the swirl chamber 3, and the ore powder can also be made into mud and transported by a diaphragm pump or a mud pump during beneficiation.
  • the feeding device 16 can also be arranged on the periphery of the swirl wheel 4. After the material enters the swirl chamber 3, it is fully mixed with the conveying medium (water or air) under the action of the swirl wheel 4, and the material is driven by the swirl flow and continuously powdered. Grinding, and finally achieve sorting.
  • the inner wall of the swirl chamber 3 on the periphery of the swirl wheel 4 can be provided with a wear-resistant layer, which can improve the service life.
  • the transmission shaft of this embodiment can be installed horizontally or vertically, and can be used as mineral processing equipment, grinding equipment, garbage disposal equipment, mud dewatering and drying equipment, etc. It can be used for dry separation, wet separation, dry grinding or wet grinding. It can be finished synchronously while grinding and selecting, which can avoid the wear and sticking of the material caused by the swirl wheel 4.
  • a discharge port 8 can be set on the upper part of the swirl chamber 3 to separate the milled materials.
  • air drying can also be used to dehydrate and dry various muds, and the ultrafine mud can be dewatered and dried.
  • the structure of the seventh embodiment of the swirl machine is as follows: on the basis of the above structure, the swirl chamber 3 near the inlet 5 of the swirl chamber is provided with a feeding device 16 and a combustion supply device 17 .
  • a feeding device 16 and a combustion supplying device 17 can be provided on the outer peripheral wall of the swirl chamber 3 near the inlet 5 of the swirl chamber.
  • the feeding device 16 can be a conveying device such as a stirring cage. It is arranged near or on the periphery of the swirl wheel 4, which can help the fuel to burn fully.
  • the combustion supply device 17 can use different fuel supply devices according to the fuel used. fuel.
  • a temperature measuring device can be used, and a temperature control device can be provided to adjust the fuel supply speed of the combustion supply device 17 according to the temperature to realize the temperature control of the swirl chamber 3 .
  • a small swirl chamber inlet 5 can also be added at the shaft end, and the transmission device 2 can be cooled by the intake air.
  • the swirl chamber 3 can be provided with a thermal insulation layer, and the inner wall of the swirl chamber 3 around the swirl wheel 4 can be provided with a refractory and wear-resistant material layer.
  • a discharge port 8 is arranged at the lower part of the swirl chamber 3 to discharge the slag regularly.
  • One or more discharge ports 8 are arranged on the upper part of the swirl chamber 3 to collect the fired materials for discharge.
  • the drive shaft of this embodiment can be installed horizontally or vertically, and can be used as a new type of kiln, reaction furnace, incinerator, drying furnace, etc., and can burn a variety of materials, such as: lime, magnesia, cement, coke gems, A variety of minerals, garbage, etc. It can achieve uniform calcination or drying of materials, and can make materials continuously pulverized while calcined or dried, and can achieve rapid and sufficient calcination or drying, and can sinter block or powder materials.
  • the block material can be directly ground, and the powder can be fired while grinding, and the powder can be separated.
  • the powder can be directly transported to the storage tank by air flow. Realize fully automatic feeding and discharging.
  • This embodiment can also be used in various fields that require drying and dehydration of products.
  • the product slurry can be sprayed into the high temperature area of the cyclone chamber 3 with the feeding device 16 .
  • the drive shaft is installed horizontally, small pieces of materials or liquid slag materials can be fired.
  • the structure of the eighth embodiment of the swirl machine is as follows: on the basis of the above structure, the swirl chamber 3 near the inlet 5 of the swirl chamber is provided with a combustion supply device 17, the swirl chamber 3 is provided with a feeding device 16, and the lower part of the swirl chamber 3 is provided with a combustion supply device 17.
  • a molten pool 18 is provided, and at least one discharge port 8 is provided in the molten pool 18 .
  • a combustion supply device 17 can be provided on the outer peripheral wall of the swirl chamber 3 near the inlet 5 of the swirl chamber. The combustion supply device 17 can use different fuel supply devices according to the fuel used. Fuel is supplied directly from the fuel line.
  • Thermocouples can be used to measure the temperature, and a temperature control device can be provided to adjust the fuel supply speed of the combustion supply device 17 according to the temperature to realize the temperature control of the swirl chamber 3 .
  • a small swirl chamber inlet 5 can also be added at the shaft end, and the transmission device 2 can be cooled by the intake air.
  • the swirl chamber 3 is provided with a feeding device 16, and one or more feeding devices 16 can be set in the swirl chamber 3.
  • the feeding device 16 can be used to blow mineral powder, limestone powder, coal powder, etc. into the swirl chamber 3, Mineral powder and limestone powder can be conveyed by air flow, and an automatic flow control device can be installed.
  • the combustion supply device 17 can usually be arranged on the periphery of the swirl wheel 4 for better combustion.
  • the flue gas contains coal gas, and the exhaust gas can be treated after the coal gas is used or the waste heat is used for power generation. The air after collecting the waste heat is sucked into the swirl cavity 3 through the inlet 5 of the swirl cavity, and the pulverized coal is fed into the swirl cavity 3 through the combustion supply device 17. sports.
  • a molten pool 18 is provided at the lower part of the swirl chamber 3 , and the molten pool 18 can be arranged at any position in the lower part of the swirl chamber 3 , one or more molten pools 18 can be arranged, or an annular molten pool 18 can be arranged around the lower part of the swirl chamber 3 .
  • the molten pool 18 can be provided with a certain depth, and the molten pool 18 can be provided with one or more discharge openings 8.
  • the discharge openings 8 can be set at the upper and lower parts of the molten pool 18 respectively, which can be realized when used for iron smelting, copper smelting, etc.
  • the slag water is separated, the lower discharge port 8 discharges the water, and the upper discharge port 8 discharges the slag.
  • the molten iron and slag water formed by the reaction flow into the molten pool 18 and the slag water is separated and discharged .
  • Set the temperature control device to control the furnace temperature
  • set the feed control device to automatically control the feeding speed of ore powder, and open the discharge port 8 regularly to discharge slag water, molten iron or copper water, etc.
  • the mineral powder and reducing agent are added in the middle section of the swirl chamber 3. After the mineral powder and the reducing agent are melted, they flow down along the inner wall of the swirl chamber 3.
  • Water can be separated.
  • the radial swirl cavity outlet 6 in the melting section swirl cavity 3 gradually expands, which can better make the molten liquid flow to the swirl cavity outlet 6, and the mineral powder and reducing agent are swirled.
  • the cavity 3 is added in the 5th stage near the inlet of the swirl cavity 3, and the molten pool 18 is set in the middle area of the swirl cavity 3 to separate the slag and water.
  • the air Suction into the air intake duct, the air can be used to cool the support device, which can reduce the heat resistance requirements of the material.
  • This embodiment can be used as a smelting furnace, a melting furnace, etc., and can smelt a variety of metals, and can be used for iron smelting, copper smelting, aluminum-silicon alloy smelting, production of smelting alkali, glass, ceramic frit, and the like.
  • the central axis of the swirl chamber 3 can be installed vertically or horizontally, and the fuel can be any fuel such as pulverized coal, gas, oil, etc. as required. No coke and pellets are used in iron making, which greatly reduces the production cost.
  • the structure of the ninth embodiment of the swirl machine is as follows: on the basis of the above structure, the swirl chamber 3 near the inlet 5 of the swirl chamber is provided with a combustion supply device 17 , and the inner wall of the swirl chamber 3 is provided with a heat recovery device 19 .
  • the swirl chamber 3 near the inlet 5 of the swirl chamber is provided with a combustion supply device 17, which can form a combustion zone in this area.
  • the combustion supply device 17 can be set according to the fuel used.
  • the solid fuel can use a stirring cage, an unloader, etc., and the liquid , Gas fuel can use nozzle and so on.
  • Combustion supply device 17 can evenly discharge coal, garbage, etc., dry desulfurization agent, etc., into swirl chamber 3 .
  • a temperature measuring device can also be installed on the inner wall of the swirl chamber 3.
  • the temperature measuring device can use thermocouples, temperature control instruments and other devices.
  • the temperature measuring device can control the combustion supply device 17 through the temperature control instrument.
  • the combustion supply device 17 can usually be arranged on the side of the swirl wheel 4 close to the outlet 6 of the swirl cavity, and can be arranged along the cross section of the swirl cavity 3 tangentially to the rotation direction of the swirl wheel 4, so that the fuel can be fed more smoothly, and at the same time, it can be better.
  • a heat recovery device 19 is arranged on the inner wall of the swirl chamber 3, and a heat recovery tube or a heat recovery box can be arranged on the inner wall of the swirl chamber 3 as the heat recovery device 19, and water, oil or gas can be used as the heat recovery medium.
  • the heat collection device 19 can be arranged close to the inner wall of the swirl chamber 3 , and the heat collection pipe can also be arranged around the inner wall of the swirl chamber 3 .
  • the heat recovery device 19 can adopt the heat recovery tube device adopted by any existing boiler, and can realize various pressure boilers as required.
  • high-pressure heat recovery pipes When used as medium-pressure, high-pressure and ultra-high pressure boilers, high-pressure heat recovery pipes can be installed in the 5th section near the inlet of the swirl chamber, and low-pressure heat recovery pipes can be installed in the 6th section near the outlet of the swirl chamber. Realize forced circulation, which can improve heat recovery efficiency.
  • This embodiment can be used as a variety of boiler equipment, and can use any fuel such as coal, oil, gas, biomass, garbage, coal-water slurry, and pulverized coal.
  • the central axis of the swirl chamber 3 can be installed vertically or horizontally, so that the fuel can achieve uniform swirl combustion in the swirl chamber 3.
  • the swirl combustion and swirl crushing can be used to fully burn the fuel.
  • coal lumps or garbage can be continuously peeled off, broken, and fully burned.
  • Precisely supplying fuel can keep the temperature of the combustion zone stable and uniform, accurately control the furnace temperature, realize low-temperature combustion, and reduce the production of nitrogen oxides.
  • Simultaneous addition of calcium carbonate stone chips during coal combustion can achieve dry desulfurization in the furnace, the temperature in the furnace is uniform, and the swirl promotes the reaction, which can achieve full dry desulfurization.
  • the swirling flow formed by the swirl chamber 3 can promote the air flow velocity on the surface of the heating device 19, which can greatly improve the heating efficiency, greatly reduce the heating area, and greatly reduce the cost.
  • the swirl motion greatly extends the moving distance of the hot air in the swirl chamber 3, which can fully transfer heat energy and achieve efficient and sufficient heat recovery.
  • a discharge port 8 can also be provided on the periphery of the swirl chamber 3 near the swirl wheel 4, so that the materials that are difficult to grind and burn can be discharged intermittently or continuously.
  • This embodiment is a high-efficiency boiler that can burn any fuel, making the burnout rate close to 100%, and greatly reducing the emissions of carbon monoxide, sulfur and nitrate. It is also a high-efficiency garbage incinerator, which can fully burn garbage and fully utilize thermal energy.
  • the fluid can be transported out at the same time, and the fluid can be separated, reacted and ground in the cyclone.
  • the swirl wheel 4 rotates, it drives the fluid to flow out from the swirl wheel 4, and the fluid forms a swirl flow in the swirl chamber 3 under the action of motion inertia.
  • the particles form independent moving individuals, which can better use centrifugal force to separate particles of different specific gravity, and use the centrifugal force generated in the swirl to realize the separation and sorting of substances with different specific gravity in the fluid.
  • the swirling flow spirals along the axial direction, and the independent moving individuals with different specific gravity move at different speeds toward the periphery of the swirl flow, and the particles or particles with larger specific gravity move to the inner wall of the swirl chamber 3 more easily and faster, and finally realize the different specific gravity. Separation of isolates.
  • the fluid is affected by fluid movement, centrifugal force and gravity to achieve the separation of various separators.
  • Various separations with different specific gravity move to different axial regions of the swirl chamber 3 respectively, and are discharged through different axial discharge ports 8 respectively, and finally realize the separation and sorting of the fluid or the removal of pollutants.
  • the fluid is gradually separated during the axial movement.
  • the flue gas can be fully and quickly contacted with the water and liquid, so that the pollutants in the flue gas can fully enter the water and the liquid, and the clean exhaust gas is discharged from the outlet 6 of the swirl chamber.
  • the swirl flow is used to promote chemical reactions, to achieve desulfurization and denitrification, and to achieve complete purification of flue gas.
  • the catalysts arranged on the inner wall of the swirl chamber 3 can be used to further promote various chemical reactions. Separation can solve water pollution, desalination of sea water, water resources, mineral processing, mineral resources, nuclear waste pollution, oxygen production and pure oxygen combustion, etc.
  • the swirl flow is used to realize the swirl grinding, so that the materials are gradually ground into fineness with the mutual friction and collision during the movement of the air flow, which can achieve high-efficiency grinding, and can grind out ultra-fine powder, nano-powder, and single-atom particles, which can solve the problem of nano-particles.
  • Material raw material can grind carbonene, can solve graphene raw material.
  • the high-speed swirl flow is used to decompose the molecules by constant friction and collision in the swirl flow, the molecular chain is opened by the high-speed swirl flow to realize the decomposition of the molecules into ions, and the swirl flow is used to achieve the separation of different ions formed by the molecular decomposition.

Abstract

一种旋流机,包括壳体(1)和传动装置(2),壳体(1)上设置传动装置(2),壳体(1)内设置旋流腔(3),旋流腔(3)横截面为圆形,旋流腔(3)内一端轴心区域设置旋流轮(4),旋流轮(4)与旋流腔(3)处在同一轴线上,传动装置(2)与旋流轮(4)连接,旋流腔(3)对应旋流轮(4)至少设置一个旋流腔进口(5),旋流腔(3)另一端设置旋流腔出口(6),壳体(1)上贯穿从旋流轮(4)到旋流腔出口(6)之间的旋流设置横截面为圆型的定子涡旋整流体(7),环绕定子涡旋整流体(7)外壁至少设置一道挡圈(9),旋流腔(3)外围至少设置一个出料口(8)。旋流机可广泛用于除尘、脱硫、脱硝、除烟、除味、抽油烟、空气净化、垃圾处理、垃圾焚烧、核废料处理、选粉、选矿、海水淡化、污水处理、净水、炼油、制氧、反应器、锅炉、燃烧器、粉磨设备、窑炉、冶炼炉、熔炉等领域。

Description

旋流机 技术领域
本发明涉及污水处理、净水、海水淡化、海洋化工、选矿、选煤、核废料处理、炼油、油气回收、垃圾处理、空气净化、除尘、脱硫、脱硝、抽油烟净化、尾气处理、除黑烟、除异味、制氧、空气分离提取、化学反应器、锅炉、燃烧器、窑炉、反应炉、粉磨、粉体制备、泥浆干化、分子分解、水分解制氢、分解CO2、分解异味气体分子等领域,具体是一种旋流机,可实现粉磨、化学反应、分离、分子分解等功能,各种功能即可单独使用也可组合使用,同时可实现流体输送。
背景技术
今天的环境污染主要包括水源污染、空气污染等,环境污染已严重影响到地球生态圈。究其原因主要是现有技术无法将烟气中的颗粒物等清除干净。
现有的抽油烟机,无法将油烟分离,造成抽油烟机清洗麻烦,造成油烟颗粒污染环境,油烟颗粒物已成为城市空气污染的又一重要污染源。
现有的污水处理设备复杂,造价太高,污水处理费用太高,处理效果一般,只能做到中水排放,污水治理已成为环境治理的重中之重。
现有的制氧设备造价太高,制氧成本太高,无法实现普及应用,致使无法实现纯氧燃烧,致使氮氧化物大量排放形成重要的污染源。
现有的净水器主要采用过滤、净水剂等方法,普遍存在无法达到更高的饮用水标准,净水费用太高等缺陷。
现有的海水淡化设备复杂,造价太高,海水淡化费用太高,能耗太大。现有的海洋化工设备复杂,造价太高,对海洋资源利用效果不理想。
现有的分离设备,主要有离心机等,普遍存在分离效果一般,能耗大等缺陷。
现有的选矿设备选矿效果一般,无法实现更精细分选,造成资源浪费和环境污染。
现有的炼油设备普遍采用高温裂解法,炼油成本高、能耗高,高温对原油内大分子破坏严重,产生大量石油气和石油渣,大大降低出油率,降低高品质油产出。对油品里面的铅、重金属、重元素等无法清除干净,造成燃油污染。
现有的选煤设备只是简单的洗煤,无法将煤充分选干净,致使煤里面的硫燃烧后形成二氧化硫,煤里面的各种金属元素等有价值的东西都没能选出来,都跑到煤灰里了,煤里面的放射性元素也跑到大气和煤灰里了,造成严重的环境污染和资源浪费。
现在的核燃料主要靠离心机精选,存在费用太高,选不干净,造成环境污染和资源浪费。核废料、核污水基本无法处理,造成严重的环境威胁。
现有的垃圾处理技术普遍采用焚烧、填埋等、焚烧后尾气处理不干净,造成严重的大气污染,填埋造成占地和地下水污染。
现有的油气回收设备普遍存在费用高昂,油气回收不彻底等问题。
现有的反应器普遍存在反应速度慢、反应不彻底、造价高、催化剂易老化等缺陷。
现有的锅炉设备、燃烧器设备等普遍存在燃烧不充分,造成严重的能源浪费,燃烧不充分造成严重的环境污染。
现有的窑炉有竖窑、回转窑、焚烧炉、反应炉等,普遍存在燃烧不充分、能耗高、效率低、体积庞大等缺陷。
现有的粉磨设备有粉碎机、雷蒙磨、风扫磨等,普遍存在能耗高、粉磨粉体效率低,超细粉体、纳米粉体制备困难等。
现有的泥浆脱水设备对超细泥浆脱水困难。
现有的分子分解没有很好的方法和设备,一般采用电解法,能耗较高,水分子分解一般采用电解,能耗和成本太高,致使氢能源无法得到更好的应用。CO2基本无法处理,致使温室气体大量排放,有机废气处理有采用光量子等分解的,普遍效果较差,能耗较高。
发明内容
充分利用流体运动,利用运动惯性,利用旋流,使流体受旋流影响,在圆周运动离心力的作用下,利用旋流实现分离,使不同体积、比重的粒子相互之间实现分离。不同体积、比重的粒子向旋流外围的运动速度不一样,流体内比重大的粒子会更早的运动到旋流外围,比重小的粒子会更晚的运动到旋流外围,利用这一点实现不同物质的分选。旋流中的每一个点相互之间都存在相对运动,利用旋流的作用,可以将胶合、溶解在一起的分子分开,使旋流中的每一个分子、原子等各种粒子形成不同运动速度的独立运动个体,利用旋流运动和离心力以及重力等使不同颗粒度、不同比重的物质进入不同区域最终实现分离。可以使溶液中的溶质与溶剂分离,可以将不同的溶质分离。在圆周运动离心力以及运动惯性的作用下可以使烟气中的颗粒物等进入水中,实现烟气净化,向本旋流机内输入碱性液体等时,还可用于烟气脱硫、脱硝、除异味等领域。利用旋流使分子相互碰撞摩擦,可大大促进化学反应,可作为脱硝设备、化学反应器等使用。利用旋流使物料在旋流中相互碰撞摩擦被不断的解离,利用旋流打开粒子团聚,使物料被不断的粉磨成细粉、超细粉或纳米粉。利用旋流燃烧加旋流粉磨使燃料充分燃烧,特别是燃煤时,可使煤块在不断燃烧的同时被不断的剥离粉磨燃烧 充分,同时使燃烧区温度保持稳定均匀,可更精准的控制炉温,可实现低温燃烧,可大大减少氮氧化物产生。利用高速旋流使分子在旋流中被不断的摩擦碰撞分解,利用高速旋流打开分子链实现分子分解,同时利用旋流实现分子分解形成的不同离子的分选,实现水分子分解制氢离子解决能源、CO2分解解决温室气体排放、有机分子分解解决空气污染、金属氧化物分子分解冶金等。
本旋流机可实现更洁净的除尘、净化空气、净化油烟、处理污水、更廉价的海水淡化、更充分的利用水资源、提取海洋资源、更高效率的选矿、处理垃圾、炼油等。
本旋流机可广泛应用于各种分离领域,可实现各种物质成份的分离、分选、提取、提纯。本旋流机可作为除尘器使用,可采用干式除尘或湿式除尘,可实现无尘化排放,可做到与优良大气环境一样的含尘量,并且不含重元素等有害物质,也可做到彻底无尘。可将黑烟清除干净,可高效清除烟气中的异味成份,可将烟气中的二恶英、重元素颗粒物等清除干净,可用于烟气脱硫、脱硝等领域,实现湿式除尘、湿式脱硫一步完成,可大大提高设备运行效率。可作为空气净化设备,可作为新型室内空气净化器使用。可作为除异味设备使用,可清除异味气体。可作为除尘器使用,可超过任何一种除尘器的除尘效果,可彻底淘汰湿电。可作为油气回收设备使用,可回收多种油蒸汽。可作为抽油烟机使用,可将油烟清除干净。可作为新型空气净化器,可去除室内的粉尘、烟尘颗粒。
可作为污水处理设备,可从污水中提取多种有用成份,实现水资源循环利用。可直接提供纯水,可达到饮用水标准,可彻底解决水污染,解决水资源紧缺问题。
可作为净水设备,可将自来水中的有害元素彻底分离出去,可以将重水(重氢水、重氧水)分离出去,可达到更高级的饮用水标准,可以从水中提取重水用于工业领域。
可作为垃圾处理设备,可干选或湿选,将有用成份分离、分选出来,有机成份压制成颗粒有机肥,无用成分填埋,可彻底杜绝环境污染,实现资源循环利用。也可用于垃圾焚烧后的烟气处理,可将烟气彻底处理干净。
可从空气中分离出氧气,也可以将空气中的各种气体分离出来,可以提取多种稀有气体。制氧成本极低,可使锅炉、窑炉、发动机、热机等实现廉价经济的纯氧燃烧,可降低能耗,提高热功效率,彻底杜绝氮氧化物排放。发动机、热机、窑炉、锅炉等也可采用废气再循环,可降低燃烧温度,降低设备材料要求。纯氧燃烧后产生的二氧化碳也可集中收集。
可作为选矿设备,可实现多种矿物、原料的分离提取、提纯,可从贫矿中筛选出多种有用矿物。可用于所有的矿物分选,可边磨边选,可将矿物里面的各种有用成分都选出来,可大大提高选矿的经济效益。用于稀土工业可选出各种元素;用于贵金属选矿可充分提取出 贵重元素。
可作为海水淡化设备、海洋化工设备,可大大降低设备造价,大大降低能耗,提高海水淡化效率。可同步从海水中提取各种有用成份,同时实现各种有用成份的分离提取、分选提纯,可用它作为海洋化工设备,可实现海水淡化无成本。
可作为炼油设备使用,可降低原油内大分子成份破坏,减少石油气和石油渣的产出,提高出油率,提高高品质油品产出。可使油品实现彻底无铅、无放射元素污染,整个生产过程无污染,可实现炼油过程彻底环保,资源彻底收得利用,可大大降低炼油成本。
可作为选煤设备使用,可采用干选或湿选,可将煤里面的硫化物、金属元素、贵重元素、放射性元素、普通矿物质等分选出来资源利用,可制成高纯煤粉或高纯水煤浆,可实现煤炭洁净燃烧。
可作为核废料处理设备使用,处理核废料时,可以将核废料里面的高放射性元素提取出来,达到一定浓度后即可重新投入核反应堆发生核嬗变成为低放物质,可以使尾料成为低放射性物质,即可玻璃固化填埋,可以使核废料没有安全隐患。
可作为反应器使用,可采用旋流使分子相互碰撞摩擦,可大大促进化学反应,可实现催化反应效果,可用于各种化学反应器,也可作为脱硝设备的催化反应设备使用。
可作为燃烧器或锅炉等使用,采用旋流燃烧加旋流破碎使燃料充分燃烧,可使用任意燃料,可使燃烧区温度保持稳定均匀,可精准控制炉温,可实现低温燃烧,可大大减少氮氧化物产生。燃煤时,可使煤块在不断燃烧的同时被不断的剥离破碎燃烧充分。同步加入碳酸钙石屑可实现炉内干法脱硫,可实现燃烧器、锅炉除尘脱硫脱硝一体化。
可作为窑炉等使用,可取代竖窑、回转窑、焚烧炉、反应炉、高炉、马蹄炉等,可使燃烧充分、可快速烧制物料、可节能、高产量、提高生产效率。可烧制水泥、石灰、氧化镁、矿粉、垃圾等,可烧制高活性石灰超细粉。可炼铁、炼铜、生产玻璃、熔块、泡花碱等。
可作为粉磨设备使用,采用旋流粉磨使颗粒物逐渐被磨细,可制出各种粉体,也可磨制面粉等,可制出全麦粉。磨制粉体可干磨或湿磨,用空气作为工作介质即可实现干磨,用水作为工作介质即可实现湿磨,可制出超细粉体、纳米粉体、单原子颗粒物等,可解决纳米材料原料,可磨制炭烯,可解决石墨烯原料。也可用作磨煤喷粉机,可对原煤干磨,可喷出煤粉喷入窑炉等燃烧。
可作为分子分解设备使用,可以将分子分解,可以将H2O、SO2、CO2、NO、HS、碳氢化合物等分子链断开实现分子分解。可分解水分子,可用水或水蒸气制氢离子,可解决能源;可处理SO2、CO2、NO、HS等,可分解SO2制硫离子,可分解CO2解决碳排放, 可利用废气制取S、C等;可处理有机废气,可将有机分子分解掉,可处理有机废气异味等。
本旋流机为实现上述目的,通过以下技术方案实现:
旋流机,包括壳体和传动装置,壳体上设置传动装置,壳体内设置旋流腔,旋流腔横截面为圆形,旋流腔内一端轴心区域设置旋流轮,旋流轮与旋流腔处在同一轴线上,传动装置与旋流轮连接,旋流腔对应旋流轮至少设置一个旋流腔进口,旋流腔另一端设置旋流腔出口,壳体上贯穿从旋流轮到旋流腔出口之间的旋流设置横截面为圆型的定子涡旋整流体,环绕定子涡旋整流体外壁至少设置一道挡圈,旋流腔外围至少设置一个出料口。
旋流轮内设旋流分离室,旋流分离室一端设置旋流分离室出口,旋流分离室另一端设置旋流分离室进口,旋流腔对应旋流分离室进口至少设置一个旋流腔进口,定子涡旋整流体一段穿过旋流分离室出口探入旋流分离室内。
旋流腔内壁上至少设置一道环绕分隔体,旋流腔外围对应环绕分隔体至少设置一个出料口。
旋流轮外围的旋流腔内壁贴近旋流轮外缘。
旋流腔轴线竖置,旋流腔下部设置环绕水。
旋流腔对应旋流轮设置喷淋装置。
靠近旋流腔进口端的旋流腔设置进料装置。
靠近旋流腔进口端的旋流腔设置进料装置和燃烧供应装置。
靠近旋流腔进口端的旋流腔设置燃烧供应装置,旋流腔设置进料装置,旋流腔下部设置熔池,熔池至少设置一个出料口。
靠近旋流腔进口端的旋流腔设置燃烧供应装置,旋流腔内壁上设置采热装置。
本旋流机的优点在于:充分利用了圆周运动和流体运动,充分利用旋流,使流体被逐渐分离,效果随线速度提高同步提高,流体沿轴向螺旋运动,在轴向运动过程中,逐渐被分离,可从工作介质中分离出多种物质。利用旋流使分子相互碰撞摩擦,可产生大量自由基,可大大促进化学反应,可实现催化效果,可作为催化反应设备使用。利用旋流粉磨使颗粒物逐渐被磨细。利用旋流燃烧加旋流粉磨使燃料充分燃烧,同时使燃烧区温度保持稳定均匀,可更精准的控制炉温,可实现低温燃烧,可大大减少氮氧化物产生。利用旋流燃烧和旋流粉磨可烧制多种物料,并且同步将物料粉磨成细粉或超细粉。利用高速旋流使分子在旋流中被不断的摩擦碰撞分解,利用高速旋流打开分子链实现分子分解,同时利用旋流实现分子分解形成的不同离子的分选,实现水分子分解制氢离子解决能源、解决温室气体排放、金属氧化物分子分解冶金、有机分子分解解决空气污染等。本旋流机具有制造简单、设备可大可小、 应用领域广泛、制造成本低、使用成本低、使用寿命长等优点。
附图说明
附图1是本旋流机的主体结构示意图;
附图2是本旋流机实施例之一的主视结构示意图;
附图3是本旋流机实施例之二的主视结构示意图;
附图4是本旋流机实施例之三的主视结构示意图;
附图5是本旋流机实施例之四的主视结构示意图;
附图6是本旋流机实施例之五的主视结构示意图;
附图7是本旋流机实施例之六的主视结构示意图;
附图8是本旋流机实施例之七的主视结构示意图;
附图9是本旋流机实施例之八的主视结构示意图;
附图10是本旋流机实施例之九的主视结构示意图。
具体实施方式
本旋流机主体结构包括旋流机,包括壳体1和传动装置2,壳体上设置传动装置2,壳体1内设置旋流3,旋流3横截面为圆形,旋流腔3内一端轴心区域设置旋流轮4,旋流轮4与旋流腔3处在同一轴线上,传动装置2与旋流轮4连接,旋流腔对应旋流轮4至少设置一个旋流腔进口5,旋流腔3另一端设置旋流腔出口6,壳体1上贯穿从旋流轮4到旋流腔出口6之间的旋流腔3设置横截面为圆型的定子涡旋整流体7,环绕定子涡旋整流体7外周至少设置一道挡圈9,旋流腔3外围至少设置一个出料口8。
壳体1的范围包括机座、支架、管道、机壳以及动力装置等,每一个部位都可统称做壳体。壳体1也可以和动力装置制成一体,形成一个整体的壳体。本旋流机可以根据需要选用不同的材料制造,可使用金属、合金、陶瓷、玻璃、塑料、尼龙、泡沫材料等材料制造。
传动装置2包括传动轴、传动轴密封装置、轴承或轴瓦、轴座等,传动装置2设置传动轴,利用传动轴实现动力输入,带动旋流机工作。传动装置2连接动力装置实现动力输入,带动旋流机工作。动力装置可以使用电机或发动机等,动力装置可直接连接传动装置2,也可以通过联轴器传动、皮带传动、链条传动、齿轮传动等实现动力输入,也可以通过皮带轮、减速机等实现变速或改变传动轴轴向,大型立式磨机可利用减速机作为传动装置。动力装置与壳体1也可直接制成一体,也可直接利用动力装置作为传动装置2。传动装置2即可以设置在一端形成悬臂结构,也可以使传动装置2的转轴另一端连接旋转稳定装置,旋转稳定装置可设置支架、轴座、轴承、轴瓦或密封装置等。传动轴密封装置可根据具体工况采用 填料密封、油缸密封、迷宫密封等多种结构。
壳体1上设置传动装置2。传动装置2可采用风机或水泵传动装置的设置方案。
壳体1内设置旋流腔3。旋流腔3可做成一体或开体结构,安装时合在一起即可,旋流腔3也可根据需要任意开体,可方便装配。旋流腔3内壁也可根据需要设耐磨材料层、耐腐蚀层或催化剂材料层等,易磨损区域也可在表面贴耐磨片或砌耐磨砖。用于窑炉烟气脱硫脱硝、化工异味处理等时,旋流腔3内壁上可以根据具体工况条件设置防腐或防腐耐磨层、催化剂层等。本旋流机用于锅炉、燃烧器等时可在旋流腔3内壁上设置耐火保温层。也可在旋流腔3内壁上设置电加热装置,可使旋流机成为一个电加热窑炉,可烧制多种物料。
旋流腔3横截面为圆形。旋流腔3内腔横截面设置成圆形,可在旋流腔3内更好的形成旋流,旋流腔3通常可设置成圆柱形结构,可简化结构,旋流腔3也可设置成多段内径不相等的圆柱形结构。旋流腔3也可设置成圆台形结构或多段圆台形结构,可根据不同的需要具体设置。旋流腔3内径向旋流腔出口端逐渐扩张,可使流体轴向运动顺畅。旋流腔3内径向旋流腔出口端逐渐缩小,可使比重较重的物质向旋流腔进口5端运动,可提高分离效果。
旋流腔3内一端轴心区域设置旋流轮4,旋流轮4与旋流腔3处在同一轴线上。旋流轮4可根据具体工况条件采用任意结构的离心叶轮、轴流叶轮、混流叶轮或轴流离心组合叶轮、转辊等,可采用所有的各种结构的叶轮。也可以在旋流轮4上设置任意的辅助装置,比如磨锤、圆辊、叶片等,通常可以在旋流轮4侧面上设置与旋流轮4直径相等的圆辊装置,圆辊装置可采用圆筒结构,圆辊装置可更好的带动流体旋转,可提高粉磨、反应、混合等效果。圆辊装置外围也可设置叶片或磨锤等,可提高粉磨或雾化等的效果。旋流轮4表面也可根据需要设置耐磨层、衬胶或防腐等。旋流轮4设置在旋流腔3内一端区域的中轴线上即可,旋流轮4输送流体的同时带动流体在旋流腔3内旋转流动形成旋流。旋流轮4外缘与旋流腔3内壁之间的距离可以根据需要任意设定,距离越近,流体振荡磨擦越剧烈;也可根据需要将旋流腔3内壁贴近旋流轮4外缘,可使旋流摩擦更剧烈,作为反应器使用时,可提高反应效果,作为粉磨设备使用时,可提高粉磨强度,可磨制出更细的粉体。
传动装置2与旋流轮4连接。传动装置2的传动轴要连接固定在旋流轮4轴心区域,保证旋流轮4旋转平稳。用于空气净化、抽油烟机等时也可以将传动装置2的电机与旋流轮4制成一体,可节省空间降低造价。也可以将传动装置2的传动轴穿过旋流轮4,传动轴两端均设置旋转稳定装置。传动轴也可采用空心轴,也可与旋流轮4焊接为一体。旋流轮4旋转时带动流体在旋流腔3内旋转流动,形成向旋流腔出口端螺旋推进旋流。
旋流腔3对应旋流轮4至少设置一个旋流腔进口5。可在旋流腔3一端或侧壁对应旋 流轮4设置一个或多个旋流腔进口5,可参照风机或水泵壳体进口的设置方案,旋流腔进口5可设置在旋流腔3轴心区域,可实现流体轴向输入。也可以在旋流腔进口5上设置导流腔,在导流腔侧壁开设进口可使流体改成径向输入。也可在旋流腔3侧壁设置旋流腔进口5利用进料装置向旋流腔3内送入物料,设置多个旋流腔进口5时可分别利用旋流腔进口5向旋流腔3内送入不同的物料。也可在旋流腔进口5设置风门或阀门等流量调节装置,可调节流量,可调节分离反应效果。
旋流腔3另一端设置旋流腔出口6。可以在旋流腔3另一端任意设置一个或多个旋流腔出口6,可在旋流腔3另一端轴心区域或侧壁设置旋流腔出口6,可实现流体轴向输出或径向输出。旋流腔出口6设置在旋流腔3轴心区域设置成圆形可提高分离效果,也可在旋流腔出口6外设置导流腔,在导流腔侧壁设出口可使流体改成切向或径向输出,导流腔也可做成涡壳型,可使物料更顺畅的排出。旋流腔出口6内径小于旋流腔3最大内径时,可使旋流腔3内形成的旋流分离出的比重较大的物质留在旋流腔3内。旋流腔出口6内径大于旋流轮4最大直径时可以减少流体阻力,旋流腔出口6内径小于旋流轮4最大直径时可以增加流体阻力,会提高分离效果。旋流腔出口6内径等于或大于旋流腔3最大内径时,可使流体更顺畅的从旋流腔出口6流出。可根据需要具体设定旋流腔出口6与旋流腔3最大内径的比例。在旋流腔出口6处的旋流腔3内设置一圈圆筒挡体或拔埽筒体可提高分离效果,在圆筒挡体上设置一圈向旋流腔出口6开口扩张的拔埽筒体可进一步提高分离效果。旋流轮4旋转带动工作介质旋转形成旋流,旋转产生的离心力使旋流中的众多粒子向旋流外围运动,最终碰到旋流腔3内壁,旋流腔3做成内径向旋流腔出口6端逐渐缩小的结构可使旋流腔3内壁与轴线成倾斜角度,可使碰到旋流腔3内壁的粒子向旋流腔进口5侧反弹,可使比重大的分离物向旋流腔进口5端运动,可提高分离效果。也可在旋流腔出口6上设置流量调节装置,可采用各种阀门、风门等,可调节流体流量,可调整旋流腔3内压力,可调节功能效果。
壳体1上贯穿从旋流轮4到旋流腔出口6之间的旋流腔3设置横截面为圆型的定子涡旋整流体7。在壳体1上设置贯穿从旋流轮4到旋流腔出口6之间的旋流腔3的横截面为圆型的定子涡旋整流体7,定子涡旋整流体7可作为壳体1的一部分,定子涡旋整流体7外周做成圆形,定子涡旋整流体7外形可作成圆柱形或圆台形,定子涡旋整流体7内可作成空腔,可利用空腔作为管道,涡旋整流体7内可以设置管道,管道连通旋流腔进口5,可以使流体通过管道进入旋流腔进口5,可利用涡旋整流体7实现流体输入,可简化结构,可利用现有的离心风机、离心水泵做成旋流机。涡旋整流体7做成空心结构时,也可将传动装置2安装在涡旋整流体7内,旋流轮4可采用任意结构的离心叶轮,可使流体通过旋流腔3一端 进入,从旋流腔3另一端输出,可用于抽油烟机净化油烟,空气净化等领域,可简化结构。定子涡旋整流体7处在从旋流轮4到旋流腔出口6之间的旋流腔3内,定子涡旋整流体7与旋流腔3处在同一条轴线上可更好的形成旋流,定子涡旋整流体7固定不动,定子涡旋整流体7外周壁对流体有附面层效应,使比重较小的物质在圆周运动离心力作用下更加贴近定子涡旋整流体7外周壁,使比重较大的物质在圆周运动离心力作用下更加远离定子涡旋整流体7外周壁。定子涡旋整流体7使流体在定子涡旋整流体7外围的旋流腔3内更好的形成一个从中心到外围转速递增的旋流,可更好地提高分离效果。定子涡旋整流体7可根据需要设置成圆柱形、圆台形或喇叭形,通常设置成圆柱形即可,定子涡旋整流体7外径可以任意设定,通常等于或小于或略大于旋流轮4直径即可。旋流腔3轴线横置安装使用时,可在定子涡旋整流体7靠近旋流轮4端设置多个支撑体,支撑体做成与旋流腔3横截面平行或呈倾斜角度,可减少阻力,可促进流体旋转。也可在旋流腔3内设置一层或多层与旋流腔3横截面呈倾斜角度的多个放射状排列的导叶,可用导叶作为定子涡旋整流体7的支撑装置,导叶可采用近似轴流叶轮叶片结构,多个放射状排列的导叶形成近似轴流叶轮状结构,可促进旋流腔3内旋流旋转,可延长旋流腔3轴向长度提高分离效果。旋流轮4旋转输送带动工作介质在定子涡旋整流体7外围的旋流腔3内向旋流腔出口6端旋转流动,旋流轮4旋转带动工作介质旋转形成旋流,工作介质为气体或液体等流体,本旋流机用于不同的应用领域时工作介质不同,旋流轮4旋转时,旋流轮4输送工作介质的同时带动工作介质在定子涡旋整流体7外围的旋流腔3内旋转流动,形成向旋流腔出口6端旋转流动推进的旋流。旋流轮4转速越高,旋流转速越高,分离、粉磨、反应等效果越好。
环绕定子涡旋整流体7外壁至少设置一道挡圈9。可环绕定子涡旋整流体7外壁设置一道或多道挡圈9,受定子涡旋整流体7外壁附面层影响,贴近涡旋整流体7外壁区域的流体转速较低,导致分离效果降低,挡圈9可阻挡流体沿贴近涡旋整流体7外壁区域轴向流动,可大幅提高分离效果,适当加大挡圈9径向宽度,可提高分离效果。湿式除尘时也可阻挡定子涡旋整流体7外壁吸附的含有污染物的水液轴向流动,使该水液沿挡圈9向外围运动,使该水液脱离涡旋整流体7外壁,可避免该水液流出旋流腔出口6外,可提高烟气净化效果。
旋流腔3外围至少设置一个出料口8。可以根据需要在旋流腔3外围的外周或底部设置一个或多个出料口8,可以分离出比重较大的分离物,使用时也可以调整好出料口8的流量,可更好地排出分离物。旋流腔3中轴线竖置安装时也可在圆周上设置多个出料口8,可更好的排出分离物。也可将出料口8轴向长度加大,最大可以在旋流腔3内壁上设置轴向贯穿的出料口8,可更好的排出粉尘等固体分离物;也可在旋流腔3内壁上轴向上设置多个出 料口8,可分选出多种比重不同的分离物。多段旋流腔3内径向旋流腔出口6端逐渐缩小的结构可以将旋流腔3轴向分割成多个区域,可以在各段旋流腔3外围设置出料口8,可以从各个出料口8分离出多种分离物。也可以在出料口8设置阀门、风门、螺杆输送器等活动密封卸料装置,可调节流量,可调节分离效果,可使分离物在旋流腔3内压力、重力、离心力作用下从旋流腔3内卸出,也可间歇打开出料口8将分离物卸出。也可在出料口8设储料仓或集灰箱,可从出料口8间歇或持续出料或排灰。也可从出料口8选出比重较大的分离物,作为磨煤设备使用时,也可在旋流腔3外围的下部底部或侧壁上设置出料口8,可从出料口8清理不易粉磨的物料,也可在出料口8上设置搅笼或卸料器等实现自动卸灰,可减少设备磨损,用于磨煤机、磨煤喷粉机等时可减少粉磨灰渣造成的额外能耗,可制出高纯煤粉,可减少硫化物、灰分等进入炉膛,可更好地除尘、脱硫。作为选矿设备使用时可实现边磨边选,可将比重较大的和较难磨的矿物从旋流腔3外围的下部或底部通过出料口8排出,将比重较轻较易粉磨的矿物从旋流腔出口6吹出。作为生活垃圾粉磨设备使用时,可在旋流腔3外围的下部底部或侧壁上设置出料口8,可将垃圾内的比重较大的物质从出料口8排出,将比重较小的物质从旋流腔出口6吹出,可直接吹入焚烧炉,剔除不宜燃烧的比重较大的不可燃物之后可更好地进行垃圾焚烧。粉磨物料时,旋流腔3中轴线竖置安装时,也可在旋流腔3上部设置出料口8,可将粉磨后的较细物料收集出来,将旋流腔3上部内径加大可更好的分离出物料。旋流轮4下侧面设置多个叶片,可以从下部旋流腔进口5进气或进水,从上部旋流腔进口5自然进料或侧壁旋流腔进口5用搅笼进料,使用时调节进风量或进水量即可调节粉体细度。可从上部出料口8分离出粉磨好的物料,可将旋流腔出口6吹出的风连接管道重新吸入下部旋流腔进口5实现闭路循环,风温高时在管道上设冷却装置对循环风冷却即可。可从下部出料口8分离出比重较大的或不易粉磨的物料,选矿时可实现边磨边选。
本旋流机工作时,旋流轮4旋转,使旋流腔3内形成旋流。本主体结构的旋流腔3中轴线可根据需要横置、竖置或斜置安装。本主体结构具有粉磨、分离、反应等功能,可同时将流体输送出去,可作为分离设备、粉磨设备、燃烧器、窑炉、反应器等使用。用于分离液体介质时,旋流腔3中轴线可竖置安装,可更好地将分离出的气体排出,避免影响分离效果,旋流腔3中轴线横置或斜置安装时,可在旋流腔3上部设置排气阀,可定时停机排气即可。用于粉磨设备、燃烧器、窑炉等时,旋流腔3中轴线也可竖置安装,可使大颗粒物继续在旋流轮4外围粉磨,可提高效率。
作为分离设备使用时,可用于多种需要分离的领域,可将比重不同的物质分离开。可作为除尘器、吸尘器、制氧设备、血浆分离机、奶油分离机、除异味设备、空气净化器、 污水处理器、净水处理设备、海水淡化设备、选矿设备、垃圾分选设备、选煤设备等使用,可同时将流体输送出去。作为除尘、吸尘设备使用时,可将气体从旋流腔进口5吸入旋流机,可从旋流腔出口6排出无尘气体,从出料口8排出灰尘,在出料口8设置活动密封卸料装置,间歇打开或固定流量排出灰尘即可。含尘量较大时,可在旋流机前面加粗除尘设备,可减少灰尘对旋流轮的磨损和粘挂。除尘或分离固体颗粒物时也可在出料口8设置出气管,出气管连通储灰仓,可设置回气管,回气管连通旋流腔进口5或靠近旋流腔进口5端的旋流腔3,可实现粉尘气流输送。可处理高温烟气,实现干式除尘。旋流轮4外围的旋流腔3内径向旋流腔出口6端逐渐扩张可促进流体轴向运动,可更好的避免粉尘等粘挂。作为吸尘器使用时,可在旋流腔进口5设置滤网将大块物体隔离,灰尘清理方便,造价便宜,没有微尘污染,更加环保。作为抽油烟机使用时,可将烟气从旋流腔进口5吸入本旋流机,可将油烟分离,使烟气排放彻底环保,处理后的无烟气体从旋流腔出口6排出,废油从出料口8排出。作为空气净化设备使用时,可作为室内空气净化器使用,可从旋流腔出口6分离出洁净空气,从出料口8分离出粉尘颗粒物等。也可作为新风系统的主机,可将分离后的洁净空气送入室内,将脏空气留在室外。作为制氧设备使用时,可将空气吸入旋流机,可从旋流腔出口6分离出氮气等,从出料口8分离出氧气,制氧成本极低,可使锅炉、窑炉、发动机等实现纯氧燃烧,可降低能耗,提高热效率,杜绝氮氧化物排放,也可采用废气再循环,可降低燃烧温度,降低设备材料要求。作为除异味设备使用时,可从旋流腔出口6分离出较轻的气体,从出料口8分离出较重的气体等,可针对不同的异味气体采用焚烧、收集或化学反应等方法处理即可。作为油气回收设备使用时,可回收多种油蒸汽,可从旋流腔出口6分离出洁净空气,从出料口8分离出油气,分离出的油气可采用冷凝、喷淋、溶剂吸收等措施回收,回收后的残余气体可重新送入旋流腔进口5再次参与分离,形成闭式循环,最终实现完全回收。作为海水淡化设备使用时,可从旋流腔出口6分离出淡水,从出料口8分离出高浓度盐水,通过蒸发析出即可获得盐。
作为选矿设备使用时,可将矿物送进本旋流机进行边磨边选,可湿选或干选,湿磨湿选效果更好,水可循环利用,可以将比重较大的金属元素、重元素从出料口8分离出来,空气或水以及比重较轻的物质从旋流腔出口6分离出来。
作为选煤设备使用时,可将煤炭制成煤粉,可采用干选或湿选,可将煤里面的硫化物、金属元素、贵重元素、放射性元素、普通矿物质等从出料口8分选出来资源利用,可将空气或水以及高纯煤粉从旋流腔出口6分离出来,可制出高纯煤粉、煤球或高纯水煤浆。
作为粉磨设备使用时,可干磨也可湿磨,湿磨磨制粉体更细。传动轴竖置时效果较 好,可利用重力使大颗粒物料始终处在旋流轮4外围区域的旋流腔3内粉磨,使粉磨好的粉体颗粒随流体离开粉磨区,从旋流腔出口6流出,可使物料在旋流腔3内实现旋流粉磨,使颗粒物在旋流内相互碰撞摩擦,直至磨细。可磨制多种粉体等,磨制粉体可干磨或湿磨,用空气作为载体即可实现干磨,用水作为载体即可实现湿磨。设置多个旋流腔进口5时可分别进需要磨制的原料和空气或水,也可设置自动加料装置,可更方便加料,可将物料粉碎后直接分选,较粗的粉体在旋流腔3内继续粉磨,较细的粉体随着空气或水通过旋流腔出口6输出后将粉体用回收设备回收即可,回收粉体后的空气或水也可重新吸入旋流腔进口5,可实现闭路循环,可更加环保,空气温度高时可设置空气冷却降温装置即可。可调节旋流腔3内流体流量,可调节粉体的粉磨细度,流体流量越小,粉体的粉磨细度越细。调节旋流腔进口5的过流面积可调节粉磨细度以及旋流腔3内压力。磨制超细粉体或纳米粉体时旋流轮4也可以采用圆辊,将旋流腔进口5对应圆辊轴心区域设置即可,可利用圆辊表面带动流体运动,流量更小,可更好的磨细粉体。加高旋流腔3的轴向高度可更好的选粉,更有利于粉体细度均匀。湿磨时本旋流机可彻底解决粉磨过程中普遍存在的粒子团聚,可实现高效粉磨,可磨出超细粉体、纳米粉体、单原子颗粒物,可磨制纳米材料原料,可磨制炭烯,可磨制石墨烯原料。也可用作磨煤喷粉机,可对原煤干磨,可直接喷入窑炉锅炉等燃烧。
作为反应设备使用时,可利用旋流使分子相互碰撞摩擦,可促进化学反应,可实现催化反应效果,可广泛用于化工领域。也可在旋流腔3内壁上采用喷涂、涂抹、贴片、砌块等方法设置催化剂层,可进一步提高化学催化反应效果,可根据具体工况选用对应的催化剂,旋流腔3内的旋流可以使粒子都能够与催化剂层接触到,可大大提高化学催化反应效果,同时可避免催化剂层表面粘附污染物,可提高催化剂层使用寿命。用于烟气脱硝时,可根据具体工况条件设置脱硝催化剂层,可实现SCR脱硝。作为脱硝设备使用,也可采用氢气、不饱和烃等作为脱硝剂,也可利用烟气中的碳氢化合物、氢气作为脱硝剂。
作为燃烧器设备使用时,传动轴横置、竖置均可,采用大颗粒燃料时,传动轴竖置效果较好,可利用重力使大颗粒燃料更好的在旋流轮4外围区域的旋流腔3内粉磨。可直接向锅炉、窑炉等提供热气,可减少锅炉改造费用,可采用任意燃料,可在旋流腔3内壁上设置耐火保温层。可利用旋流实现燃料分选,可使颗粒较大的燃料始终处在旋流轮4所处区域附近燃烧,使燃尽的灰分随气流离开旋流轮4所处区域,可使燃料在旋流腔3内实现均匀的旋流燃烧,可利用旋流燃烧加旋流破碎使燃料充分燃烧,特别是燃煤或垃圾等时,可使煤块或垃圾等在不断燃烧的同时被不断的粉磨燃烧充分。精准供给燃料,调整好风量,可使燃烧区温度保持稳定均匀,可精准控制炉温,可实现低温燃烧,可减少氮氧化物产生。同步加入 碳酸钙石屑可实现炉内干法脱硫。也可在旋流腔进口5上设置搅笼等自动供料装置,可设置多个旋流腔进口5分别供料,可通过自动供料装置向旋流腔进口5内均匀送入燃煤、生物质燃料或垃圾等以及干法脱硫剂等。可在旋流腔3内壁上设置测温装置,测温装置可采用热电偶、温控仪表等装置,测温装置可自动控制自动供料装置,炉内温度达到设定温度上限时,自动断开自动供料装置电源,当炉内温度达到设定温度下限时,自动接通自动供料装置电源即可。向旋流腔3内送入物料即可使本旋流机成为一个新型窑炉或焚烧炉,可烧制水泥、石灰、氧化镁、矿料、垃圾等,传动轴竖置使用时,可同步粉磨物料,可烧制超高活性超细石灰粉或矿粉等。加入矿粉、还原剂或反应剂等可作为反应炉使用,可炼铁、炼铜等,也可生产泡花碱、玻璃、熔块等,传动轴竖置使用时将矿粉与还原剂等在旋流腔3中段加入,矿粉与还原剂溶化后沿旋流腔3内壁流下,在旋流腔3下部外围区域设置一个熔池使渣水分离,在熔池上部设置出料口出渣,在熔池下部设置出料口出铁水或铜水等即可;传动轴横置使用时将矿粉与还原剂等在旋流腔3靠近旋流腔进口5段加入,在旋流腔3中部区域设置一个熔池使渣水分离,在熔池上部设置出料口出渣,在熔池下部设置出料口出铁水或铜水等即可。旋流轮4可利用进入的空气降温,使用耐高温不锈钢材料即可,旋流腔3采用耐火材料即可。
本旋流机实施例之一的结构是:在以上结构基础上,旋流轮4内设旋流分离室10,旋流分离室10一端设置旋流分离室出口11,旋流分离室10另一端设置旋流分离室进口12,旋流腔3对应旋流分离室进口12至少设置一个旋流腔进口5,定子涡旋整流7一段穿过旋流分离室出口11探入旋流分离室10内。旋流分离轮4内设旋流分离室10。可在旋流轮4内设旋流分离室10,可将旋流轮4内设置成空腔,利用空腔形成旋流分离室10。旋流分离室10可以设置成横截面呈圆形的空腔,可更好地保持旋流轮4的动平衡,使旋流分离室10内形成一个从中心到外围转速递增的环筒形旋流。通常旋流分离室10外围内壁设置成光面或毛面均可,设置成光面可更好地利用附面层效应,可提高分离效果。也可在旋流分离室10内的旋流分离轮4轴心区域设置增压装置,增压装置可做成增压叶片、轴流叶轮、离心叶轮或混流叶轮结构,即可提高旋流分离轮4结构强度,也可提高流体流量和压力。
旋流分离室10一端设置旋流分离室出口11。可在旋流分离室10一端设置旋流分离室出口11,旋流分离室出口11中心设置在旋流分离室10中心轴线上即可,旋流分离室出口11直径与旋流分离室10最大直径相等即可。可将旋流分离室10内腔设置成向旋流分离室出口11端逐渐扩张的结构,可更好地避免颗粒物在旋流分离室10内壁上沉积,可使分离物沿旋流分离室10内壁前进,可大大提高分离效果。旋流分离室10内腔的扩张角度可任意选择,只要保证分离物不在旋流分离室10内壁上沉积即可,旋流分离室10内腔的扩张角度 越小,越可提高分离效率。也可将旋流分离室10内腔设置成圆柱形结构,缺点是易造成分离物在旋流分离室10内壁上沉积。旋流分离室10另一端设置旋流分离室进口12。可在旋流分离室10另一端设置旋流分离室进口12,旋流分离室进口12即可设置在旋流分离室10内也可设置在旋流分离轮4上,旋流分离室进口12设置在旋流分离室10内时,可利用导流管将流体送入旋流分离室10内。旋流分离室进口12设置在旋流分离轮4上时,可将旋流分离室进口12设置在旋流分离轮4连接传动装置2的一端上,旋流分离室进口12内可设置多个支撑体,支撑体与传动装置2连接即可,可使工作介质从旋流分离室进口12端流入旋流分离室10,可实现工作介质轴流进入,也可实现多种功能,比如用于粉磨、选矿时可实现物料更好的分离。旋流腔3对应旋流分离室进口12至少设置一个旋流腔进口5。可在旋流腔3一端对应旋流分离室进口12设置一个或多个旋流腔进口5。定子涡旋整流体7一段穿过旋流分离室出口11探入旋流分离室10内,可使流体直接送入旋流分离室10内部,使流体在旋转离心力的作用下沿旋流分离室10内壁旋转前进,最终从旋流分离室出口11甩出。通常定子涡旋整流体7外壁与旋流分离室10内壁平行即可,可更好地提高旋流运动效果。定子涡旋整流体7外壁与旋流分离室10内壁之间的距离向旋流分离室出口11端逐渐缩小时,可提高流量,定子涡旋整流体7外壁与旋流分离室10内壁之间的距离向旋流分离室出口11端逐渐缩增大时,可降低流量,两者都会降低旋流运动效果。定子涡旋整流体7外壁静止,旋流分离室10内壁旋转,两者之间存在相对运动,对存在于两者之间的流体相对摩擦,定子涡旋整流体7外壁与旋流分离室10内壁之间的间隙越小,相对运动越剧烈,对存在于两者之间的流体相对摩擦越剧烈,旋流运动越剧烈,定子涡旋整流体7外壁顺应旋流分离室10内壁设置可更好地提高分离效果。定子涡旋整流体7外壁设置成光面或毛面均可,设置成光面可更好地利用附面层效应,可提高分离效果。静止的定子涡旋整流体7外壁的附面层效应可吸附比重较轻的分离物,旋转的旋流分离室10内壁产生的离心力可吸引比重较重的分离物,从中心到外围转速递增的旋流使不同比重的分离物分别运动到旋流的中心和旋流的外围,最终实现不同比重的分离物的分离。如果没有定子涡旋整流体7的存在,则不同比重的分离物在离心力的作用下都向旋流分离室10内壁运动,最终难以实现分离,缺少定子涡旋整流体7表面的摩擦作用,导致从中心到外围转速递增的旋流中心与外围转速相差不多,使分离效果大大降低,这也就是现有的离心机技术分离效果差的根本原因,定子涡旋整流体7外壁是提高旋流分离效果的关键部件。
本实施例对流体旋转大幅加速,将粒子之间的引力打开,可大幅提高分离效果。
本旋流机实施例之二的结构是:在以上结构基础上,旋流腔3内壁上至少设置一道 环绕分隔体13,旋流腔3外围对应环绕分隔体13至少设置一个出料口8。环绕分隔体13可采用法兰牌或拔埽筒体,可在旋流腔3内壁上与旋流腔3横截面平行设置一道或多道法兰牌将旋流腔3分割成多段,将旋流腔3轴向隔离成多个区域,法兰可以阻挡流体沿旋流腔3外围轴向流动,可实现分离效果。也可在法兰内口上靠近旋流腔进口5侧均设置环绕挡圈,环绕挡圈可作成圆筒形或拔埽型,环绕挡圈作成圆筒形效果较好,环绕挡圈可起到支撑作用,可使法兰平整,又可阻挡分离物向旋流腔出口6端流动,可提高分离效果。也可以在直筒状旋流腔3内设置一道或多道拔埽筒体,将拔埽筒体较粗的一端与旋流腔3内壁连接在一起即可,可简化结构,拔埽筒体较细的一端朝向旋流腔进口5端或旋流腔出口6端均可,拔埽筒体较细的一端朝向旋流腔进口5端时可更好地阻挡分离物向旋流腔出口6端流动,可提高分离效果。分离物因比重、颗粒大小等不同,在轴向运动过程中,向旋流腔3外周的运动速度不同,不同的分离物分别运动到轴向不同的区域。旋流腔3外周对应环绕分隔体13设置出料口8,可以根据需要在旋流腔3外围对应环绕分隔体13设置一个或多个出料口8,可以从各个出料口8分离出多种分离物,出料口8设置在环绕分隔体13靠近旋流腔进口5侧时,可将比重较大的分离物排出,出料口8设置在环绕分隔体13靠近旋流腔出口6侧时,可阻挡比重较大的分离物,可将比重较小的分离物排出。使用时也可调整各个出料口8流量,可更好地分离出各种分离物。
本实施例作为污水、废气处理设备使用时,可从污水、废气中提取分选各种有用成份,可同步完成除尘、脱硫、脱硝;尾气除尘时也可从粉尘中选出多种有用成份,作为除尘设备、吸尘设备使用时,可将气体从旋流腔进口5吸入本旋流机,可从旋流腔出口6排出无尘气体,从各个出料口8排出灰尘,可从各个出料口8分离出多种成份的粉尘颗粒物、多种不同成份的气体,除尘与气体分离也可同步完成。
作为空气分离设备、制氧设备、制氮设备、稀有气体制取设备使用时,可将空气吸入本旋流机,可从各个出料口8分别分离出氧气、氮气、惰性气体等多种气体,直接将各种气体收集利用即可。特殊需要时,将各种气体二次分离即可获得高纯气体。
作为选矿或选煤等设备使用时,可将矿物等送进本旋流机进行边磨边选,可湿选或干选,湿磨湿选效果更好,水可循环利用,可将比重较大的金属元素、重元素分别从出料口8分离出来,空气或水以及比重较轻的物质从旋流腔出口6分离出来,可将有用矿物从各出料口8分别分离出来。
处理污水、水质净化时,可先对污水进行生化学处理,再对中水用本旋流机处理,重元素、金属元素、沙尘、高浓盐水或盐水混合物等从轴向各个不同的出料口8排出,使达 标净水从旋流腔出口6分离出来,设置母子旋流机,用各个子旋流机对排出的高浓盐水等进行二次处理、多级处理可进一步分离多种盐分等。可将中水中的盐分、重金属等处理掉。作为净水处理设备使用时,参照海水淡化,可将水中的重元素分离掉,保留有益元素,将水中的有机成份、氯气、微生物、虫卵等与部分水从旋流腔出口6分离出来排放掉,将达标净水从靠近旋流腔出口6的出料口8排出。本旋流机也可提取重水用于工业领域。
作为炼油设备使用时,可将原油直接吸入本旋流机,原油受到旋流流体运动影响和旋流产生的离心力以及重力等共同影响,实现各种成份分离。可使含重元素、金属、硫、沥青、石蜡、重油、润滑油、柴油、煤油、汽油等依次从靠近旋流腔进口5的各个出料口8排出。可将两种油份的中间体重新输入原油中再次分离,也可设置母子旋流机,用各个子旋流机对排出的各种成份进行二次分离、多级分离,可实现各种成份的超高纯净度,可提炼出高纯度汽油、柴油、润滑油、多种石油产品、硫、重金属、铅、放射性元素等,可使油品彻底无铅、无放射元素污染。整个生产过程无污染,没有废水、废气排放,炼油过程彻底环保,资源充分收得利用,可大大降低炼油成本。低温裂解减少了高温对原油大分子结构的破坏,减少石油气、石油渣、沥青、蜡质等的产生,可提高出油率。
作为粉磨设备使用时,可分选出多种粒径的粉体,越靠近旋流腔出口6的出料口8选出的粉体越细。也可对原煤干磨、干选,可从各个出料口8中选出煤中各种矿物,从旋流腔出口6喷出煤粉,可直接喷入窑炉锅炉等燃烧。
作为核燃料精选设备或核废料处理设备使用时,可分别从各个出料口8分选出比重较小的和比重较大的有用元素,可采用多级分选,逐步提纯即可,可以大大提高精选效果,可以使尾渣更加环保。处理核废料时,可以将核废料里面的高放射性元素提取出来重新投入核反应堆发生核嬗变成为低放元素,可以将低放物质玻璃固化填埋。
本旋流机实施例之三的结构是:在以上结构基础上,旋流轮4外围的旋流腔3内壁贴近旋流轮4外缘。旋流轮4可采用任意结构的旋流轮,可尽量加大旋流轮4轴向厚度,可提高效果。可在旋流轮4靠近旋流腔出口6侧设置圆筒或圆辊,可使旋流轮4外周与旋流腔3内壁相互贴近,可更好的形成旋流摩擦。采用轴流叶轮时可缩短旋流轮叶片长度,也可在圆辊上一段或整段设置与横截面呈倾斜角度的凹槽,可代替旋流轮叶片,可提高旋流轮外周表面积;采用离心叶轮时,在旋流轮4靠近旋流腔出口6侧设置圆筒或圆辊即可,也可采用开式离心叶轮,在旋流轮4侧面设置多个叶片即可,可简化结构。旋流轮4外围的旋流腔3内壁贴近旋流轮4外缘,可使旋流摩擦更剧烈,作为反应器使用时,可提高反应效果;作为粉磨设备使用时,可提高粉磨效果,可磨制出更细的粉体;作为选矿设备使用时可更好地实 现矿物粉磨解离,可提高选矿效果。作为湿式烟气净化设备使用时,可在旋流轮4外围形成对烟气的超雾化清洗,可提高烟气净化效果。
本实施例传动轴横置或竖置安装均可,当旋流轮4转速达到一定高度时,旋流轮4外围的旋流腔3内壁紧贴旋流轮4外缘时,旋流摩擦更剧烈,可以将分子分解,可以将H2O、SO2、CO2、NO、HS、O2、碳氢化合物等分子链断开实现分子分解。可分解水分子,可用水或水蒸气制氢离子,可从旋流腔出口6分离出氢离子,从出料口8分离出氧离子,氢离子可与自然界中的氧反应燃烧,可彻底解决能源,氢离子具有更高的活性,可作为高活性还原剂,可不用催化剂常温脱硝、常温还原铁制铁粉等。氧离子可与自然界中的很多物质反应生成多种全新的化合物。可处理SO2、CO2、NO、HS等,可分解SO2制硫离子,可分解CO2解决碳排放,可利用废气制取S、C等离子,可从出料口8分离出S、C等离子,可用它们制造很多全新的化合物;可处理有机废气,可将有机分子分解掉,可用于处理废气异味等。可用它将氧气分解成氧离子,可用该氧离子作为氧化剂。该氧离子可形成O3、O4、O5、O6、O7、O8等多原子氧,可用于制造多种全新的氧化物。可将多种气体分解成离子态,可用于制造多种全新的化合物。
本实施例可作为反应器、粉磨设备、烟气净化设备等使用,可提高粉磨、反应、雾化清洗等效果。
本旋流机实施例之四的结构是:在以上结构基础上,旋流腔3轴线竖置,旋流腔3下部设置环绕水池14。将旋流腔3轴线竖置,在旋流腔3下部设置环绕水池14,可以在旋流腔进口5上设置一圈挡圈,使旋流腔3下部形成环绕水池14,环绕水池14可以与旋流腔3连成一体或分体设置,可将旋流腔3下部的机壳没入环绕水池14中,可利用水池中的水实现机壳密封,家用产品小型旋流机用于空气净化时,可设置成分体结构,可以将旋流机从环绕水池14中拿出后,将环绕水池14中的水定期添加或手动倾倒更换即可;用于抽油烟净化领域时环绕水池14与旋流腔3可连成一体,可在环绕水池14下部设置出料口8,在出料口8上设置阀门连接下水道,换水时将水全部放掉即可,环绕水池14可设置水位阀连接自来水自动加水。可以将传动装置2安装在定子涡旋整流体7内,可简化结构。可以将旋流轮4外围的旋流腔3内壁贴近旋流轮4外围,可提高净化效果,该段旋流腔3内壁可与环绕水池14设置为一体,底部设置豁口使水池保持连通即可。旋流轮4旋转时带动环绕水池14里的水向旋流腔3外周流动,同时可将少量水雾吸入旋流轮4,水雾连同空气一并从旋流轮4甩出后,沿旋流腔3向上运动,水雾凝聚在旋流腔3内壁上形成水膜,水膜保持一定厚度,可以提高水与空气的接触,可使灰尘、甲醛等吸收进入水中,最终随水一起排掉即可。使用 时注意调整好环绕水池14内的水位即可,通常水位保持与旋流轮4进口水平略下即可。
本实施例可用于家用空气净化、抽油烟净化等领域,可将空气中的粉尘、甲醛、油烟等吸收进水中。用于抽油烟时可以将油吸收进水中,可更方便排出油污,可连接自来水自动供水,可连接下水道将污水排掉。
本旋流机实施例之五的结构是:在以上结构基础上,旋流腔3对应旋流轮4设置喷淋装置15。通常可在旋流腔进口5附近或定子涡旋整流体7上对应旋流轮4进口设置喷淋装置15,喷淋装置15可设置多种形式的雾化喷头,雾化喷头连接输液管道即可,安装时调整好雾化喷头与旋流轮4之间的距离即可。喷淋装置15不断地向旋流轮4提供喷淋雾化水液,可对旋流轮4起到不断冲洗作用,用于处理黏性、油性烟气时可避免叶轮粘挂。水液从旋流轮4出来后在旋流轮4外围的旋流腔3内被旋流快速分解成更细小的水雾,使烟气在旋流轮4外围的旋流腔3内与水雾快速充分接触洗涤,实现烟气的超雾化清洗,使烟气中的各种污染物进入水雾中。烟气与水雾的混合物离开旋流轮4外围区域后进入定子涡旋整流体7外围区域,在该区域的旋流作用下实现脱雾,使烟气与水雾逐渐分离,最终脱除水雾的烟气从旋流腔出口6排出,脱除的水雾汇聚成水液从出料口8排出。定子涡旋整流体7内设置管道连通旋流轮4时,为避免没有完全喷入旋流轮4进口的多余水液在管道内积存,可在管道进口处下部开设排水口将水液排出即可。旋流轮4采用离心叶轮时也可在旋流腔3对应离心旋流轮4背面设置喷淋装置9的雾化喷头,可利用旋流轮4旋转对水雾进一步切割分离,可提高雾化效果,提高烟气净化效果。也可环绕旋流轮4外围设置多个喷头,可提高水雾雾化效果,可提高烟气雾化洗涤净化效果。也可在旋流轮4外围沿旋流腔3横截面切线方向顺应旋流轮4旋转方向设置进水管,旋流轮4旋转可以使旋流腔3内壁上的水液跟着旋转,使分离物打入水液中随水液一同排出,可在旋流腔3内壁上形成一个向旋流腔出口6端螺旋运动的水膜,可使分离物进入水膜中随水向旋流腔出口6端运动,旋流轮4外围的旋流腔3做成向旋流腔出口6端略微扩张的结构可使水液更顺畅地向旋流腔出口6端流动;旋流轮4采用轴流叶轮时,可靠近旋流轮4设置导叶,可靠近导叶设置进水管,可提高净化效果。涡旋整流体7也可以做成空管结构,可利用涡旋整流体7内部设置管道腔,可在管道腔内设置任意结构的喷淋装置,使管道腔形成一个喷淋室,在管道腔进口区域外围下部设置出水口将喷淋水液排出即可,可将烟气在旋流腔进口5之前进行一级喷淋净化处理,可提高烟气净化效果。旋流轮4进口侧的外围设置一圈圆辊可提高烟气净化效果。旋流轮4外围的旋流腔3内壁可以贴近旋流轮4外缘,旋流轮4可采用任意结构的叶轮,可尽量加大旋流轮4轴向厚度,可在旋流轮4靠近旋流腔出口6侧设置圆筒或圆辊,可使旋流轮4外周与旋流腔3内壁相互贴 近,可更好的形成旋流摩擦,可大大提高烟气雾化清洗效果。
本实施例传动轴横置、斜置、竖置安装使用均可,可取代现有的除尘器、脱硫塔等,可广泛用于各种窑炉、锅炉、焚烧炉等所有尾气处理领域,可用于所有处理烟气的领域。本实施例用于化工除异味时,可更好地收集异味成份,也可将异味成份与酸碱等反应掉,可更好地清除异味。本实施例可湿法除尘,可更高效除尘、除有害物质,可使烟气更加环保。也可将旋流机装在烟气净化末端,使用时喷入清水可提高烟气净化效果,清水可利用脱硫蒸发补充水,可彻底淘汰湿电,可同步除微尘、脱氨、除气溶胶、脱除各种污染物、水中加碱可二次脱硫等,可实现烟气近零排放。
本旋流机实施例之六的结构是:在以上结构基础上,靠近旋流腔进口5端的旋流腔3设置进料装置16。可在靠近旋流腔进口5端的旋流腔3外周壁上设置进料装置16,进料装置16可采用搅笼、卸料器、隔膜泵或泥浆泵等输送装置,可通过进料装置16向旋流腔3内均匀送入物料,选矿时也可将矿粉制成泥浆用隔膜泵或泥浆泵输送即可。进料装置16也可设置在旋流轮4外围,物料进入旋流腔3后,在旋流轮4旋转作用下与输送介质(水或空气)充分混合,物料被旋流带动起来,不断粉磨,最终实现分选。旋流轮4外围的旋流腔3内壁可设耐磨层,可提高使用寿命。
本实施例传动轴横置或竖置安装均可,可作为选矿设备、粉磨设备、垃圾处理设备、泥浆脱水干化设备等使用,可干选、湿选、干磨或湿磨,选矿时可边磨边选同步完成,可避免物料经过旋流轮4对其造成磨损、粘挂等。作为选矿设备、粉磨设备等使用时,传动轴竖置安装时效果较好,可在旋流腔3上部设置出料口8,可分离出磨选好的物料。本实施也可利用风干将各种泥浆脱水干化,可对超细泥浆进行脱水干化处理。
本旋流机实施例之七的结构是:在以上结构基础上,靠近旋流腔进口5端的旋流腔3设置进料装置16、燃烧供应装置17。可在靠近旋流腔进口5端的旋流腔3外周壁上设置进料装置16、燃烧供应装置17,进料装置16可采用搅笼等输送装置,进料装置16、燃烧供应装置17通常可设置在旋流轮4附近或外围,可有利于燃料燃烧充分,燃烧供应装置17可根据使用的燃料采用不同的燃料供应装置,固体燃料可采用搅笼,液体或气体燃料可采用燃料管直接供应燃料。可采用测温装置,可设置温控装置,根据温度调节燃烧供应装置17的燃料供应速度实现旋流腔3的温度调控。也可在轴端增设一个小的旋流腔进口5,可利用进气对传动装置2降温。旋流腔3可设置保温层,旋流轮4外围的旋流腔3内壁可设置耐火耐磨材料层。旋流腔3轴线横置安装时烧成段旋流腔3内径向旋流腔出口6端逐渐扩张,可避免物料沉积。旋流腔3下部设置一个出料口8可定期将炉渣排出。旋流腔3上部设置一个或 多个出料口8可收集烧制好的物料排出。
本实施例传动轴横置或竖置安装均可,可作为新型窑炉、反应炉、焚烧炉、干燥炉等使用,可烧制多种物料,比如:石灰、氧化镁、水泥、焦宝石、多种矿料、垃圾等。可实现物料均匀煅烧或干燥,可使物料在煅烧或干燥的同时被不断粉磨,可实现快速充分煅烧或干燥,可烧制块状或粉体物料。传动轴竖置安装时,可将块料直接磨细,边烧边磨,可烧出粉体产品,同时可实现粉体分选,可直接将粉体采用气流输送送至储罐中,可实现全自动化进料、出料。本实施例也可用于各种需要产品干燥脱水的领域,使用时将产品料浆用进料装置16喷入旋流腔3高温区域即可。传动轴横置安装时,可烧制小块物料或液体排渣物料。
本旋流机实施例之八的结构是:在以上结构基础上,靠近旋流腔进口5端的旋流腔3设置燃烧供应装置17,旋流腔3设置进料装置16,旋流腔3下部设置熔池18,熔池18至少设置一个出料口8。可在靠近旋流腔进口5端的旋流腔3外周壁上设置燃烧供应装置17,燃烧供应装置17可根据使用的燃料采用不同的燃料供应装置,固体燃料可采用搅笼,液体或气体燃料可采用燃料管直接供应燃料。可采用热电偶测温,可设置温控装置,根据温度调节燃烧供应装置17的燃料供应速度实现旋流腔3的温度调控。也可在轴端增设一个小的旋流腔进口5,可利用进气对传动装置2降温。旋流腔3设置进料装置16,可在旋流腔3设一个或多个进料装置16,可利用进料装置16向旋流腔3内吹入矿粉、石灰石粉、煤粉等,矿粉、石灰石粉可采用气流输送,可设置流量自动控制装置,可沿旋流腔3横截面切线方向顺应旋流轮4旋转方向设置,可使粉状物料更顺畅的进入旋流腔3,同时可促进旋流腔3内的旋流旋转。燃烧供应装置17通常可设置在旋流轮4外围,可更好的燃烧。烟气含有煤气,煤气利用或余热发电后进行尾气处理即可。通过旋流腔进口5将采集余热后的空气吸入旋流腔3,煤粉通过燃烧供应装置17送入旋流腔3,煤粉在旋流腔3内燃烧的同时向旋流腔出口6端运动。在旋流腔3下部设置熔池18,熔池18可设置在旋流腔3下部任意方位,可设置一个或多个熔池18,也可在旋流腔3下部环绕设置一个环形熔池18。熔池18可设有一定深度,熔池18可以设置一个或多个出料口8,通常可以在熔池18上部和下部分别设置出料口8,用于炼铁、炼铜等时可以实现渣水分离,下部出料口8出料水,上部出料口8出渣。煤粉与石灰石粉在离心力作用下进入旋流腔3内壁上的熔液中与矿粉熔液发生还原反应和造渣反应,反应形成的铁水、渣水流入熔池18后渣水分离后排出。设置温控装置控制炉温,设置进料控制装置自动控制矿粉进料速度,定期打开出料口8出渣水、铁水或铜水等即可。传动轴竖置使用时将矿粉与还原剂等在旋流腔3中段加入,矿粉与还原剂溶化后沿旋流腔3内壁流下,在旋流腔3下部外围区域设置熔池18使渣水分离即可。传动轴横置使用时,熔融 段旋流腔3内径向旋流腔出口6端逐渐扩张,可更好的使熔液向旋流腔出口6端流动,将矿粉与还原剂等在旋流腔3靠近旋流腔进口5段加入,在旋流腔3中部区域设置熔池18使渣水分离即可,定子涡旋整流体7的支撑装置也可采用空心管,可利用空心管将空气吸入进气管道,可利用空气对支撑装置降温,可降低材料耐热要求。
本实施例可作为冶炼炉、熔炉等使用,可冶炼多种金属,可用于炼铁、炼铜、炼铝硅合金、生产泡花碱、玻璃、陶瓷熔块等。旋流腔3中轴线可以竖置或横置安装,燃料可根据需要采用煤粉、气、油等任意燃料。炼铁时不用焦炭,不用球团,大大降低生产成本。
本旋流机实施例之九的结构是:在以上结构基础上,靠近旋流腔进口5端的旋流腔3设置燃烧供应装置17,旋流腔3内壁上设置采热装置19。靠近旋流腔进口5端的旋流腔3设置燃烧供应装置17,可以使该区域形成燃烧区,燃烧供应装置17可以根据所用燃料具体设定,固体燃料可采用搅笼、卸料器等,液体、气体燃料可采用喷嘴等。可通过燃烧供应装置17向旋流腔3内均匀卸入燃煤或垃圾等以及干法脱硫剂等。也可在旋流腔3内壁上设置测温装置,测温装置可采用热电偶、温控仪表等装置,测温装置可通过温控仪表控制燃烧供应装置17,当炉内温度达到设定温度上限时,自动断开燃料供给电源,当炉内温度达到设定温度下限时,自动接通燃料供给电源即可。燃烧供应装置17通常可设置在旋流轮4靠近旋流腔出口6侧,可沿旋流腔3横截面切向顺应旋流轮4旋转方向设置,可更顺畅的进燃料,同时可更好的降低旋流轮4区域的温度,可降低旋流轮4以及定子涡旋整流体7的支撑装置的磨损以及材料耐温要求。旋流腔3内壁上设置采热装置19,可在旋流腔3内壁上设置采热管或采热箱等作为采热装置19,可采用水、油或气体等作为采热介质。采热装置19可以贴近旋流腔3内壁设置,采热管也可以沿旋流腔3内壁环绕设置。采热装置19可采用现有的任意一种锅炉所采用的采热管装置,可根据需要实现各种压力的锅炉。作为中压、高压、超高压锅炉使用时可在靠近旋流腔进口5段设置高压采热管,在靠近旋流腔出口6段设置低压采热管,低压采热管与高压采热管之间采用锅炉泵实现强制循环,可提高采热效率。
本实施例可作为多种锅炉设备使用,可采用煤、油、气、生物质、垃圾、水煤浆、煤粉等任意燃料,可在旋流腔3内壁上设置耐火保温层。旋流腔3中轴线可以竖置或横置安装,可使燃料在旋流腔3内实现均匀的旋流燃烧,可利用旋流燃烧加旋流破碎使燃料充分燃烧,燃煤或垃圾时,传动轴竖置安装时可使煤块或垃圾被不断的剥离破碎燃烧充分。精准供给燃料,可使燃烧区温度保持稳定均匀,可精准控制炉温,可实现低温燃烧,可减少氮氧化物产生。燃煤时同步加入碳酸钙石屑可实现炉内干法脱硫,炉内温度均匀,旋流促进反应,可实现干法充分脱硫。旋流腔3形成的旋流可以促进采热装置19表面的气流运动速度,可 大幅提高采热效率,大大减少采热面积,大大降低造价。旋流运动使热气流在旋流腔3内的运动距离大大延长,可使热能充分传递,实现高效充分采热。焚烧垃圾或块煤时,也可在靠近旋流轮4的旋流腔3外围设置出料口8,可将难以粉磨燃烧的物料间歇或持续排出。
本实施例是一个可以烧任意燃料的高效锅炉,可使燃尽率接近100%,大大降低一氧化碳、硫和硝排放。也是一个高效垃圾焚烧器,可使垃圾充分燃烧,同时实现热能充分利用。
工作原理:本旋流机使用时可同时将流体输送出去,流体在本旋流机内实现分离、反应、粉磨。旋流轮4旋转后,带动流体从旋流轮4内流出,流体在运动惯性作用下,在旋流腔3内形成旋流,旋流使流体内各个粒子的运动速度不同,使流体内各个粒子形成一个个独立运动个体,可更好地利用离心力将不同比重的粒子分开,利用旋流内产生的离心力实现流体内不同比重物质的分离、分选。旋流沿轴向螺旋运动,不同比重的独立运动个体向旋流外围的运动速度不同,比重较大的粒子或颗粒物更容易、更快的运动到旋流腔3内壁上,最终实现不同比重的分离物的分离。流体在轴向运动过程中,受到流体运动、离心力以及重力等共同影响实现各种分离物的分离。不同比重的多种分离物分别运动到旋流腔3的不同轴向区域,分别通过轴向不同的出料口8排出,最终实现对流体的分离、分选或污染物等的脱除。流体在轴向运动过程中被逐渐分离,旋流轮4转速越高,流体运动速度越高,旋流具有的能量越大,分离效果越好。用于烟气净化时,可以使烟气与水液充分快速接触,使烟气中的污染物充分进入水液中,洁净尾气从旋流腔出口6排出。利用旋流促进化学反应,实现脱硫脱硝,实现烟气彻底净化,可以利用旋流腔3内壁上设置催化剂进一步促进多种化学反应。利用分离可解决水污染、可实现海水淡化、可解决水资源、可实现选矿、可解决矿产资源、可解决核废料污染、可制氧实现纯氧燃烧等。利用旋流实现旋流粉磨,使物料随气流运动过程中相互摩擦碰撞逐渐被粉磨细,可实现高效粉磨,可磨出超细粉体、纳米粉体、单原子颗粒物,可解决纳米材料原料,可磨制炭烯,可解决石墨烯原料。利用高速旋流使分子在旋流中被不断的摩擦碰撞分解,利用高速旋流打开分子链实现分子分解成离子,同时利用旋流实现分子分解形成的不同离子的分选。利用旋流实现旋流燃烧,利用离心力实现燃料分选,可使颗粒较大的燃料始终处在燃烧区燃烧,使燃尽的灰分随气流离开燃烧区,可使燃料在旋流腔3内实现旋流燃烧,可利用旋流燃烧加旋流粉磨使燃料充分燃烧,燃烧固体燃料时,可使燃料在不断燃烧的同时被不断剥离粉磨燃烧充分。
本发明的技术方案并不限制于本发明所述的实施例的范围内。本发明未详尽描述的技术内容均为公知技术。

Claims (10)

  1. 旋流机,包括壳体(1)和传动装置(2),其特征在于:壳体(1)上设置传动装置(2),壳体(1)内设置旋流腔(3),旋流腔(3)横截面为圆形,旋流腔(3)内一端轴心区域设置旋流轮(4),旋流轮(4)与旋流腔(3)处在同一轴线上,传动装置(2)与旋流轮(4)连接,旋流腔(3)对应旋流轮(4)至少设置一个旋流腔进口(5),旋流腔(3)另一端设置旋流腔出口(6),壳体(1)上贯穿从旋流轮(4)到旋流腔出口(6)之间的旋流腔(3)设置横截面为圆型的定子涡旋整流体(7),环绕定子涡旋整流体(7)外壁至少设置一道挡圈(9),旋流腔(3)外围至少设置一个出料口(8)。
  2. 根据权利要求1所述的旋流机,其特征在于:旋流轮(4)内设旋流分离室(10),旋流分离室(10)一端设置旋流分离室出口(11),旋流分离室(10)另一端设置旋流分离室进口(12),旋流腔(3)对应旋流分离室进口(12)至少设置一个旋流腔进口(5),定子涡旋整流体(7)一段穿过旋流分离室出口(11)探入旋流分离室(10)内。
  3. 根据权利要求1所述的旋流机,其特征在于;旋流腔(3)内壁上至少设置一道环绕分隔体(13),旋流腔(3)外围对应环绕分隔体(13)至少设置一个出料口(8)。
  4. 根据权利要求1所述的旋流机,其特征在于:旋流轮(4)外围的旋流腔(3)内壁贴近旋流轮(4)外缘。
  5. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:旋流腔(3)轴线竖置,旋流腔(3)下部设置环绕水池(14)。
  6. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:旋流腔(3)对应旋流轮(4)设置喷淋装置(15)。
  7. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:靠近旋流腔进口(5)端的旋流腔(3)设置进料装置(16)。
  8. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:靠近旋流腔进口(5)端的旋流腔(3)设置进料装置(16)和燃烧供应装置(17)。
  9. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:靠近旋流腔进口(5)端的旋流腔(3)设置燃烧供应装置(17),旋流腔(3)设置进料装置(16),旋流腔(3)下部设置熔池(18),熔池(18)至少设置一个出料口(8)。
  10. 根据权利要求1、2、3或4任一项所述的旋流机,其特征在于:靠近旋流腔进口(5)端的旋流腔(3)设置燃烧供应装置(17),旋流腔(3)内壁上设置采热装置(19)。
PCT/CN2021/104468 2020-07-08 2021-07-05 旋流机 WO2022007740A1 (zh)

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