WO2018082489A1 - 分离反应粉磨机 - Google Patents
分离反应粉磨机 Download PDFInfo
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- WO2018082489A1 WO2018082489A1 PCT/CN2017/107586 CN2017107586W WO2018082489A1 WO 2018082489 A1 WO2018082489 A1 WO 2018082489A1 CN 2017107586 W CN2017107586 W CN 2017107586W WO 2018082489 A1 WO2018082489 A1 WO 2018082489A1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B11/00—Feeding, charging, or discharging bowls
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
- B04B15/02—Other accessories for centrifuges for cooling, heating, or heat insulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
- B04B5/12—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/02—Casings; Lids
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K1/00—Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
Definitions
- the invention relates to a separator, a centrifuge, a sewage treatment, a purified water, a seawater desalination, a marine chemical, a mineral processing, a coal preparation, a nuclear fuel selection, a nuclear waste treatment, a refining, an oil and gas recovery, a garbage disposal, an air purification, a dust removal, a vacuuming, and the like.
- Desulfurization, denitrification, range cleaning, tail gas treatment, black smoke removal, odor removal, oxygen production, air separation and extraction, reactor, boiler, burner, grinding, etc., specifically a separation reaction pulverizer, can be realized Three functions of grinding, chemical reaction and separation, the three functions can be used alone or in combination.
- the existing air purification equipment has a poor purification effect, and the desulfurization and denitration equipment has high cost, high operation and maintenance cost, high energy consumption, low removal efficiency, and poor effect.
- the desulfurization, wet dust removal and denitration are mostly sprayed, and cannot be used. Particulate matter, sulfur oxide molecules, nitrogen oxide molecules and the like are sufficiently adsorbed and dissolved, resulting in low efficiency of dust removal, desulfurization and denitration.
- the existing dust removal equipments include cyclone dust removal, electric dust removal, wet electric dust removal, bag dust removal, etc., and there are generally defects such as poor dust removal effect and high energy consumption. Dust pollution has become the most important source of air pollution and has become the chief culprit.
- the existing black smoke removal and odor removal equipment are too poor, and the black smoke, many chemical odors and dioxin are basically untreated.
- the black smoke and odor gas pollution have become an important source of pollution.
- Dioxins are the most serious human beings.
- Organic pollutants have seriously affected human survival.
- Heavy elemental particles in the atmosphere have seriously threatened human health.
- the dust collection effect of the existing vacuuming equipment is not ideal, the noise is large, the dust particles are polluted, and the dust is troublesome after dust removal.
- the existing range hoods are unable to separate the soot, causing troubles in the cleaning of the range hood, causing the soot particles to pollute the environment, and the soot particles have become another important source of pollution for urban air pollution.
- the existing sewage treatment equipment is complicated, the cost is too high, the sewage treatment cost is too high, the treatment effect is general, and sewage treatment has become the top priority of environmental treatment.
- the existing oxygen production equipment is too expensive, the oxygen production cost is too high, and the universal application cannot be realized, so that pure oxygen combustion cannot be achieved, and a large amount of nitrogen oxides are discharged to form an important pollution source.
- the existing water purifiers mainly adopt methods such as filtration and water purifying agents, and there are generally defects such as failure to reach higher drinking water standards and high water purification costs.
- the existing seawater desalination equipment is complicated, the cost is too high, the seawater desalination cost is too high, and the energy consumption is too large.
- the existing marine chemical equipment is complex, the cost is too high, and the utilization of marine resources is not satisfactory.
- the existing separation equipment mainly including centrifuges, generally has the defects of general separation effect and large energy consumption.
- the existing beneficiation equipment has a general ore dressing effect and cannot achieve finer sorting, resulting in waste of resources and environmental pollution.
- the existing refinery equipment generally adopts high-temperature distillation cracking method, which has high refining cost and high energy consumption.
- the high temperature damages the macromolecules in the crude oil, and generates a large amount of petroleum gas and petroleum slag, which greatly reduces the oil yield and reduces the high-quality oil output. Lead, heavy metals, heavy elements, etc. in the oil cannot be removed, causing serious fuel pollution.
- the existing coal preparation equipment is simply washing coal, and it is impossible to fully clean the coal, so that the sulfur in the coal is burned to form sulfur dioxide, and the tail gas is desulfurized, and the air is not cleaned, causing atmospheric pollution.
- Various metal elements in the coal When valuable things were not selected, they all ran into the coal ash. The radioactive elements in the coal also ran into the atmosphere and coal ash, causing serious environmental pollution and waste of resources. The net selection of coal is an urgent task.
- 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 untreated, causing serious environmental hazards.
- the existing reactor equipment has a reaction kettle, a catalyst reaction tank or a tower, etc., and the reaction speed is ubiquitous. Slow, incomplete reaction, high cost, and easy aging of the catalyst.
- the existing grinding equipment includes a pulverizer, a Raymond mill, a wind sweeping mill, etc., and generally has high energy consumption, low efficiency of grinding powder, and difficulty in preparation of ultrafine powder.
- each particle, atom and other particles in the eddy flow can form independent movements of different motion speeds.
- Individuals use vortex motion and centrifugal force as well as gravity to cause substances of different particle sizes and different specific gravity to enter different regions.
- the solute in the solution can be separated from the solvent, and the different solutes can be separated.
- the eddy current is used to make each particle, molecule, atom and other particles in the eddy flow form an independent moving individual with different motion speeds, and fully interact with the water flow and the water mist under the action of the circular motion centrifugal force and the motion inertia, so that the smoke is covered by the water.
- the basic liquid, air, etc. When the basic liquid, air, etc. are input into the invention, it can also be used in the fields of flue gas desulfurization, denitrification, odor removal, etc., which can greatly improve the operation efficiency of the equipment and reduce the cost and operation cost.
- the eddy current causes the molecules to collide with each other, which can greatly promote the chemical reaction, can achieve the catalytic effect, and can be used as a denitration device, a chemical reactor, and the like.
- the vortex combustion and eddy current crushing make the fuel fully burned, especially when burning coal, the coal block can be continuously peeled and crushed and burned while continuously burning, and the temperature in the combustion zone is kept stable and uniform, and the furnace temperature can be controlled more accurately. It can achieve low temperature combustion and completely eliminate nitrogen oxides. Simultaneous addition of calcium carbonate stone chips during coal combustion can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can fully realize the full desulfurization by dry method.
- the boiler dust removal, desulfurization and denitrification integration can be realized, and the boiler can be completely environmentally friendly.
- the invention can realize cleaner dust removal, cleaner air purification, cleaner purifying soot, cleaner sewage treatment, cheaper seawater desalination, more fully utilizing water resources, more fully extracting marine resources, and higher Efficient beneficiation, cleaner waste disposal, and more efficient refining.
- the invention can be widely applied to various separations Equipment field. It can be used as a new type of centrifuge and separator. It has better separation effect and can separate, sort, extract and purify various components.
- the invention can be used as a dust remover, and can adopt dry dust removal or wet dust removal, can not only remove PM2.5 particles, but also can remove PM0.01 particles, and can basically achieve dust-free discharge, and can be done with It has the same dust content as the excellent atmospheric environment, and does not contain harmful substances such as heavy elements. It can also be completely dust-free.
- the invention can remove the black smoke; can effectively remove the odor component in the flue gas; can remove the dioxin and heavy element particles in the flue gas; when the water liquid adopts an alkaline liquid or adds various desulfurizing agents, It can be used in the fields of flue gas desulfurization and denitrification, and realizes wet dust removal, wet desulfurization and wet denitration in one step, which can greatly improve the operation efficiency of equipment.
- the invention can be used as an air purification device and can be used as a new indoor air purifier. It can be used as an odor-eliminating device to remove odorous gases. It can be used as a dust collector and can exceed the dust removal effect of any type of dust collector.
- the invention can be used as a vehicle and ship exhaust gas processor, can complete dust removal and smoke removal, can simultaneously replace the three-way catalytic converter, can never block, never aging, can make the exhaust gas complete the ternary reaction in the invention, realize denitration, removal Hydrocarbons, in addition to carbon monoxide, can efficiently remove particulate matter, nitrogen oxides, etc. in the exhaust gas.
- the invention can be used as an oil and gas recovery device, and can recover a plurality of oil vapors.
- the invention can be used as a range hood, which can clean the soot and make the flue gas discharge completely environmentally friendly.
- the invention can be used as a novel air purifier to remove dust and soot particles in the room.
- the invention can be used as a vacuum cleaner, has convenient dust cleaning, low noise, good dust collecting effect, low cost and more energy saving, and is used as a vacuum cleaner without dust pollution, and is more sanitary and environmentally friendly.
- the invention can be used as a sewage treatment device, and can extract a plurality of useful components from the sewage to realize resource recycling. Pure water can be directly supplied to meet drinking water standards, which can completely solve water pollution and solve water shortage problems.
- the invention can be used as a water purifying device, can completely separate harmful elements in tap water, and can separate heavy water (heavy hydrogen water, heavy oxygen water), can reach higher drinking water standards, and can make people drink more pure. Healthy drinking water. Heavy water can be extracted from water for industrial use.
- the invention can be used as a garbage disposal device. After the garbage is pulverized into granules, the granules are transported by water to carry out wet selection, the useful components are separated and sorted, and the useless components and the organic components are pressed into granular organic fertilizer. It 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 completely cleaned.
- the invention can separate oxygen from the air, can also separate various gases in the air, and can extract a plurality of rare gases.
- the low cost of oxygen production enables boilers, kilns, engines, heat engines, etc. to achieve cheap and economical pure oxygen combustion, which can reduce energy consumption, improve heat efficiency, completely eliminate nitrogen oxide emissions, and reduce engine volume, weight and displacement. , increase the torque.
- Exhaust gas recirculation can also be used for engines, heat engines, kilns, boilers, etc., which can reduce combustion temperatures and reduce equipment material requirements.
- the carbon dioxide produced by the combustion of pure oxygen can be collected centrally. If it can be sent to the seabed at high pressure, it can form dry ice and be stored in the deep ocean. It can completely solve the carbon emissions.
- the invention can be used as a beneficiation equipment, and can realize separation, extraction, purification and impurity removal of a plurality of minerals and raw materials, and can select a plurality of useful minerals from the lean ore.
- the ore can be pulverized into granules, and the granules can be transported by water or gas for wet selection. It can be used for all mineral sorting. It can select all kinds of useful ingredients in minerals, which can make tailings completely harmless and greatly improve the economic and environmental benefits of mineral processing. Together they are rubbish, and separation is gold.
- various elements can be selected; for precious metal beneficiation, valuable elements can be fully extracted.
- the invention can be used as seawater desalination equipment and marine chemical equipment, which can greatly reduce equipment cost, reduce seawater desalination cost, greatly reduce energy consumption, improve seawater desalination efficiency, and increase fresh water production. Simultaneously extract various useful ingredients from seawater, and at the same time realize separation, extraction and sorting and purification of various useful ingredients, which can be used as salt extraction equipment and marine chemical equipment, which can greatly reduce equipment cost.
- various minerals can be extracted from the rivers and lakes, which can better protect the environment and resources. The water quality of rivers, lakes and seas will be better, and the earth's ecological environment can be better protected.
- the invention When the invention is used as an oil refining equipment, low temperature cracking of crude oil can be achieved, the destruction of macromolecular components in the crude oil can be reduced, the output of petroleum gas and petroleum slag can be reduced, the oil yield can be improved, and the output of high quality oil can be improved.
- the oil can be completely lead-free and free of radioactive elements.
- the whole production process is free of pollution, and there is no waste water or exhaust gas emission.
- the refining process can be completely environmentally friendly, and the resources can be completely utilized, which can greatly reduce the refining cost.
- the coal When the invention is used as a coal preparation equipment, the coal can be made into coal powder, and the dry selection or wet selection can be used, and the sulfide, metal element, precious element, radioactive element and common mineral in the coal can be sorted out. It can be made into high-purity pulverized coal or high-purity coal water slurry. It can also be dewatered by dewatering sieve to make high-purity briquettes. Burning such high-purity coal can achieve clean combustion of coal, which is comparable to natural gas. Tail The gas can be desulfurized and dedusted without further desulfurization; low-temperature combustion can be achieved, nitrogen oxides can be produced, and denitrification can be eliminated.
- the selection effect can be greatly improved, the cost can be greatly reduced, and the tailings can be made more environmentally friendly.
- the high-radioactive elements in the nuclear waste can be extracted, and after reaching a certain concentration, the nuclear reactor can be re-introduced into a nuclear reactor and become a low-level substance, which can make the tailings become a low-level radioactive material, that is, the glass can be solidified and landfilled. It can make nuclear waste no safety hazard. With the birth of new energy, the nuclear reactor will be transformed into a nuclear waste incineration furnace.
- the vortex can be used to cause the molecules to collide with each other, which can greatly promote the chemical reaction, can realize the catalytic effect, and can be used as a catalytic reaction device of the denitration device.
- the vortex combustion and eddy current crushing are used to fully burn the fuel, and any fuel can be used, so that the temperature in the combustion zone can be kept stable and uniform, the furnace temperature can be controlled more accurately, and low temperature combustion can be realized, which can be thoroughly Eliminate the production of nitrogen oxides.
- burning coal the coal can be continuously burned and burned while being continuously burned.
- Simultaneous addition of calcium carbonate stone chips can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can fully realize the full desulfurization by dry method. It can realize the integration of burner, boiler dust removal, desulfurization and denitrification, and achieve complete environmental protection.
- the eddy current crushing and grinding is used to gradually grind the particles, and various powders can be prepared, and the flour can be ground, and the whole wheat flour can be prepared.
- the milled powder can be dry-grinded or wet-milled, and dry grinding can be realized by using air as a carrier, and wet grinding can be realized by using water as a carrier, and ultra-fine powder, nano-powder and the like can be produced. It can also be used as a coal dusting machine or a coal-fired shotcrete machine, which can dry or wet the raw coal, and can spray coal powder or coal slurry into the kiln to burn.
- the separation reaction pulverizer comprises a casing and a transmission device, the transmission device is arranged on the casing, the casing cavity is arranged in the casing, the vortex wheel is arranged in the casing cavity, the transmission device is connected with the vortex wheel, and the casing cavity is provided at one end of the casing cavity, the casing cavity The other end is provided with a housing cavity outlet.
- At least one surrounding partition is disposed on the inner wall of the housing cavity, and the outer circumference of the housing cavity is correspondingly disposed around the partition.
- At least one of the inner walls of the housing cavity is adjacent to the outer edge of the vortex wheel.
- the shower chamber inlet communicates with the shower chamber, the spray chamber is provided with a shower chamber inlet, and the spray chamber is provided with a plurality of shower devices.
- a liquid supply device is disposed on the inner wall of the outer periphery of the housing cavity.
- the housing cavity end is provided with a housing cavity inlet, and the other end of the housing cavity is provided with a housing cavity outlet.
- a heat collecting device is disposed on the inner wall of the casing cavity.
- An automatic feeding device is arranged on the inlet of the casing cavity, a temperature measuring device is arranged on the inner wall of the casing cavity, and the temperature measuring device controls the automatic feeding device.
- a flow regulating device is disposed on the outlet of the housing cavity.
- a plurality of fluid shifting devices are disposed on the outer circumference of the vortex wheel and in the axial direction.
- the invention has the advantages that the circular motion and the fluid motion are fully utilized, the vortex motion is fully utilized, the fluid is gradually separated, and the effect is synchronously increased with the increase of the rotational speed.
- the fluid moves helically in the axial direction and is gradually separated during the axial movement.
- the eddy current causes the molecules to collide with each other to generate a large amount of free radicals, which can greatly promote the chemical reaction, can achieve a catalytic effect, and can be used as a catalytic reaction device.
- the granules are gradually ground by eddy current crushing.
- the vortex combustion and vortex breaking are used to fully burn the fuel, and the temperature in the combustion zone is kept stable and uniform, the furnace temperature can be controlled more accurately, and low-temperature combustion can be realized, and the generation of nitrogen oxides can be completely eliminated.
- the coal When burning coal, the coal can be continuously burned and burned while being continuously burned.
- Simultaneous addition of calcium carbonate stone chips can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can fully realize the full desulfurization by dry method. It can realize the integration of boiler dust removal, desulfurization and denitrification, and achieve complete environmental protection for burners and boilers.
- the invention has the advantages of simple manufacture, large or small equipment, wide application fields, low manufacturing cost, simple manufacturing process, low use cost, low maintenance cost and long service life.
- Figure 1 is a schematic view of the main structure of the present invention
- FIG. 2 is a schematic front view showing the structure of one embodiment of the present invention.
- Figure 3 is a schematic front view showing the structure of the second embodiment of the present invention.
- Figure 4 is a schematic front view showing the structure of the third embodiment of the present invention.
- Figure 5 is a front view showing the structure of the fourth embodiment of the present invention.
- Figure 6 is a front view showing the structure of the fifth embodiment of the present invention.
- Figure 7 is a schematic front view showing the structure of the sixth embodiment of the present invention.
- Figure 8 is a schematic front view showing the structure of the seventh embodiment of the present invention.
- Figure 9 is a front view showing the structure of the eighth embodiment of the present invention.
- Figure 10 is a front view showing the structure of a ninth embodiment of the present invention.
- the main structure of the present invention comprises a casing 1 and a transmission device 2, and a transmission device 2 is arranged on the casing 1.
- the casing 1 is provided with a casing cavity 3, and a vortex wheel 4 is arranged in the casing cavity 3, and the outer circumference of the vortex wheel 4 and the axial direction
- a plurality of fluid-swapping devices 5 are disposed on the upper side, and the transmission device 2 is connected to the vortex wheel 4.
- the housing chamber 3 is provided with a housing chamber inlet 6 at one end, and the housing chamber outlet 7 is disposed at the other end of the housing chamber 3.
- the scope of the casing 1 includes a base, a bracket, a pipe, a casing, and a power unit, and each part may be collectively referred to as a casing.
- the housing 1 can also be integrally formed with the power unit to form a unitary housing.
- the invention can be made of different materials according to needs, and can be made of materials such as metal, alloy, ceramic, glass, glass steel, carbon fiber, plastic, nylon, foam and the like.
- the transmission device 2 includes a transmission shaft, a bearing or a bearing bush, a shaft seat, etc., and the transmission device 2 is provided with a transmission shaft, and the power input is realized by the transmission shaft to drive the work of the invention.
- the transmission device 2 is connected to the power device to realize power input, and drives the work of the present invention.
- the power unit can use a motor or an engine.
- the power unit can be directly connected to the transmission unit 2, or can be powered by a coupling drive, a belt drive, a chain drive, a gear drive, or the like, or can be realized by a pulley, a reducer, or the like.
- the exhaust gas from the engine can be connected to the housing chamber inlet 6 to directly push the device to operate, which simplifies the structure and can simultaneously replace the muffler.
- the power unit and the housing 1 can also be directly integrated, or the power unit can be directly used as the transmission unit 2. It is also possible to adjust the rotation speed by using a frequency conversion technique or the like, and the separation reaction effect can be adjusted.
- the transmission device 2 can be disposed at one end to form a cantilever structure, and the other end of the rotating shaft of the transmission device 2 can be connected to the rotation stabilization device, which can greatly lengthen the axial length of the device, and can improve the reaction separation effect.
- the rotation stabilizer can be equipped with brackets, shaft seats, bearings, bushings or seals to make the rotation more stable.
- the rotary stabilizer device can be provided with a thrust bearing, which can better improve the service life, the bracket can be made detachable, and the bearing can be easily installed and disassembled, and the bracket can be respectively set with multiple screw ejector adjustments.
- Radial and axial position; the bearing housing can also be made into an axial open structure, which is more convenient for installation and disassembly.
- the shaft seal device When the drive shaft is installed vertically and the treatment liquid is used, the shaft seal device can be set at the same time, and the flow plate synchronously rotating with the rotation shaft can be arranged on the rotating shaft above the lower bearing, so that the leaked water can be thrown out to the periphery to avoid water leakage. Go to the lower bearing.
- a surrounding flow path may be arranged on the outer circumference of the lower portion of the casing cavity to avoid leakage of water from the axial center region and increase the intake runner area.
- a transmission 2 is arranged on the housing 1.
- the transmission device 2 can adopt a setting scheme of a fan or a water pump transmission device.
- the power terminal of the transmission device 2 can be generally disposed at the upper portion of the casing 1 for easy disassembly.
- a housing cavity 3 is provided in the housing 1.
- the housing cavity 3 can be formed as an integral or open structure, and can be assembled together when installed.
- the housing cavity 3 can also be opened as needed, which can be easily assembled.
- the inner wall of the housing cavity 3 can also be provided with a wear-resistant material layer or a corrosion-resistant layer to improve the service life.
- the glass scale can be used for anti-corrosion during desulfurization and denitrification, and the wearable area can also be attached with wear-resistant sheets or wear-resistant bricks on the surface. At the time, repair and maintenance can be done.
- the cross section of the interior of the housing cavity 3 can generally be arranged in a circular shape to better form eddy currents in the housing cavity 3.
- the central axis of the housing chamber 3 is installed vertically, so that the flue gas moves from the bottom to the bottom, and the water liquid moves from the top to the bottom.
- the housing cavity 3 can be generally formed into a cylindrical shape that is as thick as the upper and lower sides, and the structure can be simplified.
- the housing cavity 3 can be made thicker toward the inlet end as needed, and a plurality of sections having a different inner diameter or a polygonal structure can be used. Different functional effects are achieved separately.
- the inner wall of the casing cavity 3 may be provided with an anticorrosive or anticorrosive wear layer according to specific working conditions.
- a refractory insulation layer can be arranged on the inner wall of the casing chamber 3.
- An eddy current wheel 4 is disposed in the housing chamber 3.
- the vortex wheel 4 is preferably disposed on the central axis of the housing cavity 3, and the outer circumference of the vortex wheel 4 is preferably disposed parallel to the inner wall of the housing cavity 3.
- the vortex wheel 4 can be integrally arranged in a cylindrical shape, a plurality of cylindrical unequal diameters, a truncated cone shape or a multi-section truncated cone shape having an unequal diameter.
- the flow wheel 4 is generally arranged in a cylindrical shape, and the outer portion of the vortex wheel 4 can conform to the shell.
- the inner wall of the body cavity 3 is arranged, and the longer the axial length of the vortex wheel 4 is, the better the effect is.
- the ratio of the axial length of the vortex wheel 4 to the diameter of the vortex wheel 4 can be arbitrarily set according to requirements, and can be as far as possible without affecting the rotation stability of the vortex wheel 4 Increasing the axial length of the vortex wheel 4; generally, the vortex wheel 4 is arranged as a whole, and the vortex wheel 4 can be arranged in a hollow or solid structure; the vortex wheel 4 can also be arranged in a plurality of separate structures and installed together.
- the outer peripheral surface of the vortex wheel 4 may be provided as a smooth surface or a matte surface, and the fluid layer may be driven by the boundary layer effect of the outer peripheral surface of the vortex wheel 4 to improve the separation effect; or may be disposed on all or part of the outer circumference of the vortex wheel 4 Threads, grooves or a plurality of fluid-pushing devices improve the fluid plucking effect; or a plurality of blades of any structure can be evenly distributed as a fluid on all or part of the outer circumference of the vortex wheel 4 according to working conditions.
- the blade can also be inclined at an angle to the axial direction, which can function as an axial flow impeller, which can supercharge the fluid and promote the axial movement of the fluid;
- the fluid shifting device can also adopt round sticks, round tubes, etc.
- the distance between the inner walls of the body cavity 3 can be arbitrarily adjusted according to needs. The closer the distance is, the more intense the fluid oscillation is.
- the inner wall of any one of the casing cavities 3 can be attached to the outer edge of the vortex wheel 4 as needed, and the inner wall of the casing cavity 3 is close to the vortex wheel 4 Edge, can make eddy current friction more intense, as a reactor When used, the reaction effect can be improved. When used as a grinding device, the grinding strength can be improved, and the disadvantage is increased wear; the vortex wheel 4 can be made of different materials according to requirements, and can be used for metal, ceramic, fiberglass, carbon fiber, plastic. , foam materials, etc.
- the transmission 2 is connected to the vortex wheel 4.
- the transmission shaft of the transmission device 2 is to be connected and fixed to the axial center region of the vortex wheel 4 to ensure smooth rotation of the vortex wheel 4, and a wheel disc, a shaft plate, a wheel body and the like can be arranged in the axial center region of the vortex wheel 4.
- the drive shaft can also be a hollow shaft or welded to the vortex wheel 4 to simplify the structure.
- the motor of the transmission 2 can also be integrated with the vortex wheel 4, which can save space and reduce the cost.
- a plurality of axial flow impellers may also be used as the vortex wheel 4, and the plurality of axial flow impellers may be coaxially mounted on the transmission shaft of the transmission device 2, and the disadvantage is that the structure is complicated.
- a housing cavity inlet 6 is provided at one end of the housing chamber 3.
- a housing cavity inlet 6 may be provided at one end of the housing cavity 3, and the housing cavity inlet 6 may be disposed on the side wall of the housing cavity 3, and one or more housing cavity inlets 6 may be disposed; or at the housing cavity 3 where the housing cavity inlet 6 is located
- the volute-shaped or annular flow guiding cavity is arranged to facilitate fluid entering the housing cavity 3, so that the fluid enters along the tangential direction of the cross-section of the housing cavity 3, which can reduce the wear of the vortex wheel 4; the housing cavity inlet 6 can also be disposed in the housing cavity 3 axis At the end, fluid axial input is achieved.
- a flow regulating device such as a damper or a valve at the inlet 6 of the casing cavity, which can better adjust the fluid movement speed and flow rate, can better adjust the separation reaction effect, and the flow regulating device can also adopt automatic control, which can be better realized.
- Flow regulation When the invention is used as a coal dusting machine, the effect of providing a damper at the inlet 6 of the casing cavity is better.
- the invention When the invention is used as a burner, a boiler or the like, it can be ignited at the inlet 6 of the casing chamber, or an igniter can be arranged at the inlet 6 of the casing chamber to realize automatic ignition.
- An automatic feeding device such as a stirrer or a discharger may be disposed on the inlet 6 of the casing cavity to uniformly discharge coal, biomass fuel or garbage, etc. into the inlet 6 of the casing cavity, and a dry desulfurizing agent, etc., when using a fluid fuel, It is also possible to arrange the fuel lance on the housing chamber inlet 6.
- the other end of the housing chamber 3 is provided with a housing chamber outlet 7.
- a housing cavity outlet 7 may be provided at the other end of the housing cavity 3, and the housing cavity outlet 7 may be disposed on the side wall of the housing cavity 3 to better utilize centrifugal force, which may facilitate the connection of the casing cavity outlet 7 to the pipe.
- the cross-section of the housing cavity 3 at the outlet 7 of the housing cavity can also be made into a volute shape, which can better utilize the centrifugal force, can make the fluid discharge more smoothly, can be more energy-saving, and can be arranged on the vortex wheel in the volute.
- the moving device, the fluid shifting device can also be arranged as a plurality of long blades connected in the axial direction, which can act as a boosting impeller, can output the fluid at a higher pressure, and can increase the flow rate.
- the housing chamber outlet 7 can also be placed at the shaft end for axial fluid output. It is also possible to provide a flow regulating device on the outlet 7 of the casing cavity, which can adopt various valves, dampers, etc., and the flow regulating device can adjust the fluid flow, and is adjustable.
- the pressure in the entire housing cavity 3 can improve the functional effect.
- the drive shaft of the present invention having the main structure can be installed horizontally, vertically or obliquely. When installed vertically, the effect is better, and the floor space can be saved.
- Four vertical columns can be arranged on the outer periphery of the casing 1 to form four squares, and beam support can be respectively arranged below and above the casing, and the beam can be disassembled when the equipment is maintained.
- the main structure can be used as a reactor, a burner, a grinding device, etc., and can simultaneously transport the fluid.
- the vortex When the invention is used as a reactor, the vortex can be used to cause molecules to collide with each other, which can promote chemical reaction and achieve catalytic effect. It can be widely used in the chemical industry, and can be used as a denitration device, and can be used for denitration by using hydrogen or hydrocarbons. At low temperatures, natural gas or methanol can be pyrolyzed into hydrogen as a denitration agent; hydrocarbons in the flue gas and hydrogen can also be used as denitration agents, or by adjusting the atmosphere of the furnace or spraying water into the high temperature zone of the furnace. The steam reacts the carbon particles and carbon monoxide in the flue gas to produce hydrogen as a denitration agent, which can reduce the cost and purify the flue gas.
- the flue gas can also be subjected to a dry desulfurization reaction in the casing cavity 3, and an alkali metal or calcium hydroxide can be used as a dry desulfurizing agent, and the desulfurizing agent is pulverized into a fine powder in the casing cavity 3 to participate in the desulfurization reaction.
- the hot gas can be directly supplied to the boiler, the kiln, etc., and the boiler transformation cost can be reduced, and any fuel such as coal, oil, gas, biomass, garbage, coal water slurry, coal powder, etc. can be used.
- a refractory insulation layer is arranged on the inner wall of the casing cavity 3.
- the drive shaft of the vortex wheel 4, the fluid shifting device 5 and the transmission device 2 can be made of high temperature resistant material, and the wind shaft or water spray can be arranged on the transmission shaft of the transmission device 2.
- the cooling device such as a wheel can also spray the water on the wind impeller, and a water receiving tank body is arranged around the wind impeller so that the collected water can be collected and returned to the pool.
- the central axis of the housing cavity 3 is vertically installed, and the housing cavity inlet 6 can be disposed on the lower side wall of the housing cavity 3, which can better utilize the gravity to realize fuel sorting, so that the larger fuel of the granularity is always in the housing cavity.
- 3 Lower combustion, so that the burnt ash leaves the combustion zone upwards with the airflow, so that the fuel can achieve uniform vortex combustion in the casing cavity 3, and the vortex combustion and eddy current crushing can be used to fully burn the fuel, especially when burning coal or garbage. It can make the coal block or garbage and the like continue to be burned and burned continuously while being continuously burned.
- the fuel is precisely supplied, and the air volume is adjusted, the temperature in the combustion zone can be kept stable and uniform, the furnace temperature can be controlled more accurately, and low-temperature combustion can be achieved, which can eliminate the generation of nitrogen oxides.
- Simultaneous addition of calcium carbonate stone chips can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can achieve sufficient desulfurization by dry method. It is also possible to slightly increase the inner diameter of the housing chamber 3 at the inlet 6 of the housing chamber to better store the fire and maintain combustion. It is also possible to provide an automatic feeding device such as a stirrer and a discharger on the inlet 6 of the casing cavity.
- the plurality of housing chamber inlets 6 can also be separately fed, and the coal, biomass fuel or garbage, etc., and the dry desulfurizing agent can be uniformly discharged into the housing chamber inlet 6 through the automatic feeding device, and the gas and fuel oil are used.
- the fuel spray gun is an automatic feeding device.
- a temperature measuring device can be arranged on the inner wall of the casing cavity 3. The temperature measuring device can adopt a thermocouple, a temperature control instrument and the like, and the temperature measuring device can automatically control the automatic feeding device, and automatically disconnect when the temperature in the furnace reaches the upper limit of the set temperature.
- the automatic feeding device power supply can automatically turn on the power supply of the automatic feeding device when the temperature in the furnace reaches the lower limit of the set temperature.
- a gap can be increased between the lower part of the casing and the transmission shaft, and the air can be cooled to the drive shaft.
- the invention When the invention is used as a grinding device, it can be dry-grinded or wet-grinded, and dry-grinding is more energy-saving.
- the housing cavity inlet 6 When the central axis of the housing cavity 3 is installed vertically, the housing cavity inlet 6 can be disposed on the lower side wall of the housing cavity 3 at the periphery of the vortex wheel 4, and the material to be ground can be discharged from the housing cavity inlet 6 or can be set.
- Automatic unloading device Gravity can be better utilized to achieve particle sorting, so that larger particles of material can always be ground in the lower part of the housing cavity 3, so that the powdered powder particles leave the grinding zone with the airflow and flow out from the casing cavity outlet 7.
- the material can be vortex-grinded in the housing cavity 3, so that the particles collide with each other in the vortex until it is ground. It can grind a variety of powders, pulverized coal, etc., and can also grind flour, etc.
- the milled powder can be dry-grinded or wet-milled, and dry grinding can be realized by using air as a carrier, and wet grinding can be realized by using water as a carrier.
- the casing cavity inlet 6 can be disposed on the outer periphery of the casing cavity 3, and can simultaneously enter the raw materials and air or water to be ground, and the material can be directly sorted after being crushed, and the coarser powder is continuously ground in the casing cavity 3, The fine powder is output through the casing cavity outlet 7 with air or water.
- It can also be used as a coal dusting machine. It can dry the raw coal and spray coal powder from the outlet of the casing cavity. It can be directly injected into the kiln boiler to burn. It is also possible to provide a ash cleaning port on the bottom or side wall of the lower part of the casing cavity 3, which can open the ash cleaning port to clean the materials which are not easy to be ground, or can set the stirring cage or the unloader on the ash cleaning port to realize automatic ash discharging. It can reduce equipment wear and can reduce the extra energy consumption caused by grinding ash and slag when used in coal mill, coal dusting machine, burner, boiler, etc. It can produce high-purity coal powder, which can reduce sulfide, ash, etc. Entering the furnace to burn, it can better remove dust and desulfurization. It can achieve clean combustion of coal.
- the separation effect can be achieved, and the utility model can be used for dust removal, desulfurization, denitration, sewage treatment.
- Technology areas that require separation such as seawater desalination.
- the structure of one embodiment of the present invention is such that, on the basis of the main body structure, at least one inner surrounding wall 8 is disposed on the inner wall of the housing cavity 3, and the outer periphery of the housing cavity 3 is provided with a discharge opening 9 corresponding to the surrounding separator 8.
- the distance between the outer edge of the vortex wheel 4 and the inner wall of the housing cavity 3 can be increased, and one or more can be arranged on the inner wall of the housing cavity 3.
- the channel surrounds the separator 8 and axially isolates the casing cavity 3 into a plurality of regions.
- the surrounding separator 8 can block the axial flow of the fluid along the outer circumference of the casing cavity 3, and the separation effect can be achieved, and the inner wall of the casing cavity 3 and the vortex wheel 4 can be simultaneously
- the increased space between the outer edges can increase the residence time and the moving distance of the fluid in the housing cavity 3, thereby improving the chemical reaction effect.
- the separator has different moving speeds to the outer circumference of the casing chamber 3 due to the difference in specific gravity, particle size, and the like, and the different separators move to different axial regions. The greater the distance between the inner wall of the casing chamber 3 and the outer edge of the vortex wheel 4, the less likely the separation material rebounds to the periphery of the vortex wheel 4, and the better the separation effect.
- the surrounding partitioning body 8 When a partitioning body 8 is disposed on the inner wall of the housing cavity 3, the surrounding partitioning body 8 may be disposed near the housing cavity outlet 7 or spirally disposed along the inner wall of the housing cavity 3, and the plurality of surrounding spacers 8 may also be spirally arranged to enable the separation body.
- the axial flow along the inner wall of the casing cavity 3 toward the inlet 6 end of the casing cavity can improve the separation effect.
- a plurality of surrounding partitions 8 are disposed on the inner wall of the casing chamber 3 in parallel with the cross section of the casing chamber 3, so that fluid can be prevented from flowing axially along the inner wall of the casing chamber 3, and the separation effect can be improved.
- the inner wall of the casing cavity 3 When the inner wall of the casing cavity 3 is disposed around the partition body 8, the inner wall of the casing cavity 3 may be integrated with the surrounding partition body 8, and the inner wall of the casing cavity 3 may be arranged to gradually reduce the inner diameter of the outlet end of the casing cavity 7 . Simplify the structure and improve the separation.
- the vortex wheel 4 is arranged to have a truncated cone shape whose outer diameter gradually increases toward the end of the casing chamber outlet 7 to increase the flow rate.
- the outer periphery of the casing cavity 3 is provided with a discharge port 9 corresponding to the surrounding partition body 8.
- a plurality of discharge ports 9 can be arranged in the axial direction, and a plurality of separation objects can be separated, and the flow rate of each discharge port 9 can be adjusted during use.
- a baffle or a draft tube can also be arranged along the tangential direction of the cross section of the housing cavity 3, which can better cut out the fluid, which can be more convenient for discharging; or a plurality of discharge ports can be arranged on the circumference. 9, can improve the separation effect; can also connect a plurality of discharge ports 9 in the axial direction through the pipeline, which can be more convenient for centralized discharge, and can also connect the inlet end 6 of the casing cavity of the pipeline with the casing cavity 3, The separated gas is again sucked into the housing chamber 3, and the dust removing effect can be improved when used for dust removal.
- a movable sealing and discharging device such as a valve, a damper and a screw conveyor at the discharge port 9, which can adjust the flow rate and adjust the separation effect, so that the separation object can be separated from the shell by the pressure, gravity and centrifugal force in the housing cavity 3.
- the body cavity 3 is discharged, and the movable sealing and discharging device can be intermittently opened to discharge the separated object.
- a dust collecting box can be arranged at the discharge port 9, and the discharge port 9 can be intermittently opened to discharge the ash.
- the inner wall of the housing cavity 3 can be arranged parallel to the axis to avoid axial flow of the separator and improve the separation effect.
- the central axis of the housing cavity 3 of the embodiment can be installed vertically, horizontally or obliquely, and can be arbitrarily set according to requirements, and is used for dressing, seawater desalination, sewage treatment, dry dust removal, etc., and is installed horizontally or obliquely.
- the embodiment can be used as a dust remover, a vacuum cleaner, an oxygen generator, a plasma separator, a cream separator, an odor removing device, an engine exhaust gas purifier, an air purifier, a sewage processor, a water purification device, and desalination.
- Equipment, ore dressing equipment, waste treatment equipment, coal preparation equipment, nuclear fuel selection equipment or nuclear waste treatment equipment can be used to transport fluids at the same time.
- the discharge port 9 is disposed at the lower portion of the casing cavity 3 to better utilize the gravity to discharge the dust.
- the pressure in the housing cavity 3 at the outlet 7 of the housing cavity is greater than the pressure in other regions, which can better ensure that the separation of the other regions does not leak to the outlet 7 of the housing cavity, and the area of the outlet 7 of the housing cavity can be reduced. Or connect the outlet pipe to increase the pressure. It is also possible to provide a damper or valve or the like on the housing chamber outlet 7 to regulate the pressure in the housing chamber 3 at the outlet 7 of the housing chamber.
- the dust suction device When used as sewage and waste gas treatment equipment, it can extract and sort various useful components from sewage and waste gas, and can simultaneously complete dust removal, desulfurization and denitrification.
- various useful components can be selected from dust as dust removal equipment.
- the dust suction device When the dust suction device is used, the gas can be sucked from the casing cavity inlet 6 into the present invention, the dust-free gas can be discharged from the casing cavity outlet 7, the dust is discharged from each discharge port 9, and the movable sealing discharge device is arranged at the discharge port 9.
- the dust can be discharged intermittently or at a fixed flow rate, and dust particles of various components and gases of various components can be separated from each discharge port 9, and dust separation and gas separation can also be completed simultaneously.
- the gas pipe When the dust is removed or the solid particles are separated, the gas pipe may be disposed at the discharge port 9, and the gas outlet pipe is connected to the ash storage bin, and the gas return pipe may be disposed, and the gas return pipe may be connected to the casing cavity inlet 6 or the casing cavity 3 near the inlet end of the casing cavity.
- the dust air flow can be realized; the housing cavity 3 can also be formed into a volute shape, and the separation effect is poor.
- the discharge port 9 is disposed at the outlet of the volute, which is more convenient for cleaning.
- a filter When used as a vacuum cleaner, a filter can be installed in the inlet 6 of the housing cavity to isolate large objects, dust is easy to clean, low noise, cheaper cost, more energy-saving, no dust pollution, and more environmentally friendly. It can process high-temperature flue gas, realize high-temperature flue gas dry dust removal, and dry denitration can be completed simultaneously when hydrogen gas is injected.
- the ash storage box can also be arranged outside the discharge port 9, or a plurality of discharge ports 9 can be combined to share one ash storage box and the ash outlet, which can be more convenient for ash, and can also be used for the burner.
- An air heating pipe is arranged in the gray box, and the heating air is sucked into the inlet 6 of the casing cavity to better cool the dust.
- multi-channel surrounding separators 8 can also be arranged near the inlet of the casing cavity, which can remove the dust first, which can reduce the wear of the equipment, and can also increase the inner diameter of the casing cavity 3, thereby improving the separation effect.
- the denitration reaction zone can be arranged near the outlet of the casing cavity, which can realize denitration after flue gas dedusting; or a plurality of surrounding separators 8 can be arranged near the outlet of the casing cavity, which can be 6 segments near the inlet of the casing cavity.
- the slaked lime powder can be sent to the dry desulfurization reaction zone, or the diaphragm pump can be used to transport the slaked lime milk, so that the flue gas can be completely desulfurized and then the dust is finally removed; or it can be close to the shell.
- Body cavity inlet 6 segments and close to the housing cavity In the 7th section of the mouth, a plurality of surrounding separators 8 are respectively arranged, and a dry desulfurization reaction zone is arranged between the two, and the slaked lime can be sent to the dry desulfurization reaction zone, and the dust can be removed first, then the dry desulfurization is completed, and finally completed. Purification of dust and the like.
- an oxygen generator When used as an air separation device, an oxygen generator, a nitrogen generator, or a rare gas preparation device, air can be taken into the present invention, and various gases such as oxygen, nitrogen, and inert gas can be separated from each discharge port 9 directly. Collect and use various gases. When special needs are required, the various gases are separated twice to obtain a high purity gas.
- an oxygen generating apparatus air can be sucked into the present invention, and nitrogen gas or the like can be separated from the casing chamber outlet 7 to separate oxygen from the discharge port 9.
- the low cost of oxygen production enables pure oxygen combustion in boilers, kilns, engines, etc., which can reduce energy consumption, improve thermal efficiency, and eliminate nitrogen oxide emissions. Exhaust gas recirculation can also be used to reduce combustion temperatures and reduce equipment material requirements.
- the mineral or garbage When used as a mineral processing equipment or a garbage disposal equipment, the mineral or garbage can be pulverized into granules, and the granules can be sent to the present invention by water or air for wet selection or dry selection: the water can be recycled, and the metal elements having a large specific gravity can be The heavy elements are separated from the discharge port 9, the useless components are separated from the outlet of the casing cavity 7, and the useless components can be landfilled after dehydration, and the organic components can be naturally fermented and degraded, thereby achieving harmlessness, eliminating environmental pollution and realizing resource recycling. use.
- the useful ingredients, various minerals and useless components can be separated from the respective discharge ports 9 respectively.
- the useless components When the garbage is disposed, the useless components can be landfilled, and the organic components are fermented and pressed into granular organic fertilizers, which can completely eliminate environmental pollution and realize resource recycling. use.
- coal When used as a coal preparation equipment, coal can be made into coal powder, which can be selected by dry or wet selection.
- the sulfide, metal element, precious element, radioactive element and common mineral in the coal can be 9 points from the discharge port.
- Selecting resources for utilization, high-purity pulverized coal or coal-water slurry can be separated from the shell cavity outlet 7, which can be made into high-purity pulverized coal or high-purity coal water slurry, or the coal-water slurry can be dehydrated by dewatering sieve to make high purity.
- the briquettes can be used to transport and burn high-purity coal to achieve clean combustion of coal. It can be compared with natural gas, and the tail gas can be desulfurized and dedusted.
- fresh water When used as a seawater desalination apparatus, fresh water can be separated from the casing chamber outlet 7, high-concentration brine can be separated from the discharge port 9, and salt can be obtained by evaporation.
- the standard water, organic components, gas components, heavy elements, metal elements, sand dust, high-concentration brine or brine mixture can be discharged from different discharge ports 9.
- the invention provides a mother and a child, and the secondary treatment and multi-stage treatment of the discharged high-concentration brine, organic components, gas components and the like can further separate a plurality of salts, organic components and gas components.
- the salt in the sewage can be used Dissolve, heavy metal, etc., refer to seawater desalination, separate the sewage containing high concentration of organic components from the shell cavity outlet 7 for biochemical treatment, and the treated water returns to the sewage of the primary treatment system, and the water from the standard is obtained.
- the discharge port 9 can be separated and discharged.
- the seawater desalination can be used to separate heavy elements in the water, retain beneficial elements, and clean the organic components, chlorine, microorganisms, and eggs in the water.
- the heavy water can be separated, so that the tap water quality exceeds the mineral water and snow mountain spring water. Heavy water can also be extracted for industrial use.
- the crude oil When used as an oil refining equipment, the crude oil can be directly sucked into the present invention, and the crude oil is affected by the vortex fluid movement and the centrifugal force generated by the vortex and the gravity, thereby achieving low temperature cracking and realizing separation of various components.
- Heavy elements, metals, sulfur, asphalt, paraffin, heavy oil, lubricating oil, diesel oil, kerosene, gasoline, etc. may be sequentially discharged from the respective discharge ports 9 near the inlet 6 of the casing chamber.
- the two oil intermediates can be re-introduced into the crude oil to be separated again, and the mother and child can be set up according to the present invention, and the various components of the present invention are subjected to secondary separation and multi-stage separation, thereby realizing various components.
- High purity can extract high-purity gasoline, diesel, lubricating oil, wax, a variety of petroleum products, sulfur, heavy metals, metals, lead, radioactive elements, etc., so that the oil is completely lead-free, no radioactive elements.
- the whole production process is non-polluting, there is no waste water, exhaust gas emission, the refining process is completely environmentally friendly, and the resources are fully utilized, which can greatly reduce the refining cost.
- Low-temperature cracking greatly reduces the damage of high-molecular structure of crude oil by high temperature, reduces the production of petroleum gas, petroleum slag, asphalt, wax, etc., can greatly improve the oil yield and improve the oil yield of high-quality oil.
- the present embodiment when used as a grinding device, when a plurality of surrounding separators 8 are disposed on the inner wall of the casing cavity 3 near the casing cavity outlet 7, the powders of various particle sizes can be sorted, and the closer to the casing cavity outlet 7 The finer the powder selected at the discharge port 9 is, the ultrafine powder or the nano powder can be produced, and the carbene can also be produced.
- the raw coal can also be dry-ground, and the dry selection can be completed at the same time.
- Various minerals in the coal can be selected from the respective discharge ports 9, and the coal powder can be sprayed from the outlet of the casing cavity 7 and can be directly injected into the kiln boiler to be burned.
- the heat storage can be better.
- a plurality of surrounding partitions 8 are disposed on the inner wall of the casing chamber 3 near the outlet of the casing chamber 7, the dry dust removal in the furnace can be better achieved.
- the flue gas When used as a range hood, the flue gas can be sucked from the casing cavity inlet 6 into the present invention, the soot can be separated, the flue gas discharge is completely environmentally friendly, and the treated smokeless gas is discharged from the casing cavity outlet 7, and the waste oil is discharged.
- the port 9 is discharged.
- the machine When used as an air purifying device, it can be used as a new indoor air purifier, and can separate clean air from the casing cavity outlet 7 and separate dust particles from the discharge port 9. Also the master of the fresh air system The machine can send the separated clean air into the room and leave the dirty air outdoors.
- a lighter gas When used as an odor-eliminating device, a lighter gas can be separated from the casing cavity outlet 7, and a heavier gas can be separated from the discharge port 9, and can be treated by incineration, collection or chemical reaction for different odorous gases. can.
- oil and gas recovery equipment When used as an oil and gas recovery equipment, a variety of oil vapors can be recovered, and clean air can be separated from the outlet of the casing chamber 7, and oil and gas can be separated from the discharge port 9, and the separated oil and gas can be recovered by means of condensation, spraying, solvent absorption and the like.
- the recovered residual gas can be re-introduced into the casing cavity inlet 6 to participate in the separation again, forming a closed cycle, and finally achieving complete recovery.
- the useful elements with a small specific gravity and a large specific gravity can be separated from the casing cavity outlet 7 and the discharge port 9, respectively, and multi-stage sorting can be adopted. Purification can be done, which can greatly improve the selection effect and make the tailings more environmentally friendly.
- the high-radioactive elements in the nuclear waste can be extracted and re-introduced into the nuclear reactor.
- the core is turned into a low-level element, and the low-level material glass can be solidified and landfilled.
- the structure of the second embodiment of the present invention is that, on the basis of the above structure, at least one of the inner walls of the casing cavity 3 is close to the outer edge of the vortex wheel 4.
- the inner wall of any one of the casing cavities 3 can be brought close to the outer edge of the vortex wheel 4 as needed, and the inner wall of the casing cavity 3 is close to the outer edge of the vortex wheel 4, so that the eddy current friction can be more severe, and the inner wall of a section of the casing cavity 3 close to the inlet 6 of the casing cavity can be generally close.
- the engine exhaust processor can improve the three-way catalytic reaction effect, it can also use the exhaust gas from the engine to connect the casing cavity inlet 6 to directly push the equipment to operate, which can simplify the structure, can replace the muffler at the same time, and can also import the casing cavity 6 and
- the housing chamber outlets 7 are respectively disposed in the axial direction to allow the exhaust shaft to be axially extended.
- the transmission device 2 can utilize the existing full-floating bearing used in the turbocharger, and can utilize the lubrication system and the cooling system of the engine.
- An engine intake booster may also be disposed at either end of the housing chamber 3, and may be generally disposed at the housing chamber inlet 6 end, the housing chamber inlet 6 may be disposed on the side wall of the housing chamber 3, and the housing chamber outlet 7 may be disposed at the shaft end. It is more convenient to connect the exhaust pipe, which simplifies the structure.
- the engine intake booster may adopt the structure of various existing engine turbochargers, and the engine intake booster pressurizes the intake of the engine.
- the vortex wheel 4 drives the booster impeller of the engine intake booster to rotate, and the turbocharger 4 is used instead of the turbocharger turbine.
- turbocharger can also be used as an engine turbocharger, and the turbocharger and the three-way catalyst can be used. Replace all. It is usually close to the inner wall of a section of the housing cavity 3 near the inlet 6 of the housing cavity The outer edge of the vortex wheel 4.
- the embodiment can also be used as a burner, a reactor, a grinding device, a beneficiation device, etc., and can be used as a burner to remove dust in the furnace, and the fuel can be placed in a region close to the outer edge of the vortex wheel 4 on the inner wall of the casing cavity 3.
- the flue gas can be disposed on the inner wall of the casing chamber 3 to surround the partition 8 to perform dry dust removal, and dust of various sizes can be separated from each discharge port 9.
- the flue gas When used as a reactor, it can be used for flue gas denitration, dry desulfurization, dry dedusting, chemical reactor, etc., so that the flue gas can complete denitration reaction and dry desulfurization in a section of the inner wall of the casing cavity 3 close to the outer edge of the swirl wheel 4.
- hydrocarbons and hydrogen generated in the flue gas of the kiln can be used as a denitration agent, and an alkali metal or calcium hydroxide can be used as a dry desulfurizing agent, and the desulfurizing agent is continuously pulverized into fine powder in the casing cavity 3.
- the fine powder continuously participates in the desulfurization reaction, so that the flue gas can be disposed on the inner wall of the casing cavity 3 around the partition body 8 to perform dry dust removal, and dust of various sizes can be separated from each discharge port 9.
- the chemical reaction can be promoted, and the reacted substance can be sorted.
- the material can be ground in a region of the inner wall of the casing cavity 3 close to the outer edge of the vortex wheel 4, and a region surrounding the separator 8 is disposed on the inner wall of the casing cavity 3 to complete powder sorting. Powders of various particle sizes or specific gravities can be separated from the respective discharge ports 9.
- the use of water as a transport medium in dressing is better for wet grinding and wet selection.
- the structure of the third embodiment of the present invention is: on the basis of the above structure, the housing chamber inlet 6 communicates with the shower chamber 10, the shower chamber 10 is provided with a shower chamber inlet 11, and the shower chamber 10 is provided with a plurality of shower devices 12.
- the shower chamber 10 may be disposed outside the casing cavity inlet 6.
- the casing cavity inlet 6 may be externally connected to the shower chamber 10.
- the casing cavity inlet 6 may be arbitrarily disposed on the side wall or the shaft end of the casing cavity 3 according to a specific structure, and the shower room 10 A spray tower or a spray box of various structures can be used, or the spray chamber 10 can be directly replaced by a flue, which can simplify the structure and save space, and the central axis of the shower chamber 10 can be horizontally or vertically.
- One or more shower chamber inlets 11 may be provided on the end face or side wall of the spray chamber away from the inlet 6 end of the housing chamber.
- the shower room 10 is provided with a plurality of shower devices 12, and the shower device 12 can adopt various nozzles or nozzles of various structures, and a plurality of nozzles, nozzles and the like of various structures can be disposed in the shower chamber 10, and can be installed in the shower room.
- a plurality of nozzles or nozzles are densely arranged around the inner wall of the outer circumference, and water is sprayed toward the center of the shower chamber 10 in the radial direction to form a dense atomization zone in the shower chamber 10. It is also possible to provide a water jacket cavity on the outer wall or the inner wall of the shower room 10, and uniformly distribute the nozzle or the nozzle on the inner wall of the shower chamber 10 to communicate with the water jacket chamber, thereby simplifying the structure.
- a vortex nozzle to spray in the axial direction of the shower chamber 10 in the direction of countercurrent flow of the flue gas, which simplifies the structure.
- a plurality of water pipes may be disposed in the shower room 10, and a spray head is arranged on the pipe wall to maximize the dense atomization of the water liquid.
- Spray The device 12 is connected to a water supply device that includes a pump, a pipe, a sedimentation tank, or a water tank.
- the water supply device can continuously spray a liquid such as water or alkaline water into the shower chamber 10 through the shower device 12.
- One or more liquid outlets may be disposed in the lower portion of the shower chamber 10, so that the water can flow out from the lower portion of the shower chamber 10 into the pool of the water supply device to form a circulating liquid supply.
- the inner wall of the shower room 10 can also be protected by glass scales.
- the spray chamber 10 can also be made of acid-resistant stainless steel or other corrosion-resistant materials, which simplifies the manufacturing process.
- the outer wall of the shower room 10 can also be insulated according to the specific conditions to avoid freezing.
- the discharge port 9 near the end of the casing cavity outlet 7 can also be connected to the casing cavity inlet 6 or the casing cavity 3 near the casing cavity inlet 6 through a pipe, so that the separated steam-water mixture can be re-entered into the casing cavity 3 for secondary separation, and an air flow can be formed.
- the channel allows the separation to be smoothly discharged.
- the transmission shaft of the present invention of the present invention can be used for transverse, oblique, and vertical installation, and can be used for boiler, kiln, etc. to simultaneously complete air intake, air supply, dust removal, desulfurization, and denitrification.
- the flue gas can be used to complete the primary dust reduction in the shower chamber 10, and the water mist is cleaned in the casing cavity 3, and finally the dehydration is completed, and finally the flue gas is completely purified.
- the liquid supply device 23 is disposed on the inner wall of the outer periphery of the casing chamber 3.
- the liquid supply device 23 may be arbitrarily disposed on the outer peripheral wall of the casing chamber 3 as needed.
- the liquid supply device 23 may adopt an outlet pipe, a water outlet or a nozzle, a nozzle, etc., and an auxiliary facility of the liquid supply device 23 includes a pump, a pipe, a flow control valve, A device such as a sedimentation tank or a water tank may flow or spray a liquid such as water or alkaline water into the casing chamber 3 through a liquid supply device 23 such as a water pipe, a water outlet or a shower head.
- the vortex wheel 4 rotates to make the water liquid and the flue gas more fully contact and collide, so that the flue gas is thoroughly washed and purified by the water liquid, and the swirling wheel 4 rotates to rotate the water liquid on the inner wall of the casing cavity 3, so that the separated matter together with the water liquid discharge.
- the discharge port 9 near the end of the casing cavity outlet 7 can also be connected to the casing cavity inlet 6 or the casing cavity 3 near the casing cavity inlet 6 through a pipe, so that the separated steam-water mixture can be re-entered into the casing cavity 3 for secondary separation, and an air flow can be formed.
- the channel allows the separation to be smoothly discharged.
- one or more liquid supply devices 23 are disposed near the end of the casing cavity outlet 7 to spray clean water into the casing cavity 3, which can improve the dust removal effect, and the clean water can be used for desulfurization and dust removal of the supplementary water or the treated clean water.
- the provision of a plurality of liquid supply devices 23 in the axial direction enables multi-stage purification, and the effect is better.
- a ring corresponding to the liquid supply device 23 on the inner mouth of a surrounding separator 8 as needed.
- a liquid supply device 23 Surrounding the water retaining ring around the periphery of the vortex wheel 4, a liquid supply device 23 is arranged around the water retaining ring to the end of the casing cavity outlet 7.
- the surrounding water retaining ring can block the water liquid from leaking axially to the inlet end of the casing cavity 6 and surround the water retaining ring.
- the expansion of the inner diameter of the ring opening toward the end of the outlet 7 of the casing cavity can better prevent leakage of water to the inlet 6 of the casing chamber by centrifugal force.
- a dry denitration reaction zone or a dry desulfurization, denitration and dedusting combined reaction zone is arranged, and the water liquid cleaning is realized in the second half of the axis of the casing cavity to complete the wet dust removal dehydration or the wet denitration dust removal dehydration to realize the flue gas purification.
- a plurality of surrounding separators 8 may be disposed near the inlet 6 end of the casing cavity to dry the large particles.
- the surrounding separator 6 can be disposed adjacent to the inlet 6 of the casing cavity, and the dry grinding material and the wet collecting powder can be realized, and the collection efficiency can be greatly improved.
- One or more surrounding partitions 8 may be disposed on the inner wall of the casing cavity 3 on the side of the casing inlet 6 on the surrounding water retaining ring.
- the discharge port 9 corresponding to the surrounding partition 8 may be connected to the casing cavity inlet 6 through the pipe. The separator is re-entered into the housing cavity inlet 6.
- a plurality of surrounding partitions 8 may be disposed on the inner wall of the casing cavity 3 on the side of the casing inlet 6 on the surrounding water retaining ring, and the discharge port 9 near the inlet 6 side of the casing may be connected to the casing cavity inlet 6 to leave the remaining
- the port 9 has a portion of the dry material.
- the powder can be collected by wet method, and the coarser powder can be selected and sent back to the inlet of the casing cavity to continue grinding, which can better control the fineness of the powder.
- the transmission shaft can be placed transversely, obliquely, or vertically. It can replace the existing dust collector, desulfurization tower, and denitration equipment, and can be widely used in various exhausts of various furnaces, boilers, incinerators, vehicles, and the like.
- the field of treatment can be used in all areas where flue gas is treated.
- a strong oxidizing agent such as hydrogen peroxide and urea may be added to the aqueous solution, and nitric oxide may be oxidized to polynitrogen oxide, and the reaction may be absorbed by urea or caustic soda, lime or calcium carbonate.
- the amount of ash is large, and the nitrate, halide and salt in the water can be taken away in large quantities, so that the boiler and the like can no longer produce desulfurization waste water and slag waste water, which can greatly improve environmental protection benefits.
- the water consumption is very small, a little water can be used, and the energy consumption of the pump is greatly reduced, which is basically negligible.
- the odor component can be better collected when the chemical odor is removed, and the odor component can be reacted with the acid and alkali to better remove the odor.
- the embodiment can realize the dust removal by the wet method, can remove dust more effectively, remove harmful substances, and can make the flue gas more environmentally friendly.
- the structure of the fifth embodiment of the present invention is: based on the above structure, the housing cavity 3 is provided with a housing cavity inlet 6 at the axial end of the housing cavity 3, and the housing cavity outlet 7 is provided at the other end of the housing cavity 3. a housing can be provided at the axial end of the housing cavity 3 The body cavity inlet 6 is provided with a housing cavity outlet 7 at the other end of the housing cavity 3, so that the fluid shaft can be axially extended.
- the invention of the embodiment can be used as an engine exhaust gas processor, and can directly drive the equipment operation by connecting the exhaust gas discharged from the engine to the casing cavity inlet 6, which can simplify the structure, can simultaneously replace the muffler, and can make the exhaust gas shaft enter the shaft, and the transmission device 2
- the existing turbocharged full-floating bearing can be utilized, and the engine's lubrication system and cooling system can be utilized.
- the structure of the sixth embodiment of the present invention is: on the basis of the above structure, the heat collecting device 13 is disposed on the inner wall of the casing cavity 3.
- the distance between the outer edge of the vortex wheel 4 and the inner wall of the casing cavity 3 can be increased, and a heat collecting pipe or a heating heat box can be arranged on the inner wall of the casing cavity 3 as the heat collecting device 13, and water, oil or gas can be used as the mining. Heat medium.
- the heat collecting device 13 can be disposed close to the inner wall of the casing cavity 3.
- the heating pipe can have a certain gap between the heat collecting pipe and the inner wall of the casing cavity 3, so that the heat efficiency can be better improved.
- a protective plate can also be arranged on the heating pipe, and the protective plate can be arranged on the windward side to improve the heating area and reduce the surface wear of the heating pipe, thereby playing a protective role.
- the heat collecting device 13 can be a heating tube device used in any of the existing boilers, and a boiler of various pressures can be realized as needed.
- a medium-pressure, high-pressure, ultra-high pressure boiler a high-pressure heating pipe can be arranged near the lower part of the casing cavity 3
- a low-pressure heating pipe is arranged near the upper part of the casing cavity 3
- a boiler pump is used to achieve a forced circulation between the low-pressure heating pipe and the high-pressure heating pipe. Can increase heating efficiency.
- An air heat exchange device may also be disposed on the inner wall of the casing cavity 3.
- the air heat exchange device may adopt a heat collecting pipe to pass air entering the inlet 6 of the casing cavity through the heat collecting pipe, and the air heat exchange device may heat the air entering the inlet 6 of the casing cavity.
- the air heat exchange device can be disposed behind the heat collecting of the liquid heat collecting device 13, so that the flue gas can be collected by the liquid heat collecting device 13 and then collected by the air heat exchange device, so that the heat energy can be more fully utilized.
- a ash cleaning port may also be arranged on the lower side wall of the casing cavity 3, and the ash cleaning port may be periodically opened to clean the particles which are not easily pulverized, or the stirring hopper or the unloader may be arranged on the ash cleaning port to realize automatic ash discharging.
- the embodiment can be used as a plurality of boiler equipments, and can adopt any fuel such as coal, oil, gas, biomass, garbage, coal water slurry, coal powder, etc., and can be provided with a refractory thermal insulation layer on the inner wall of the casing cavity 3, the vortex wheel 4,
- the transmission shaft of the fluid dialing device 5 and the transmission device 2 can be made of high temperature resistant material, and the cooling shaft of the transmission shaft of the transmission device 2 can also be provided with a wind impeller or a water spray cooling wheel, or the water can be sprayed on the wind impeller.
- the water tank body is arranged around the wind impeller, so that the collected water can be collected and returned to the pool.
- the central axis of the housing cavity 3 can be installed vertically or horizontally, and the vertical installation effect is better.
- the housing cavity inlet 6 is disposed on the lower sidewall of the housing cavity 3, and the utility model can better utilize the gravity to realize fuel sorting.
- the larger particle fuel is always burned in the lower part of the casing cavity 3, so that the burnt ash leaves the combustion zone upwards with the airflow, so that the fuel can be in the casing cavity 3 Uniform vortex combustion can be realized, and the fuel can be fully burned by vortex combustion and eddy current crushing. Especially when coal is burned, the coal block can be continuously burned and burned while being continuously burned.
- the fuel is precisely supplied, and the air volume is adjusted, the temperature in the combustion zone can be kept stable and uniform, the furnace temperature can be accurately controlled, and low-temperature combustion can be achieved, which can eliminate the generation of nitrogen oxides.
- Simultaneous addition of calcium carbonate stone chips during coal combustion can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can achieve sufficient desulfurization by dry method.
- the vortex formed by the casing cavity 3 can promote the velocity of the airflow on the surface of the heating device 13, which can greatly improve the heating efficiency, greatly reduce the heating area, and greatly reduce the cost.
- the vortex motion greatly extends the moving distance of the hot air flow in the housing cavity 3, so that the heat energy can be fully transmitted, and efficient and full heat recovery can be realized.
- a gap can be increased between the lower part of the casing and the transmission shaft, and the air can be cooled to the drive shaft.
- This embodiment is a high-efficiency boiler capable of burning any fuel, which can achieve a burn-up rate of 100%, completely avoiding black smoke, and greatly reducing carbon monoxide, sulfur and nitrate emissions.
- the structure of the seventh embodiment of the present invention is: on the basis of the above structure, the automatic feeding device 14 is disposed on the inlet 6 of the casing cavity, and the temperature measuring device 15 is disposed on the inner wall of the casing cavity 3, and the temperature measuring device 15 controls the automatic feeding device 14.
- An automatic feeding device 14 such as a stirrer or a discharger may be disposed on the inlet 6 of the casing cavity, or a plurality of casing inlets 6 may be respectively provided for feeding, and may be uniformly discharged into the inlet 6 of the casing through the automatic feeding device 14.
- the fuel spray gun is an automatic feed device 14.
- the temperature measuring device 15 can be arranged on the inner wall of the housing cavity 3.
- the temperature measuring device 15 can adopt a thermocouple, a temperature control instrument and the like, and the temperature measuring device 15 can control the automatic feeding device 14 through the temperature control instrument, when the temperature in the furnace reaches the setting When the upper limit of the temperature is set, the power supply of the automatic feeding device 14 is automatically turned off, and when the temperature in the furnace reaches the lower limit of the set temperature, the power supply of the automatic feeding device 14 is automatically turned on.
- the furnace temperature can be controlled more accurately, and the burner, the boiler and the like can be automated.
- the structure of the eighth embodiment of the present invention is: on the basis of the above structure, the flow regulating device 19 is disposed on the outlet 7 of the casing cavity.
- the flow regulating device 19 can be disposed on the outlet 7 of the casing cavity.
- the flow regulating device 19 can adopt various valves, dampers, etc., and the flow regulating device 19 can adjust the flow rate and adjust the pressure in the casing cavity 3 to better achieve the effect.
- the flow rate and pressure can be adjusted, and the effect can be better improved.
- the structure of the ninth embodiment of the present invention is such that, on the basis of any of the above structures, a plurality of fluid-swapping devices 5 are disposed on the outer circumference of the vortex wheel 4 and in the axial direction.
- a plurality of fluid-swapping devices 5 may be disposed on the outer circumference of the vortex wheel 4 and in the axial direction, so that the fluid-swapping device 5 can be evenly distributed on the outer circumference of the vortex wheel 4.
- Available at A plurality of blades of arbitrary structure are evenly distributed on the outer circumference of the vortex wheel 4 as a fluid shifting device 5.
- the blades can be inclined at an angle to the axial direction, and can function as an axial flow impeller, which can supercharge the fluid and promote the fluid axial direction.
- the fluid dialing device 5 can also adopt various structures such as round sticks and round tubes, and the effect is poor. Other conveying equipment is needed to help the fluid to enter and exit the present invention, and is generally not used.
- the fluid shifting device 5 can be dispersed in a sporadic arrangement, or can be arranged to have a certain inclination angle with respect to the axial or radial direction, or can be configured as an axial flow impeller blade structure, can increase the airflow disturbance, can improve the effect, and adopt the blade
- the whole plate can be segmented and cut, and the plate can be twisted to form a plurality of ternary blades with integrated roots. It can be hand-made or stamped by stamping equipment, which simplifies manufacturing.
- the blades may be integrally connected to the vortex wheel 4 in the axial direction, and the plurality of blades may be radially disposed on the outer circumference of the vortex wheel 4. It is also possible to arrange the blades as a whole strip and to be disposed on the outer circumference of the vortex wheel 4 in the axial direction.
- the disadvantage is that the fluid cannot be axially swayed, and the fluid is not better broken, the effect is poor, and generally it is not used.
- the fluid dialing device 5 can form an axial and radial displacement of the fluid, so that the fluid can form a oscillating vortex between the outer circumference of the vortex wheel 4 and the inner wall of the housing chamber 3, which can better circulate the fluid.
- the distance between the outer edge of the fluid dialing device 5 and the inner wall of the housing cavity 3 can be arbitrarily adjusted as needed, and the closer the distance, the more intense the fluid oscillation friction.
- This embodiment can increase the fluid flow rate and pressure, and can improve the crushing strength when used for grinding.
- the fluid can be simultaneously transported out, and the fluid is separated and purified in the invention.
- the fluid After the vortex wheel 4 rotates, the fluid forms a vortex in the casing cavity 3, and the fluid is rotated by the outer periphery of the vortex wheel 4, and the vortex causes the movement speed of each particle in the fluid to be different, so that each particle in the fluid forms an independent movement.
- Individuals can better use centrifugal force to separate particles of different specific gravity, and use the centrifugal force generated in the vortex to separate and sort the different specific gravity materials in the fluid.
- the eddy current advances spirally along the axial direction, and the individual moving bodies of different specific gravity move to the periphery of the eddy current at different speeds, and the particles or particles with larger specific gravity are more easily and quickly settled onto the inner wall of the casing cavity 3.
- the separation of various separations is achieved by the combined effects of fluid motion, centrifugal force and gravity.
- a plurality of separators of different specific gravity are respectively moved to different axial regions of the housing cavity 3, and are respectively discharged through the axially different discharge ports 9, thereby finally achieving separation, sorting or removal of pollutants, etc. Separation of solutes in solution.
- the fluid is gradually separated and purified during the axial movement.
- flue gas purification it can make flue gas and water liquid fast enough The rapid contact makes the flue gas fully washed and purified by the water liquid, so that the flue gas fully washed and purified can be fully dehydrated, discharged from the casing cavity outlet 7, and the eddy current is used to promote the chemical reaction to realize the desulfurization and off-slurry, and the flue gas is completely purified.
- Adjusting the flue gas flow can achieve high removal of dust particles in the flue gas, and can remove the height of black smoke, dust, sulfur dioxide, nitrogen oxides, dioxins, and some chemical odors to achieve the height of the flue gas.
- Purification can realize the source control of air pollution, realize the source control of cockroaches, and finally solve the air pollution and eliminate cockroaches. Separation can solve water pollution and solve environmental pollution.
- the eddy current is realized by eddy current, and the fuel is sorted by centrifugal force, so that the larger fuel is always burned in the combustion zone, so that the burnt ash leaves the combustion zone with the gas flow, so that the fuel can achieve uniform eddy current in the casing cavity 3.
- Combustion, vortex combustion and vortex breaking can be used to fully burn the fuel.
- the fuel When the solid fuel is burned, the fuel can be continuously burned and burned while being continuously burned. Regardless of the fuel used, the fuel is precisely supplied, and the air volume is adjusted, the temperature in the combustion zone can be kept stable and uniform, the furnace temperature can be controlled more accurately, and low-temperature combustion can be achieved, which can eliminate the generation of nitrogen oxides.
- Simultaneous addition of calcium carbonate stone chips during coal combustion can achieve dry desulfurization in the furnace, uniform temperature in the furnace, and eddy current to promote the reaction, which can achieve sufficient desulfurization by dry method.
- the vortex formed by the casing cavity 3 can promote the velocity of the airflow on the surface of the heat collecting device 13, can improve the heating efficiency, can reduce the heating area, and can reduce the cost.
- the vortex motion makes the moving distance of the hot air flow in the housing cavity 3 prolonged, so that the heat energy can be fully transmitted, and finally the high-efficiency heat is realized. It can realize dust removal in boilers, burners, etc., which can make emissions more environmentally friendly.
- the use of water mist cleaning to achieve wet dust removal can make the flue gas completely environmentally friendly.
- the eddy current is used to realize the eddy current grinding, so that the material is gradually pulverized by the frictional collision during the movement of the airflow, and the high-efficiency grinding can be realized, and the ultrafine powder can be ground.
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Abstract
一种分离反应粉磨机,包括壳体(1)和传动装置(2),壳体上设置传动装置,壳体内设置壳体腔(3),壳体腔内设置涡流轮(4),传动装置与涡流轮连接,壳体腔一端设置壳体腔进口(6),壳体腔另一端设置壳体腔出口(7)。上述分离反应粉磨机充分利用了涡流运动和流体运动,利用涡流使分子相互碰撞摩擦,使流体被逐渐分离,可实现烟气高度净化,可解决大气污染和水污染,可实现燃料充分低温燃烧,从而解决环境污染。
Description
本发明涉及分离器、离心机、污水处理、净水、海水淡化、海洋化工、选矿、选煤、核燃料精选、核废料处理、炼油、油气回收、垃圾处理、空气净化、除尘、吸尘、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、反应器、锅炉、燃烧器、粉磨等领域,具体是一种分离反应粉磨机,可实现粉磨、化学反应、分离三大功能,三大功能即可单独使用也可组合使用。
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。大气污染已严重影响到地球生态圈,究其原因主要是技术原因,现有技术无法将烟气中的颗粒物清除干净,PM2.5排放指标都难以实现。布袋除尘和电除尘一般只能做到粉尘含量20毫克/标方左右,即使增加湿式电除尘多级处理后除尘效果只能做到5毫克/标方左右。
现有的空气净化设备净化效果太差,脱硫脱硝设备造价高,运行、维护费用高,能耗高,脱除效率低,效果不好,脱硫、湿式除尘、脱硝多采用喷淋法,无法将颗粒物、硫氧化物分子、氮氧化物分子等充分吸附溶解,造成除尘、脱硫、脱硝效率低下。现有的除尘设备有旋风除尘、电除尘、湿式电除尘、布袋除尘等,普遍存在除尘效果太差,能耗大等缺陷,粉尘污染已成为大气污染最重要的污染源,成为霾的罪魁祸首。
现有的除黑烟、除异味设备净化效果太差,对黑烟、许多化工异味、二恶英基本无法处理,黑烟、异味气体污染已成为重要污染源,二恶英是人类制造的最可怕的有机污染物,已严重影响到人类的生存。大气中的重元素颗粒物已经严重威胁人类健康。
现有的车船尾气处理设备处理效果太差,普遍没有除尘、脱硫,三元催化脱硝效果太差,旧车基本无用,车船尾气排放已成为重要的大气污染源。
现有吸尘设备吸尘效果不理想,噪音大,有微尘颗粒污染,除尘后处理灰尘麻烦。
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,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蒸馏裂解法,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,造成严重的燃油污染。
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,还要尾气脱硫处理,还脱不干净造成大气环境污染,煤里面的各种金属元素等有价值的好东西都没能选出来,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。煤炭净选已刻不容缓。
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,造成严重的环境隐患。
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,造成严重的大气环境污染,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。
现有的反应器设备有反应釜、催化剂反应罐或塔等,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,特别是燃煤锅炉燃尽率只有80%左右,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,超细粉体制备困难等。
发明内容
利用全新的分离方法,利用全新的涡流分离原理,充分利用流体运动,利用涡流,使流体受涡流影响,在圆周运动离心力的作用下,利用涡流实现分离,使不同体积、比重的粒子相互之间实现分离。不同体积、比重的粒子向涡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涡流外围,比重小的粒子会更晚的运动到涡流外围,利用这一点实现不同物质的分选。涡流中的每一个点相互之间都存在相对运动,利用涡流的作用,可以将胶合、溶解在一起的分子分开,使涡流中的每一个分子、原子等各种粒子形成不同运动速度的独立运动个体,利用涡流运动和离心力以及重力等使不同颗粒度大小、不同比重的物质进入不同区域。可以使溶液中的溶质与溶剂实现分离,可以将不同的溶质实现分离。利用涡流使涡流中的每一个颗粒物、分子、原子等各种粒子形成不同运动速度的独立运动个体,在圆周运动离心力以及运动惯性的作用下与水流、水雾充分碰撞接触,使烟气被水充分洗涤,使烟气中的颗粒物等进入水中,实现烟气净化。向本发明内输入碱性液体、空气等时,还可用于烟气脱硫、脱硝、除异味等领域,可大大提高设备运行效率,降低造价和运行成本。利用涡流使分子相互碰撞摩擦,可大大促进化学反应,可实现催化效果,可作为脱硝设备、化学反应器等使用。利用涡流燃烧加涡流破碎使燃料充分燃烧,特别是燃煤时,可使煤块在不断燃烧的同时被不断的剥离破碎燃烧充分,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,可彻底杜绝氮氧化物产生。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,涡流促进反应,可彻底实现干法充分脱硫。可实现锅炉除尘脱硫脱硝一体化,使锅炉实现彻底环保。本发明可实现更洁净的除尘、更洁净的净化空气、更洁净的净化排出油烟、更洁净的处理污水、更廉价的实现海水淡化、更充分的利用水资源、更充分提取海洋资源、更高效率的选矿、更洁净的处理垃圾、更高效率的炼油等。本发明可广泛应用于各种分离
设备领域。可用它作为新型离心机、分离机使用,它的分离效果更好,可实现各种物质成份的分离、分选、提取、提纯。
本发明可作为除尘器使用,可采用干式除尘或湿式除尘,不但可以将PM2.5颗粒物清除干净,而且可以将PM0.01的颗粒物清除干净,基本可实现无尘化排放,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。
本发明可将黑烟清除干净;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;水液采用碱性液体或加入各种脱硫剂时,可用于烟气脱硫、脱硝等领域,实现湿式除尘、湿式脱硫、湿式脱硝一步完成,可大大提高设备运行效率。
本发明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。
本发明可作为车船尾气处理器使用,可完成除尘、除烟,可同时取代三元催化器,可永不堵塞、永不老化,可使尾气在本发明内完成三元反应,实现脱硝、除碳氢化合物、除一氧化碳,可将尾气中的颗粒物、氮氧化物等高效清除。
本发明可作为油气回收设备使用,可回收多种油蒸汽。
本发明可作为抽油烟机使用,可将油烟清除干净,使烟气排放彻底环保。
本发明可作为新型空气净化器使用,可去除室内的粉尘、烟尘颗粒。
本发明可作为吸尘器使用,灰尘清理方便,噪音低,吸尘效果好,造价便宜,更加节能,作为吸尘器使用时没有微尘污染,更加卫生、环保。
本发明可作为污水处理设备,可从污水中提取多种有用成份,实现资源循环利用。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。
本发明可作为净水设备,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,可使人们喝上更纯净、健康的饮用水。可以从水中提取重水用于工业领域。
本发明可作为垃圾处理设备,可将垃圾粉碎成颗粒后,用水流输送颗粒进行湿选,将有用成份分离、分选出来,无用成份与有机成份压制成颗粒有机肥,
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。
本发明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,降低发动机体积、重量、排量,提高扭矩。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可集中收集,如能够高压送入海底可形成干冰永久储存在海洋深处,可彻底解决碳排放。
本发明可作为选矿设备,可实现多种矿物、原料的分离提取、提纯、除杂质,可以从贫矿中筛选出多种有用矿物。可将矿石粉碎成颗粒,用水或气输送颗粒进行湿选活干选。可用于所有的矿物分选,可将矿物里面的各种有用成分都选出来,可使尾矿彻底无害,可大大提高选矿的经济效益和环境效益。合在一起是垃圾,分开就是金子。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。
本发明可作为海水淡化设备、海洋化工设备,可大大降低设备造价,降低海水淡化成本,大大降低能耗,提高海水淡化效率,提高淡水产量。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,可用它作为提盐设备、海洋化工设备,可大大降低设备造价。随着能源技术、材料技术的进步,可从江河湖海中提取各种矿物,可更好的保护环境、资源,江河湖海水质将更好,可更好的保护地球生态环境。
本发明作为炼油设备使用时,可实现原油低温裂解,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,没有废水、废气排放,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。
本发明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、普通矿物质等分选出来资源利用,可制成高纯煤粉或高纯水煤浆,也可将水煤浆用脱水筛脱水后制成高纯煤球,烧这样的高纯煤即可实现煤炭的洁净燃烧,可以跟天然气相媲美,尾
气可不用再脱硫除尘;可实现低温燃烧,可不产生氮氧化物,可不用再脱硝。
本发明作为核燃料精选设备使用时,可以大大提高精选效果,可以大大降低成本,可以使尾矿更加环保。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,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,即可玻璃固化填埋了,可以使核废料没有安全隐患了。随着新能源的诞生,核反应堆将蜕变为核废料焚烧处理炉。
本发明作为反应器使用时,可采用涡流使分子相互碰撞摩擦,可大大促进化学反应,可实现催化效果,可作为脱硝设备的催化反应设备使用。
本发明作为燃烧器或锅炉使用时,采用涡流燃烧加涡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,可更精准的控制炉温,可实现低温燃烧,可彻底杜绝氮氧化物产生。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,炉内温度均匀,涡流促进反应,可彻底实现干法充分脱硫。可实现燃烧器、锅炉除尘脱硫脱硝一体化,实现彻底环保。
本发明作为粉磨设备使用时,采用涡流破碎研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,用空气作为载体即可实现干磨,用水作为载体即可实现湿磨,可制出超细粉体、纳米粉体等。也可用作磨煤喷粉机或磨煤喷浆机,可对原煤干磨或湿磨,可喷出煤粉或煤浆喷入窑炉等燃烧。
本发明为实现上述目的,通过以下技术方案实现:
分离反应粉磨机,包括壳体和传动装置,壳体上设置传动装置,壳体内设置壳体腔,壳体腔内设置涡流轮,传动装置与涡流轮连接,壳体腔一端设置壳体腔进口,壳体腔另一端设置壳体腔出口。
壳体腔内壁上至少设置一道环绕分隔体,壳体腔外周对应环绕分隔体设置出料。
至少有一段壳体腔内壁贴近涡流轮外缘。
壳体腔进口外连通喷淋室,喷淋室设置喷淋室进口,喷淋室设置多个喷淋装置。
壳体腔外周内壁上设置供液装置。
壳体腔轴端设置壳体腔进口,壳体腔另一端轴端设置壳体腔出口。
壳体腔内壁上设置采热装置。
壳体腔进口上设置自动供料装置,壳体腔内壁上设置测温装置,测温装置控制自动供料装置。
壳体腔出口上设置流量调节装置。
涡流轮外周圆周上和轴向上均设置多个流体拨动装置。
本发明的优点在于:充分利用了圆周运动和流体运动,充分利用涡流运动,使流体被逐渐分离,效果随转速提高同步提高。流体沿轴向螺旋运动,在轴向运动过程中,逐渐被分离。利用涡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。利用涡流破碎研磨使颗粒物逐渐被磨细。利用涡流燃烧加涡流破碎使燃料充分燃烧,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,可彻底杜绝氮氧化物产生。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,炉内温度均匀,涡流促进反应,可彻底实现干法充分脱硫。可实现锅炉除尘脱硫脱硝一体化,使燃烧器、锅炉实现彻底环保。本发明具有制造简单、设备可大可小、应用领域广泛、制造成本低、制造工艺简单、使用成本低、维护费用低、使用寿命长等优点。
附图1是本发明的主体结构示意图;
附图2是本发明实施例之一的主视结构示意图;
附图3是本发明实施例之二的主视结构示意图;
附图4是本发明实施例之三的主视结构示意图;
附图5是本发明实施例之四的主视结构示意图;
附图6是本发明实施例之五的主视结构示意图;
附图7是本发明实施例之六的主视结构示意图;
附图8是本发明实施例之七的主视结构示意图;
附图9是本发明实施例之八的主视结构示意图;
附图10是本发明实施例之九的主视结构示意图。
本发明的主体结构包括壳体1和传动装置2,壳体1上设置传动装置2,壳体1内设置壳体腔3,壳体腔3内设置涡流轮4,涡流轮4外周圆周上和轴向上均设置多个流体拨动装置5,传动装置2与涡流轮4连接,壳体腔3一端设置壳体腔进口6,壳体腔3另一端设置壳体腔出口7。
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。本发明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、玻璃钢、碳纤维、塑料、尼龙、泡沫材料等材料制造。
传动装置2包括传动轴、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,带动本发明工作。传动装置2连接动力装置实现动力输入,带动本发明工作。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。作为发动机尾气处理器使用时,也可以利用发动机排出的废气连接壳体腔进口6直接推动设备运行,可简化结构,可同时代替消声器。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。也可采用变频技术等调整转速,可调整分离反应效果。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,可大幅加长设备的轴向长度,可提高反应分离效果。旋转稳定装置可设置支架、轴座、轴承、轴瓦或密封装置等,可以使旋转更加稳定。本发明传动轴竖置安装使用时,旋转稳定装置可设置推力轴承,可更好地提高使用寿命,支架可做成可以拆卸的,可方便安装拆卸轴承,支架可分别设置多个螺丝顶杆调整径向和轴向位置;轴承座也可做成轴向开体结构,可更方便安装拆卸。传动轴竖置安装使用处理液体时,设置轴密封装置的同时可在下部轴承上方的转轴上设置与转轴同步旋转的挡流牌,可将泄漏的水液向外围甩出,可避免水液泄漏到下部轴承上。湿法处理烟气时,为避免水液沿轴心区域漏下,可在壳体腔下部外周设置环绕流道,即可避免水液从轴心区域泄露,也可提高进气流道面积。
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,传动装置2的传动轴竖置安装时,通常传动装置2连接动力端可设在壳体1上部,可方便拆卸。
壳体1内设置壳体腔3。壳体腔3可做成一体或开体结构,安装时合在一起即可,壳体腔3也可根据需要任意开体,可方便装配。壳体腔3内壁也可根据需要设耐磨材料层或耐腐蚀层等提高使用寿命,脱硫脱硝时可采用玻璃鳞片防腐,易磨损区域也可在表面贴耐磨片或砌耐磨砖,设备维护时,进行修补维护即可。壳体腔3内腔横截面通常可以设置成圆形,可在壳体腔3内更好的形成涡流。壳体腔3中轴线竖置安装,可使烟气从下向上运动,使水液从上向下运动。壳体腔3通常可以做成上下一样粗的圆柱形,可简化结构,也可根据需要将壳体腔3做成向进口端逐渐增粗的结构、多段内径不一样粗的结构或多边型结构,可分别实现不同的功能效果。用于窑炉烟气脱硫脱硝、化工异味处理等时,壳体腔3内壁上可以根据具体工况条件设置防腐或防腐耐磨层。本发明用于锅炉、燃烧器等时可在壳体腔3内壁上设置耐火保温层。
壳体腔3内设置涡流轮4。涡流轮4设置在壳体腔3的中轴线上效果较好,涡流轮4外周与壳体腔3内壁平行设置效果较好。涡流轮4可整体设置成圆柱形、直径不相等的多段圆柱形、圆台形或直径不相等的多段圆台形等结构,通常将流轮4设置成圆柱形即可,涡流轮4外部可以顺应壳体腔3内壁设置,涡流轮4轴向长度越长效果越好,涡流轮4轴向长度与涡流轮4直径的比例可根据需要任意设定,可在不影响涡流轮4旋转稳定的基础上尽量加大涡流轮4轴向长度;通常将涡流轮4设置成一个整体即可,可将涡流轮4设置成空心或实心结构;也可以将涡流轮4设置成多个分体结构,安装在一起即可;涡流轮4外周表面可以设置成光面或毛面,可利用涡流轮4外周表面的附面层效应带动流体运动,可提高分离效果;也可以在涡流轮4全部或部分外周上设置螺纹、沟槽或多个流体拨动装置提高流体拨动效果;也可以根据工况要求在涡流轮4全部或部分外周均匀分布设置多个任意结构的叶片作为流体拨动装置,叶片也可以与轴向呈一定倾斜角度,可以起到轴流叶轮的作用,可以对流体增压输送,促进流体轴向运动;流体拨动装置也可采用圆棍、圆管等多种结构;流体拨动装置数量越多,对流体的破碎、搅拌效果越剧烈;流体拨动装置径向长度越短分离反应效果越好,流体流量压力越小;涡流轮4外缘与壳体腔3内壁之间的距离可以根据需要任意调整,距离越近,流体振荡磨擦越剧烈;也可根据需要将任意一段壳体腔3内壁贴近涡流轮4外缘,壳体腔3内壁贴近涡流轮4外缘,可使涡流摩擦更剧烈,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,缺点是加大磨损;涡流轮4可以根据需要选用不同的材料制造,可使用金属、陶瓷、玻璃钢、碳纤维、塑料、泡沫材料等制造。
传动装置2与涡流轮4连接。传动装置2的传动轴要连接固定在涡流轮4轴心区域,保证涡流轮4旋转平稳,可在涡流轮4轴心区域设置轮盘、轴盘、轮体等。传动轴也可采用空心轴,也可与涡流轮4焊接为一体,可简化结构。用于空气净化、抽油烟机等时也可以将传动装置2的电机与涡流轮4制成一体,可节省空间降低造价。也可以采用多个轴流叶轮作为涡流轮4,多个轴流叶轮同轴安装在传动装置2的传动轴上即可,缺点是结构复杂。
壳体腔3一端设置壳体腔进口6。可在壳体腔3一端设置壳体腔进口6,壳体腔进口6可设置在壳体腔3侧壁上,可设置一个或多个壳体腔进口6;也可在壳体腔进口6所在的壳体腔3处设置蜗壳形或环形导流腔,可更方便流体进入壳体腔3,使流体沿壳体腔3横截面切线方向进入,可减少涡流轮4磨损;壳体腔进口6也可设置在壳体腔3轴端,可实现流体轴向输入。也可在壳体腔进口6设置风门或阀门等流量调节装置,可更好地调节流体运动速度和流量,可更好地调节分离反应效果,流量调节装置也可采用自动化控制,可更好地实现流量调节。本发明作为磨煤喷粉机使用时,在壳体腔进口6设置风门效果更好。本发明作为燃烧器、锅炉等使用时,可在壳体腔进口6点火,也可在壳体腔进口6设置点火枪,可实现自动点火。也可在壳体腔进口6上设置搅笼、卸料器等自动供料装置向壳体腔进口6内均匀卸入燃煤、生物质燃料或垃圾等以及干法脱硫剂等,采用流体燃料时,也可将燃料喷枪设置在壳体腔进口6上即可。
壳体腔3另一端设置壳体腔出口7。可在壳体腔3另一端设置壳体腔出口7,壳体腔出口7可以设在壳体腔3侧壁上,可更好地利用离心力,可更方便壳体腔出口7连接管道。也可以将壳体腔出口7处的壳体腔3横截面做成蜗壳形,可更好地利用离心力,可使流体更顺畅的排出,可更加节能,蜗壳内的涡流轮上可以设置流体拨动装置,流体拨动装置也可以设置成沿轴向连接的多个长叶片,可起到增压叶轮的作用,可使流体以更高的压力输出,同时可提高流量。壳体腔出口7也可以设置在轴端,可实现流体轴向输出。也可以在壳体腔出口7上设置流量调节装置,可采用各种阀门、风门等,流量调节装置可调节流体流量,可调
整壳体腔3内压力,可提高功能效果。
本发明工作时,涡流轮4旋转,使壳体腔3内形成涡流。本主体结构的本发明传动轴可横置、竖置或斜置安装。竖置安装时,效果更好,可节约占地面积,可在壳体1的外围设置四根竖柱形成四方框,在机壳下方和上方分别设置横梁支撑,设备维护时拆开横梁即可。本主体结构可作为反应器、燃烧器、粉磨设备等使用,可同时将流体输送出去。
本发明作为反应器使用时,可利用涡流使分子相互碰撞摩擦,可促进化学反应,可实现催化效果,可广泛用于化工领域,可作为脱硝设备使用,可采用氢气、碳氢化合物等作为脱硝剂,温度较低时可采用天然气或甲醇高温裂解成氢气作为脱硝剂;也可利用烟气中的碳氢化合物、氢气作为脱硝剂,也可通过调整窑炉气氛或者向炉内高温带喷水蒸汽将烟气中的碳颗粒、一氧化碳反应掉制出氢气作为脱硝剂,可降低成本、净化烟气。也可使烟气在壳体腔3内完成干式脱硫反应,可用碱金属或氢氧化钙等作为干式脱硫剂,脱硫剂在壳体腔3内粉磨成细粉参与脱硫反应。
本发明作为燃烧器设备使用时,可直接向锅炉、窑炉等提供热气,可减少锅炉改造费用,可采用煤、油、气、生物质、垃圾、水煤浆、煤粉等任意燃料,可在壳体腔3内壁上设置耐火保温层,涡流轮4、流体拨动装置5和传动装置2的传动轴可采用耐高温材料制造,传动装置2的传动轴上也可设置风叶轮或水喷洒冷却轮等冷却装置,也可将水液喷洒在风叶轮上,在风叶轮周围设置接水箱体,使甩出的水液收集流回水池即可。壳体腔3中轴线竖置安装,壳体腔进口6可设置在壳体腔3下部侧壁上效果较好,可更好地利用重力实现燃料分选,可使颗粒较大的燃料始终处在壳体腔3下部燃烧,使燃尽的灰分随气流向上离开燃烧区,可使燃料在壳体腔3内实现均匀的涡流燃烧,可利用涡流燃烧加涡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剥离破碎燃烧充分。不管使用什么燃料,精准供给燃料,调整好风量时,均可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,可杜绝氮氧化物产生。同步加入碳酸钙石屑可实现炉内干法脱硫,炉内温度均匀,涡流促进反应,可实现干法充分脱硫。也可将壳体腔进口6处的壳体腔3内径稍微加大,可更好的蓄火维持燃烧。也可在壳体腔进口6上设置搅笼、卸料器等自动供料装
置,也可设置多个壳体腔进口6分别供料,可通过自动供料装置向壳体腔进口6内均匀卸入燃煤、生物质燃料或垃圾等以及干法脱硫剂等,采用燃气、燃油、水煤浆、煤粉等作为燃料时,燃料喷枪即为自动供料装置。可在壳体腔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。机壳下部与传动轴之间可加大缝隙,可进风对传动轴降温。
本发明作为粉磨设备使用时,可干磨也可湿磨,干磨更加节能。壳体腔3中轴线竖置安装时,壳体腔进口6可设置在涡流轮4外围的壳体腔3下部侧壁上效果较好,可从壳体腔进口6卸入需要粉磨的物料,也可设置自动卸料装置。可更好地利用重力实现颗粒分选,可使颗粒较大的物料始终处在壳体腔3下部粉磨,使粉磨好的粉体颗粒随气流向上离开粉磨区,从壳体腔出口7流出,可使物料在壳体腔3内实现涡流研磨,使颗粒物在涡流内相互碰撞摩擦,直至磨细。可磨制多种粉体、煤粉等,也可磨制面粉等,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。壳体腔进口6可以设置在壳体腔3外周上,可以同时进需要磨制的原料和空气或水,可将物料粉碎后直接分选,较粗的粉体在壳体腔3内继续粉磨,较细的粉体随着空气或水通过壳体腔出口7输出。也可用作磨煤喷粉机,可对原煤干磨,从壳体腔出口7喷出煤粉,可直接喷入窑炉锅炉等燃烧。也可在壳体腔3下部底部或侧壁上设置清灰口,可打开清灰口清理不易粉磨的物料,也可在清灰口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、燃烧器、锅炉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、灰分等进入炉膛燃烧,可更好地除尘、脱硫。可实现燃煤的洁净化燃烧。
壳体腔3做成向壳体腔进口6端逐渐增粗的结构或多段内径不一样粗向壳体腔进口6端依次增粗的结构时,可实现分离效果,可用于除尘、脱硫、脱硝、污水处理、海水淡化等需要分离的技术领域。
本发明实施例之一的结构是:在主体结构基础上,壳体腔3内壁上至少设置一道环绕分隔体8,壳体腔3外周对应环绕分隔体8设置出料口9。可将涡流轮4外缘与壳体腔3内壁之间的距离加大,可在壳体腔3内壁上设置一道或多
道环绕分隔体8,将壳体腔3轴向隔离成多个区域,环绕分隔体8可以阻挡流体沿壳体腔3外周轴向流动,可实现分离效果,同时可使壳体腔3内壁与涡流轮4外缘之间的空间加大,可使流体在壳体腔3内的滞留时间和运动距离加大,可提高化学反应效果。分离物因比重、颗粒大小等不同,向壳体腔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。壳体腔3内壁与涡流轮4外缘之间的距离越大,分离物越不容易回弹到涡流轮4外围,分离效果越好。壳体腔3内壁上设置一道环绕分隔体8时,可将环绕分隔体8设置在壳体腔出口7附近或沿壳体腔3内壁螺旋设置,多道环绕分隔体8也可螺旋设置,可使分离物沿壳体腔3内壁向壳体腔进口6端轴向流动,可提高分离效果。通常在壳体腔3内壁上与壳体腔3横截面平行设置多道环绕分隔体8,可避免流体沿壳体腔3内壁轴向流动,可提高分离效果。壳体腔3内壁上设置一道环绕分隔体8时,也可以将壳体腔3内壁与环绕分隔体8合为一体,可以将壳体腔3内壁设置成向壳体腔出口7端内径逐渐缩小的结构,可简化结构,提高分离效果。涡流轮4设置成向壳体腔出口7端外径逐渐加大的圆台形可提高流量。壳体腔3外周对应环绕分隔体8设置出料口9,可以在轴向上设置多个出料口9,可以分离出多种分离物,使用时可以调整好各个出料口9的流量,可更好地分离出多种分离物。出料口9内也可以沿壳体腔3横截面切线方向设置导流板或导流管,可更好地将流体切出,可更方便出料;也可在圆周上设置多个出料口9,可提高分离效果;也可以将轴向上的多个出料口9通过管道连通在一起,可更便于集中出料,也可将管道的壳体腔进口6端与壳体腔3连通,可使分离出的气体重新吸入壳体腔3内,用于除尘时可提高除尘效果。也可以在出料口9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,可使分离物在壳体腔3内压力、重力、离心力作用下,从壳体腔3内卸出,也可间歇打开活动密封卸料装置将分离物卸出。除尘时也可在出料口9设集灰箱,可间歇打开出料口9排灰。壳体腔3内壁可以设置成与轴线平行,可避免分离物轴向流动,可提高分离效果。
本实施例壳体腔3中轴线竖置、横置或斜置安装均可,可根据需要任意设置,用于选矿、海水淡化、污水处理、干式除尘等时,横置或斜置安装较好。本实施例可作为除尘器、吸尘器、制氧设备、血浆分离机、奶油分离机、除异味设备、发动机尾气净化器、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、垃圾处理设备、选煤设备、核燃料精选设备或核废料处理设备等使用,可同时将流体输送出去。干式除尘时,壳体腔3中轴线横置或斜置安装时,出料口9设置在壳体腔3下部可更好的利用重力排出粉尘。本发明使用时,壳体腔出口7处的壳体腔3内的压力大于其它区域的压力,可更好地保证其它区域的分离物不向壳体腔出口7泄漏,可采用缩小壳体腔出口7的面积或连接出口管道等提高压力。也可在壳体腔出口7上设置风门或阀门等装置调节壳体腔出口7处的壳体腔3内的压力。
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,可将气体从壳体腔进口6吸入本发明,可从壳体腔出口7排出无尘气体,从各个出料口9排出灰尘,在出料口9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,可从各个出料口9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。除尘或分离固体颗粒物时也可在出料口9设置出气管,出气管连通储灰仓,可设置回气管,回气管连通壳体腔进口6或靠近壳体腔进口6端的壳体腔3即可,可实现粉尘气流输送;也可将壳体腔3做成蜗壳形,分离效果较差,一般不用,将出料口9设置在蜗壳出口处,可更方便清灰。作为吸尘器使用时,可在壳体腔进口6设置滤网将大块物体隔离,灰尘清理方便,噪音低,造价便宜,更加节能,没有微尘污染,更加环保。可处理高温烟气,实现高温烟气干式除尘,喷入氢气等时可同步完成干式脱硝。
除尘时也可以在出料口9外设置储灰箱,也可将多个出料口9合并共用一个储灰箱和出灰口,可更方便出灰,用于燃烧器时也可在储灰箱内设置空气采热管,将采热空气吸入壳体腔进口6即可,可更好地使灰尘降温。用于烟气净化时,也可在靠近壳体腔进口6段设置多道环绕分隔体8,可将粉尘先行脱除,可减少设备磨损,也可将壳体腔3内径加大,可提高分离效果和流量,可在靠近壳体腔出口7段设置脱硝反应区,可实现烟气除尘后再脱硝;也可在靠近壳体腔出口7段设置多道环绕分隔体8,可在靠近壳体腔进口6段设置干法脱硫反应区,可将消石灰粉送入干法脱硫反应区,也可采用隔膜泵输送消石灰乳,可使烟气完成干法脱硫后再将粉尘等最后脱除;也可在靠近壳体腔进口6段和靠近壳体腔出
口7段分别设置多道环绕分隔体8,在两者中间设置干式脱硫反应区,可将消石灰送入干式脱硫反应区,可将粉尘先行脱除后再完成干法脱硫,最后再完成粉尘等的净化。
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,可将空气吸入本发明,可从各个出料口9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。作为制氧设备使用时,可将空气吸入本发明,可从壳体腔出口7分离出氮气等,从出料口9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。
作为选矿设备、垃圾处理设备使用时,可将矿物或垃圾粉碎成颗粒后,用水或空气将颗粒送进本发明进行湿选或干选:水可循环利用,可以将比重较大的金属元素、重元素分别从出料口9分离出来,无用成份从壳体腔出口7分离出来,无用成份脱水后可填埋,有机成分可自然发酵降解,最终实现无害化,可杜绝环境污染,实现资源循环利用。可以将有用成份、多种矿物、无用成份从各个出料口9分别分离出来,垃圾处理时,无用成份可填埋,有机成份发酵后压制成颗粒有机肥,可彻底杜绝环境污染,实现资源循环利用。
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9分选出来资源利用,可将高纯煤粉或水煤浆从壳体腔出口7分离出来,可制成高纯煤粉或高纯水煤浆,也可将水煤浆用脱水筛脱水后制成高纯煤球,可有利于运输,烧这样的高纯煤即可实现煤炭的洁净燃烧,可以跟天然气相媲美,尾气可不用再脱硫除尘。
作为海水淡化设备使用时,可从壳体腔出口7分离出淡水,从出料口9分离出高浓度盐水,通过蒸发析出即可获得盐。处理污水、水质净化或海水淡化时,可使达标净水、有机成份、气体成份、重元素、金属元素、沙尘、高浓盐水或盐水混合物等从各个不同的出料口9排出。设置母子本发明,用各个子本发明对排出的高浓盐水、有机成份、气体成份等进行二次处理、多级处理可进一步分离多种盐分、有机成份、气体成份。作为污水处理设备使用时,可将污水中的盐
分、重金属等处理掉,参照海水淡化,将含有高浓度有机成分的污水从壳体腔出口7分离出进行生化处理,处理后的中水回到一级处理系统的污水中,将达标净水从出料口9分离出排放即可。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、虫卵等处理干净。可将重水分离掉,可使自来水水质超过矿泉水、雪山冰泉水。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发明,原油受到涡流流体运动影响和涡流产生的离心力以及重力等共同影响,实现低温裂解,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、汽油等依次从靠近壳体腔进口6的各个出料口9排出。可将两种油份的中间体重新输入原油中再次分离,也可设置母子本发明,用各个子本发明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、蜡质、多种石油产品、硫、重金属、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。低温裂解大大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,可大大提高出油率,可提高高品质油品的出油率。
本实施例作为粉磨设备使用时,在靠近壳体腔出口7的壳体腔3内壁上设置多道环绕分隔体8时,可分选出多种粒径的粉体,越靠近壳体腔出口7的出料口9选出的粉体越细,可制出超细粉或纳米粉体,也可制出碳烯。也可对原煤干磨,可同时完成干选,可从各个出料口9中选出煤中各种矿物,从壳体腔出口7喷出煤粉,可直接喷入窑炉锅炉等燃烧。
本实施例作为燃烧器使用时可更好的蓄热,在靠近壳体腔出口7的壳体腔3内壁上设置多道环绕分隔体8时,可更好地实现炉内干式除尘。
作为抽油烟机使用时,可将烟气从壳体腔进口6吸入本发明,可将油烟分离,使烟气排放彻底环保,处理后的无烟气体从壳体腔出口7排出,废油从出料口9排出。
作为空气净化设备使用时,可作为新型室内空气净化器使用,可从壳体腔出口7分离出洁净空气,从出料口9分离出粉尘颗粒物等。也可新风系统的主
机,可将分离后的洁净空气送入室内,将脏空气留在室外。
作为除异味设备使用时,可从壳体腔出口7分离出较轻的气体,从出料口9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,可从壳体腔出口7分离出洁净空气,从出料口9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壳体腔进口6再次参与分离,形成闭式循环,最终实现完全回收。
本发明作为核燃料精选设备或核废料处理设备使用时,可分别从壳体腔出口7和出料口9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。
本发明实施例之二的结构是:在以上结构基础上,至少有一段壳体腔3内壁贴近涡流轮4外缘。可根据需要将任意一段壳体腔3内壁贴近涡流轮4外缘,壳体腔3内壁贴近涡流轮4外缘,可使涡流摩擦更剧烈,通常可将靠近壳体腔进口6的一段壳体腔3内壁贴近涡流轮4外缘;作为反应器或燃烧器使用时,可提高反应效果;作为粉磨设备使用时,可提高粉磨效果;作为选矿设备使用时可更好地实现矿物解理,可提高效果;作为发动机尾气处理器使用时可提高三元催化反应效果,也可以利用发动机排出的废气连接壳体腔进口6直接推动设备运行,可简化结构,可同时代替消声器,也可将壳体腔进口6和壳体腔出口7都分别设置在轴向上,使尾气轴进轴出,传动装置2上可以利用现有的涡轮增压上采用的全浮轴承,可利用发动机的润滑系统和冷却系统等。也可在壳体腔3任一端设置发动机进气增压器,通常可设在壳体腔进口6端,壳体腔进口6可设在壳体腔3侧壁上,壳体腔出口7可设在轴端,可更方便连接排气管,可简化结构。发动机进气增压器可采用现有的各种发动机涡轮增压器的结构,发动机进气增压器对发动机的进气增压。涡流轮4带动发动机进气增压器的增压叶轮旋转,利用涡流轮4代替了涡轮增压器的涡轮,可同时作为发动机涡轮增压器使用,可将涡轮增压器、三元催化器全部替代。通常可将靠近壳体腔进口6的一段壳体腔3内壁贴近
涡流轮4外缘。
本实施例也可作为燃烧器、反应器、粉磨设备、选矿设备等使用,作为燃烧器使用时可实现炉内除尘,可使燃料在壳体腔3内壁贴近涡流轮4外缘的一段区域内完成燃烧,可使烟气在壳体腔3内壁上设置环绕分隔体8的区域完成干式除尘,可从各个出料口9分离出各种粒度的粉尘。作为反应器使用时可用于烟气脱硝、干式脱硫、干式除尘、化学反应器等,可使烟气在壳体腔3内壁贴近涡流轮4外缘的一段区域内完成脱硝反应和干式脱硫反应,可采用窑炉烟气中产生的碳氢化合物、氢气等作为脱硝剂,可用碱金属或氢氧化钙等作为干式脱硫剂,脱硫剂在壳体腔3内不断的被粉磨成细粉,细粉不断的参与脱硫反应,可使烟气在壳体腔3内壁上设置环绕分隔体8的区域完成干式除尘,可从各个出料口9分离出各种粒度的粉尘。作为化学反应器使用时,可促进化学反应,同时可将反应后的物质实现分选。作为粉磨设备或选矿设备使用时,可使物料在壳体腔3内壁贴近涡流轮4外缘的一段区域内完成粉磨,在壳体腔3内壁上设置环绕分隔体8的区域完成粉体分选,可从各个出料口9分离出各种不同粒度或比重的粉体。选矿时采用水作为输送介质湿磨湿选效果更好。
本发明实施例之三的结构是:在以上结构基础上,壳体腔进口6外连通喷淋室10,喷淋室10设置喷淋室进口11,喷淋室10设置多个喷淋装置12。可在壳体腔进口6外设置喷淋室10,壳体腔进口6外连通喷淋室10即可,壳体腔进口6可根据具体结构任意设置在壳体腔3的侧壁或轴端,喷淋室10可采用多种结构的喷淋塔或喷淋箱等,也可以直接用烟道代替喷淋室10,可简化结构,节省空间,喷淋室10中心轴线横置或竖置均可。可在喷淋室远离壳体腔进口6端的端面或侧壁上设置一个或多个喷淋室进口11。喷淋室10设置多个喷淋装置12,喷淋装置12可采用多种结构的喷头或喷嘴等,可在喷淋室10设置多个多种结构的喷头、喷嘴等,可在喷淋室10外周内壁上环绕密集设置多个喷头或喷嘴,沿径向向喷淋室10中心喷水,可在喷淋室10内形成稠密雾化区。也可以在喷淋室10外壁或内壁上设置水套腔,将喷头或喷嘴均匀分布设置在喷淋室10内壁上与水套腔连通即可,可简化结构。也可利用涡流喷嘴设置在喷淋室10轴心区域向烟气逆流方向喷雾,可简化结构。大型设备喷淋室10直径较大时,也可在喷淋室10内设置多条水管,在管壁上设置喷头,使水液最大化的稠密雾化。喷淋
装置12连接水液供给装置,水液供给装置包括泵、管道、沉淀池或水箱等装置,水液供给装置可通过喷淋装置12向喷淋室10内持续喷入水或碱水等液体。喷淋室10下部可以设置一个或多个出液口,可使水液从喷淋室10下部流出进入水液供给装置的水池中,形成循环供液。用于脱硫脱硝时,喷淋室10内壁也可采用玻璃鳞片防腐,设备维护时,进行修补维护即可;喷淋室10也可采用耐酸不锈钢或其它耐腐蚀材料制造,可简化制造工艺。北方严寒地区,喷淋室10外壁上也可以根据具体情况设置保温层保温,可避免结冰。用于脱硝时,也可在水液里加入催化剂、尿素等,用尿素吸收氮氧化物反应即可。靠近壳体腔出口7端的出料口9也可以通过管道连接壳体腔进口6或靠近壳体腔进口6处的壳体腔3,可使分离出的汽水混合物重新进入壳体腔3二次分离,可形成气流通道,可使分离物顺畅排出。
本实施例的本发明传动轴横置、斜置、竖置安装使用均可,用于锅炉、窑炉等时可同步完成引风、送风、除尘、脱硫、脱硝。可使烟气在喷淋室10内完成初级降尘,在壳体腔3内完成水雾清洗,最终完成脱水,最终实现烟气彻底净化。
本发明实施例之四的结构是:在以上结构基础上,壳体腔3外周内壁上设置供液装置23。可在壳体腔3外周内壁上根据需要任意设置供液装置23,供液装置23可采用出水管、出水口或喷头、喷嘴等,供液装置23的附属设施包括泵、管道、流量控制阀、沉淀池或水箱等装置,可通过水管、出水孔或喷头等供液装置23向壳体腔3内流入或喷入水或碱水等液体。也可在壳体腔3外壁上设置水套,在壳体腔3壁上打孔即可。涡流轮4旋转使水液与烟气更充分的接触碰撞,使烟气被水液彻底洗涤净化,涡流轮4旋转可以使壳体腔3内壁上的水液跟着旋转,使分离物随水液一同排出。靠近壳体腔出口7端的出料口9也可以通过管道连接壳体腔进口6或靠近壳体腔进口6处的壳体腔3,可使分离出的汽水混合物重新进入壳体腔3二次分离,可形成气流通道,可使分离物顺畅排出。除尘时在靠近壳体腔出口7端设置一个或多个供液装置23向壳体腔3内喷入清水,可提高除尘效果,清水可用脱硫除尘的补充水或处理后的清水。在轴向上设置多个供液装置23可实现多级净化,效果更好。
也可以根据需要在一道环绕分隔体8内口上对应供液装置23设置一道环
绕在涡流轮4外围的环绕挡水圈,环绕挡水圈向壳体腔出口7端设置供液装置23,环绕挡水圈可阻挡水液沿轴向向壳体腔进口6端泄露,环绕挡水圈口沿向壳体腔出口7端内径扩张可利用离心力更好地避免水液向壳体腔进口6端泄露。可实现湿式除尘干式脱硫脱硝一体化、干式脱硫除尘湿式脱硝一体化或干式脱硝湿式除尘脱硫一体化,干式脱硫后可大大减少设备腐蚀,可大大降低设备造价,可在壳体腔3内壁前半段区域设置干式脱硝反应区或干式脱硫脱硝除尘联合反应区,在壳体腔3轴线后半段区域实现水液清洗,完成湿式除尘脱水或湿式脱硝除尘脱水,实现烟气净化。为减少粉尘对壳体腔3内壁磨损,也可在靠近壳体腔进口6端设置多道环绕分隔体8将大的颗粒物干式除尘。本实施例用于粉磨物料时,靠近壳体腔进口6段可以不设置环绕分隔体8,可实现干式粉磨物料、湿式收集粉料,可大幅提高收集效率。也可在环绕挡水圈向壳体腔进口6侧的壳体腔3内壁上设置一道或多道环绕分隔体8,对应环绕分隔体8设置的出料口9可通过管道连通壳体腔进口6,可使分离物重新进入壳体腔进口6。也可在环绕挡水圈向壳体腔进口6侧的壳体腔3内壁上设置多道环绕分隔体8,可将靠近壳体腔进口6侧的出料口9连通壳体腔进口6,将其余的出料口9出一部分干料。可实现粉体湿法收集,可将较粗粉体选出后重新送入壳体腔进口6继续粉磨,可更好地控制粉体细度。
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、脱硝设备,可广泛用于各种窑炉、锅炉、焚烧炉、车船等所有尾气处理领域,可用于所有处理烟气的领域。用于脱硝时,也可在水液里加入双氧水等强氧化剂和尿素等,可以将一氧化氮氧化成多氧化氮,用尿素或火碱、石灰或碳酸钙等吸收反应即可。除尘与脱硫一体化后,灰量较大,可以将水液里的硝酸盐、卤化物和盐分等大量带走,可以使锅炉等不再产生脱硫废水和冲渣废水,可大大提高环保效益。本实施例用水量极少,稍微一点水即可,水泵能耗大大减少,基本可忽略不计。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。本实施例可实现湿法除尘,可更高效的除尘、除有害物质,可使烟气更加环保。
本发明实施例之五的结构是:在以上结构基础上,壳体腔3轴端设置壳体腔进口6,壳体腔3另一端轴端设置壳体腔出口7。可在壳体腔3轴端设置壳
体腔进口6,在壳体腔3另一端轴端设置壳体腔出口7,可使流体轴进轴出。
本实施例的本发明可作为发动机尾气处理器使用,可以利用发动机排出的废气连接壳体腔进口6直接推动设备运行,可简化结构,可同时代替消声器,可使尾气轴进轴出,传动装置2上可以利用现有的涡轮增压上采用的全浮轴承,可利用发动机的润滑系统和冷却系统等。
本发明实施例之六的结构是:在以上结构基础上,壳体腔3内壁上设置采热装置13。可将涡流轮4外缘与壳体腔3内壁之间的距离加大,可在壳体腔3内壁上设置采热管或采热箱等作为采热装置13,可采用水、油或气体等作为采热介质。采热装置13可以贴近壳体腔3内壁设置,采热装置13采用采热管时,采热管可以与壳体腔3内壁之间留有一定间隙,可更好地提高才热效率。采热管上也可以设置防护板,防护板可以设置在迎风面,即可提高采热面积也可减轻采热管表面磨损,可起到防护作用。采热装置13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壳体腔3下部设置高压采热管,在靠近壳体腔3上部设置低压采热管,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。也可在壳体腔3内壁上设置空气热交换装置,空气热交换装置可采用采热管,将进入壳体腔进口6的空气通过采热管,空气热交换装置可以将进入壳体腔进口6的空气加热。可以将空气热交换装置设置在液体采热装置13的采热后方,可以使烟气通过液体采热装置13采热后再通过空气热交换装置采集余热,可更充分的利用热能。也可在壳体腔3下部侧壁上设置清灰口,可定期打开清灰口清理不易粉碎的颗粒物,也可在清灰口上设置搅笼或卸料器等实现自动卸灰。
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,可在壳体腔3内壁上设置耐火保温层,涡流轮4、流体拨动装置5和传动装置2的传动轴可采用耐高温材料制造,传动装置2的传动轴上也可设置风叶轮或水喷洒冷却轮等冷却装置,也可将水液喷洒在风叶轮上,在风叶轮周围设置接水箱体,使甩出的水液收集流回水池即可。壳体腔3中轴线可以竖置或横置安装,竖置安装效果较好,壳体腔进口6设置在壳体腔3下部侧壁上效果较好,可更好地利用重力实现燃料分选,可使颗粒较大的燃料始终处在壳体腔3下部燃烧,使燃尽的灰分随气流向上离开燃烧区,可使燃料在壳体腔3
内实现均匀的涡流燃烧,可利用涡流燃烧加涡流破碎使燃料充分燃烧,特别是燃煤时,可使煤块在不断燃烧的同时被不断的剥离破碎燃烧充分。不管使用什么燃料,精准供给燃料,调整好风量时,均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,可杜绝氮氧化物产生。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,涡流促进反应,可实现干法充分脱硫。壳体腔3形成的涡流可以促进采热装置13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。涡流运动使热气流在壳体腔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。机壳下部与传动轴之间可加大缝隙,可进风对传动轴降温。
本实施例是一个可以烧任意燃料的高效锅炉,可使燃尽率达到100%,彻底不冒黑烟,大大降低一氧化碳、硫和硝排放。
本发明实施例之七的结构是:在以上结构基础上,壳体腔进口6上设置自动供料装置14,壳体腔3内壁上设置测温装置15,测温装置15控制自动供料装置14。可在壳体腔进口6上设置搅笼、卸料器等自动供料装置14,也可设置多个壳体腔进口6分别供料,可通过自动供料装置14向壳体腔进口6内均匀卸入燃煤或垃圾等以及干法脱硫剂等,采用燃气、燃油、水煤浆、煤粉等作为燃料时,燃料喷枪即为自动供料装置14。可在壳体腔3内壁上设置测温装置15,测温装置15可采用热电偶、温控仪表等装置,测温装置15可通过温控仪表控制自动供料装置14,当炉内温度达到设定温度上限时,自动断开自动供料装置14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14电源即可。
本实施例可以更精准的控制炉温,可实现燃烧器、锅炉等自动化。
本发明实施例之八的结构是:在以上结构基础上,壳体腔出口7上设置流量调节装置19。可以在壳体腔出口7上设置流量调节装置19,流量调节装置19可采用各种阀门、风门等,流量调节装置19可调节流量,调整壳体腔3内压力,可更好地实现效果。
本实施例可以调节流量、压力,可更好地提高效果。
本发明实施例之九的结构是:在以上任意结构基础上,涡流轮4外周圆周上和轴向上均设置多个流体拨动装置5。可在涡流轮4外周圆周上和轴向上均设置多个流体拨动装置5,可使流体拨动装置5均匀分布在涡流轮4外周。可在
涡流轮4外周均匀分布设置多个任意结构的叶片作为流体拨动装置5,叶片可以与轴向呈一定倾斜角度,可以起到轴流叶轮的作用,可以对流体增压输送,促进流体轴向运动。流体拨动装置5也可采用圆棍、圆管等多种结构,效果较差,需采用其它的输送设备帮助流体进出本发明,一般不采用。流体拨动装置5可以分散零星设置,也可以设置成与轴向或径向呈一定倾斜角度的结构,也可设置成轴流叶轮叶片的结构,均可增加气流扰动,可提高效果,采用叶片时,叶片也可以根部连接为一体,可采用整条板材上分段裁口,将板材扭转形成多个根部连成一体的三元叶片,可手工制作也可采用冲压设备冲压成型,可简化制造工艺,叶片可以沿轴向与涡流轮4连接为一体,多个叶片可以呈放射状设置在涡流轮4外周上即可。也可以将叶片设置成整条,沿轴向设置在涡流轮4外周上,缺点是不能对流体产生轴向拨动,也不宜将流体更好地打碎,效果较差,一般不用。流体拨动装置5可以对流体形成轴向、径向拨动,可以使流体在涡流轮4外周与壳体腔3内壁之间形成震荡涡流,可更好地搅旋流体。流体拨动装置5外缘与壳体腔3内壁之间的距离可以根据需要任意调整,距离越近,流体振荡磨擦越剧烈。流体拨动装置5数量越多,对流体的破碎、搅拌效果越剧烈;流体拨动装置5径向长度越短分离、反应效果越好,流体流量压力越小。
本实施例可以提高流体流量和压力,用于粉磨时可提高破碎强度。
工作原理:本发明使用时可同时将流体输送出去,流体在本发明内实现分离净化。涡流轮4旋转后,使流体在壳体腔3内形成涡流,利用涡流轮4外周打碎流体同时带动流体旋转,涡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,利用涡流内产生的离心力实现流体内不同比重物质的分离、分选。涡流沿轴向螺旋前进,不同比重的独立运动个体向涡流外围的运动速度不同,比重较大的粒子或颗粒物更容易、更快的沉降到壳体腔3内壁上。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壳体腔3的不同轴向区域,分别通过轴向不同的出料口9排出,最终实现对流体的分离、分选或污染物等的脱除,实现对溶液中溶质的分离。流体在轴向运动过程中被逐渐分离净化,涡流轮4轴向长度越长,流体轴向运动距离越长,分离净化效果越好。用于烟气净化时,可以使烟气与水液充分快
速接触,使烟气被水液充分洗涤净化,可以使充分洗涤净化后的烟气实现充分脱水,从壳体腔出口7排出,利用涡流促进化学反应,实现脱硫脱销,实现烟气彻底净化。调节烟气流量可实现对烟气中粉尘颗粒物等的高度清除,可将黑烟、粉尘、二氧化硫、氮氧化物、二恶英、部分化工异味等高度脱除干净,可实现对烟气的高度净化,可实现大气污染的源头治理,实现霾的源头治理,最终可解决大气污染,消灭霾。利用分离可解决水污染,解决环境污染。利用涡流实现涡流燃烧,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,可使燃料在壳体腔3内实现均匀的涡流燃烧,可利用涡流燃烧加涡流破碎使燃料充分燃烧,燃烧固体燃料时,可使燃料在不断燃烧的同时被不断的剥离破碎燃烧充分。不管使用什么燃料,精准供给燃料,调整好风量时,均可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,可杜绝氮氧化物产生。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,涡流促进反应,可实现干法充分脱硫。壳体腔3形成的涡流可以促进采热装置13表面的气流运动速度,可提高采热效率,可减少采热面积,可降低造价。涡流运动使热气流在壳体腔3内的运动距离延长,可使热能充分传递,最终实现高效采热。可实现锅炉、燃烧器等的炉内除尘,可使排放更加环保。利用水雾清洗实现湿式除尘,可使烟气实现彻底环保。利用涡流实现涡流粉磨,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。
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)
- 分离反应粉磨机,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)内设置壳体腔(3),壳体腔(3)内设置涡流轮(4),传动装置(2)与涡流轮(4)连接,壳体腔(3)一端设置壳体腔进口(6),壳体腔(3)另一端设置壳体腔出口(7)。
- 根据权利要求1所述的分离反应粉磨机,其特征在于:壳体腔(3)内壁上至少设置一道环绕分隔体(8),壳体腔(3)外周对应环绕分隔体(8)设置出料口(9)。
- 根据权利要求2所述的分离反应粉磨机,其特征在于:至少有一段壳体腔(3)内壁贴近涡流轮(4)外缘。
- 根据权利要求2所述的分离反应粉磨机,其特征在于:壳体腔进口(6)外连通喷淋室(10),喷淋室(10)设置喷淋室进口(11),喷淋室(10)设置多个喷淋装置(12)。
- 根据权利要求2所述的分离反应粉磨机,其特征在于:壳体腔(3)外周内壁上设置供液装置(23)。
- 根据权利要求2所述的分离反应粉磨机,其特征在于:壳体腔(3)轴端设置壳体腔进口(6),壳体腔(3)另一端轴端设置壳体腔出口(7)。
- 根据权利要求1所述的分离反应粉磨机,其特征在于:壳体腔(3)内壁上设置采热装置(13)。
- 根据权利要求1所述的分离反应粉磨机,其特征在于:壳体腔进口(6)上设置自动供料装置(14),壳体腔(3)内壁上设置测温装置(15),测温装置(15)控制自动供料装置(14)。
- 根据权利要求1所述的分离反应粉磨机,其特征在于:壳体腔出口(7)上设置流量调节装置(19)。
- 根据权利要求1、2、3、4、5、6、7、8或9任一项所述的分离反应粉磨机,其特征在于:涡流轮(4)外周圆周上和轴向上均设置多个流体拨动装置(5)。
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CN109847892A (zh) * | 2019-03-20 | 2019-06-07 | 兰州大学 | 一种还原扩散法制备稀土类-过渡金属合金除杂质的装置 |
CN111425280A (zh) * | 2020-01-08 | 2020-07-17 | 江西天美生物科技有限公司 | 活性炭磷酸活化尾气净化装置 |
CN112220083A (zh) * | 2020-09-26 | 2021-01-15 | 武汉木兰山水生态农业发展有限公司 | 一种猪饲料高效加工方法 |
CN113713683A (zh) * | 2021-08-24 | 2021-11-30 | 桐乡磊石微粉有限公司 | 一种粉体混合输送设备及其输送方法 |
CN113713683B (zh) * | 2021-08-24 | 2024-03-26 | 桐乡磊石微粉有限公司 | 一种粉体混合输送设备及其输送方法 |
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