CN107638963A - Separation reaction flour mill - Google Patents
Separation reaction flour mill Download PDFInfo
- Publication number
- CN107638963A CN107638963A CN201710980384.1A CN201710980384A CN107638963A CN 107638963 A CN107638963 A CN 107638963A CN 201710980384 A CN201710980384 A CN 201710980384A CN 107638963 A CN107638963 A CN 107638963A
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- China
- Prior art keywords
- housing chamber
- housing
- chamber
- vortex
- inwall
- Prior art date
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Classifications
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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
-
- 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
-
- 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
-
- 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
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Processing Of Solid Wastes (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
Flour mill, including housing and transmission device are reacted in one kind separation, and transmission device is set on housing, housing chamber is set in housing, vortex wheel is set in housing chamber, transmission device is connected with vortex wheel, housing chamber one end sets housing chamber import, and the housing chamber other end sets housing chamber to export.Dedusting, desulphurization and denitration are can be widely used for, smoke abatement, taste removal, car and boat tail gas clean-up, smoke pumping, purification of air, petroleum vapor recovery, garbage disposal, nuclear waste disposal, powder, ore dressing is selected, desalinization, sewage disposal, water purification, refines oil, the field such as oxygen processed, reactor, boiler, burner, milling equipment, smoke height purification can be achieved, can solve atmosphere pollution and water pollution, haze can be utterly destroyed, can solve water scarcity, water pollution, environmental pollution.Various powders, including nano-powder can be prepared.Can be achieved fuel abundant low-temperature burning, can not produce nitrogen oxides, can dry type desulfurizing dedusting in stove, it is thoroughly environmentally friendly that boiler can be achieved.
Description
Technical field
The present invention relates to separator, centrifuge, sewage disposal, water purification, desalinization, marine chemical industry, ore dressing, coal separation, core
Fuel is selected, nuclear waste disposal, oil refining, petroleum vapor recovery, garbage disposal, purification of air, dedusting, dust suction, desulphurization and denitration, oil pumping
Cigarette purification, vent gas treatment, except black smoke, eliminate the unusual smell, the neck such as oxygen processed, air separation and Extraction, reactor, boiler, burner, grinding
Domain, it is specifically a kind of separation reaction flour mill, grinding, chemical reaction, separation three zones can be achieved, three zones can be independent
Used using also can be combined.
Background technology
The environmental pollution of today mainly includes pollution of waterhead, air pollution etc., and environmental pollution has seriously affected earth life
State circle.Atmosphere pollution has seriously affected earth ecology circle, and mainly technical reason of tracing it to its cause, prior art can not be by flue gas
In particulate matter remove clean, PM2.5 discharge indexs are all difficult to.Bag-type dust and electric precipitation can only typically accomplish that dust contains
20 milligrams/mark side left and right is measured, even if dust removing effects can only accomplish 5 milligrams/mark Fang Zuo after increase wet-esp multistep treatment
It is right.
Existing air cleaning facility clean-up effect is too poor, desulphurization denitration high equipment cost, and operation, maintenance cost are high, energy
Consumption is high, and removal efficiency is low, and effect is bad, and desulfurization, wet dust removal, denitration use spray process more, can not be by particulate matter, oxysulfide
The fully absorption dissolving such as molecule, nitrogen oxides molecule, causes dedusting, desulphurization and denitration efficiency low.Existing cleaner has rotation
Wind dedusting, electric precipitation, wet-esp, bag-type dust etc., the defects of generally existing dust removing effects are too poor, and energy consumption is big, dust are dirty
Dye turns into the most important pollution sources of atmosphere pollution, turns into the arch-criminal of haze.
It is existing except black smoke, the equipment clean that eliminates the unusual smell effect are too poor, to black smoke, many chemical industry peculiar smell, dioxin substantially without
Method processing, black smoke, gas with foreign flavor pollution turn into important pollution sources, and dioxin is the most fearful organic contamination of mankind's manufacture
Thing, the existence of the mankind is seriously affected.Heavy element particulate matter in air serious threat human health.
Existing car and boat tail gas treatment device treatment effect is too poor, generally without dedusting, desulfurization, three-element catalytic denitration effect
Too poor, used car is substantially useless, and car and boat exhaust emissions turns into the important source of atmospheric pollution.
Existing dust collection equipment pick-up performance is undesirable, and noise is big, there is dust particale pollution, dedusting post processing dust trouble.
Existing smoke exhaust ventilator, oil smoke can not be separated, cause smoke exhaust ventilator cleaning trouble, cause smoke particle to pollute ring
Border, smoke particle thing have turned into the another important pollution sources of urban air pollution.
Existing sewage disposal device is complicated, and cost is too high, and sewage disposal expense is too high, and treatment effect is general, and sewage is controlled
Reason has turned into the most important thing of environmental improvement.
Existing oxygen generating plant cost is too high, and oxygen cost processed is too high, can not realize popularization and application, causes that pure oxygen can not be realized
Burning, causes nitrogen oxides largely to discharge to form important pollution sources.
Existing water purifier mainly using filtering, water purification agent the methods of, generally existing, which is unable to reach, higher drinks water gauge
Standard, the defects of water purification expense is too high.
Existing sea water desalting equipment is complicated, and cost is too high, and desalinization expense is too high, and energy consumption is too big.Existing ocean
Chemical industry equipment is complicated, and cost is too high, undesirable to marine resources utilizing status.
Existing separation equipment, mainly there is centrifuge etc., the defects of generally existing separating effect is general, and energy consumption is big.
Existing preparation equipment aeneficiation effect is general, can not realize finer sorting, cause the wasting of resources and environmental pollution.
Existing refining equipment generally uses high temperature distillation cracking process, and oil refining cost is high, high energy consumption, and high temperature is to big in crude oil
Molecule destroys serious, generation bulk petroleum gas and petroleum slag, substantially reduces oil yield, reduction high quality oils output.To in oil product
The lead in face, heavy metal, heavy element etc. can not be removed clean, cause serious fuel oil pollution.
Existing cleaning unit is simple coal washing, can not fully be selected coal totally, after causing the combustion of sulfur inside coal
Sulfur dioxide is formed, also wants tail gas desulfurization to handle, also takes off and does not cause air environmental pollution totally, the various metallic elements inside coal
Fail to elect etc. valuable goodies, all go in coal ash, the radioactive element inside coal also goes to air and coal
In ash, serious environmental pollution and the wasting of resources are caused.Coal cleans very urgent.
Present nuclear fuel is selected mainly by centrifuge, and it is too high expense to be present, and choosing is not clean, causes environmental pollution and resource
Waste.Nuke rubbish, core sewage can not be handled substantially, cause serious environment hidden danger.
Existing technology of garbage disposal is not generally clean using burning, landfill etc., tail gas after incineration processing, causes serious
Air environmental pollution, landfill causes to take up an area and underground water pollution.
Existing oil-gas recovery device generally existing high cost, the problems such as petroleum vapor recovery is not thorough.
Existing reactor apparatus has reactor, catalyst reaction tank or tower etc., and generally existing reaction speed is slow, reacts not
Thoroughly, the defects of cost is high, catalyst is easy to aging.
The burning of the generally existings such as existing boiler plant, burner apparatus is insufficient, particularly coal-burning boiler burn-off rate
Have 80% or so, cause serious energy waste, burning is insufficient to cause serious environmental pollution.
Existing milling equipment has pulverizer, Raymond mill, air swept mill, and generally existing high energy consumption, grinding powder efficiency are low,
Superfine powder prepares difficulty etc..
The content of the invention
Using brand-new separation method, using brand-new vortex separation principle, fluid motion is made full use of, using vortex,
Make fluid by vortes interference, in the presence of circular motion centrifugal force, separation is realized using vortex, make different volumes, proportion
Particle realizes separation between each other.The movement velocity of different volumes, the particle of proportion to vortex periphery is different, proportion in fluid
Big particle can be earlier move to vortex periphery, what the small particle of proportion can be more late move to vortex periphery utilizes this point
Realize the sorting of different material.There is relative motion in each point in vortex, can be with using the effect of vortex between each other
The glued, molecule of dissolving together is separated, the various particles such as each molecule in vortex, atom is formed different motion speed
Degree self-movement individual, using eddy motion and centrifugal force and gravity etc. make variable grain degree size, different specific weight thing
Matter enters different zones.The solute in solution can be made to realize with solvent to separate, different solutes can be realized separation.Utilize
The self-movement individual that the various particles such as each particulate matter made in vortex, molecule, atom form different motion speeds is vortexed,
With current, the abundant making contact of water smoke in the presence of circular motion centrifugal force and motional inertia, flue gas is set fully to be washed by water
Wash, the particulate matter in flue gas etc. is entered in water, realize gas cleaning.When akaline liquid, air etc. are inputted into the present invention, also
Available for flue gas desulfurization, denitration, the field such as eliminate the unusual smell, and is greatly improved equipment operating efficiency, reduces cost and operating cost.Profit
Make the mutual collision friction of molecule with vortex, chemical reaction can be greatly promoted, catalytic effect can be achieved, denitration device can be used as, changed
Reactor etc. is learned to use.Make full combustion of fuel using swirl combustion plus vortex are broken, when particularly coal-fired, coal cinder can be made not
It is abundant by the broken burning of continuous stripping while disconnected burning, while combustion zone temperature is kept stable and uniform, can be more accurately
Furnace temperature is controlled, low-temperature burning can be achieved, can thoroughly prevent nitrogen oxides generation.Calcium carbonate aggregate chips is synchronously added when coal-fired to be realized
Dry desulfurization in stove, in-furnace temperature is uniform, and vortex promotes reaction, can thoroughly realize the abundant desulfurization of dry method.Boiler dusting can be achieved
Desulfurization and denitrification integral, boiler is set to realize thoroughly environmental protection.The present invention can be achieved cleaner dedusting, cleaner purification air,
Cleaner purification discharge oil smoke, cleaner processing sewage, more cheap realize desalinization, more fully utilize water money
Source, more fully extraction marine resources, the ore dressing of higher efficiency, the oil refining etc. of cleaner processing rubbish, higher efficiency.The present invention
It can be widely applied to various separation equipment fields.Novel centrifuge, seperator use can be used it as, its separating effect is more
It is good, separation, sorting, extraction, the purification of various Matter Compositions can be achieved.
The present invention can use as deduster, can use dry dust removal or wet dust removal, not only can be by PM2.5 particulate matters
Remove clean, and PM0.01 particulate matter can be removed clean, dustlessization discharge can be achieved substantially, can accomplish with it is excellent greatly
The same dustiness in compression ring border, and without harmful substances such as heavy elements, can also accomplish thoroughly dustless.
The present invention can remove black smoke clean;Can high-efficient cleaning remove flue gas in peculiar smell composition;Can by the dioxin in flue gas,
The removings such as heavy element particulate matter are clean;When aqueous is using akaline liquid or addition various desulfurizing agents, available for flue gas desulfurization, denitration
Deng field, realize that wet dust removal, wet type desulfurizing, the step of wet type denitration one are completed, and are greatly improved equipment operating efficiency.
The present invention can be used as air cleaning facility, can be used as novel indoor air device.It can be used as to eliminate the unusual smell and set
It is standby to use, gas with foreign flavor can be removed.It can be used as deduster, the dust removing effects of any deduster can be exceeded.
The present invention can use as car and boat exhaust gas treating device, can complete dedusting, smoke abatement, can substitute ternary catalyzing unit simultaneously,
Can never block, never aging, tail gas can be made to complete three elementary reactions in the present invention, realize denitration, except hydrocarbon, except one
Carbonoxide, the particulate matter in tail gas, nitrogen oxides etc. can efficiently be removed.
The present invention can use as oil-gas recovery device, recyclable a variety of oil vapours.
The present invention can use as smoke exhaust ventilator, can remove totally oil smoke, make fume emission thoroughly environmentally friendly.
The present invention can use as air purifier, can remove indoor dust, soot dust granule.
The present invention can use as dust catcher, and dust cleaning is convenient, and noise is low, and pick-up performance is good, low cost, more supernumerary segment
Can, there is no dust pollution when being used as dust catcher, it is relatively sanitary, environmentally friendly.
The present invention can be used as sewage disposal device, and a variety of useful compositions can be extracted from sewage, realize resource circulation utilization.
Pure water can be directly provided, can reach drinking water standard, water pollution can be thoroughly solved, solve the problems, such as water scarcity.
The present invention can be used as purifier, can be completely separated away the harmful element in running water, can be by heavy water(Weight
Hydrogen water, heavy oxygen water)Separate, can reach the drinking water standard of higher level, people can be made to drink purer, healthy drink
Water.Heavy water can be extracted from water and is used for industrial circle.
The present invention can be used as refuse treatment plant, and after rubbish being ground into particle, wet separation is carried out with current conveying particle,
By the separation of useful composition, sort out, useless composition is pressed into granular organic fertilizer with organic component, can thoroughly prevent environment dirt
Dye, realizes resource circulation utilization.The fume treatment after waste incineration is can also be used for, flue gas can thoroughly be handled clean.
The present invention can isolate oxygen from air, can also separate the various gases in air, can extract
A variety of rare gas.Oxygen cost processed is extremely low, can make the cheap economic pure oxygen burning of the realizations such as boiler, kiln, engine, heat engine,
Energy consumption can be reduced, improves heat power efficiency, thoroughly prevents discharged nitrous oxides, reduces engine volume, weight, discharge capacity, improves and turns round
Square.Engine, heat engine, kiln, boiler etc. can also use waste gas to recycle, and can reduce ignition temperature, reduce equipment and materials requirement.
After pure oxygen burning caused carbon dioxide can centralized collection, if high pressure be sent into seabed can form dry ice permanent storage in ocean
Depths, can thoroughly solve carbon emission.
The present invention can be used as preparation equipment, and multi mineral, the separation and Extraction of raw material, purification, the removal of impurity, Ke Yicong can be achieved
A variety of valuable minerals are filtered out in lean ore.Ore can be ground into particle, wet separation work dry separation is carried out with water or gas conveying particle.Can
For all sorting minerals, the various useful components inside mineral can all be elected, mine tailing can be made thoroughly harmless, can be significantly
Improve the economic benefit and environmental benefit of ore dressing.It is rubbish to be combined, and is exactly separately gold.It can be selected respectively for rare-earth industry
Kind element;Noble element can be fully extracted for noble metal ore dressing.
The present invention can be used as sea water desalting equipment, marine chemical industry equipment, can substantially reduce equipment manufacturing cost, reduce desalinization
Cost, energy consumption is substantially reduced, improve desalinization efficiency, improve fresh water yield.Synchronously can be extracted from seawater it is various it is useful into
Part, while the separation and Extraction of various useful compositions, sorting purification are realized, and salt equipment, marine chemical industry equipment can be used it as, can
Substantially reduce equipment manufacturing cost., can be from the marine various mineral of extraction in rivers lake with energy technology, the progress of material technology, can be more
Environmental protection well, resource, rivers,lakes and seas water quality will be more preferable, and can preferably preserve our planet ecological environment.
The present invention is used as refining equipment in use, crude oil low temperature pyrolyzer can be realized, can reduce macromolecular composition in crude oil and break
It is bad, the output of oil gas and petroleum slag is reduced, improves oil yield, improves high-quality oil product output.Oil product can be made to realize thorough nothing
Lead, pollute without radioactive element, whole production process is pollution-free, is discharged without waste water, waste gas, oil refining process thorough ring can be achieved
Protect, resource, which is thoroughly received, to be utilized, and can substantially reduce oil refining cost.
The present invention is used as cleaning unit in use, coal can be made into coal dust, can use dry separation or wet separation, can be by inside coal
Sulfide, metallic element, noble element, radioactive element, common mineral matter etc. sort out the utilization of resources, can be made into high-purity
Coal dust or high-purity water-coal-slurry, high-purity coal briquette is made after also water-coal-slurry can be dehydrated with dewatering screen, high-purity coal as burning can be real
The clean combustion of existing coal, can compare favourably with natural gas, and tail gas can not have to desulfurization and dedusting again;Low-temperature burning can be achieved, can not
Nitrogen oxides is produced, denitration again can not had to.
The present invention is used as nuclear fuel picking equipment in use, selected effect can be greatly improved, and can substantially reduce cost,
Mine tailing can be made more environmentally-friendly.When handling nuke rubbish, the high radioactivity element extraction inside nuke rubbish can be come out, reach one
Determine can to put into after concentration nuclear reactor again nuclear transmutation occurs to turn into low to put material, tailing can be made to turn into low-activity thing
Matter, you can glass solidification fills, and nuke rubbish can be made not have potential safety hazard.With the birth of new energy, nuclear reactor will
Change in quality for nuke rubbish incinerator.
The present invention is used as reactor in use, vortex can be used to make the mutual collision friction of molecule, can greatly promote chemical anti-
Should, catalytic effect can be achieved, can be used as the catalytic reaction device of denitration device.
The present invention makes full combustion of fuel as burner or boiler in use, adding using swirl combustion and being vortexed to crush, can
Using any fuel, combustion zone temperature can be made to keep stable and uniform, can more accurately control furnace temperature, low-temperature burning can be achieved, can
Thoroughly prevent nitrogen oxides generation.When coal-fired, coal cinder can be made abundant by the broken burning of continuous stripping while continuous burning.
The synchronous calcium carbonate aggregate chips that adds can realize dry desulfurization in stove, and in-furnace temperature is uniform, and vortex promotes reaction, can thoroughly realize dry method
Abundant desulfurization.Burner, boiler dusting desulfurization and denitrification integral can be achieved, realize thoroughly environmental protection.
The present invention is used as milling equipment in use, making particulate matter gradually levigate using vortex crushing grinding, can make each
Kind powder, can also grind flour etc., can make wholemeal.Grinding powder can dry grind or wet-milling, can be real as carrier by the use of air
Now dry grind, wet-milling can be achieved by the use of water as carrier, superfine powder, nano-powder etc. can be made.It also is used as coal-grinding and powder-spraying machine
Or coal-grinding pulp shooting machine, raw coal dry grinding or wet-milling can be sprayed coal dust or coal slurry spray into the burning such as kiln.
The present invention to achieve the above object, is achieved through the following technical solutions:
Flour mill, including housing and transmission device are reacted in separation, and transmission device is set on housing, housing chamber, shell are set in housing
Vortex wheel is set in body cavity, and transmission device is connected with vortex wheel, and housing chamber one end sets housing chamber import, and the housing chamber other end is set
Put housing chamber outlet.
Housing cavity wall up to sets and correspondingly sets discharging around spacer body around spacer body, housing chamber periphery together less.
At least a piece housing cavity wall presses close to vortex wheel outer rim.
Spray chamber is connected outside housing chamber import, spray chamber sets spray chamber import, and spray chamber sets multiple spray equipments.
Liquid feed device is set on the inwall of housing chamber periphery.
Housing chamber shaft end sets housing chamber import, and housing chamber other end shaft end sets housing chamber to export.
Heat-collecting device is set on housing cavity wall.
Automatic feeder is set in housing chamber import, temperature measuring equipment is set on housing cavity wall, and temperature measuring equipment control is certainly
Dynamic feeding device.
Housing chamber sets flow regulator in outlet.
On the circumference of vortex wheel periphery and it is respectively provided with multiple fluid striking gears on axial direction.
The advantage of the invention is that:Circular motion and fluid motion are taken full advantage of, makes full use of eddy motion, makes fluid
It is gradually released, effect improves synchronous improve with rotating speed.Fluid screw vertically, in axial movement, gradual quilt
Separation.Make the mutual collision friction of molecule using vortex, a large amount of free radicals can be produced, chemical reaction can be greatly promoted, can be achieved to urge
Change effect, can be used as catalytic reaction device.Make particulate matter gradually levigate using crushing grinding is vortexed.Utilize swirl combustion
Add vortex is broken to make full combustion of fuel, while combustion zone temperature is kept stable and uniform, can more accurately control furnace temperature, can be real
Existing low-temperature burning, it can thoroughly prevent nitrogen oxides generation.When coal-fired, coal cinder can be made constantly to be peeled off while continuous burning
Broken burning is abundant.The synchronous calcium carbonate aggregate chips that adds can realize dry desulfurization in stove, and in-furnace temperature is uniform, and vortex promotes reaction,
The abundant desulfurization of dry method can thoroughly be realized.Boiler dusting desulfurization and denitrification integral can be achieved, burner, boiler is realized thorough ring
Protect.The present invention have be simple to manufacture, equipment is changeable, application field is extensive, manufacturing cost is low, manufacturing process is simple, use
The advantages that cost is low, maintenance cost is low, service life is long.
Brief description of the drawings
Accompanying drawing 1 is the agent structure schematic diagram of the present invention;
Accompanying drawing 2 is the main structure diagram of one of the embodiment of the present invention;
Accompanying drawing 3 is two main structure diagram of the embodiment of the present invention;
Accompanying drawing 4 is three main structure diagram of the embodiment of the present invention;
Accompanying drawing 5 is four main structure diagram of the embodiment of the present invention;
Accompanying drawing 6 is five main structure diagram of the embodiment of the present invention;
Accompanying drawing 7 is six main structure diagram of the embodiment of the present invention;
Accompanying drawing 8 is seven main structure diagram of the embodiment of the present invention;
Accompanying drawing 9 is eight main structure diagram of the embodiment of the present invention;
Accompanying drawing 10 is nine main structure diagram of the embodiment of the present invention.
Embodiment
The agent structure of the present invention includes housing 1 and transmission device 2, and transmission device 2 is set on housing 1, is set in housing 1
Housing chamber 3, sets vortex wheel 4 in housing chamber 3, and multiple fluid striking gears are respectively provided with the periphery circumference of vortex wheel 4 and on axial direction
5, transmission device 2 is connected with vortex wheel 4, and the one end of housing chamber 3 sets housing chamber import 6, and the other end of housing chamber 3 sets housing chamber to go out
Mouth 7.
The scope of housing 1 includes support, support, pipeline, casing and power set etc., and each position, which can be referred to as, does
Housing.Housing 1 can also be formed integrally with power set, form the housing of an entirety.The present invention can select as needed
Different material manufactures, the materials such as metal, alloy, ceramics, glass, fiberglass, carbon fiber, plastics, nylon, foamed material can be used
Material manufacture.
Transmission device 2 includes power transmission shaft, bearing or bearing shell, axle bed etc., and transmission device 2 sets power transmission shaft, utilizes power transmission shaft
Realize that power inputs, drive present invention work.The connecting power device of transmission device 2 realizes that power inputs, and drives present invention work.
Power set can use motor or engine etc., and power set can be directly connected to transmission device 2, can also be passed by shaft coupling
Dynamic, belt transmission, chain drive, gear drive etc. realize that power inputs, and can also be become by realizations such as belt pulley, reductors
Speed.As engine tail gas processing device in use, the waste gas connection housing chamber import 6 of engine discharge can also be utilized directly to push away
Dynamic equipment operation, can simplify structure, can replace silencer simultaneously.Power set can also be directly prepared into one with housing 1, also can be straight
Connect by the use of power set and be used as transmission device 2.Also converter technique etc. can be used to adjust rotating speed, can adjust separation reaction effect.Pass
Dynamic device 2 can be set forms cantilever design at one end, and the rotating shaft other end of transmission device 2 can also be made to connect spin stabilization
Device, the axial length of equipment can be significantly lengthened, Reaction Separation effect can be improved.Spin stabilization device can be set support, axle bed,
Bearing, bearing shell or sealing device etc., rotation can be made more stable.Power transmission shaft of the present invention is vertically arranged when installing and using, spin stabilization
Thrust bearing can be set in device, can preferably improve service life, and support can be made demountable, can facilitate installing/dismounting axle
Hold, support can set multiple screw push rods to adjust radial and axial position respectively;Bearing block, which may be alternatively configured, axially opens body structure, can
More convenient installing/dismounting.Power transmission shaft is vertically arranged when installing and using treatment liquid, can be in lower bearing while setting shaft sealer
Baffle board with rotating shaft synchronous rotary is set in the rotating shaft of top, and the aqueous that can be will leak out is thrown away to the periphery, aqueous can be avoided to let out
Drain on lower bearing.During wet-treating flue gas, to avoid aqueous from leaking down along central core region, it can be set in housing chamber lower, outer perimeter
Around runner, you can avoid aqueous from being revealed from central core region, can also improve air inlet runner area.
Transmission device 2 is set on housing 1.Transmission device 2 can use the plan of establishment of blower fan or water pump transmission device, transmission
When the power transmission shaft of device 2 is vertically arranged installation, usual transmission device 2 connects power end and may be provided in the top of housing 1, can conveniently dismantle.
Housing chamber 3 is set in housing 1.Housing chamber 3 can be made of one or open body structure, be combined during installation, shell
Body cavity 3 also can arbitrarily open body as needed, can be convenient for assembly.The inwall of housing chamber 3 can also set wear-resistant material layer or resistance to as needed
Corrosion layer etc. improves service life, and glass flake anti-corrosion can use during desulphurization denitration, and region easy to wear also can be wear-resisting in surface patch
Piece builds abrasive brick, during plant maintenance, carries out repair maintenance.The lumenal cross-section of housing chamber 3 can be usually set to circle,
Vortex can be preferably formed in housing chamber 3.The axis of housing chamber 3 is vertically arranged installation, flue gas can be made to move from bottom to top, make aqueous
Move from the top down.Housing chamber 3 can generally make cylinder equally thick up and down, can simplify structure, also can as needed by
Housing chamber 3 makes the different thick structure of the structure to the gradual thickening of entrance point, multistage internal diameter or polygonal structure, can be real respectively
Existing different functional effect., can basis on the inwall of housing chamber 3 during for de-suphur of kiln fume denitration, chemical industry peculiar odor treatment etc.
Specific working condition sets anti-corrosion or anticorrosion antiwear layer.The present invention is used to set on the inwall of housing chamber 3 when boiler, burner etc.
Put refractory insulating layer.
Vortex wheel 4 is set in housing chamber 3.It is preferable that vortex wheel 4 is arranged on effect on the axis of housing chamber 3, outside vortex wheel 4
Week and the inwall of housing chamber 3 effect that be arranged in parallel are preferable.Vortex wheel 4 can whole installation into cylinder, diameter unequal multistage circle
The structures such as cylindricality, truncated cone-shaped or the unequal multistage truncated cone-shaped of diameter, stream wheel 4 is generally arranged to cylinder, vortex wheel 4
Outside can comply with the setting of the inwall of housing chamber 3, and the longer effect of the axial length of vortex wheel 4 is better, the axial length of vortex wheel 4 and vortex
Taking turns the ratio of 4 diameters can arbitrarily set as needed, can be tried one's best on the basis of the spin stabilization of vortex wheel 4 is not influenceed and increase vortex
Take turns 4 axial lengths;Vortex wheel 4 is generally arranged to an entirety, vortex wheel 4 can be arranged to hollow or solid construction;
Vortex wheel 4 can also be arranged to multiple Split type structures, be installed together;The outer surface of vortex wheel 4 can be arranged to light
Face or hair side, fluid motion is driven using the boundary effect of the outer surface of vortex wheel 4, separating effect can be improved;Can also
It is threaded on 4 all or part of periphery of vortex wheel, groove or multiple fluid striking gears improve fluid and stir effect;Also may be used
The blade of multiple arbitrary structures is set to be dialled as fluid to be uniformly distributed according to working condition requirement in 4 all or part of periphery of vortex wheel
Dynamic device, blade can also can play a part of axial wheel, can be pressurized with convection body defeated with being in axially certain angle of inclination
Send, promote fluid to be axially moved;Fluid striking gear can also use the various structures such as pole, pipe;Fluid striking gear quantity
More, the broken of convection body, mixing effect are more violent;Fluid striking gear radical length is shorter, and separation reaction effect is better, stream
Body flow pressure is smaller;The distance between the outer rim of vortex wheel 4 and the inwall of housing chamber 3 can be adjusted arbitrarily as needed, and distance is got over
Closely, fluid oscillating friction is more violent;Also any one inwall of piece housing chamber 3 can be pressed close into the outer rim of vortex wheel 4, housing chamber as needed
3 inwalls press close to the outer rim of vortex wheel 4, and eddy friction can be made more violent, as reactor in use, reaction effect can be improved, as
For milling equipment in use, grinding intensity can be improved, shortcoming is increased wear;Vortex wheel 4 can select different materials as needed
Material manufacture, the manufacture such as metal, ceramics, fiberglass, carbon fiber, plastics, foamed material can be used.
Transmission device 2 is connected with vortex wheel 4.The power transmission shaft of transmission device 2 will be fastened on the central core region of vortex wheel 4,
Ensure that vortex wheel 4 rotates steadily, wheel disc, reel, wheel body etc. can be set in the central core region of vortex wheel 4.Power transmission shaft can also use sky
Mandrel, it can be also welded as a whole with vortex wheel 4, structure can be simplified.It will can also be driven during for purification of air, smoke exhaust ventilator etc.
The motor of device 2 is formed integrally with vortex wheel 4, can save space reduction cost.Multiple axial wheels can also be used as whirlpool
Stream wheel 4, multiple axial wheels are coaxially mounted on the power transmission shaft of transmission device 2, and shortcoming is complicated.
The one end of housing chamber 3 sets housing chamber import 6.Housing chamber import 6, housing chamber import 6 can be set in the one end of housing chamber 3
It may be provided in the side wall of housing chamber 3, one or more housing chamber imports 6 can be set;Also can be in the housing where housing chamber import 6
Scroll casing shape or annular diversion cavity are set at chamber 3, fluid can be more convenient and enter housing chamber 3, make fluid along the cross section tangent line of housing chamber 3
Direction enters, and can reduce vortex wheel 4 and wear;Housing chamber import 6 may also be arranged on the shaft end of housing chamber 3, and it is axially defeated that fluid can be achieved
Enter.Also the flow regulator such as air door or valve can be set in housing chamber import 6, can preferably adjusts fluid motion speed and stream
Amount, can preferably adjust separation reaction effect, and flow regulator can also use Automated condtrol, and flow tune can be better achieved
Section.The present invention is used as coal-grinding and powder-spraying machine in use, setting air door effect more preferable in housing chamber import 6.The present invention as burner,
Boiler etc. also can set burning torch in housing chamber import 6, automatic ignition can be achieved in use, can be lighted a fire in housing chamber import 6.
Also can be set in housing chamber import 6 automatic feeders such as stirring cage, discharger be uniformly discharged into housing chamber import 6 it is coal-fired,
Biomass fuel or rubbish etc. and dry-desulphurizer etc., during using fluid fuel, also Fuel lance can be arranged on housing chamber
In import 6.
The other end of housing chamber 3 sets housing chamber to export 7.In the other end of housing chamber 3 housing chamber can be set to export 7, housing chamber
Outlet 7 can be located in the side wall of housing chamber 3, can better profit from centrifugal force, can be more convenient housing chamber and be exported 7 connecting pipes.
Scroll casing shape can be made in the cross section of housing chamber 3 that housing chamber is exported at 7, centrifugal force can be better profited from, fluid can be made more suitable
It smooth discharge, can more save, fluid striking gear can be set in the vortex wheel in spiral case, fluid striking gear can also be set
Axially connecting multiple linear leafs are set to, supercharging impeller can be played a part of, fluid can be made with higher pressure output, simultaneously
Flow can be improved.Housing chamber outlet 7 can also be arranged on shaft end, and fluid can be achieved and axially export.7 can also be exported in housing chamber
Upper setting flow regulator, various valves, air door etc. can be used, flow regulator adjustable fluid flow, can adjust shell
Pressure in body cavity 3, functional effect can be improved.
During present invention work, vortex wheel 4 rotates, and makes to form vortex in housing chamber 3.The power transmission shaft of the present invention of this agent structure
Can it is horizontal, be vertically arranged or tilting installation.When being vertically arranged installation, effect is more preferable, can save floor occupying area, and can be set in the periphery of housing 1
Four mullions form four square frames, and cross beam support is set respectively in casing above and below, take crossbeam apart during plant maintenance.This
Agent structure can be used as reactor, burner, milling equipment etc. to use, and simultaneously can transfer out fluid.
The present invention is used as reactor in use, making the mutual collision friction of molecule using vortex, can promote to chemically react, can
Catalytic effect is realized, can be widely used for chemical field, can be used as denitration device, hydrogen, hydrocarbon etc. can be used to make
For denitrfying agent, natural gas or methanol Pintsch process can be used into hydrogen as denitrfying agent when temperature is relatively low;It can also be used in flue gas
Hydrocarbon, hydrogen as denitrfying agent, also by adjusting furnace atmosphere or steam can be sprayed water by cigarette to furnace high-temperature band
Carbon particle, reaction of carbon monoxide in gas fall to make hydrogen as denitrfying agent, can reduce cost, purifying smoke.Also flue gas can be made
Dry type desulfurizing reaction is completed in housing chamber 3, can be by the use of alkali metal or calcium hydroxide etc. as dry desulfurizer, desulfurizing agent is in housing
The inner powder of chamber 3 wears into fine powder and participates in desulphurization reaction.
The present invention is used as burner apparatus in use, hot gas directly can be provided to boiler, kiln etc., can reduce boiler improvement
Expense, any fuel such as coal, oil, gas, biomass, rubbish, water-coal-slurry, coal dust can be used, can be set on the inwall of housing chamber 3 resistance to
Fiery heat-insulation layer, the power transmission shaft of vortex wheel 4, fluid striking gear 5 and transmission device 2 can use exotic material to manufacture, transmission dress
Put and the cooling device such as fan blade or water sprinkling cooling wheel may also set up on 2 power transmission shaft, aqueous can be also sprayed on fan blade,
Water receiving casing is set around fan blade, and the aqueous for making to throw away, which is collected, flows back to pond.The axis of housing chamber 3 is vertically arranged installation,
Housing chamber import 6 may be provided on the lower sides of housing chamber 3 that effect is preferable, can better profit from gravity and realize that fuel sorts, can
The larger fuel of particle is in the lower combustion of housing chamber 3 all the time, the ash content of after-flame is made with the upward out combustion zone of air-flow
Fuel realizes uniform swirl combustion in housing chamber 3, makes full combustion of fuel using swirl combustion plus vortex are broken, especially
When being coal-fired or rubbish etc., coal cinder or rubbish etc. can be made abundant by the broken burning of continuous stripping while continuous burning.No
Pipe uses any fuel, precisely supplies fuel, when adjusting air quantity, combustion zone temperature is kept stable and uniform, can be more smart
Accurate control furnace temperature, low-temperature burning can be achieved, nitrogen oxides generation can be prevented.Synchronous addition calcium carbonate aggregate chips, which can be realized in stove, to be done
Method desulfurization, in-furnace temperature is uniform, and vortex promotes reaction, and the abundant desulfurization of dry method can be achieved.Also can be by the housing at housing chamber import 6
The internal diameter of chamber 3 somewhat increases, and can preferably store fire and maintain burning.Also stirring cage, discharger etc. can be set automatic in housing chamber import 6
Feeding device, may also set up multiple housing chamber imports 6 and be fed respectively, can by automatic feeder into housing chamber import 6
It is even to be discharged into coal-fired, biomass fuel or rubbish etc. and dry-desulphurizer etc., using conducts such as combustion gas, fuel oil, water-coal-slurry, coal dusts
During fuel, Fuel lance is automatic feeder.Temperature measuring equipment can be set on the inwall of housing chamber 3, and temperature measuring equipment can use
The devices such as thermocouple, temperature control instrument, temperature measuring equipment can automatically control automatic feeder, and in-furnace temperature reaches the design temperature upper limit
When, it is automatic to disconnect automatic feeder power supply, when in-furnace temperature reaches design temperature lower limit, turn on automatically automatic feeder
Power supply.Gap can be increased between casing bottom and power transmission shaft, can air intake to power transmission shaft cool.
The present invention is used as milling equipment in use, the also wet-milling that can dry grind, dry grinding more save.Erect the axis of housing chamber 3
When putting installation, it is preferable that housing chamber import 6 may be provided at effect on the lower sides of housing chamber 3 of the periphery of vortex wheel 4, can be from housing chamber
Import 6 is discharged into the material for needing grinding, may also set up automatic discharge unit.Gravity can be better profited from and realize grain sorting, can
The larger material of particle is in the bottom grinding of housing chamber 3 all the time, make the good powder granule of grinding with the upward out grinding of air-flow
Area, from the outflow of housing chamber outlet 7, material can be made to realize vortex grinding in housing chamber 3, particulate matter is mutually collided in vortex
Friction, until levigate.A variety of powders, coal dust etc. can be ground, can also grind flour etc., grinding powder can dry grind or wet-milling, with sky
Dry grinding can be achieved as carrier in gas, and wet-milling can be achieved by the use of water as carrier.Housing chamber import 6 can be arranged on housing chamber 3
On periphery, it can enter to need the raw material and air or water that grind simultaneously, will can directly be sorted after crushing material, thicker powder exists
Continue grinding in housing chamber 3, thinner powder passes through the output of housing chamber outlet 7 with air or water.Coal-grinding also is used as to dust
Machine, raw coal can be dry grinded, spray coal dust from housing chamber outlet 7, the burning such as Kiln boiler can be injected directly into.Also can be in housing chamber 3
Cleaning door is set in lower base or side wall, the material that cleaning door cleaning is not easy grinding can be opened, can also be set on cleaning door
Stirring cage or discharger etc. realize automatic ash-discharging.Equipment attrition can be reduced, for coal pulverizer, coal-grinding and powder-spraying machine, burner, boiler etc.
When can reduce additional energy caused by grinding lime-ash, high-purity coal dust can be made, sulfide can be reduced, ash grade into burner hearth fire
Burn, can preferably dedusting, desulfurization.Coal-fired purifying burning can be achieved.
Housing chamber 3 make to the gradual thickening in the end of housing chamber import 6 structure or multistage internal diameter is different slightly enters to housing chamber
Mouthful 6 ends successively the structure of thickening when, separating effect can be achieved, available for dedusting, desulphurization and denitration, sewage disposal, desalinization etc.
Need the technical field separated.
The structure of one of the embodiment of the present invention is:On the basis of agent structure, at least provided with one of ring on the inwall of housing chamber 3
Around spacer body 8, the periphery of housing chamber 3 correspondingly sets discharging opening 9 around spacer body 8.Can be by the outer rim of vortex wheel 4 and the inwall of housing chamber 3
The distance between increase, one or multi-channel circular spacer body 8 can be set on the inwall of housing chamber 3, by the axial isolation of housing chamber 3 into
Multiple regions, it can stop that fluid flows along the peripheral, axial of housing chamber 3 around spacer body 8, separating effect can be achieved, while can make
Space between the inwall of housing chamber 3 and the outer rim of vortex wheel 4 increases, can make holdup time of the fluid in housing chamber 3 and motion away from
From increasing, chemical reaction effect can be improved.Isolate is because of differences such as proportion, granular sizes, to the movement velocity of the periphery of housing chamber 3
Difference, different isolates move to axially distinct region respectively.The distance between the inwall of housing chamber 3 and the outer rim of vortex wheel 4
Bigger, isolate is less susceptible to spring back to the periphery of vortex wheel 4, and separating effect is better.Set to surround together on the inwall of housing chamber 3 and divide
During spacer 8, housing chamber outlet 7 can will be arranged on around spacer body 8 and nearby or along the spiral inner wall of housing chamber 3 will be set, plurality of circumferential
Spacer body 8 also can spiral set, can make isolate along the inwall of housing chamber 3 to the end of housing chamber import 6 axially flow, separation can be improved
Effect.Be arranged in parallel plurality of circumferential spacer body 8 generally on the inwall of housing chamber 3 with the cross section of housing chamber 3, can avoid fluid along shell
The inwall of body cavity 3 axially flows, and can improve separating effect.When circular spacer body 8 together is set on the inwall of housing chamber 3, it can also incite somebody to action
The inwall of housing chamber 3 be integrated around spacer body 8, the inwall of housing chamber 3 can be arranged to housing chamber export 7 end internal diameters by
Tapered small structure, structure can be simplified, improve separating effect.Vortex wheel 4 is arranged to be gradually increased to 7 end external diameters of housing chamber outlet
Truncated cone-shaped can improve flow.The periphery of housing chamber 3 correspondingly sets discharging opening 9 around spacer body 8, can set in the axial direction multiple
Discharging opening 9, can isolate a variety of isolates, and the flow of each discharging opening 9 can be adjusted during use, can preferably be isolated
A variety of isolates.Deflector or mozzle can also be set along the cross section tangential direction of housing chamber 3 in discharging opening 9, can be preferably
Fluid is cut out, can be more convenient to discharge;Multiple discharging openings 9 also can be circumferentially set, separating effect can be improved;Can also be by axle
Upward multiple discharging openings 9 together, can be more convenient for concentrating discharging by pipeline communication, also can be by the housing chamber import 6 of pipeline
End connects with housing chamber 3, and the gas that can make to isolate is again in suction casing body cavity 3, can improve dust removing effects during for dedusting.
The movable sealing devices for discharging such as valve, air door, screw conveyor can be set in discharging opening 9, regulating flow quantity, can adjust separation
Effect, it can make isolate in housing chamber 3 under pressure, gravity, centrifugal action, be drawn off out of housing chamber 3, also can intermittently be opened
Movable sealing device for discharging draws off isolate.Also dust collecting box can be set in discharging opening 9 during dedusting, can intermittently open the row of discharging opening 9
Ash.The inwall of housing chamber 3 can be arranged to and diameter parallel, and isolate can be avoided axially to flow, can improve separating effect.
The axis of the present embodiment housing chamber 3 is vertically arranged, horizontal or tilting installation, can arbitrarily set, be used for as needed
When ore dressing, desalinization, sewage disposal, dry dust removal etc., horizontal or tilting installation is preferable.The present embodiment can be used as deduster,
Dust catcher, oxygen generating plant, blood separator, cream-milk separator, the equipment that eliminates the unusual smell, engine tail gas purifier, air purifier,
Apparatus for treating sewage, water purification apparatus, sea water desalting equipment, preparation equipment, refuse treatment plant, cleaning unit, nuclear fuel essence
Optional equipment or nuclear waste disposal equipment etc. use, and simultaneously can transfer out fluid.During dry dust removal, the axis of housing chamber 3 is horizontal
Put or during tilting installation, discharging opening 9, which is arranged on the bottom of housing chamber 3, can preferably utilize gravity discharge dust.The present invention in use,
The pressure in housing chamber 3 at housing chamber outlet 7 is more than the pressure in other regions, can better ensure that the isolate in other regions
Not to the leakage of housing chamber outlet 7, the area for reducing housing chamber outlet 7 or connection outlet pipeline etc. can be used to improve pressure.Also may be used
Pressure in housing chamber 3 at the device adjustment housings such as air door or valve chamber outlet 7 is set in housing chamber outlet 7.
Various useful compositions are sorted in use, can be extracted from sewage, waste gas as sewage, waste gas treatment equipment, can be same
Step completes dedusting, desulphurization and denitration;Also a variety of useful compositions can be selected during tails dedusting from dust, as cleaner, dust suction
Equipment can export the 7 dustless gases of discharge in use, gas can be sucked into the present invention from housing chamber import 6 from housing chamber, from each
Discharging opening 9 discharges dust, and movable sealing device for discharging is set in discharging opening 9, and interval is opened or firm discharge discharge dust,
Dust particle, the gas of a variety of different components of multiple components can be isolated from each discharging opening 9, dedusting separates with gas
It can synchronously complete.Also escape pipe can be set in discharging opening 9 when dedusting or separation solid particulate matter, escape pipe connection ash-storing bin can
Muffler, muffler connection housing chamber import 6 or the housing chamber 3 close to the end of housing chamber import 6 are set, dust gas can be achieved
Stream conveying;Also housing chamber 3 can be made scroll casing shape, separating effect is poor, does not have to typically, and discharging opening 9 is arranged on into volute outlet
Place, can be more convenient deashing.As dust catcher in use, in housing chamber import 6 filter screen can be set to isolate lump, dust is clear
Reason is convenient, and noise is low, low cost, more saves, more environmentally-friendly without dust pollution.High-temperature flue gas can be handled, realizes high temperature
Flue gas dry-type dedusting, dry type denitration can be synchronously completed when spraying into hydrogen etc..
Ash storage box can also be set during dedusting outside discharging opening 9, multiple discharging openings 9 can also be merged to a shared ash storage box
And ash hole, ash discharge can be more convenient, also in ash storage box air can be set to adopt heat pipe during for burner, hot-air suction will be adopted
Housing chamber import 6, preferably dust can be made to cool., also can be close to 6 sections of settings of housing chamber import during for gas cleaning
Plurality of circumferential spacer body 8, dust can be removed in advance, equipment attrition can be reduced, the internal diameter of housing chamber 3 can also increased, can improved
Separating effect and flow, denitration reaction area can be set exporting 7 sections close to housing chamber, denitration again after flue gas ash removal can be achieved;
Plurality of circumferential spacer body 8 can be set exporting 7 sections close to housing chamber, at 6 sections close to housing chamber import dry desulfurization can be set anti-
Area is answered, slaked lime powder can be sent into dry desulfurization reaction zone, membrane pump conveying calcium hydroxide breast can be also used, can complete flue gas dry
Dust etc. is finally removed again after method desulfurization;Also 7 sections can be exported and set respectively close to 6 sections of housing chamber import and close housing chamber
Plurality of circumferential spacer body 8, it is situated between and dry type desulfurizing reaction zone is set, calcium hydroxide can be sent into dry type desulfurizing reaction zone, can
Dry desulfurization is completed after dust is removed in advance again, finally completes the purification of dust etc. again.
As air separation equipment, oxygen generating plant, the equipment of making nitrogen, rare gas producing equipment in use, air can be inhaled
Enter the present invention, the multiple gases such as oxygen, nitrogen, inert gas can respectively be isolated by from each discharging opening 9, directly by various gases
Collection utilization.During special requirement, various gas secondary separations can be obtained into high-purity gas.Used as oxygen generating plant
When, the present invention can be drawn air into, 7 can be exported from housing chamber and isolate nitrogen etc., oxygen is isolated from discharging opening 9.Oxygen processed into
This is extremely low, and boiler, kiln, engine etc. can be made to realize pure oxygen burning, can reduce energy consumption, improves the thermal efficiency, prevents nitrogen oxides
Discharge.Also waste gas can be used to recycle, ignition temperature can be reduced, reduce equipment and materials requirement.
As preparation equipment, refuse treatment plant in use, mineral or rubbish can be ground into particle after, with water or air
Particle is sent into the present invention and carries out wet separation or dry separation:Water reusable edible, can be by the larger metallic element of proportion, heavy element point
Do not separated from discharging opening 9, useless composition is separated from housing chamber outlet 7, can be filled after useless composition dehydration, You Jicheng
Point can spontaneous fermentation degraded, finally realize innoxious, environmental pollution can be prevented, realize resource circulation utilization.Can by it is useful into
Part, multi mineral, useless composition respectively are isolated by coming from each discharging opening 9, and during garbage disposal, useless composition can fill, organic
Granular organic fertilizer is pressed into after composition fermentation, can thoroughly prevent environmental pollution, realize resource circulation utilization.
As cleaning unit in use, coal can be made into coal dust, dry separation or wet separation can be used, can be by the vulcanization inside coal
Thing, metallic element, noble element, radioactive element, common mineral matter etc. sort out the utilization of resources from discharging opening 9, can be by height
Pure coal dust or water-coal-slurry are separated from housing chamber outlet 7, be can be made into high-purity coal dust or high-purity water-coal-slurry, can also be used water-coal-slurry
High-purity coal briquette is made after dewatering screen dehydration, can be advantageous to transport, high-purity coal as burning is the clean combustion that coal can be achieved, can
To be compared favourably with natural gas, tail gas can not have to desulfurization and dedusting again.
As sea water desalting equipment in use, can export 7 from housing chamber isolates fresh water, isolated from discharging opening 9 highly concentrated
Salt solution is spent, salt can be obtained by evaporating precipitation.Handle sewage, purification of water quality or during desalinization, water purification up to standard, organic can be made
Composition, gas ingredients, heavy element, metallic element, sand and dust, high strong brine or saline mixture etc. are from each different discharging opening 9
Discharge.The mothers and sons present invention is set, two are carried out to high strong brine, organic component, gas ingredients of discharge etc. with each height present invention
Secondary processing, multistep treatment can further separate a variety of salinities, organic component, gas ingredients.As sewage disposal device in use,
Salinity in sewage, heavy metal etc. can be disposed, with reference to desalinization, by the sewage containing high concentration organic principle from housing
Carry out biochemical treatment 7 is isolated in chamber outlet, and the reclaimed water after processing is returned in the sewage of coagulation system, by water purification up to standard from going out
Material mouth 9 isolates discharge.As water purification apparatus in use, with reference to desalinization, the heavy element in water can be separated
Fall, retain beneficial element, the processing such as the organic component in water, chlorine, microorganism, worm's ovum is clean.Heavy water can be separated, can
Tap water quality is set to exceed mineral water, snow mountain flood icing water.Also it can extract heavy water and be used for industrial circle.
As refining equipment in use, crude oil can be directly sucked in the present invention, crude oil by vortex fluid motion influence and
The joint effect such as centrifugal force caused by vortex and gravity, realizes low temperature pyrolyzer, realizes various composition separation.Member containing weight can be made
Element, metal, sulphur, pitch, paraffin, heavy oil, lubricating oil, diesel oil, kerosene, gasoline etc. are successively from close to each of housing chamber import 6
Discharging opening 9 is discharged.The intermediate of two kinds of oil contents can be re-entered in crude oil and separated again, may also set up the mothers and sons present invention, use
Each height present invention carries out secondary separation, multi-stage separation to the various compositions of discharge, and the superelevation degree of purity of various compositions can be achieved,
High-purity gasoline, diesel oil, lubricating oil, wax, a variety of oil products, sulphur, heavy metal, metal, lead, radioactive element can be extracted
Deng, can make oil product thoroughly it is unleaded, without radioactive element pollute.Whole production process is pollution-free, is discharged without waste water, waste gas, oil refining
Process is thoroughly environmentally friendly, and resource, which is fully received, to be utilized, and can substantially reduce oil refining cost.Low temperature pyrolyzer greatly reduces high temperature to crude oil
The destruction of macromolecular structure, the generation of oil gas, petroleum slag, pitch, wax etc. is reduced, oil yield is greatly improved, can improve
The oil yield of high-quality oil product.
The present embodiment is as milling equipment in use, setting multiple tracks ring on the inwall of housing chamber 3 close to housing chamber outlet 7
During around spacer body 8, the powder of a variety of particle diameters can be sub-elected, the powder that the discharging opening 9 closer to housing chamber outlet 7 is selected is thinner,
Superfine powder or nano-powder can be made, can also make carbene.Also raw coal can be dry grinded, dry separation can be completed simultaneously, can from it is each go out
Various mineral in coal are selected in material mouth 9, coal dust is sprayed from housing chamber outlet 7, the burning such as Kiln boiler can be injected directly into.
The present embodiment when being used as burner can more preferable accumulation of heat, on the inwall of housing chamber 3 close to housing chamber outlet 7
When plurality of circumferential spacer body 8 is set, dry dust removal in stove can be better achieved.
As smoke exhaust ventilator in use, flue gas can be sucked into the present invention from housing chamber import 6, oil smoke can be separated, make cigarette
Gas discharge thoroughly environmental protection, the smokeless gas after processing are discharged from the discharge of housing chamber outlet 7, waste oil from discharging opening 9.
As air cleaning facility in use, can be used as novel indoor air device, 7 points can be exported from housing chamber
Pure air is separated out, dust particle etc. is isolated from discharging opening 9.Also can VMC main frame, can be by the cleaning after separation
Air is sent into interior, and dirty air is stayed in into outdoor.
As eliminating the unusual smell, equipment isolates lighter gas in use, 7 can be exported from housing chamber, is isolated from discharging opening 9
Heavier gas etc., different gas with foreign flavor can be directed to and handled using the methods of burning, collect or chemically react.
As oil-gas recovery device in use, recyclable a variety of oil vapours, 7 can be exported from housing chamber and isolates clean sky
Gas, oil gas is isolated from discharging opening 9, the oil gas isolated can use the measure recovery such as condensation, spray, solvent absorption, after recovery
Residual gas can be re-fed into housing chamber import 6 and participate in separation again, form closed cycle, it is final to realize recovery completely.
The present invention is as nuclear fuel picking equipment or nuclear waste disposal equipment in use, 7 Hes can be exported from housing chamber respectively
Discharging opening 9 sub-elects that proportion is less and the larger useful element of proportion, can use multipass sort, progressively purification, can be with
Selected effect is greatly improved, tailings can be made more environmentally-friendly., can be by the high radioactivity member inside nuke rubbish when handling nuke rubbish
Element extracts input nuclear reactor generation nuclear transmutation again and puts element as low, can put material glass solidification landfill by low.
Two structure of the embodiment of the present invention is:On above architecture basics, at least inwall of a piece housing chamber 3 presses close to whirlpool
Stream 4 outer rims of wheel.Any one inwall of piece housing chamber 3 can be pressed close into the outer rim of vortex wheel 4 as needed, the inwall of housing chamber 3 presses close to vortex
4 outer rims are taken turns, eddy friction can be made more violent, the inwall of a piece housing chamber 3 that can generally will be close to housing chamber import 6 presses close to vortex wheel
4 outer rims;As reactor or burner in use, reaction effect can be improved;As milling equipment in use, grinding effect can be improved
Fruit;Mineral cleavage can be better achieved when being used as preparation equipment, effect can be improved;Used as engine tail gas processing device
When can improve three-element catalytic reaction effect, the waste gas connection housing chamber import 6 of engine discharge can also be utilized to push directly on and is set
Received shipment row, structure can be simplified, silencer can be replaced simultaneously, also housing chamber import 6 and housing chamber outlet 7 can be all separately positioned on
On axial direction, tail gas axle is entered axle and go out, the full-floating bearing used in existing turbocharging can be utilized on transmission device 2, can profit
With the lubricating system of engine and cooling system etc..Also air-admission pressure-booster for engine can be set in the either end of housing chamber 3, generally may be used
The end of housing chamber import 6 is located at, housing chamber import 6 may be provided in the side wall of housing chamber 3, and housing chamber outlet 7 may be provided in shaft end, can be more square
Just blast pipe is connected, structure can be simplified.Air-admission pressure-booster for engine can use the knot of existing various turbocharger of motor
Structure, plenum of the air-admission pressure-booster for engine to engine.Vortex wheel 4 drives the supercharging impeller rotation of air-admission pressure-booster for engine
Turn, the turbine of turbocharger is instead of using vortex wheel 4, can be used simultaneously as turbocharger of motor, can be by turbine
Booster, ternary catalyzing unit replacing whole.The inwall of a piece housing chamber 3 that housing chamber import 6 can generally be will be close to presses close to vortex wheel 4
Outer rim.
The present embodiment can also be used as burner, reactor, milling equipment, preparation equipment etc. to use, and be used as burner
When can realize dedusting in stove, fuel can be made to press close in the inwall of housing chamber 3 burning is completed in one section of region of the outer rim of vortex wheel 4, can
Flue gas is set on the inwall of housing chamber 3 and complete dry dust removal around the region of spacer body 8, can be isolated from each discharging opening 9
The dust of various granularities.It can be used for denitrating flue gas, dry type desulfurizing, dry dust removal, chemical reactor etc. when being used as reactor,
Flue gas can be made to press close in one section of region of the outer rim of vortex wheel 4 to complete denitration reaction and dry type desulfurizing reaction in the inwall of housing chamber 3, can
Denitrfying agent is used as using caused hydrocarbon, hydrogen etc. in kiln gas, can be by the use of alkali metal or calcium hydroxide etc. as dry
Formula desulfurizing agent, desulfurizing agent constantly constantly participate in desulphurization reaction into fine powder, fine powder by grinding in housing chamber 3, can make flue gas
Set on the inwall of housing chamber 3 and complete dry dust removal around the region of spacer body 8, various grains can be isolated from each discharging opening 9
The dust of degree.As chemical reactor in use, can promote to chemically react, while reacted material can be realized and sorted.Make
For milling equipment or preparation equipment in use, that material can be made to press close in the inwall of housing chamber 3 is complete in one section of region of the outer rim of vortex wheel 4
Into grinding, set on the inwall of housing chamber 3 and complete powder sorting around the region of spacer body 8, can isolated from each discharging opening 9
The powder of various different grain sizes or proportion.It is more preferable as pumped (conveying) medium wet-milling wet separation effect using water during ore dressing.
Three structure of the embodiment of the present invention is:On above architecture basics, spray chamber 10 is connected outside housing chamber import 6,
Spray chamber 10 sets spray chamber import 11, and spray chamber 10 sets multiple spray equipments 12.Spray can be set outside housing chamber import 6
Room 10, housing chamber import 6 connect spray chamber 10 outside, and housing chamber import 6 can arbitrarily be arranged on housing chamber 3 according to concrete structure
Side wall or shaft end, spray chamber 10 can use the spray column or spraying box etc. of various structures, directly can also replace spraying with flue
Room 10 is drenched, structure can be simplified, saves space, the central axis of spray chamber 10 is horizontal or is vertically arranged.Can be in spray chamber away from housing
One or more spray chamber imports 11 are set on the end face at the end of chamber import 6 or side wall.Spray chamber 10 sets multiple spray equipments 12,
Spray equipment 12 can use shower nozzle or nozzle of various structures etc., and shower nozzle, the spray of multiple various structures can be set in spray chamber 10
Mouth etc., multiple shower nozzles or nozzle can be set around intensive on the periphery inwall of spray chamber 10, radially be sprayed to the center of spray chamber 10
Water, dense range of atomization can be formed in spray chamber 10.Water-jacket space can also be set on the outer wall of spray chamber 10 or inwall, by shower nozzle
Or nozzle is uniformly set on the inwall of spray chamber 10 and connected with water-jacket space, can simplify structure.Eddy spray can also be used
Mouth is arranged on the central core region of spray chamber 10 and sprayed to flue gas adverse current direction, can simplify structure.The diameter of large scale equipment spray chamber 10 compared with
When big, a plurality of water pipe can be also set in spray chamber 10, shower nozzle is set on tube wall, makes aqueous maximumlly dense atomization.Spray
Shower device 12 connects aqueous feedway, and aqueous feedway includes the devices such as pump, pipeline, sedimentation basin or water tank, aqueous supply
Device can persistently spray into the liquid such as water or buck into spray chamber 10 by spray equipment 12.The bottom of spray chamber 10 can set one
Individual or multiple liquid outlets, aqueous can be made to be exited into from the bottom of spray chamber 10 in the pond of aqueous feedway, form circulation and supply
Liquid.During for desulphurization denitration, the inwall of spray chamber 10 can also use glass flake anti-corrosion, and during plant maintenance, carrying out repair maintenance is
Can;Spray chamber 10 also can use acid-resistant stainless steel or other resistant materials to manufacture, and can simplify manufacturing process.Northern severe cold
Area, as the case may be heat-insulation layer can also be set to be incubated on the outer wall of spray chamber 10, can avoid freezing.During for denitration, also may be used
Catalyst, urea etc. are added in aqueous, with urea absorption reaction of nitrogen oxides.The discharging at 7 ends is exported close to housing chamber
Mouth 9 can also connect housing chamber import 6 or the housing chamber 3 at housing chamber import 6 by pipeline, can make the carbonated drink isolated
Mixture reenters the secondary separation of housing chamber 3, can form gas channel, can make the smooth discharge of isolate.
The power transmission shaft of the present invention of the present embodiment is horizontal, it is tilting, be vertically arranged and install and use, can during for boiler, kiln etc.
Synchronously complete air inducing, air-supply, dedusting, desulphurization and denitration.Flue gas can be made to complete primary depositing dust in spray chamber 10, in housing chamber 3
Water smoke cleaning is completed, dehydration is finally completed, finally realizes that flue gas thoroughly purifies.
Four structure of the embodiment of the present invention is:On above architecture basics, feed flow is set to fill on the periphery inwall of housing chamber 3
Put 23.Any as needed on the periphery inwall of housing chamber 3 liquid feed device 23 can be set, liquid feed device 23 can use outlet pipe,
Delivery port or shower nozzle, nozzle etc., the affiliated facility of liquid feed device 23 include pump, pipeline, flow control valve, sedimentation basin or water tank etc.
Device, the liquid such as water or buck can be flowed into or sprayed into housing chamber 3 by the liquid feed devices such as water pipe, apopore or shower nozzle 23.
Also water jacket can be set on the outer wall of housing chamber 3, is beaten on the wall of housing chamber 3.Hole makes aqueous and flue gas more in the rotation of vortex wheel 4
Sufficient contact-impact, flue gas is set to rotate the aqueous that can make on the inwall of housing chamber 3 by the thorough washing, purifying of aqueous, vortex wheel 4
And then rotate, isolate is together discharged with aqueous.The discharging opening 9 at 7 ends is exported close to housing chamber to be connected by pipeline
Housing chamber import 6 or the housing chamber 3 at housing chamber import 6, the steam water interface that can make to isolate reenter housing chamber 3
Secondary separation, gas channel can be formed, the smooth discharge of isolate can be made.During dedusting 7 ends setting one is being exported close to housing chamber
Or multiple liquid feed devices 23 spray into clear water into housing chamber 3, dust removing effects can be improved, clear water can use desulfurization and dedusting supplement water or
Clear water after processing.Multistage purification can be realized by setting multiple liquid feed devices 23 in the axial direction, and effect is more preferable.
Vortex can also be looped around together corresponding to liquid feed device 23 on spacer body 8 internal orifice together and set as needed
The circular retaining ring of the periphery of wheel 4, export 7 ends to housing chamber around retaining ring and liquid feed device 23 is set, can stop around retaining ring
Aqueous is revealed to the end of housing chamber import 6 vertically, and centrifugation can be utilized to the end internal diameter expansion of housing chamber outlet 7 around retaining ring opening's edge
Power preferably avoids aqueous from being revealed to the end of housing chamber import 6.Wet dust removal dry type desulfurizing denitrification integral, dry type desulfurizing can be achieved
Dedusting wet type denitrification integral or dry type denitration dust-remover are integrated, can greatly reduce equipment corrosion after dry type desulfurizing,
Equipment manufacturing cost can be substantially reduced, dry type denitration reaction area or dry type desulfurizing denitration can be set in the inwall front half section region of housing chamber 3
Dedusting association response area, the 3 axis second half section of housing chamber region realize aqueous clean, complete wet dust removal dehydration or wet type denitration
Dedusting is dehydrated, and realizes gas cleaning.To reduce dust to the inner wall abrasion of housing chamber 3, can also be set close to the end of housing chamber import 6
Plurality of circumferential spacer body 8 is by big particulate matter dry dust removal.When the present embodiment is used for grinding material, close to 6 sections of housing chamber import
It can be not provided with surrounding spacer body 8, dry type grinding material, collected wet powder can be achieved, collection efficiency can be greatly improved.Also may be used
One or multi-channel circular spacer body 8 is being set on the inwall of housing chamber 3 of the retaining ring to the side of housing chamber import 6, it is corresponding to surround
The discharging opening 9 that spacer body 8 is set can make isolate reenter housing chamber import 6 by pipeline communication housing chamber import 6.
Also can plurality of circumferential spacer body 8 be set on the inwall of housing chamber 3 of the retaining ring to the side of housing chamber import 6, shell can be will be close to
The discharging opening 9 of the side of body cavity import 6 connects housing chamber import 6, and remaining discharging opening 9 is gone out into a part of siccative.It is wet that powder can be achieved
Method is collected, and is re-fed into housing chamber import 6 after being selected compared with coarse dispersion and is continued grinding, can better control over powder fineness.
The present embodiment power transmission shaft is horizontal, it is tilting, be vertically arranged and install and use, may replace existing deduster, desulfurizing tower, de-
Nitre equipment, all vent gas treatment fields such as various kilns, boiler, incinerator, car and boat are can be widely used for, available for all processing cigarettes
The field of gas.During for denitration, the strong oxidizers such as hydrogen peroxide and urea etc. can be also added in aqueous, can be by nitric oxide oxygen
Polyoxygenated nitrogen is melted into, with absorbing reactions such as urea or caustic soda, lime or calcium carbonate.Dedusting with it is desulfurization integrated after, ash quantity
It is larger, the nitrate in aqueous, halide and salinity etc. can largely be taken away, boiler etc. can be made no longer to produce desulfurization wastewater
With flushing cinder waste water, environmental benefit is greatly improved.The present embodiment water consumption is few, somewhat little water, and pump energy consumption is significantly
Reduce, it is substantially negligible.When the present embodiment eliminates the unusual smell for chemical industry, peculiar smell composition can be preferably collected, also can be by peculiar smell
Composition and soda acid etc. react away, and can preferably remove peculiar smell.The present embodiment can realize wet dedusting, dedusting that can be more efficient, remove
Harmful substance, flue gas can be made more environmentally-friendly.
Five structure of the embodiment of the present invention is:On above architecture basics, the shaft end of housing chamber 3 sets housing chamber import 6,
The other end shaft end of housing chamber 3 sets housing chamber to export 7.Housing chamber import 6 can be set in the shaft end of housing chamber 3, it is another in housing chamber 3
Hold shaft end to set housing chamber to export 7, flow axis can be made to enter axle and gone out.
The present invention of the present embodiment can be used as engine tail gas processing device, and the waste gas of engine discharge can be utilized to connect
Body contact body cavity import 6 pushes directly on equipment operation, can simplify structure, can replace silencer simultaneously, tail gas axle can be made to enter axle and gone out, and passes
The full-floating bearing used in existing turbocharging, lubricating system and cooling using engine can be utilized on dynamic device 2
System etc..
Six structure of the embodiment of the present invention is:On above architecture basics, heat-collecting device is set on the inwall of housing chamber 3
13.The distance between the outer rim of vortex wheel 4 and the inwall of housing chamber 3 can be increased, can be set on the inwall of housing chamber 3 and adopt heat pipe or adopt
Hot tank etc. is used as heat-collecting device 13, and water, oil or gas etc. can be used to be used as and adopt thermal medium.Heat-collecting device 13 can press close to housing chamber
3 inwalls are set, and when heat-collecting device 13 adopts heat pipe, certain interval can be left between the inwall of housing chamber 3 by adopting heat pipe, can be more
The ability thermal efficiency is improved well.Protective plate can also be set by adopting on heat pipe, protective plate can be arranged on windward side, you can heat is adopted in raising
Area, which can also mitigate, adopts tube surface abrasion, can play protective action.Heat-collecting device 13 can use any one existing boiler
It is used to adopt heat-pipe apparatus, the boiler of various pressure can be realized as needed.Used as middle pressure, high pressure, superpressure boiler
When can close to the bottom of housing chamber 3 set high pressure adopt heat pipe, close to the top of housing chamber 3 set low pressure adopting heat pipe, low pressure adopts heat
Pipe and high pressure are adopted and realize forced circulation using boiler pump between heat pipe, can be improved and be adopted the thermal efficiency.Also can be set on the inwall of housing chamber 3
Heat exchange device for air is put, heat exchange device for air can adopt heat pipe, will enter the air of housing chamber import 6 by adopting heat
Pipe, heat exchange device for air can heat the air for entering housing chamber import 6.Heat exchange device for air can be arranged on liquid
Body heat-collecting device 13 adopts hot rear, and flue gas can be made to pass through heat exchange device for air again after adopting heat by liquid heat-collecting device 13
Waste heat is gathered, can more fully utilize heat energy.Also cleaning door can be set on the lower sides of housing chamber 3, can periodically opens deashing
Mouth cleaning is not easy the particulate matter crushed, also on cleaning door stirring cage or discharger etc. can be set to realize automatic ash-discharging.
The present embodiment can use as a variety of boiler plants, can use coal, oil, gas, biomass, rubbish, water-coal-slurry, coal dust
Etc. any fuel, refractory insulating layer can be set on the inwall of housing chamber 3, vortex wheel 4, fluid striking gear 5 and transmission device 2
Power transmission shaft can use exotic material to manufacture, and fan blade or water sprinkling cooling wheel etc. are may also set up on the power transmission shaft of transmission device 2
Cooling device, aqueous can be also sprayed on fan blade, water receiving casing is set around fan blade, the aqueous for making to throw away collects stream
Back pool.The axis of housing chamber 3 can be vertically arranged or horizontal installation, is vertically arranged that installation effect is preferable, and housing chamber import 6 is arranged on
Effect is preferable on the lower sides of housing chamber 3, can better profit from gravity and realize that fuel sorts, can make the larger fuel of particle all the time
The lower combustion of housing chamber 3 is in, makes the ash content of after-flame with the upward out combustion zone of air-flow fuel can be made to be realized in housing chamber 3
Uniform swirl combustion, make full combustion of fuel using swirl combustion plus vortex are broken, when particularly coal-fired, coal cinder can be made to exist
While constantly burning broken burning is peeled off by continuous fully.No matter what fuel used, fuel is precisely supplied, adjusts wind
During amount, it combustion zone temperature is kept stable and uniform, furnace temperature can be precisely controlled, low-temperature burning can be achieved, nitrogen oxidation can be prevented
Thing produces.Calcium carbonate aggregate chips is synchronously added when coal-fired can realize dry desulfurization in stove, and in-furnace temperature is uniform, and vortex promotes reaction,
The abundant desulfurization of dry method can be achieved.The vortex that housing chamber 3 is formed can promote the air speed on the surface of heat-collecting device 13, can be big
Width improves and adopts the thermal efficiency, greatly reduces and adopts hot area, substantially reduces cost.Eddy motion makes fortune of the thermal current in housing chamber 3
Dynamic distance greatly prolongs, and heat energy can be made fully to transmit, and realization efficiently fully adopts heat.Seam can be increased between casing bottom and power transmission shaft
Gap, can air intake to power transmission shaft cool.
The present embodiment is an efficient boiler that can burn any fuel, and burn-off rate can be made to reach 100%, is not emitted thoroughly black
Cigarette, substantially reduce carbon monoxide, sulphur and nitre discharge.
Seven structure of the embodiment of the present invention is:On above architecture basics, Automatic-feeding is set to fill in housing chamber import 6
14 are put, temperature measuring equipment 15 is set on the inwall of housing chamber 3, temperature measuring equipment 15 controls automatic feeder 14.Can be in housing chamber import 6
The automatic feeders 14 such as upper setting stirring cage, discharger, may also set up multiple housing chamber imports 6 and are fed respectively, can be by automatic
Feeding device 14 is uniformly discharged into coal-fired or rubbish etc. and dry-desulphurizer etc. into housing chamber import 6, using combustion gas, fuel oil,
When water-coal-slurry, coal dust etc. are as fuel, Fuel lance is automatic feeder 14.Thermometric can be set on the inwall of housing chamber 3
Device 15, temperature measuring equipment 15 can use the devices such as thermocouple, temperature control instrument, and temperature measuring equipment 15 can be controlled automatic by temperature control instrument
Feeding device 14, it is automatic to disconnect the power supply of automatic feeder 14 when in-furnace temperature reaches the design temperature upper limit, work as in-furnace temperature
When reaching design temperature lower limit, the power supply of turn on automatically automatic feeder 14.
The present embodiment can more accurately control furnace temperature, and the automation such as burner, boiler can be achieved.
Eight structure of the embodiment of the present invention is:On above architecture basics, Flow-rate adjustment is set to fill in housing chamber outlet 7
Put 19.It can be exported in housing chamber and flow regulator 19 is set on 7, flow regulator 19 can use various valves, air door
Deng, the regulating flow quantity of flow regulator 19, pressure in housing chamber 3 is adjusted, effect can be better achieved.
The present embodiment can adjust flow, pressure, can preferably improve effect.
Nine structure of the embodiment of the present invention is:On any of the above architecture basics, on the periphery circumference of vortex wheel 4 and axially
On be respectively provided with multiple fluid striking gears 5.On the periphery circumference of vortex wheel 4 and multiple fluid striking gears can be respectively provided with axial direction
5, fluid striking gear 5 can be made to be evenly distributed on the periphery of vortex wheel 4.It is multiple any that setting can be uniformly distributed in the periphery of vortex wheel 4
The blade of structure can play the work of axial wheel as fluid striking gear 5, blade with being in axially certain angle of inclination
With, can be with convection body pressure-increasing unit, promotion fluid is axially moved.Fluid striking gear 5 can also use a variety of knots such as pole, pipe
Structure, effect is poor, and other conveying equipments need to be used to help the fluid disengaging present invention, do not used typically.Fluid striking gear 5 can
With the scattered fragmentary structure for setting, can also being arranged to and be in axially or radially certain angle of inclination, axle stream leaf can be configured as
The structure of impeller blade, can increase flow perturbation, effect can be improved, during using blade, blade can also root connect as one,
It can use on whole piece sheet material and be segmented rabbet, sheet material is reversed to form the ternary blade that multiple roots are connected, can be made by hand
Also pressing equipment punch forming can be used, manufacturing process can be simplified, blade can connect as one with vortex wheel 4 vertically, more
Individual blade can be radially arranged on the periphery of vortex wheel 4.Blade can also be arranged to whole piece, be axially arranged on
On the periphery of vortex wheel 4, shortcoming is to be unable to convection body generation axially to stir, and also should not preferably smash fluid, and effect is poor, one
As do not have to.Fluid striking gear 5 can be formed axial direction with convection body, radially be stirred, and can make fluid in the periphery of vortex wheel 4 and housing
Concussion vortex is formed between the inwall of chamber 3, can preferably stir rotary fluid.Between the outer rim of fluid striking gear 5 and the inwall of housing chamber 3
Distance can be adjusted arbitrarily as needed, and distance is nearer, and fluid oscillating friction is more violent.The quantity of fluid striking gear 5 is more, right
The broken of fluid, mixing effect are more violent;The shorter separation of the radical length of fluid striking gear 5, reaction effect are better, fluid flow
Pressure is smaller.
The present embodiment can improve fluid flow and pressure, can improve breaking strength during for grinding.
Operation principle:The present invention simultaneously can transfer out fluid when using, and fluid realizes isolation of purified in the present invention.
After vortex wheel 4 rotates, fluid is formed vortex in housing chamber 3, smash fluid using the periphery of vortex wheel 4 while drive fluid to revolve
Turning, vortex makes the movement velocity of each particle in fluid different, each particle in fluid is formed the individual of self-movement one by one,
Centrifugal force can be better profited to separate the particle of different specific weight, realized using caused centrifugal force in vortex not year-on-year in fluid
Separation, the sorting of heavy substance.Vortex is threadingly advanced vertically, and the self-movement individual of different specific weight is fast to the peripheral motion of vortex
Degree is different, and the larger particle of proportion or particulate matter are easier, be deposited to faster on the inwall of housing chamber 3.Fluid is being axially moved
During, realized that various isolates are separated by joint effects such as fluid motion, centrifugal force and gravity.Different specific weight it is more
Kind isolate moves to the axially different region of housing chamber 3 respectively, is discharged respectively by axially distinct discharging opening 9, final real
The removing of separation, sorting or the pollutant of existing convection body etc., realizes the separation to solute in solution.Fluid is in axial movement
In be gradually released purification, the axial length of vortex wheel 4 is longer, and fluid axial direction move distance is longer, and isolation of purified effect is better.With
When gas cleaning, flue gas and the abundant Rapid contact of aqueous can be made, make flue gas by the abundant washing, purifying of aqueous, can be made fully
Flue gas after washing, purifying realizes fully dehydration, from the discharge of housing chamber outlet 7, promotes chemical reaction using vortex, realizes desulfurization
It is out of stock, realize that flue gas thoroughly purifies.Regulation flue gas flow can be realized to the removing of the height of dust particle in flue gas etc., can will be black
The height such as cigarette, dust, sulfur dioxide, nitrogen oxides, dioxin, part chemical industry peculiar smell removes clean, the achievable height to flue gas
Degree purification, can be achieved the watershed management of atmosphere pollution, realize the watershed management of haze, can finally solve atmosphere pollution, eliminate haze.Profit
Can solve water pollution with separation, solve environmental pollution.Swirl combustion is realized using vortex, realizes that fuel sorts using centrifugal force,
The larger fuel of particle can be made to be in combustion zone burning all the time, the ash content of after-flame is left combustion zone with air-flow, fuel can be made to exist
Uniform swirl combustion is realized in housing chamber 3, makes full combustion of fuel, burning solid combustion using swirl combustion plus vortex are broken
During material, fuel can be made abundant by the broken burning of continuous stripping while continuous burning.What, no matter fuel used, precisely supply
To fuel, when adjusting air quantity, it combustion zone temperature is kept stable and uniform, can more accurately control furnace temperature, can be achieved low
Temperature burning, nitrogen oxides generation can be prevented.Calcium carbonate aggregate chips is synchronously added when coal-fired can realize dry desulfurization in stove, in-furnace temperature
Uniformly, vortex promotes reaction, and the abundant desulfurization of dry method can be achieved.The vortex that housing chamber 3 is formed can promote the surface of heat-collecting device 13
Air speed, can improve and adopt the thermal efficiency, can reduce and adopt hot area, cost can be reduced.Eddy motion makes thermal current in shell
Move distance in body cavity 3 extends, and heat energy can be made fully to transmit, and final realize efficiently adopts heat.Boiler, burner etc. can be achieved
Dedusting in stove, discharge can be made more environmentally-friendly.Wet dust removal is realized using water smoke cleaning, flue gas can be made to realize thoroughly environmental protection.Utilize
Vortex realizes vortex grinding, makes material gradually thin by grinding with mutual frictional impact during air motion, and efficient powder can be achieved
Mill, can grind superfine powder.
Technical scheme is not restricted in the range of embodiment of the present invention.The not detailed description of the present invention
Technology contents be known technology.
Claims (10)
1. separation reaction flour mill, including housing(1)And transmission device(2), it is characterised in that:Housing(1)It is upper that transmission dress is set
Put(2), housing(1)Interior setting housing chamber(3), housing chamber(3)Interior setting vortex wheel(4), transmission device(2)With vortex wheel(4)
Connection, housing chamber(3)One end sets housing chamber import(6), housing chamber(3)The other end sets housing chamber to export(7).
2. separation reaction flour mill according to claim 1, it is characterised in that:Housing chamber(3)At least provided with one on inwall
Road is around spacer body(8), housing chamber(3)Periphery is correspondingly around spacer body(8)Discharging opening is set(9).
3. separation reaction flour mill according to claim 2, it is characterised in that:An at least piece housing chamber(3)Inwall pastes
Nearly vortex wheel(4)Outer rim.
4. separation reaction flour mill according to claim 2, it is characterised in that:Housing chamber import(6)Outer connection spray chamber
(10), spray chamber(10)Spray chamber import is set(11), spray chamber(10)Multiple spray equipments are set(12).
5. separation reaction flour mill according to claim 2, it is characterised in that:Housing chamber(3)Set and supply on the inwall of periphery
Liquid device(23).
6. separation reaction flour mill according to claim 2, it is characterised in that:Housing chamber(3)Shaft end sets housing chamber to enter
Mouthful(6), housing chamber(3)Other end shaft end sets housing chamber to export(7).
7. separation reaction flour mill according to claim 1, it is characterised in that:Housing chamber(3)Set on inwall and adopt hot charging
Put(13).
8. separation reaction flour mill according to claim 1, it is characterised in that:Housing chamber import(6)Upper setting is automatic to supply
Expect device(14), housing chamber(3)Temperature measuring equipment is set on inwall(15), temperature measuring equipment(15)Control automatic feeder(14).
9. separation reaction flour mill according to claim 1, it is characterised in that:Housing chamber exports(7)Upper setting flow is adjusted
Regulating device(19).
10. the separation reaction flour mill according to claim 1,2,3,4,5,6,7,8 or 9 any one, it is characterised in that:Whirlpool
Stream wheel(4)On the circumference of periphery and it is respectively provided with multiple fluid striking gears on axial direction(5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/CN2017/107586 WO2018082489A1 (en) | 2016-11-04 | 2017-10-25 | Separation reaction powder grinding machine |
Applications Claiming Priority (46)
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CN201610966035 | 2016-11-04 | ||
CN201610966035X | 2016-11-04 | ||
CN2016109760786 | 2016-11-07 | ||
CN201610976078 | 2016-11-07 | ||
CN2016109903811 | 2016-11-10 | ||
CN201610990381 | 2016-11-10 | ||
CN201611016970 | 2016-11-18 | ||
CN2016110169706 | 2016-11-18 | ||
CN201611134525 | 2016-12-10 | ||
CN201611134525X | 2016-12-10 | ||
CN2016111353078 | 2016-12-11 | ||
CN201611135307 | 2016-12-11 | ||
CN2017100445437 | 2017-01-21 | ||
CN201710044543 | 2017-01-21 | ||
CN201710051374X | 2017-01-23 | ||
CN201710051374 | 2017-01-23 | ||
CN2017100623523 | 2017-02-02 | ||
CN201710062352 | 2017-02-02 | ||
CN2017100674667 | 2017-02-07 | ||
CN201710067466 | 2017-02-07 | ||
CN2017101186783 | 2017-03-01 | ||
CN201710118678 | 2017-03-01 | ||
CN2017101260616 | 2017-03-05 | ||
CN201710126061 | 2017-03-05 | ||
CN2017101621968 | 2017-03-17 | ||
CN201710162196 | 2017-03-17 | ||
CN201710167323 | 2017-03-20 | ||
CN2017101673233 | 2017-03-20 | ||
CN201710175766 | 2017-03-22 | ||
CN2017101757667 | 2017-03-22 | ||
CN2017101796604 | 2017-03-23 | ||
CN201710179660 | 2017-03-23 | ||
CN201710268600 | 2017-04-23 | ||
CN201710268600X | 2017-04-23 | ||
CN2017102729433 | 2017-04-24 | ||
CN201710272943 | 2017-04-24 | ||
CN201710349843 | 2017-05-17 | ||
CN2017103498436 | 2017-05-17 | ||
CN201710435219 | 2017-06-10 | ||
CN2017104352198 | 2017-06-10 | ||
CN2017105780484 | 2017-07-15 | ||
CN201710578048 | 2017-07-15 | ||
CN2017106029986 | 2017-07-22 | ||
CN201710602998 | 2017-07-22 | ||
CN201710964178 | 2017-10-16 | ||
CN2017109641781 | 2017-10-16 |
Publications (1)
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CN107638963A true CN107638963A (en) | 2018-01-30 |
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CN201710980384.1A Pending CN107638963A (en) | 2016-11-04 | 2017-10-19 | Separation reaction flour mill |
CN201721351462.3U Expired - Fee Related CN207576674U (en) | 2016-11-04 | 2017-10-19 | Separation reaction flour mill |
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Application Number | Title | Priority Date | Filing Date |
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CN201721351462.3U Expired - Fee Related CN207576674U (en) | 2016-11-04 | 2017-10-19 | Separation reaction flour mill |
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CN (2) | CN107638963A (en) |
WO (1) | WO2018082489A1 (en) |
Cited By (1)
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WO2020108432A1 (en) * | 2018-11-28 | 2020-06-04 | 陈久斌 | Vortex machine |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110013919B (en) * | 2019-03-11 | 2023-10-17 | 中国水利水电科学研究院 | Vacuum pipeline magnetic suspension rock-soil centrifuge |
CN109847892A (en) * | 2019-03-20 | 2019-06-07 | 兰州大学 | A kind of reduction-diffusion process prepares the deimpurity device of terres rares-transition metal alloy |
CN110369058B (en) * | 2019-07-27 | 2021-02-26 | 沛县祥龙矿山机械配件有限公司 | Auxiliary equipment matched with steel ball coal mill of boiler of thermal power plant |
CN111425280B (en) * | 2020-01-08 | 2022-01-28 | 江西天美生物科技有限公司 | Activated carbon phosphoric acid activated tail gas purification device |
CN112220083A (en) * | 2020-09-26 | 2021-01-15 | 武汉木兰山水生态农业发展有限公司 | Efficient processing method of pig feed |
CN113713683B (en) * | 2021-08-24 | 2024-03-26 | 桐乡磊石微粉有限公司 | Powder mixing and conveying equipment and conveying method thereof |
CN113996401B (en) * | 2021-11-16 | 2022-09-23 | 湖南先导电子陶瓷科技产业园发展有限公司 | Titanate ceramic powder high temperature rapid synthesis equipment |
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WO2009051545A1 (en) * | 2007-10-15 | 2009-04-23 | Atlas Copco Drills Ab | Device and method for separating particles out from a fluid |
DE102008005439B3 (en) * | 2008-01-22 | 2009-09-10 | Milosiu, Johann-Marius, Dipl.-Ing. | Method for separating carbon dioxide from gas mixtures by centrifuge, involves continuously filling gas mixture from external connection into rotary drum |
CN201431923Y (en) * | 2009-06-24 | 2010-03-31 | 中国石化集团胜利石油管理局钻井工艺研究院 | Vertical cyclone separator |
CN101875027A (en) * | 2009-12-15 | 2010-11-03 | 陈久斌 | Whirlpool separator |
CN102441501A (en) * | 2011-07-15 | 2012-05-09 | 陈久斌 | Separator |
CN203695230U (en) * | 2013-03-15 | 2014-07-09 | 陈久斌 | Swirler |
CN104841574A (en) * | 2013-10-11 | 2015-08-19 | 陈久斌 | Separator |
-
2017
- 2017-10-19 CN CN201710980384.1A patent/CN107638963A/en active Pending
- 2017-10-19 CN CN201721351462.3U patent/CN207576674U/en not_active Expired - Fee Related
- 2017-10-25 WO PCT/CN2017/107586 patent/WO2018082489A1/en active Application Filing
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020108432A1 (en) * | 2018-11-28 | 2020-06-04 | 陈久斌 | Vortex machine |
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CN207576674U (en) | 2018-07-06 |
WO2018082489A1 (en) | 2018-05-11 |
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