CN102441501A - Separator - Google Patents
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- CN102441501A CN102441501A CN2011102963876A CN201110296387A CN102441501A CN 102441501 A CN102441501 A CN 102441501A CN 2011102963876 A CN2011102963876 A CN 2011102963876A CN 201110296387 A CN201110296387 A CN 201110296387A CN 102441501 A CN102441501 A CN 102441501A
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Abstract
A separator comprises a casing; at least one casing cavity is arranged in the casing; a driving device is mounted on the casing; a vortex separating cylinder is arranged in the casing cavity; the driving device is connected with the vortex separating cylinder; a vortex separating chamber is arranged in the vortex separating cylinder; a fluid inlet is formed at one end of the vortex separating chamber; a plurality of vortex separating chamber outlets are formed on the periphery of the vortex separating chamber; a casing cavity inlet corresponds to the fluid inlet; and the casing cavity is provided with at least two casing cavity outlets. The separator can achieve the separation of fluid from vortex through adopting a brand-new separating principle and a brand-new separating method, making the best of the circular motion and the fluid motion, and utilizing vortex with the rotating speed progressively increased from the center to the periphery. The separator can be widely used in the fields such as sewage disposal, dust removal, dust absorption, garbage disposal, powder concentrating, mineral separation, seawater desalination, ocean chemical engineering, oxygen production, hydrogen production, nano material manufacturing, harmful gas resolving treatment, refrigeration, reactors, oil refining, metallurgy and the like, can provide clean energy, solves the energy problem and the environment pollution problem, and can thoroughly create an environment of blue sky, white cloud and clear water.
Description
Technical field
The present invention relates to fields such as seperator equipment, centrifuge instrument, sewage disposal device, sea water desalting equipment, marine chemical industry equipment, preparation equipment, refuse treatment plant, hydrogen producer, carbon dioxide resolution process equipment, pernicious gas resolution process equipment, nano material manufacturing equipment, reactor apparatus, air cleaning facility, cleaner, dust collection equipment, air-conditioning, refrigeration plant, oxygen generating plant, specifically is a kind of separator.
Background technology
The environmental pollution of today comprises that mainly pollution of waterhead, air pollution, refuse pollution, cold-producing medium are to the destruction of ozone layer, greenhouse gas emission etc.Existing sewage disposal device is complicated, and cost is too high, and the sewage disposal expense is too high, and treatment effect is general, and waste water control has become the most important thing of environmental improvement.Existing air cleaning facility clean-up effect is general, can't thoroughly handle dust, thoroughly handle carbon dioxide, nitrogen oxide, oxysulfide.Defectives such as existing cleaner has cyclone dust removal, electric precipitation, bag-type dust etc., and the ubiquity dust removing effects is undesirable, and energy consumption is big, dust pollution has become most important pollution sources.Burning, landfill, compost scheme are mainly adopted in existing garbage disposal, the ubiquity contaminated environment, and the resource circulation utilization effect is undesirable, waste resource, problem such as the garbage disposal effect is undesirable.Existing air-conditioning, refrigeration plant generally adopt ammonia, freon refrigeration, have contaminated environment, and energy consumption is high, and refrigerating efficiency is low, can't realize lower temperature.Existing hydrogen producer is complicated, and process for making hydrogen is complicated, adopts the water electrolysis hydrogen production energy consumption too high, and manufacturing cost is high, makes fuel hydrogen become extravagant hope, causes carbon dioxide isothermal chamber gas to discharge in a large number.Existing oxygen generating plant cost is too high, and system oxygen cost is too high, can't realize popularization and application, causes and can't realize pure oxygen burning, causes nitrogen oxide to discharge the formation important pollution sources in a large number.Existing dust collection equipment pick-up performance is undesirable, and noise is big, and micronic dust particle contamination air is arranged, dedusting post processing dust trouble.Defectives such as existing separation equipment mainly contains centrifuge, seperator etc., and the ubiquity equipment manufacturing cost is high, and separating effect is general, and energy consumption is big.Existing sea water desalting equipment is complicated, and cost is too high, and the desalinization expense is too high, and energy consumption is too big.Existing marine chemical industry complex equipments, cost is too high, utilizes effect undesirable to marine resources.Existing preparation equipment cost is too high, and the ore dressing effect is general, can't realize meticulousr sorting, causes the wasting of resources and environmental pollution.Existing nano material manufacturing equipment can't be produced more tiny nano material.The realization response of existing reactors equipment is limited in one's ability, can't create special reaction condition, causes course of reaction complicated, and the chemical products manufacturing cost is improved greatly, and some resource can't be utilized, and causes the wasting of resources and environmental pollution.
Summary of the invention
The present invention provides a kind of separator, adopts brand-new separation method, adopts brand-new eddy current separation principle; Make full use of fluid motion; The eddy current that utilizes rotating speed from the center to the periphery to increase progressively makes fluid automatically from the suction vortex of eddy current center, makes fluid the motion process peripheral from the eddy current center to eddy current, receive vortes interference; Under the circular motion action of centrifugal force, the eddy current that utilizes rotating speed from the center to the periphery to increase progressively is realized separating.
Utilize the long more characteristics of the oval more girth of radius of circle; When each point all centers on the center of circle and does the circular motion of same rotational speed in the circle; The linear velocity of the circular motion of point far away more is high more from the center of circle; Under the acting in conjunction of centrifugal force, make the fluid that gets into from the circle center the field of this circular motion under the action of centrifugal force in the peripheral motion process of circle, receive the acting in conjunction of phase mutual friction and acceleration of motion between the fluid particles to form the eddy current that increases progressively of rotating speed from the center to the periphery down.
Utilize the centrifugal force that produces in the eddy current, make the particle of different volumes, proportion realize each other separating.The particle of different volumes, proportion is different to the peripheral movement velocity of eddy current, and heavy particle is faster to the peripheral movement velocity of eddy current.Fluid from the eddy current separation chamber fluid inlet to the motion process of minor air cell's fluid issuing, in the fluid heavy particle can be more early move to the eddy current periphery, the little particle of proportion more evening move to the eddy current periphery, utilize this point to realize the sorting of different material.
Theory analysis: the rotating speed of eddy current outermost equates that with the rotating speed of minor air cell's inwall the rotating speed at eddy current center is 0.Minor air cell's rotating speed is high more, and the rotational speed of eddy current that increases progressively of rotating speed increases progressively fast more from the center to the periphery.All there is relative motion each other in each point in the vortex field; Motion makes each point produce interaction force each other; Fluid molecule in the vortex field is far away more apart from the eddy current center, and its linear velocity is fast more, and the linear velocity of the molecule of the eddy current center position adjacent with it is lower; Can rub between them, can produce a force of rolling friction.When eddy current cylinder rotating speed reaches certain speed; After molecule gets into the eddy current separation chamber from the import of eddy current separation chamber; Molecule is in the motion process of eddy current periphery; Receive vortes interference to make molecule quickened rotation suddenly, can break the balance of molecule self-field when the rotary acceleration of this unexpected acceleration rotation acquires a certain degree, the molecule profile is changed.Molecule is a solid space, is an elastic space.The movement velocity of molecule is fast more from eddy current cylinder axle center linear velocity far away in the eddy current; There is the frictional force that rotates and knead in the eddy current center between the peripheral adjacent molecule of eddy current; Molecule receives a rotation stranding from eddy current and hugs frictional force, just as hugging dough with hand rubbing, makes static molecule rubbed rotation fast; There is the power of rubbing, separating in eddy current to the object in the eddy current, and this power improves with the raising of rotational speed of eddy current synchronously.This power can make fluid separated well, utilizes this power also can molecular structure destroyed molecular separation, makes molecule separated as brine electrolysis, can become atom to molecular separation, is twisted into atom linear.This power is skilful power, can be described as that art is good for strength.The separated back of molecule forms linear atom, and the major axis of linear atom remains parallel with the eddy current bowl spindle under the turning effort of eddy current cylinder, and linear atom is that rotating shaft rotates at a high speed with the major axis, and rotating speed is identical with eddy current cylinder rotating speed.Atom can show as special characteristics of plasma after becoming linear particle, can form a kind of special plasma.The eddy current separation chamber be an eddy current generating chamber also be a linear particle generator, this point capable of using makes this separator use as a kind of special reactor.Utilize the effect of eddy current, can molecular structure is destroyed molecular separation, make molecule separated as brine electrolysis.The separating treatment completely that can utilize this point to accomplish carbon dioxide, oxysulfide, nitrogen oxide purifies.Can be widely used in the tail gas clean-up process field, the byproduct after tail gas clean-up is handled can be used as the new energy or material is used.Can directly produce hydrogen, produce heat energy, inexhaustible clean energy resource is provided, thoroughly solve energy problem, solve the greenhouse gas emission problem with combustion of hydrogen with steam.
This separator can be realized 100% dedusting; 100% dispose of sewage makes full use of water resource; Cleaner disposal of refuse.
The present invention realizes through following technical scheme for realizing above-mentioned purpose:
Separator comprises housing, and at least one housing chamber is set in the housing; Transmission device is installed on the housing, the eddy current cylinder is set in the housing chamber, transmission device is connected with the eddy current cylinder; Establish the eddy current separation chamber in the eddy current cylinder, eddy current separation chamber one end is offered fluid inlet, and eddy current separation chamber periphery is established the outlet of a plurality of eddy current separation chamber; Corresponding fluid inlet is provided with the import of housing chamber, and the housing chamber is provided with at least two housing chamber outlets.The outlet of housing chamber connects the movable sealing device for discharging.Establish runner in the outlet of eddy current separation chamber.Housing top is provided with the High Pressure Shell chamber.Eddy current cylinder outer wall in the High Pressure Shell chamber is provided with a plurality of blades.Establish annular block body in the eddy current cylinder.Transmission device is installed at the housing two ends respectively, and eddy current cylinder one end is provided with supporter, and transmission device passes the import of housing chamber and connects supporter.The import of housing chamber connects diversion cavity, and diversion cavity is provided with the diversion cavity import.Establish a plurality of housings chamber in the housing, each housing chamber is provided with the outlet of housing chamber respectively.The housing cavity wall is provided with nozzle.
The invention has the advantages that: utilize brand-new separation method, made full use of circular motion and fluid motion, fluid is separated by eddy current, separating effect improves synchronously with rotating speed and improves.
The present invention has and makes simple, low cost of manufacture, advantages such as use cost is low, maintenance cost is low, long service life.
Separator of the present invention can be widely used in various separation equipments field.Available it replace existing all centrifuges, seperator, its separating effect is better, can realize separation, sorting, extraction, the purification of various material compositions, also can realize the decomposition of multiple gaseous compound, and is separable, sub-elect multiple element.
This separator can be used as air cleaning facility, can be used as deduster and uses, and can thoroughly remove dust, realizes 100% dust removal efficiency, can surpass the dust removing effects of any deduster.Its inexpensive, more energy-conservation.This separator also can be used as novel desulfurization, denitration device uses, and can ammonia or alkaline solution atomizing back be sucked in the separator together with sulfur-containing smoke gas in the lump, realizes desulfurization, dedusting in the separator inter-sync.
This separator also can be used as smoke exhaust ventilator and uses, and can oil smoke be separated, and makes fume emission environmental protection more.
This separator can be used as dust catcher and uses, and can filter screen be set at the dust suction mouth of pipe, the long fibre thing is filtered in filter screen, to clear up separately get final product.The cleaning of this separating device of dust is convenient, and noise is low, and pick-up performance is good, and inexpensive is more energy-conservation, does not have dust pollution when using as dust catcher, more health, environmental protection.
This separator can be used as sewage disposal device, can from sewage, extract multiple useful component, realizes resource circulation utilization.Can 100% dispose of sewage can directly provide pure water, can reach drinking water standard, can thoroughly solve water resource pollution, solves the water scarcity problem.
This separator can be used as refuse treatment plant, can rubbish be dried fragmentation, be ground into suspended particulate after; Can directly utilize the air-flow transports particles to carry out dry separation; Also available current transports particles is carried out wet separation, and useful composition is separated, sorts out, and useless composition and organic component lump together and be pressed into granular organic fertilizer; Can thoroughly stop environmental pollution, realize resource circulation utilization.
This separator can be isolated oxygen from air, system oxygen cost is extremely low, can make boiler, kiln, hot machine etc. realize cheap economic pure oxygen burning, and is capable of reducing energy consumption, improves the thermal efficiency, thoroughly stops discharged nitrous oxides.Oxygen is delivered in the room, can makes oxygen-enriched environment, realize that indoor air purifies, this separator can be used as the novel air clarifier and uses.
This separator can be used as sea water desalting equipment, can reduce equipment manufacturing cost greatly, reduces the desalinization cost, cuts down the consumption of energy greatly, improves desalinization efficient, improves fresh water yield.Can from seawater, extract various useful components synchronously, realize separation and Extraction, the sorting purification of various useful components simultaneously.Available it as marine chemical industry equipment, can reduce equipment manufacturing cost greatly.
This separator can be used as preparation equipment, can realize separation and Extraction, purification, the removal of impurity of multi mineral, raw material, can mineral powder be broken into suspended particulate, can directly utilize the air-flow transports particles, directly dry separation, and also available current transports particles is carried out wet separation.When being used for the ceramic raw material deironing, high-purity raw can be obtained, the raw material processing cost can be reduced.
But this separator production nano material, but metal material powder such as production nanometer copper, iron, aluminium, nickel, silicon also can be produced nonmetallic materials powder such as nano ceramics, silicate, glass, aluminium oxide, zirconia, titanium alloy, can produce multiple nano material.During this separator production nano material powder, can add nitrogen or other inert gas as protective gas, can be directly with nitrogen or other inert gas as atomization gas.Can use cooling of water smoke, mist of oil or gas cooled, cooling medium is sprayed in the shell separator get final product.
This separator can be used as reactor and uses, and can under specific temperature, the fluid of needs reaction directly be imported in the separator in proportion, and fluid can fast reaction in the shell separator chamber, but fast reaction speed.For making sufficient reacting between the fluid, can make fluid entering separator repeatedly, make and fully accomplish reaction between the fluid.RFCC field in can being applied to refine oil, used vapour with in the high steam atomizing back input separator, after can catalyst being atomized together add heavy oil in the separator as atomization gas, can strengthen catalytic reaction, can improve oil yield greatly.
Theory analysis: this separator is pernicious gases such as separating carbon dioxide, oxysulfide, nitrogen oxide, hydrogen sulfide, dioxin thoroughly, can the molecule of these pernicious gases thoroughly be separated into atom.This separator can separate carbon, element sulphur, and oxygen element, protium, nitrogen element are separated in the air, accomplishes thorough processing, purification to pernicious gas.Byproduct after tail gas clean-up is handled all is a nanometer powder, can be used as the new energy or material and uses.The energy field of the various atoms self of separated formation and the energy field of the atom in the external environment are uneven, will energy exchange take place with the external world, or heat absorption, or heat release.The oxygen element in the hydrone in the atom mass rate external environment of oxygen element and protium and the atomic mass of protium are smaller a little, and that part of quality that lacks has discharged in oxyhydrogen reaction.After hydrone was separated, isolated oxygen element and protium must be kept the energy balance with external environment condition, will absorb energy, showed as heat absorption.The gas that separator is discharged can form cold air, and this point capable of using is carried out the low-temperature receiver utilization, can be with the host computer system of this separator as novel air conditioner, air-conditioning, and steam capable of using is finished the work, and can thoroughly realize the pollution-free of refrigeration plant.This separator can produce ultralow temperature as air conditioner.As air conditioner, when air-conditioning uses, can make a steam jar, in separator, import water vapour; After water vapour is separated into oxygen and hydrogen; Oxygen is delivered into the room, hydrogen is directly emitted or collect utilization, also can be with hydrogen through behind the heating device; Light and add the hot water and steam jar, make and produce steam in the jar.Heating device also can be used as the low-temperature receiver utilization, can further improve refrigerating efficiency.This separator can be realized energy circulation, makes oxidation reaction become a link on the energy circulation chain, and the energy that oxidation reaction is discharged becomes from the external environment condition borrow.Energy is transformed to be formed: the energy circulation chain of---separator separates is absorbed heat from external environment---oxidation reaction heat release through the oxidation reaction heat release.Adopt this energy endless-chain can make energy cycle applications, directly water steam extraction hydrogen utilizes hydrogen as fuel, and clean energy resource completely can be provided, and can thoroughly solve energy problem, solves greenhouse gas emission, solves environmental pollution.Capable of using separator feedway that acts as a fuel can directly be contained in it on the vehicles such as car, ship, aircraft, also can be directly and kiln etc. need the coordinative composition of equipments of fuel to use, directly water can provide hydrogen fuel endlessly.
Theory analysis: this separator can be used as novel metallurgical equipment and uses; Available it refine multiple element; After can ore being vaporized with technical methods such as LASER HEATING, arc heated, fuel combustion heating, get into separator, realize the ore molecular separation; Extract multiple element, smelting process is environmental protection more.The separator moving component can adopt the exotic material manufacturing, and stationary parts such as housing can adopt multiple cooling technology to reduce material requirements.When adopting fast cooling technology, but the multiple nano material powder of Direct Production.Under the prior art condition, be used to refine very practicalities of low boiling element such as lead, can realize that pollution-free refining is plumbous.This separator also can be used in the various hydrometallurgys, can better extract various elements.This separator also can be used for alloy and separates, and can the multiple element in the liquid alloy liquation be separated.
Description of drawings
Accompanying drawing 1 is the agent structure sketch map of separator of the present invention;
Accompanying drawing 2 is main TV structure sketch mapes of one of separator embodiment of the present invention;
Accompanying drawing 3 be in the accompanying drawing 2 A-A to the sectional structure sketch map;
Accompanying drawing 4 is main TV structure sketch mapes of two of separator embodiment of the present invention;
Accompanying drawing 5 is main TV structure sketch mapes of three of separator embodiment of the present invention;
Accompanying drawing 6 be in the accompanying drawing 5 B-B to the sectional structure sketch map;
Accompanying drawing 7 is main TV structure sketch mapes of four of separator embodiment of the present invention;
Accompanying drawing 8 is main TV structure sketch mapes of five of separator embodiment of the present invention;
Accompanying drawing 9 is main TV structure sketch mapes of six of separator embodiment of the present invention;
Accompanying drawing 10 is main TV structure sketch mapes of seven of separator embodiment of the present invention;
Accompanying drawing 11 is main TV structure sketch mapes of eight of separator embodiment of the present invention;
The specific embodiment
The agent structure of separator of the present invention comprises housing 1, and at least one housing chamber 2 is set in the housing 1, and transmission device 3 is installed on the housing 1; Eddy current cylinder 4 is set in the housing chamber 2, and transmission device 3 is connected with eddy current cylinder 4, establishes eddy current separation chamber 5 in the eddy current cylinder 4; Eddy current separation chamber 5 one ends are offered fluid inlet 6; Eddy current separation chamber 5 peripheries are established a plurality of eddy current separation chamber outlet 8, and corresponding fluid inlet 6 is provided with housing chamber import 9, and housing chamber 2 is provided with at least two housing chamber outlets 10.
The scope of housing 1 comprises support, casing and power set etc., and each position all can be referred to as and be done housing.Housing also can be processed one with power set, forms the housing of an integral body.
At least one housing chamber 2 is set in the housing 1, and housing chamber inner chamber cross section can be arranged to circle, and the inwall of housing chamber periphery can be established wear-resistant material layer or anti-corrosion layer etc. as required and improve housing service life or increase the scope of application.Two housing chambeies are set can the upper case body cavity be arranged to the High Pressure Shell chamber, utilize the high-pressure fluid in the High Pressure Shell chamber to suppress the endoceliac low-pressure fluid of portion's shell of staying, avoid the fluid in the lower case body cavity to flow into the upper case body cavity.A plurality of housings chamber is set provides the auxiliary shell chamber, utilize the auxiliary shell chamber to realize the more property demand, can carry out sorting, carry but convection cell carries out water conservancy diversion.
Eddy current cylinder 4 is set in the housing chamber 2.Eddy current cylinder 4 is reserved cavity zone in the peripheral housing chamber, utilizes that cavity zone is realized the dredging of separator, compiled, sorting, collection.Eddy current cylinder 4 can be selected the material different manufacturing as required for use: rotating speed is demanding, can select the Materials with High Strength manufacturing for use; Need the fluid temperature (F.T.) of pressurized delivered high, select resistant to elevated temperatures Materials with High Strength for use; Mordant chemical fluid adopts anticorrosive material; Eddy current cylinder 4 can use metal, pottery, glass, carbon fiber, plastic or other material.The eddy current cylinder of metal material can adopt the moulding of casting technique one-step casting, and the eddy current cylinder of materials such as pottery can be fired shaping.
Establish eddy current separation chamber 5 in the eddy current cylinder 4, eddy current separation chamber 5 can be arranged to the rounded cavity of cross section, can better keep the dynamic balancing of eddy current cylinder, can make in the eddy current separation chamber and better to form the eddy current that increases progressively of rotating speed from the center to the periphery.The inwall at 5 two ends, eddy current separation chamber can be arranged to plane or globoidal structure.Being arranged to planar structure can simplified manufacturing technique; Being arranged to globoidal structure can avoid fluid to attach on eddy current separation chamber 5 inwalls; Simultaneously can make fluid motion more smooth and easy; Reduce the friction between eddy current separation chamber's 5 inwalls and the fluid, can reduce energy loss, reduce wall friction causes in fluid and the eddy current separation chamber 5 vibration, noise.Simultaneously can improve eddy current cylinder 4 bulk strengths, make eddy current cylinder 4 can bear higher rotating speed.
Eddy current separation chamber 5 one ends are offered fluid inlet 6, and fluid inlet 6 is opened in the central region of eddy current separation chamber 5, and the center of the center of fluid inlet 6 and eddy current separation chamber 5 can make eddy current separation chamber 5 when fluid gets into, keep rotation steadily on same axis.Fluid inlet 6 diameter can be confirmed according to eddy current separation chamber 5 diameters; Can confirm the dimension scale of fluid inlet 6 diameters and eddy current separation chamber 5 diameters according to concrete separation requirement; Reduced size ratio when separation requirement is high; Generally speaking, the dimension scale of fluid inlet 6 diameters and eddy current separation chamber 5 diameters can be selected: 0.382-0.618: 1.
Eddy current separation chamber 5 peripheries are established a plurality of eddy current separation chamber outlet 8, and eddy current separation chamber outlet 8 is located at the most peripheral of eddy current separation chamber 5, eddy current separation chamber outlet 8 are evenly distributed on the circumference of eddy current separation chamber 8 to get final product.When eddy current separation chamber periphery wall approached, directly punching promptly can be used as eddy current separation chamber outlet 8 on periphery wall.
Corresponding fluid inlet 6 is provided with housing chamber import 9, and fluid inlet 6 gets final product with housing chamber import 9 corresponding settings.
This separator can be used as uses such as dust catcher, deduster, powder selector, apparatus for treating sewage, sea water desalting equipment, oxygen generating plant, air separation equipment, nano material manufacturing equipment.When separator uses high speed driving unit; Available it use as refrigeration plant, the available water steam is as cold-producing medium, the separable steam of separator; Can from lower case body cavity outlet 10, isolate oxygen; From upper case body cavity outlet 10, isolate hydrogen, hydrogen can directly emit, and oxygen directly is delivered in room or the cool room can produces low temperature environment.This separator also can be used as pernicious gas separating treatment equipment such as carbon dioxide, oxysulfide, nitrogen oxide, hydrogen sulfide, dioxin and uses.Solid state component such as carbon, sulphur can be separated from lower case body cavity outlet 10, and elemental gas such as oxygen are isolated from upper case body cavity outlet 10.
The structure of one of embodiment of the invention is: on the agent structure basis, housing chamber outlet 10 connects movable sealing device for discharging 18.Movable sealing device for discharging 18 can be provided with devices such as valve, air door, screw conveyor, and movable sealing device for discharging 18 scalable flows can make separator according to fractional dose, under the effect of housing internal pressure and gravity, in housing, draw off.Also but batch (-type) is opened the movable sealing device for discharging separator is drawn off.When this separator used as dust catcher, deduster etc., movable sealing device for discharging 18 can be made into ash bin, grey chamber etc.Upper case body cavity outlet also can not connect the movable sealing device for discharging, is arranged to the outlet of firm discharge, and advantage is can simplified structure; Shortcoming is to regulate flow; Can't the adjustment housings internal pressure, be unfavorable for realizing better that fluid separates, be unfavorable for realizing better energy-saving effect.
The further structure of present embodiment is: establish runner 15 in 5 outlets 6 of eddy current separation chamber.During eddy current separation chamber 5 periphery wall thickness, establish passage 15 in 5 outlets 6 of eddy current separation chamber, runner 15 ports of export help fluid towards the opposite direction of minor air cell's direction of rotation and from the eddy current separation chamber, throw away.Runner 15 can reduce the friction between fluid and the eddy current cylinder to the expansion of vortex wheel peripheral openings, can be more energy-conservation.Upper vortex tube outer rim is provided with vanelets or increases the quantity of runner 15 or the fluid pressure that length can increase housing chamber 2 upper areas.
The cyclone separator arrangement of present embodiment is strengthened more, has all functions of agent structure.
Two structure of the embodiment of the invention is: on above architecture basics, housing 1 top is provided with High Pressure Shell chamber 13.Can in the housing chamber, toroidal membrane be set, the housing chamber is divided into two housing chambeies up and down, the upper case body cavity can be arranged to High Pressure Shell chamber 13.
The cyclone separator arrangement of present embodiment is strengthened more.Except that having above body function, the present embodiment separator also can be used as smoke exhaust ventilator and uses, and can oil smoke be separated, and makes fume emission environmental protection more, and the flue gas after the processing can be discharged from upper case body cavity outlet 10, and waste oil is discharged from lower case body cavity outlet 10.
Three structure of the embodiment of the invention is: on above architecture basics, eddy current cylinder 4 outer walls in the High Pressure Shell chamber 13 are provided with a plurality of blades 17.Can a plurality of blades 17 be uniformly set on eddy current cylinder 4 outer walls that are in the High Pressure Shell chamber, blade 17 can play the effect of impeller blade, can improve the pressure in High Pressure Shell chamber.
The separator of present embodiment can better be carried the fluid after the separation, can avoid isolated object to get into the High Pressure Shell chamber better, improves the degree of purity of isolated fluid.
Four structure of the embodiment of the invention is: on above architecture basics, establish annular block body 7 in the eddy current cylinder 4.Annular block body 7 middle parts are provided with round mouth, and the round mouth area can equate with fluid inlet 6 areas, annular block body 7 surfaces be arranged to plane or globoidal structure all can, annular block body 7 is buffer fluid better, the raising separating effect.
The cyclone performance of present embodiment is more reliable and more stable, has all functions of above embodiment.
Five structure of the embodiment of the invention is: on above architecture basics, transmission device 3 is installed at housing 1 two ends respectively, and eddy current cylinder 4 one ends are provided with supporter 20, and transmission device 3 passes housing chamber import 9 and connects supporters 20.Can transmission device 3 be installed respectively at the housing two ends, power set can connect the transmission device of an end, also can on the transmission device at two ends, connect power set respectively, can improve power.Supporter 20 can be made the impeller pattern, and the impeller periphery is fastened on fluid inlet 6 edges or eddy current separation chamber 5 inwalls, transmission device 3 is passed the connection of impeller axle center district get final product, and supporter 20 makes eddy current cylinder 4 spin stabilizations along with transmission device 3 rotations.
The separator of present embodiment can improve eddy current cylinder 4 rotational stabilizations, and it is mobile that separator is not afraid of, and can adapt to more multi-state requirement.
Six structure of the embodiment of the invention is: on above architecture basics, housing chamber import 9 connects diversion cavity 21, and diversion cavity 21 is provided with diversion cavity import 22.Diversion cavity 21 can be arranged to multiple pattern, and the effect of diversion cavity 21 is that more convenient pipeline connects, and one or more diversion cavity imports 22 can be set as required.Diversion cavity 21 can be arranged on around the housing chamber import 9, can make things convenient for pipeline to connect.
The separator of present embodiment can improve eddy current cylinder 4 rotational stabilizations, and it is mobile that separator is not afraid of, and can adapt to more multi-state requirement, can connect by more convenient pipeline.
Seven structure of the embodiment of the invention is: on above architecture basics, establish a plurality of housings chamber 2 in the housing 1, each housing chamber 2 is provided with housing chamber outlet 10 respectively.Can in the housing chamber, toroidal membrane be set, the housing chamber is divided into a plurality of housings chamber.
Present embodiment can be realized the further sorting of separator, can make the separator of different specific weight get into different housing chambeies, realizes the sorting of separator.Can be used for ore dressing, select powder, different material sorting in the useful component sorting in the garbage disposal sorting, sewage disposal, marine chemical industry, gas with various composition sorting etc. during gas separates.
Present embodiment can be used as use such as catalytic cracking reaction equipment in preparation equipment, sewage disposal device, air cleaning facility, refuse treatment plant, oxygen generating plant, the equipment of making nitrogen, reactor, the oil refining with the further sorting of separator.The separator of different specific weight is different to the peripheral movement velocity of eddy current, and fluid exports from fluid inlet 6 to the upper case body cavity 10 the motion process, and the separator of different specific weight gets into different housing chambeies respectively, can realize the sorting of different separators.When using, can from sewage, waste gas, extract as sewage, waste gas treatment equipment, the various useful components of sorting.Kiln tail gas capable of using extracts sulfur dioxide relieving haperacidity, extracts carbon dioxide etc., realizes the utilization of resources.Can from dust, select multiple useful composition during tails dedusting.
Available it as sea water desalting equipment, marine chemical industry equipment, oxygen generating plant, the equipment of making nitrogen, etc. use.Can from High Pressure Shell chamber outlet 14, export fresh water during as sea water desalting equipment, marine chemical industry equipment, sewage disposal device use; Can directly reach drinking water standard; Can from housing chamber outlet 10, export the salt solution of various compositions, various salt solution capable of using further extract multiple useful element.As oxygen generating plant, when the equipment of making nitrogen uses, can air be imported separator, can from housing chamber outlet 10, isolate multiple gases such as oxygen, from upper case body cavity outlet 10, isolate nitrogen, oxygen can be collected utilization.
When the present embodiment separator uses as refuse treatment plant, can rubbish be dried fragmentation, be ground into suspended particulate after, can directly utilize air-flow that particle transport is advanced separator, directly dry separation.Also available current transports particles is carried out wet separation, and useful composition is separated, and useless composition and organic component lump together and be pressed into granular organic fertilizer, can thoroughly stop environmental pollution, realizes resource circulation utilization.
When the present embodiment separator is used for oil refining catalytic cracking reaction equipment; Can in separator, import steam, after the oil atomizing, send into separator as atomization gas; Can directly add in the separator in the lump after the atomizing catalyst; Can strengthen catalytic reaction, catalytic reaction is carried out in the eddy current separation chamber fast, and the various oil contents of formation do not get into different housing chambeies.This programme can improve oil yield greatly.
When the present embodiment separator uses as reactor, can be under specific temperature, the fluid of needs reaction directly to be imported in the separator in proportion, fluid can fast reaction in the housing chamber of separator, but fast reaction speed.For making sufficient reacting between the fluid, can make fluid entering separator repeatedly, make and fully accomplish reaction between the fluid.The compound of reacted heterogeneity can get in the different housing chambeies, realizes the sorting of heterogeneity compound.
When separator uses high speed driving unit, available it as uses such as carbon dioxide resolution process equipment, pernicious gas resolution process equipment.When using, can from upper case body cavity outlet 10, export innocuous gas, from lower case body cavity outlet 10, export useful element as carbon dioxide resolution process equipment, pernicious gas resolution process equipment etc.
Eight structure of the embodiment of the invention is: on above architecture basics, housing chamber 2 inwalls are provided with nozzle 19.When fluid need cool off or heat, can nozzle 19 be set at housing chamber 2 inwalls, can in housing, spray into the cooling or the medium of heating through nozzle 19, make to keep certain temperature environment in the housing, make fluid can accomplish required physics or chemical reaction.Can use water smoke, mist of oil cooling or gas cooled.
Present embodiment can be used as uses such as nano material manufacturing equipment, reactor apparatus, air cleaning facility, carbon dioxide resolution process equipment, pernicious gas resolution process equipment.When being used for production nano material powder, but metal material powder such as production nanometer copper, iron, aluminium, nickel, silicon also can be produced nonmetallic materials powder such as nano ceramics, silicate, glass, aluminium oxide, zirconia, titanium alloy, can produce multiple nano material.Can add nitrogen or other inert gas as protective gas, can be directly with nitrogen or other inert gas as atomization gas, after material liquefaction; After conventional atomization plant atomizing, atomization gas directly is delivered into separator, atomization gas further separates in eddy current cylinder 4, atomizing; Form littler droplet, droplet throws away the back in the eddy current cylinder 4 and gets into housing chamber 2, in housing chamber 2, run into the cooling or the medium of heating of nozzle 19 devices ejection after; Sedimentation in housing chamber 2; Finally outlet 10 is discharged from the housing chamber, can produce more tiny nano material, can bring the revolution of nano material.
The present embodiment separator can be produced the azotized carbon nano material in theory; A kind of production imagination is proposed: with CO gas and a large amount of nitrogen input separators here; Use the high speed dynamic power machine on the separator transmission device, make the cylinder rotating speed reach high, make the rotating speed of eddy current very high.After the molecule import got into the eddy current separation chamber, molecule received the influence of eddy current to make the field of molecule self quickened rotation suddenly, and the acceleration of this unexpected acceleration is high, when acquiring a certain degree, makes molecular separation become atom.Atom is further broken the balance of self-field by huge rotary acceleration, atomic structure is changed.The eddy current separation chamber can separate into carbon ion and oxonium ion with carbon monoxide molecule, and nitrogen molecule also can separate into the nitrogen ion.After throwing away from the eddy current separation chamber, under the particular environment temperature, nitrogen ion and carbon ion can react and generate the carbonitride molecule, form the azotized carbon nano material powder.Need certain temperature condition during manufacturing simultaneously, temperature is controlled in certain scope.
When separator of the present invention uses; Can fluid be sucked separator automatically, fluid gets into the eddy current cylinder automatically under the turning effort of eddy current cylinder high speed; Pass the outlet outflow of eddy current cylinder from the housing chamber; The motion process that fluid exports from fluid inlet to the housing chamber, receive common influence such as vortex fluid motion effects and eddy current centrifugal force and gravity etc., realize that various compositions separate.
Technical scheme of the present invention is not restricted in the scope of embodiment of the present invention.The present invention not technology contents of detailed description is known technology.
Claims (10)
1. separator comprises housing (1), it is characterized in that: at least one housing chamber (2) is set in the housing (1); Housing (1) is gone up transmission device (3) is installed; Eddy current cylinder (4) is set in the housing chamber (2), and transmission device (3) is connected with eddy current cylinder (4), establishes eddy current separation chamber (5) in the eddy current cylinder (4); Eddy current separation chamber (5) one ends are offered fluid inlet (6); Eddy current separation chamber (5) periphery is established a plurality of eddy current separation chamber outlet (8), and corresponding fluid inlet (6) is provided with housing chamber import (9), and housing chamber (2) are provided with at least two housing chamber outlets (10).
2. separator according to claim 1 is characterized in that: housing chamber outlet (10) connects movable sealing device for discharging (18).
3. separator according to claim 1 is characterized in that: establish runner (15) in eddy current separation chamber (5) outlets (6).
4. separator according to claim 1 is characterized in that: housing (1) top is provided with High Pressure Shell chamber (13).
5. separator according to claim 4 is characterized in that: eddy current cylinder (4) outer wall in High Pressure Shell chamber (13) is provided with a plurality of blades (17).
6. separator according to claim 1 is characterized in that: establish annular block body (7) in the eddy current cylinder (4).
7. separator according to claim 1 is characterized in that, transmission device (3) is installed at housing (1) two ends respectively, and eddy current cylinder (4) one ends are provided with supporter (20), and transmission device (3) passes housing chamber import (9) and connects supporter (20).
8. separator according to claim 7 is characterized in that: housing chamber import (9) connects diversion cavity (21), and diversion cavity (21) is provided with diversion cavity import (22).
9. according to claim 1,2,3,4,5,6,7 or 8 each described separators, it is characterized in that: establish a plurality of housings chamber (2) in the housing (1), each housing chamber (2) is provided with housing chamber outlet (10) respectively.
10. according to claim 1,2,3,4,5,6,7 or 8 each described separators, it is characterized in that: housing chamber (2) inwall is provided with nozzle (19).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011102963876A CN102441501A (en) | 2011-07-15 | 2011-09-24 | Separator |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201110207547 | 2011-07-15 | ||
| CN201110207547.5 | 2011-07-15 | ||
| CN201110249663 | 2011-08-17 | ||
| CN201110249663.3 | 2011-08-17 | ||
| CN2011102963876A CN102441501A (en) | 2011-07-15 | 2011-09-24 | Separator |
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| CN102441501A true CN102441501A (en) | 2012-05-09 |
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| CN2011102963876A Pending CN102441501A (en) | 2011-07-15 | 2011-09-24 | Separator |
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| WO2015051745A1 (en) * | 2013-10-11 | 2015-04-16 | 陈久斌 | Separator |
| CN105682878A (en) * | 2013-10-21 | 2016-06-15 | 里-马奇（英国）有限公司 | Process for separating a synthetic turf product |
| WO2018082489A1 (en) * | 2016-11-04 | 2018-05-11 | 陈久斌 | Separation reaction powder grinding machine |
| CN108993784A (en) * | 2018-06-06 | 2018-12-14 | 浙江海洋大学 | A kind of method and apparatus of continuous hypergravity separation two-dimension nano materials |
| WO2020108432A1 (en) * | 2018-11-28 | 2020-06-04 | 陈久斌 | Vortex machine |
| CN114534418A (en) * | 2022-02-18 | 2022-05-27 | 阳光氢能科技有限公司 | Gas-liquid separator and hydrogen production system |
| CN115121378A (en) * | 2017-02-28 | 2022-09-30 | 唐凌霄 | Driven centrifugal unit, manufacturing method and using method thereof and solid-liquid separation equipment thereof |
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- 2011-09-24 CN CN2011102963876A patent/CN102441501A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015051745A1 (en) * | 2013-10-11 | 2015-04-16 | 陈久斌 | Separator |
| CN105682878A (en) * | 2013-10-21 | 2016-06-15 | 里-马奇（英国）有限公司 | Process for separating a synthetic turf product |
| CN105682878B (en) * | 2013-10-21 | 2017-10-24 | 里-马奇（英国）有限公司 | For the technique for separating artificial grass product |
| WO2018082489A1 (en) * | 2016-11-04 | 2018-05-11 | 陈久斌 | Separation reaction powder grinding machine |
| CN115121378A (en) * | 2017-02-28 | 2022-09-30 | 唐凌霄 | Driven centrifugal unit, manufacturing method and using method thereof and solid-liquid separation equipment thereof |
| CN108993784A (en) * | 2018-06-06 | 2018-12-14 | 浙江海洋大学 | A kind of method and apparatus of continuous hypergravity separation two-dimension nano materials |
| CN108993784B (en) * | 2018-06-06 | 2020-08-18 | 浙江海洋大学 | Method and device for separating two-dimensional nano material by continuous supergravity |
| WO2020108432A1 (en) * | 2018-11-28 | 2020-06-04 | 陈久斌 | Vortex machine |
| CN114534418A (en) * | 2022-02-18 | 2022-05-27 | 阳光氢能科技有限公司 | Gas-liquid separator and hydrogen production system |
| CN114534418B (en) * | 2022-02-18 | 2023-11-28 | 阳光氢能科技有限公司 | Gas-liquid separator and hydrogen production system |
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Application publication date: 20120509 |