CN101972716A - Gas-solid centrifugal separation and exhaust integrated machine - Google Patents
Gas-solid centrifugal separation and exhaust integrated machine Download PDFInfo
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Abstract
The invention discloses a gas-solid centrifugal separation and exhaust integrated machine, comprising a rotator system and a stator system, wherein the rotator system rotates in the stator system to achieve gas-solid centrifugal separation and discharge the separated gas and solid particles at the same time; and the stator system comprises centrifugal fan impellers (3), a rotary gas-solid separation chamber assembly (4), an isolation cylinder (5), a central exhaust pipe (6), an anti-swirl hood (7), a rotary dust storage chamber, a dust discharge assembly (9) and a spindle (11). The integrated machine is a two-in-one device capable of automatically absorbing dust-containing gas, continuously separating the carried solid particles from the gas, automatically removing the solid particles and automatically discharging the gas at the same time. The integrated machine can improve the separative efficiency of ultrafine particles, can be applied in an occasion with the high temperature about 400 DEG C, and can reduce the occupied area.
Description
Technical field
The present invention relates to the gas solid separation technical field, be specifically related to a kind of gas-solid centrifugation and exhaust integrated machine, carry two big functions to finish gas solid separation and gas, improve the separative efficiency of solid ultra-fine grain (particle diameter≤10 μ m) with an equipment.Be mainly used in the dust pelletizing system of industries such as oil, chemical industry, medicine, smelting iron and steel, non-ferrous metal metallurgy, cement plant, thermoelectricity boiler, grain processing plant, coking plant.
Background technology
The gas solid separation of dusty gas is the main technique flow process of industries such as oil, chemical industry, medicine, mine, metallurgy, cement, thermoelectricity, grain processing.Reducing the pollution of all types of industries dust to atmosphere, is the environmental protection problem that the current whole world is paid attention to.
The gas solid separation of dusty gas is divided with regard to big aspect two classes, and a class is a dry method dust, and a class is wet dedusting.Though some hydrofilters to fine grain separative efficiency height, bring water to pollute and the wasting of resources, because available raw material behind most dust collection, just lost using value after the immersion, be water insensitive material, reclaim and also want dry, increase energy consumption.In addition in the winter of cold district, also to heat and be incubated dust pelletizing system, increase power consumption.So occasion is as far as possible without wet dedusting mostly.At present, dry method dust is the most frequently used dedusting method.Dry dust removal equipment mainly contains cyclone separator, electrostatic precipitator, sack cleaner and all kinds of inertial dust separator.Wherein to be dust-contained airflow enter the cylindrical shell shape of spinning along tangent line to the basic principle of cyclone separator rotatablely moves, and under centrifugal action grit separated.As shown in Figure 1.Simple in structure because of it, reliable, 100 for many years, most widely used general in industry.The shortcoming of cyclone separator is very low to the separative efficiency of fine particle.Introduce according to list of references [1] table 1-18, when the solid grain size in the dusty gas 〉=50 μ m, the separative efficiency of cyclone separator can reach 94%, but when solid grain size in the dusty gas is 5 μ m, separative efficiency only 27%, when particle diameter was 1 μ m, separative efficiency only was 8%.According to list of references [1] table 1-21 regulation, when the solid grain size in the dusty gas≤10 μ m, must adopt sack cleaner or electrostatic precipitator.During the velocity perturbation of cyclone dust collectors inlet air flow, bigger in addition to the separative efficiency influence.
The basic principle of sack cleaner is to capture dust with the fibroid filter bag.The separative efficiency height of sack cleaner, be solid grain size in the gas be 1 μ m, the separative efficiency of sack cleaner is also up to 99%
[1], it is the highest deduster of separative efficiency in the present dry collector.But the average filtration speed of sack cleaner is that (0.017～0.02m/s), so when the flow of dusty gas was big, the filtering surface of fiber was very big, causes equipment huge, investment is high, and can only be applicable to the occasion of gas temperature≤250 ℃ for 1～1.2m/min
[2], in the allowable temperature scope, when being higher than 80 ℃, temperature is high more, and the price of filter pocket material is high more.Except that sack cleaner cost height, operating cost is also higher, because of filter bag wearing and tearing and grit fouling obstruction, needs often to change filter bag.
The basic principle of electrostatic precipitator is under the high voltage electric field effect, makes the particle particle in the dust-contained airflow charged, and is attracted, captures.The separative efficiency height of electrostatic precipitator is that the separative efficiency of 5 μ m is 99% for particle diameter
[1], be that the separative efficiency of 1 μ m is 86% to particle diameter
[1]The average flow velocity of dusty gas is 0.4～1.8m/s in electrostatic precipitator
[1]So area of passage is also bigger.Because high-tension system is arranged, its structure is more complicated, and the one-time investment expense and the operation and maintenance cost of electrostatic precipitator are also higher.
Can in dusty gas, solid grain size be when proportion is higher in 1～10 mu m range, work out that the low deduster of a kind of cost replaces or part replaces sack cleaner and electrostatic precipitator, and this is pursuing one's goal of present gas solid separation researcher.
Since O.Morse in 1886 had obtained first patent of cyclone separator, the technology of cyclone separator was constantly developed always, to main two aspects, the one, theoretical research, the one, the experimental study of dividing of its research.For the separative efficiency and the minimizing flow losses that improve cyclone separator, experimental study is divided into two aspects again, and the one, each geometric parameter and the inlet velocity of optimization cyclone separator; The one, the version of change cyclone separator.This two aspect has all obtained obvious effects.Effect is preferably U.S. Pat 2941621 aspect the parameter optimizing, this patent be reduced with separation chamber's cylinder to 80mm, improved separative efficiency, for the catalyst dust of particle diameter≤10 μ m separating effect has preferably been arranged.In order to satisfy big flow, more a plurality of separate unit tubule cyclone separators are made array in parallel.Because tubule quantity is more, cause equipment huge, complex structure is made difficulty, easily produces the assignment of traffic inequality between each single tube, and dust problem such as play a reversed role causes separative efficiency to reduce.When charge flow rate fluctuation was big, separative efficiency was lower especially, and time is everlasting on the ground far away of hundreds of rice around the refinery catalytic cracking unit, and naked eyes just can be seen the catalyst dust of one deck white.Because the separating force of cyclone separator depends on the diameter of dusty gas inlet velocity and separation chamber, so the fluctuation of inlet gas flow is the inevitable shortcoming of cyclone separator to the influence of separative efficiency.
Changing version has certain innovation, and patent documentation CN85200870U makes cyclone separator into several by an air inlet exactly, and concrete structure is seen shown in Figure 2.In this patent documentation the air velocity of each air inlet is brought up to 100m/s, improve 4～5 times than the speed of former cyclone separator air inlet, this improvement has improved separative efficiency.But import department's flow resistance can increase, and air velocity only can reach 100m/s in import department, and after air-flow entered the annular release chamber, air velocity can descend rapidly, can not keep high centrifugal acceleration in whole volute chamber always.The big minor swing of air velocity of import department can influence separative efficiency simultaneously.
Increase centrifugal force and be the effective way that improves the gas-solid separator separative efficiency.Chinese patent literature ZL02103986.0,02103989.5 and CN2766964Y made effective achievement in this respect, their common characteristic is to adorn the pinwheel of a rotation in being similar to the circular cylindrical shell of cyclone separator, as the described pinwheel structure of CN2766964Y: " pinwheel 3 by U font needle-like seedling radially evenly dense arrangement layering stacked combination on wheel hub, form.There is at least one pinwheel to be fixed on the turning cylinder." its structural principle as shown in Figure 3, pinwheel 3 is to do dead axle by driven by motor to rotate among the figure.The flow direction of dusty gas can be tangential with pinwheel and flow (or helical flow), also can be axial flow.The effect of pinwheel be with gas in solid particle collide, make particle obtain higher centrifugal force, thereby improve the separative efficiency of ultra-fine grain.According to this patent documentation statement, be the particle of 2 μ m to particle diameter, separative efficiency can improve 2 times.This be one greatly the progress.Obviously, the main solid particles of this pinwheel additional in the patent documentation increases rotation function, improves separative efficiency.This improvement has increased by a cover rotor, added energy consumption, and entering and discharging of dusty gas must provide kinetic energy by blower fan.
List of references:
[1] Zhang Dianyin, Wang Chun. the deduster handbook. Beijing. the .2004.10 of Chemical Industry Press;
[2] [pellet] Huffman (HoffIllalan, A.C), [U.S.] Si Tanyin (stcin, L. E.) work, Peng Weiming, Ji Zhongli translates. and cyclone separator-principle, design and engineering are used. Beijing; Chemical Industry Press, 2004.7.
Summary of the invention
In order to improve the centrifugal force of solid particle in the gas, the present invention proposes a kind of gas-solid centrifugation and exhaust integrated machine, and a centrifugal blower fan blade wheel is fixed, centrifugal blower fan blade wheel axis and circular cylinder dead in line in the top of the circular cylinder of installing axis normal.The auxiliary more simultaneously relevant cylinder that increases constructs corresponding rotation separation chamber and runner.Cylinder is rotated with centrifugal blower fan blade wheel, and centrifugal blower fan blade wheel applies rotational kinetic energy for simultaneously the solid particle in gas and the gas, and the centrifugal force that particle obtains is compared with cyclone separator and increased tens of times, not only improves solid ultra-fine grain (particle diameter≤10 μ m)
[1]Separative efficiency, make dusty gas suck all-in-one automatically simultaneously, purify back gas and flow out all-in-one automatically.Saved and be the supporting blower fan of cyclone separator.Dusty gas enters all-in-one by cylinder top central axis downward (rotor-support-foundation system relatively).Purify back gas by (rotor-support-foundation system relatively) outflow downwards of cylindrical shell lower central axis.Solid particle is radially got rid of automatically by rotary barrel.The present invention has realized gas-solid centrifugation and two functions of exhaust.
As follows for realizing the concrete technical scheme that purpose of the present invention adopts:
A kind of gas-solid centrifugation and exhaust integrated machine are made of rotor-support-foundation system and stator system.Rotor-support-foundation system is installed on the stator system.Stator system is installed on the ground frame (frame does not mark).Rotor-support-foundation system rotates in fixed axis in stator system under the drive of motor (motor does not mark) during work.
Rotor-support-foundation system comprises centrifugal blower fan blade wheel, rotation gas solid separation chamber component, insulated cylinder, central row tracheae, anti-whirlpool cover, rotates dust-storage chamber and parts such as dust exhaustor assembly, hydraulic cylinder and axle.
Described centrifugal blower fan blade wheel is fixed on the axle, is arranged at the upper end of all-in-one, rotates under the drive of axle, and the rotating torque of axle is passed to impeller.
Described rotation gas solid separation chamber component comprises upper circular cylindrical shell, middle part truncated cone-shaped cylindrical shell, bottom circular cylinder body and the lower end end cap that distributes vertically.Described upper circular cylindrical shell is fixedlyed connected with centrifugal blower fan blade wheel by connector, and the bottom circular cylinder body is connected with the lower end end cap by connector, connects by described middle part truncated cone-shaped cylindrical shell between described upper circular cylindrical shell and the bottom circular cylinder body.The central axes of this rotation gas solid separation chamber component and the dead in line of centrifugal blower fan blade wheel and axle.
Described insulated cylinder coaxial package is in the upper circular cylindrical shell of rotation gas solid separation chamber component, and the circular annular region between two cylinders constitutes gas solid separation chamber A.This insulated cylinder is fixedlyed connected with the wheel disc of centrifugal blower fan blade wheel.
The top of described gas solid separation chamber A is provided with one group of guide vane, and this group guide vane is evenly installed along gas solid separation chamber A hoop, and with corresponding respectively being connected of blade of centrifugal blower fan blade wheel.
Described central row tracheae is coaxial to be installed in the insulated cylinder, annular region between two cylinders constitutes concentric circles annular channel C, this central row tracheae axially prolongation downwards stretches out insulated cylinder, and the annular region that forms between its extension and the upper circular cylindrical shell constitutes concentric circles annular channel B.This center exhaust pipe lower part has been wholely set spoke and wheel hub, and is installed on the axle by this spoke and wheel hub.All be drilled with oilhole on described spoke and the axle, and corresponding together with, for hydraulic cylinder provides turnover pressure oil.
Described anti-whirlpool cover is positive truncated cone-shaped cylindrical shell, inner wall surface thereof is provided with several along the equally distributed bearing rib of circumference, in order to will prevent that whirlpool cover fixing coaxial socket is installed on the exhaust tube wall of center, the auger edge, bottom of the anti-whirlpool of truncated cone-shaped cover forms an annular gap D with the upper circular cylinder inboard wall face of rotation gas solid separation chamber component, and this clearance D is that separated solid particle flows to the passage that the foot that rotates dust-storage chamber and dust exhaustor assembly rotates dust-storage chamber.The outside wall surface looping gap E of cover upper end, anti-whirlpool conelet margin and center blast pipe.Entering the small part gas that rotates dust-storage chamber upwards flows out from gap E.
Described rotation dust-storage chamber and the coaxial socket of dust exhaustor assembly are arranged on the lower end of central row tracheae, be used to store solid particle and the intermittently discharge that gas solid separation goes out, this rotation dust-storage chamber and dust exhaustor assembly comprise hydraulic cylinder and are separately positioned on this hydraulic cylinder the hydraulic cylinder upper cover plate and the hydraulic cylinder lower cover at two ends up and down, on the described hydraulic cylinder upper cover plate circular cylinder is set, in order to the coaxial socket of the outside wall surface of central row tracheae.The radially outward outstanding hydraulic cylinder of described hydraulic cylinder lower cover, the ledge outmost turns is coaxially arranged with vertical short cylinder, and it forms the rotation G of dust-storage chamber with hydraulic cylinder and ledge, is used to store the solid particle that gas solid separation goes out
Rotating dust-storage chamber and dust exhaustor assembly can be along the all-in-one axis direction, and the outside wall surface along the central row tracheae moves up and down within the specific limits, but can not rotate.Its purpose that moves up and down is intermittently dust discharge.
Described stator system comprises journal bearing and axial thrust bearing assembly, dusty gas import, case component, static dust-storage chamber spiral dust exhaustor, purifies back gas vent, journal bearing assembly and hydraulic circuit swivel joint.
Described journal bearing and axial thrust bearing assembly and journal bearing assembly are arranged at a two ends respectively, are used for the rotation of supporting rotor system axis; Described dusty gas import comprises seal and the adpting flange between air inlet pipe, stator and the rotor, is used for dusty gas is imported all-in-one; Described case component comprises the connector between casing, casing and the ground bracing frame, the static dust-storage chamber of casing bottom, and rotor-support-foundation system is arranged in this case component; Described static dust-storage chamber spiral dust exhaustor comprises spiral fluted shaft, the outer cylinder of spiral fluted shaft, end cap, the seal of carrying dust, is used for the solid of intermittently getting rid of from the rotation G of dust-storage chamber is discharged; Gas vent comprises seal and the adpting flange between escape pipe, stator and the rotor after described the purification, is used for the gas after separating is discharged; Described hydraulic circuit swivel joint is the connector that connects between the hydraulic system oil circuit oil circuit interior with being located at axle.
The present invention has following characteristics with respect to prior art:
1. compare the centrifugal force that makes solid particle under the equal conditions with cyclone separator and improve several times, the cut diameter of separated solid particle is dwindled several times, has improved the separative efficiency of ultra-fine grain (particle diameter≤10 μ m).But increase energy consumption hardly,, saved the energy consumption of blower fan, that is to say that this rotation energy consumption is that air blast must be paid for gas provides kinetic energy because also improved the kinetic energy of gas when improving particle centrifugal force.Also save supporting blower fan, reduced floor space.
2. if further improve the rotating speed of gas-solid centrifugation and air draft all-in-one, can replace sack cleaner.Reduce and the supporting blower fan of sack cleaner simultaneously.Can reduce the one-time investment of equipment significantly.Reduced floor space.
3. because the rotating speed and the diameter of the cylinder of rotation gas solid separation chamber component 4 are depended in the present invention to the separating force of solid particle, so when no matter the flow at dusty gas import 2 places fluctuates much, can not influence separative efficiency, overcome the inherent defect of cyclone separator.
4. gas-solid centrifugation and exhaust integrated machine can be used for the hot conditions about 400 ℃.
Description of drawings
Fig. 1 a kind of cyclone separator structure figure of the prior art
Fig. 2 a kind of centrifugal separating device structure chart of the prior art
Fig. 3 mechanical rotor whizzer of the prior art structure chart
Fig. 4 gas-solid centrifugation of the present invention and exhaust integrated machine structure chart
The structure chart of Fig. 5 rotation of the present invention dust-storage chamber and dust exhaustor assembly 9
Specific embodiments
The invention will be further described below in conjunction with the drawings and specific embodiments.
Shown in Fig. 3-5, a kind of gas-solid centrifugation and exhaust integrated machine are made of rotor-support-foundation system and stator system.Rotor-support-foundation system is installed on the stator system.Stator system is installed on the ground frame (frame does not mark).Rotor-support-foundation system rotates in fixed axis in stator system under the drive of motor (motor does not mark) during work.
Rotor-support-foundation system comprises centrifugal blower fan blade wheel 3, rotation gas solid separation chamber component 4, insulated cylinder 5, central row tracheae 6, anti-whirlpool cover 7, rotates dust-storage chamber and parts such as dust exhaustor assembly 9, hydraulic cylinder 10 and axle 11.
Described centrifugal blower fan blade wheel 3 is fixed on the axle 11, is arranged at the upper end of all-in-one, rotates under the drive of axle 11, and the rotating torque of axle 11 is passed to impeller.
Described rotation gas solid separation chamber component 4 comprises upper circular cylindrical shell, middle part truncated cone-shaped cylindrical shell, bottom circular cylinder body and the lower end end cap that distributes vertically.Described upper circular cylindrical shell is fixedlyed connected with centrifugal blower fan blade wheel 3 by connector, and the bottom circular cylinder body is connected with the lower end end cap by connector, connects by described middle part truncated cone-shaped cylindrical shell between described upper circular cylindrical shell and the bottom circular cylinder body.The central axes of this rotation gas solid separation chamber component 4 and the dead in line of centrifugal blower fan blade wheel 3 and axle 11.
Described insulated cylinder 5 coaxial packages are in the upper circular cylindrical shell of rotation gas solid separation chamber component 4, and the circular annular region between two cylinders constitutes gas solid separation chamber A, sees shown in Figure 4.This insulated cylinder 5 is fixedlyed connected with the wheel disc of centrifugal blower fan blade wheel 3.
The top of described gas solid separation chamber A is provided with one group of guide vane, and this group guide vane is evenly installed along gas solid separation chamber A hoop, and with corresponding respectively being connected of blade of centrifugal blower fan blade wheel 3.
Described central row tracheae 6 coaxial being installed in the insulated cylinder 5, annular region between two cylinders constitutes concentric circles annular channel C, this central row tracheae 6 axially prolongation downwards stretches out insulated cylinder 5, the annular region that forms between its extension and the upper circular cylindrical shell constitutes concentric circles annular channel B, sees shown in Figure 4.These central row tracheae 6 bottoms have been wholely set spoke and wheel hub, and are installed on the axle 11 by this spoke and wheel hub.Described spoke all is drilled with oilhole with axle on 11, and corresponding together with, for hydraulic cylinder 10 provides turnover pressure oil.
Described anti-whirlpool cover 7 is positive truncated cone-shaped cylindrical shell, inner wall surface thereof is provided with several along the equally distributed bearing rib of circumference, cover 7 fixing coaxial sockets and be installed on central row tracheae 6 outer walls in order to will prevent the whirlpool, the auger edge, bottom of the anti-whirlpool of truncated cone-shaped cover 7 forms an annular gap D with the upper circular cylinder inboard wall face of rotation gas solid separation chamber component 4, and this clearance D is that separated solid particle flows to the passage that the foot that rotates dust-storage chamber and dust exhaustor assembly 9 rotates dust-storage chamber.The outside wall surface looping gap E of 7 upper end conelet margin and center blast pipes 6 is covered in anti-whirlpool.Entering the small part gas that rotates dust-storage chamber upwards flows out from gap E.
Described rotation dust-storage chamber and the 9 coaxial sockets of dust exhaustor assembly are arranged on the lower end of central row tracheae 6, be used to store solid particle and the intermittently discharge that gas solid separation goes out, the structure of this rotation dust-storage chamber and dust exhaustor assembly 9 as shown in Figure 4, comprise hydraulic cylinder and be separately positioned on this hydraulic cylinder the hydraulic cylinder upper cover plate and the hydraulic cylinder lower cover at two ends up and down, on the described hydraulic cylinder upper cover plate circular cylinder is set, in order to the coaxial socket of the outside wall surface of central row tracheae 6.The radially outward outstanding hydraulic cylinder of described hydraulic cylinder lower cover, the ledge outmost turns is coaxially arranged with vertical short cylinder, and it forms the rotation G of dust-storage chamber with hydraulic cylinder and ledge, is used to store the solid particle that gas solid separation goes out.
Rotating dust-storage chamber and dust exhaustor assembly 9 can be along the all-in-one axis direction, and the outside wall surface along central row tracheae 6 moves up and down within the specific limits, but can not rotate.Its purpose that moves up and down is intermittently dust discharge.
Described stator system comprises journal bearing and axial thrust bearing assembly 1, dusty gas import 2, case component 8, static dust-storage chamber spiral dust exhaustor 12, purifies back gas vent 13, journal bearing assembly 14 and hydraulic circuit swivel joint 15.
Described journal bearing and axial thrust bearing assembly 1 and journal bearing assembly 14 are arranged at axle 11 two ends respectively, are used for the rotation of supporting rotor system axis 11; Described dusty gas import 2 comprises seal and the adpting flange between air inlet pipe, stator and the rotor, is used for dusty gas is imported all-in-one; Described case component 8 comprises the connector between casing, casing and the ground bracing frame, the static dust-storage chamber of casing bottom, and rotor-support-foundation system is arranged in this case component 8; Described static dust-storage chamber spiral dust exhaustor 12 comprises spiral fluted shaft, the outer cylinder of spiral fluted shaft, end cap, the seal of carrying dust, is used for the solid of intermittently getting rid of from the rotation G of dust-storage chamber is discharged; Gas vent 13 comprises seal and the adpting flange between escape pipe, stator and the rotor after described the purification, is used for the gas after separating is discharged; Described hydraulic circuit swivel joint 15 is the connectors that connect between the hydraulic system oil circuit oil circuit interior with being located at axle 11.
Dusty gas is sucked all-in-one automatically, enters all-in-one by dusty gas import 2, and the shaft axis direction enters centrifugal blower fan blade wheel 3 annular entrance then, turns to and radially enters centrifugal blower fan blade wheel leaf road.Dusty gas rotates around axis under the blade of Ye Daonei promotes, and dusty gas also produces radially centrifugal motion at Ye Daonei simultaneously, and after dusty gas flowed out impeller leaf road, the shaft axis direction flowed to annular gas solid separation chamber A (seeing shown in Figure 4) again.In annular gas solid separation chamber A, dusty gas had both been followed rotor-support-foundation system and has been done definitely and rotatablely move, simultaneously again in the circular passage under the guiding of guide vane, and the rotor axis direction relative motion of line of spinning relatively.The solid particle that carries in gas and the gas obtains certain centrifugal kinetic energy under the acting in conjunction of centrifugal blower fan blade wheel 3 and the A of gas-solid separation chamber.The solid particle that carries in the gas overcomes the upper circular tube internal face motion of gas flow resistance to rotation gas solid separation chamber component 4 under the effect of this centrifugal kinetic energy, be separated gas.After purified gas flows out the gas-solid A of separation chamber by this kinetic energy, enter the circular passage B (seeing shown in Figure 4) of insulated cylinder 5 bottoms.After gas arrives among the B of circular passage, turn over turnback (actual is that helix flows), flow up into circular passage C (seeing shown in Figure 4) at axis direction.After arriving circular passage C the top, gas turns over turnback again, enters the circular passages that central row tracheae 6 and axle 11 constitute.Gas this circular passage flow to along axis all-in-one bottom after, turn to again radially, gas vent 13 is discharged all-in-one automatically after purifying, and purifies back gas and enters the user pipe system.
After separated solid particle reaches internal face by the upper circular tube of rotation gas solid separation chamber component 4, under action of centrifugal force, be close to wall, again under the drive of spiral air flow and under the acting in conjunction of gravity, particle at internal face along spiral motion, move among the G of rotation dust-storage chamber (seeing shown in Figure 4) that rotates dust-storage chamber and dust exhaustor assembly 9 through annular gap D (seeing shown in Figure 4), and deposition wherein.Flow out through annular gap E (seeing shown in Figure 4) and enter the small part gas that rotates dust-storage chamber.Solid particle in rotating Dust Storage Room may be carried secretly again by eddy airstream, and then the effect every whirlpool cover 7 designs for avoiding this phenomenon.Rotate solid particle among the G of dust-storage chamber reach a certain amount of after, make the epicoele of hydraulic cylinder 10 advance pressure oil (hydraulic oil of hydraulic cylinder 10 cavity of resorptions is by being located at the oil circuit oil sump tank in the axle 11) by the automatic controlling system hydraulic valve.The oil pressure of epicoele promotes to rotate dust-storage chamber and dust exhaustor assembly 9 moves upward, after the relative connection of radially dust-exhausting port of the radially dust-exhausting port that rotates dust-storage chamber and rotation gas solid separation chamber component 4, be deposited on solid particle among the rotation G of dust-storage chamber radially is discharged to static case component 8 under action of centrifugal force bottom.The dust discharge time up, the automatic controlling system hydraulic valve, make the cavity of resorption of hydraulic cylinder advance pressure oil (hydraulic oil of epicoele is by being located at the oil circuit oil sump tank in the axle), under oil pressure promotes, rotate dust-storage chamber and 9 declines of dust exhaustor assembly, close dust-exhausting port, gas-solid centrifugation and exhaust integrated machine rotor system stop dust discharge.Be discharged to the solid particle of static case component 8 bottoms, get rid of in limited time automatically by the static dust-storage chamber spiral dust exhaustor 12 that is located at the bottom.Rotate the interval time of dust-storage chamber's dust discharge and the dust discharge time of the length of each dust discharge time and static dust-storage chamber spiral dust exhaustor 12 and can revise the automatic control program setting arbitrarily.
Each parts in the rotor-support-foundation system can all use metal material, are being subjected to the mobile additional high-abrasive material in parts place that washes away.Stator system all can use the metal material manufacturing.
Can design cooling jacket in the associated components of the wall that contacts with gas in the described rotor-support-foundation system, but its cooling agent gas, also liquid.So that the present invention can be used under the higher temperature.
In order to verify the actual separation effect of gas-solid centrifugation of the present invention and exhaust integrated machine, the cyclone separator of now choosing whirl cylinder internal diameter in the cyclone separator series that Potou city roc crane environmental protection machinery Co., Ltd produces and be 2m object as a comparison carries out the effect contrast.Suppose also to be 2m, 1450 rev/mins of rotating speeds with the impeller diameter of the supporting air blast of this cyclone separator.Cyclone separator import wind speed is 23m/s.In the gas-solid that separates, gas is air, and solid particle is the alundum (Al dust.The calculating formula 4-23 of cut diameter calculates contrast in the citing document [1].
d
cCut diameter
The viscosity of μ air
The flow of Q gas
ρ
PThe density of particle
H cylinder height
The V tangential velocity
G is an acceleration of gravity
Result of calculation is 2.9 μ m with the cut diameter that cyclone separator separates, and the cut diameter of separating with the air draft all-in-one with the gas-solid centrifugation is 0.44 μ m.Cut diameter narrows down to 1/6.59.
Claims (5)
1. a gas-solid centrifugation and exhaust integrated machine comprise rotor-support-foundation system and stator system, and described rotor-support-foundation system rotates in stator system, and gas and solid particle after realizing the gas-solid centrifugation and discharging separation simultaneously respectively is characterized in that,
Described rotor-support-foundation system comprises centrifugal blower fan blade wheel (3), rotation gas solid separation chamber component (4), insulated cylinder (5), central row tracheae (6), anti-whirlpool cover (7), rotates dust-storage chamber and dust exhaustor assembly (9) and rotating shaft (11), described centrifugal blower fan blade wheel (3) is positioned at the upper end of all-in-one, described rotation gas solid separation chamber component (4) is fixedly connected on this centrifugal blower fan blade wheel (3) below, rotation synchronous with it; Described insulated cylinder (5) is coaxial to be socketed in the rotation gas solid separation chamber component (4), fixedly connected with the wheel disc of centrifugal blower fan blade wheel (3) in its cylindrical shell top, this insulated cylinder (5) forms gas solid separation chamber A with rotation gas solid separation chamber component (4) circular annular region between the two, central row tracheae (6) is coaxial to be socketed in the rotating shaft (11) and rotating shaft (11) rotation synchronously, central row tracheae (a 6) part in the axial direction is positioned at insulated cylinder (5), another part is positioned at outside the insulated cylinder (5), part and the annular region between the insulated cylinder (5) that this central row tracheae (6) is positioned at insulated cylinder (5) constitute circular ring path C, and annular region constitutes circular ring path B between described another part of central row tracheae (6) and the rotation gas solid separation chamber component (4); Described anti-whirlpool cover 7 is positive truncated cone-shaped cylindrical shell, and coaxial package is on central row tracheae (6) outer wall, and rotation synchronous with it prevents that the auger edge of whirlpool cover (7) bottom and the internal face of rotation gas solid separation chamber component (4) form an annular gap D;
Described centrifugal blower fan blade wheel (3) rotates under the driving of rotating shaft (11), automatically be drawn into dusty gas in the all-in-one, the gas solid separation chamber A that the Ye Daozhong that enters centrifugal blower fan blade wheel (3) obtains to enter behind the rotation function rotation carries out the gas-solid centrifugation, gas after the centrifugation enters central row tracheae (6) successively behind circular ring path B and circular ring path C, and outlet discharge by communicating with this central row tracheae (6) bottom, the solid particle that centrifugation goes out is under the acting in conjunction of centrifugal force and gravity, be close to rotation gas solid separation chamber component (4) internal face and enter into the G of rotation dust-storage chamber that rotates dust-storage chamber and dust exhaustor assembly (9) through annular gap D, and and then discharge all-in-one, gas and solid particle after finishing the gas-solid centrifugation and discharging separation simultaneously respectively.
2. a kind of gas-solid centrifugation according to claim 1 and exhaust integrated machine, it is characterized in that, described rotation gas solid separation chamber component (4) comprises the upper circular cylindrical shell of arranging vertically, middle part truncated cone-shaped cylindrical shell, bottom circular cylinder body and lower end end cap, described upper circular cylindrical shell is fixedlyed connected with centrifugal blower fan blade wheel (3), the bottom circular cylinder body is connected with the lower end end cap, connect by described middle part truncated cone-shaped cylindrical shell between described upper circular cylindrical shell and the bottom circular cylinder body, the central axis of this rotation gas solid separation chamber component (4) and the dead in line of centrifugal blower fan blade wheel (3) and rotating shaft (11), described gas solid separation chamber A is formed by the circular annular region between this upper circular cylindrical shell and the insulated cylinder (5), and described circular ring path B is made of the circular annular region between described another part of this upper circular cylindrical shell and central row tracheae (6).
3. a kind of gas-solid centrifugation according to claim 1 and 2 and exhaust integrated machine, it is characterized in that, the outside wall surface of the conelet margin and center blast pipe (6) of described anti-whirlpool cover (7) upper end forms annular gap E, and entering the portion gas that rotates among the G of dust-storage chamber can upwards flow out from this annular gap E.
4. according to described a kind of gas-solid centrifugation of one of claim 1-3 and exhaust integrated machine, it is characterized in that, the upper end of described gas solid separation chamber A is provided with one group of guide vane, this group guide vane is evenly installed along gas solid separation chamber A hoop, and, produce screw in order to the relative shaft axis of guiding dust-contained airflow with corresponding respectively being connected of each blade of centrifugal blower fan blade wheel (3).
5. according to described a kind of gas-solid centrifugation of one of claim 1-4 and exhaust integrated machine, it is characterized in that, described rotation dust-storage chamber and dust exhaustor assembly (9) be coaxial to be socketed on the outside wall surface of central row tracheae (6), it is positioned at the below of anti-whirlpool cover (7), be used to store solid particle and the intermittently discharge that gas solid separation goes out, this rotation dust-storage chamber and dust exhaustor assembly (9) comprising: hydraulic cylinder and be separately positioned on this hydraulic cylinder up and down upper cover plate and the lower cover at two ends, wherein, described upper cover plate is provided with a circular cylinder, in order to the coaxial socket of outside wall surface of central row tracheae (6), described lower cover radially outward protrudes in hydraulic cylinder, outstanding annular section outmost turns is coaxial to be socketed with vertical short cylinder, the space that itself and hydraulic cylinder outer wall and described outstanding annular section constitute forms the described rotation G of dust-storage chamber, hydraulic oil in the described hydraulic cylinder promotes described rotation dust-storage chamber off and on and dust exhaustor assembly (9) moves up and down along central row tracheae (6), be used to make the radially dust-exhausting port that rotates the G of dust-storage chamber intermittently to be communicated with radially dust-exhausting port on the rotation gas solid separation chamber component (4), realize being deposited on the solid particle that rotates among the G of dust-storage chamber under action of centrifugal force by radially intermittently discharge.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102937129A CN101972716B (en) | 2010-09-27 | 2010-09-27 | Gas-solid centrifugal separation and exhaust integrated machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010102937129A CN101972716B (en) | 2010-09-27 | 2010-09-27 | Gas-solid centrifugal separation and exhaust integrated machine |
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| Publication Number | Publication Date |
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| CN101972716A true CN101972716A (en) | 2011-02-16 |
| CN101972716B CN101972716B (en) | 2012-05-09 |
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| CN2010102937129A Active CN101972716B (en) | 2010-09-27 | 2010-09-27 | Gas-solid centrifugal separation and exhaust integrated machine |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102698892A (en) * | 2012-05-25 | 2012-10-03 | 刘宇婧 | Combined rotary gas-solid separation and exhaust all-in-one machine |
| CN102886316A (en) * | 2012-09-18 | 2013-01-23 | 东北石油大学 | Hydrocyclone used for three-phase medium separation |
| CN102950064A (en) * | 2012-09-28 | 2013-03-06 | 刘宇婧 | Energy-saving dusting machine |
| CN106975576A (en) * | 2017-02-24 | 2017-07-25 | 宁波神通模塑有限公司 | A kind of adjustable cyclonic separator |
| CN107755106A (en) * | 2017-09-25 | 2018-03-06 | 浙江德清华丝纺织有限公司 | A kind of air processor for spinning and weaving workshop |
| CN109351060A (en) * | 2018-12-19 | 2019-02-19 | 扬州智厨科技有限公司 | A kind of Combined dust-cleaning apparatus |
| CN113351383A (en) * | 2021-05-28 | 2021-09-07 | 江西理工大学 | Wear-resisting solid-liquid separation swirler |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102698892A (en) * | 2012-05-25 | 2012-10-03 | 刘宇婧 | Combined rotary gas-solid separation and exhaust all-in-one machine |
| CN102886316A (en) * | 2012-09-18 | 2013-01-23 | 东北石油大学 | Hydrocyclone used for three-phase medium separation |
| CN102886316B (en) * | 2012-09-18 | 2014-07-02 | 东北石油大学 | Hydrocyclone used for three-phase medium separation |
| CN102950064A (en) * | 2012-09-28 | 2013-03-06 | 刘宇婧 | Energy-saving dusting machine |
| CN102950064B (en) * | 2012-09-28 | 2013-11-20 | 刘宇婧 | Energy-saving dusting machine |
| CN106975576A (en) * | 2017-02-24 | 2017-07-25 | 宁波神通模塑有限公司 | A kind of adjustable cyclonic separator |
| CN107755106A (en) * | 2017-09-25 | 2018-03-06 | 浙江德清华丝纺织有限公司 | A kind of air processor for spinning and weaving workshop |
| CN109351060A (en) * | 2018-12-19 | 2019-02-19 | 扬州智厨科技有限公司 | A kind of Combined dust-cleaning apparatus |
| CN109351060B (en) * | 2018-12-19 | 2021-07-23 | 扬州智厨科技有限公司 | Combined dust removing device |
| CN113351383A (en) * | 2021-05-28 | 2021-09-07 | 江西理工大学 | Wear-resisting solid-liquid separation swirler |
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Application publication date: 20110216 Assignee: Huangshi Sunny Science & Technology Development Co., Ltd. Assignor: Huazhong University of Science and Technology Contract record no.: 2015420000131 Denomination of invention: Gas-solid centrifugal separation and exhaust integrated machine Granted publication date: 20120509 License type: Exclusive License Record date: 20150709 |
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