WO1998035756A1 - Appareil de traitement d'un materiau et ventilateur associe - Google Patents

Appareil de traitement d'un materiau et ventilateur associe Download PDF

Info

Publication number
WO1998035756A1
WO1998035756A1 PCT/GB1998/000422 GB9800422W WO9835756A1 WO 1998035756 A1 WO1998035756 A1 WO 1998035756A1 GB 9800422 W GB9800422 W GB 9800422W WO 9835756 A1 WO9835756 A1 WO 9835756A1
Authority
WO
WIPO (PCT)
Prior art keywords
fan
air stream
cyclone chamber
impeller
cyclonic air
Prior art date
Application number
PCT/GB1998/000422
Other languages
English (en)
Inventor
Jim D. Barnes
Derald Meador
Don A. Brock
Pat Janus
Christopher F. N. Seebach
Charles L. Ice
Mark Youds
Colin Jarrett
Original Assignee
Next Century Technologies Ltd.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Next Century Technologies Ltd. filed Critical Next Century Technologies Ltd.
Priority to EP98903191A priority Critical patent/EP1039970B1/fr
Priority to DE69826517T priority patent/DE69826517D1/de
Priority to AT98903191T priority patent/ATE276833T1/de
Priority to AU60009/98A priority patent/AU742906B2/en
Publication of WO1998035756A1 publication Critical patent/WO1998035756A1/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00—Other disintegrating devices or methods
    • B02C19/06—Jet mills
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
    • B02C13/02—Disintegrating by mills having rotary beater elements ; Hammer mills with horizontal rotor shaft
    • B02C13/06—Disintegrating by mills having rotary beater elements ; Hammer mills with horizontal rotor shaft with beaters rigidly connected to the rotor
    • B02C13/08—Disintegrating by mills having rotary beater elements ; Hammer mills with horizontal rotor shaft with beaters rigidly connected to the rotor and acting as a fan
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C19/00—Other disintegrating devices or methods
    • B02C19/18—Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00—Details, component parts, or accessories
    • F04D29/26—Rotors specially for elastic fluids
    • F04D29/28—Rotors specially for elastic fluids for centrifugal or helico-centrifugal pumps for radial-flow or helico-centrifugal pumps
    • F04D29/281—Rotors specially for elastic fluids for centrifugal or helico-centrifugal pumps for radial-flow or helico-centrifugal pumps for fans or blowers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/10—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
    • F26B17/107—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers pneumatically inducing within the drying enclosure a curved flow path, e.g. circular, spiral, helical; Cyclone or Vortex dryers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00—Drying solid materials or objects by processes not involving the application of heat
    • F26B5/02—Drying solid materials or objects by processes not involving the application of heat by using ultrasonic vibrations

Definitions

  • the present invention relates to apparatus for processing a material and an impeller suction fan for processing materials.
  • apparatus and an impeller suction fan for granulating, drying or dewatering a material In particular, but not exclusively, it relates to apparatus and an impeller suction fan for granulating, drying or dewatering a material.
  • Apparatus for granulating materials whereby no grinding element is involved are well known.
  • the principle of such apparatus is to granulate the material due to collision and self abrasion between the individual lumps or aggregates of the material within at least one vortex formed in a cyclonic air stream.
  • US Patent No. 5402947 describes such an apparatus in which an air stream at high pressure, together with the material to be granulated, is fed into a cyclone chamber. A single vortex formed within the chamber entraps the material and subjects it to violent turbulence thereby causing it to break up through collision and self-abrasion. However, the movement of the material within the vortex causes severe abrasion and wear of the walls of the cyclone chamber.
  • the fan was subject to severe wear with unacceptable metal losses from the blades of the fan.
  • the apparatus was not suitable for processing harder material such as stone, coal, cement etc.
  • the present invention seeks to overcome the above mentioned disadvantages by providing apparatus capable of processing very hard materials efficiently whilst minimising wear of the fan.
  • the vortices created in the cyclonic air stream carry further harmonic frequencies generated by the specially designed apparatus, this sets up a pulse from the standing wave configuration within the system, and this causes pockets of air within the standing wave to achieve a velocity beyond the sonic range.
  • This can be tuned for a particular type of material which enhances the ability of the vortices created to break up very hard and soft materials such as stone and to dry materials.
  • apparatus for processing a material comprising a cyclone chamber; an impeller suction fan for creating a cyclonic air stream within the cyclone chamber, the fan having an inlet and an outlet for passage of the air stream therethrough; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material in the cyclone chamber, wherein the cyclonic air stream includes non- conflicting effects of vacuum forming centripetal vortices, parts of which travel at supersonic speeds; series of harmonics and subsequent subharmonics inherent in the apparatus and induced, supersonic resonance; standing wave; thermal shock; pressure changes; cavitation; the stresses of which in combination convert the potential energy of material conveyed by the cyclonic air stream to kinetic energy.
  • the cross-sectional area of the cyclone chamber is within the range of 24 to 29% of the cross-sectional area of the inlet of the fan, more preferably, it is approximately 26% of the cross-sectional area of the inlet of the fan.
  • the area of the inlet of the fan is within the range of 28 to 35% of the fan's circumferential outlet area, more preferably, it is approximately 32% of the fan's circumferential outlet area.
  • the discharge area of the outlet of the fan is within the range of 19 to 27% of the fan's circumferential outlet area, more preferably, it is approximately 24% of the fan's circumferential outlet area.
  • the length of the cyclone chamber is variable. This may be achieved by the cyclone chamber comprising a conduit and a sleeve concentric with and in slidable engagement with the conduit such that movement thereof varies the length of the cyclone chamber.
  • the apparatus further comprises a fan casing for supporting the impeller suction fan, the fan having a plurality of radially extending vanes.
  • the clearance between the outermost edge of the vanes and the fan casing may vary around the circumference of the fan such that, in operation, at least two thirds of the vanes are fully pressurised.
  • the forward edge of each vane of the fan may be l/24th of the diameter of the fan greater than the radius of the cyclone chamber.
  • the fan casing may be lined with a layer of high abrasion resistant material and the layer of high abrasion resistant material may further comprise a groove extending circumferentially around the fan casing.
  • Each vane may be coated with a high abrasion resistant plastics material.
  • the apparatus further comprises a separator for separating the granulated material from the cyclonic air stream.
  • the feed assembly comprises a hopper extending partly into the cyclone chamber so that the material is fed into the path of the cyclonic air stream, or alternatively, it comprises a hopper and an auger-driven conveyor, the conveyer extending partly into the cyclone chamber or hopper so that the material is fed into the path of the cyclonic air stream.
  • the distance between the feed assembly and the fan inlet may be adjustable.
  • an externally generated frequency is induced into the cyclonic air stream
  • the material is processed within the cyclonic air stream before the air stream is disturbed by the fan
  • the apparatus may include any one of or any combination of the following processes processing, drying, and dewatering.
  • an impeller suction fan for a processor comprising a central hub and plurality of vanes extending radially from the hub for creating a cyclonic air stream, wherein the cyclonic air stream includes non-conflicting effects of vacuum forming centripetal vortices, parts of which travel at supersonic speeds; series of harmonics and subsequent subharmonics inherent in the processor and induced; supersonic resonance, standing wave, thermal shock; pressure changes, cavitation; the stresses of which in combination convert the potential energy of material conveyed by the cyclonic air stream to kinetic energy.
  • the vanes extend forwardly from the hub of the fan at an angle within the range of 30 to 50° to the axis of rotation of the fan, more preferably, the vanes of the fan extend forwardly at an angle of 45° to the axis of rotation of the fan
  • each of the vanes has a slot extending substantially parallel to the axis of rotation of the fan and having a width within the range 0.5 to 4% of the overall length of the vane
  • the slot may be located at a distance from the hub of the fan at the edge of the impeller inlet
  • the fan further comprises an interrupter located on the hub for disturbing the air within a zone immediately in front of the hub.
  • the diameter of the interrupter may be approximately equal to the diameter of the hub.
  • each vane extends radially at an angle within the range of 3 to 17° to the radius of the fan
  • each vane is concave in profile such that the concavity faces in the direction of rotation of the fan.
  • each vane is coated with a high abrasion resistant plastics material.
  • curvature of the vanes is adjusted for a particular material by computer aided design to take account of fluid dynamics and wear rates.
  • the apparatus for processing a material according to the first aspect of the present invention may incorporate an impeller suction fan according to the second aspect of the present invention.
  • apparatus for processing a material comprising a cyclone chamber; an impeller suction fan for creating a cyclonic air stream within the cyclone chamber, the fan having an inlet and an outlet for passage of the air stream therethrough; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material in the cyclone chamber, wherein the cross-sectional area of the cyclone chamber is within the range of 24 to 29% of the cross-sectional area of the inlet of the fan.
  • the cross-sectional area of the cyclone chamber is approximately 26% of the cross-sectional area of the inlet of the fan.
  • apparatus for processing a material comprising a cyclone chamber; an impeller suction fan for creating a cyclonic air stream within the cyclone chamber, the fan having an inlet and an outlet for passage of the air stream therethrough; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material within the cyclone chamber, wherein the area of the inlet of the fan is within the range of 28 to 35% of the fan's circumferential outlet area.
  • the area of the inlet of the fan is approximately 32% of the fan's circumferential outlet area.
  • apparatus for processing a material comprising a cyclone chamber; an impeller suction fan for creating a cyclonic air stream within the cyclone chamber, the fan having an inlet and an outlet for passage of the air stream therethrough; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material in the cyclone chamber, wherein the discharge area of the outlet of the fan is within the range of 19 to 27% of the fan's circumferential outlet area.
  • the discharge area of the outlet of the fan is approximately 24% of the fan's circumferential outlet area.
  • apparatus for processing a material comprising a cyclone chamber; a fan casing for supporting an impeller suction fan, the fan casing having an inlet and an outlet; an impeller suction fan having a plurality of radially extending vanes for creating a cyclonic air stream within the cyclone chamber via the inlet of the fan casing; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material within the cyclone chamber, wherein the clearance between the outermost edge of the vanes and the fan casing varies around the circumference of the fan such that, in operation, at least two-thirds of the vanes are fully pressurised.
  • apparatus for processing material comprising a cyclone chamber; an impeller suction fan for creating a cyclonic air stream within the cyclone chamber; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material within the cyclone chamber, wherein the length of the cyclone chamber is variable In this way the length of the cyclone chamber can be adjusted to tune the apparatus to achieve the standing wave at the particular harmonic frequencies generated by a specially designed fan
  • apparatus for processing a material comprising a cyclone chamber; a fan casing for supporting an impeller suction fan, the casing having an inlet and an outlet; an impeller suction fan having a plurality of radially extending vanes for creating a cyclonic air stream within the cyclone chamber via the inlet of the fan casing; and a feed assembly for feeding material into the path of the cyclonic air stream for processing the material within the cyclone chamber, wherein the forward edge of each vane of the fan is 1/24 of the diameter of the fan greater than the radius of the cyclone chamber.
  • an impeller suction fan comprising a central hub and plurality of vanes extending radially from the hub for creating a cyclonic air stream, the vanes extending forwardly from the hub of the fan at an angle within the range of 30 to 50° to the axis of rotation of the fan Preferably, the vanes extend at an angle of 45° to the axis of rotation.
  • an impeller suction fan comprising a central hub and a plurality of vanes extending radially from the hub for creating a cyclone air stream, each of the vanes having a slot extending substantially parallel to the axis of rotation of the fan and having a width within the range 0.5 to 4% of the overall length of the vane.
  • an impeller suction fan comprising a central hub; a plurality of vanes extending radially from the hub for creating a cyclonic air stream, and an interrupter located on the hub for disturbing the air within a zone immediately in front of the hub.
  • the vortices created inside the chamber are such that the power is optimised. This is due to the harmonic frequencies which create high energy pockets which can cause the break up of very hard material Consequently rocks are powdered and material dried at a distance from the impeller within the cyclone chamber.
  • the apparatus and fan produce an harmonic/frequency which sets up pulses from the standing configuration within the system, and this is critical because, on occasion pockets of air through the standing wave achieve a velocity beyond the sonic range.
  • These conditions when optimised by the various aspects of the present invention, i.e high local vorticity and high energy dissipation, will in some cases produce Abrikosov vortices When hard rock is processed by the machine, which has only one moving part, the ions orbiting the Abrikosov vortices will collide and may produce fusion
  • the apparatus of the present invention is capable of grinding a material down by 1500: 1 which is comparable with prior art devices which only achieve a reduction of 4: 1.
  • the processing of the material may be further optimised by introducing an externally generated frequency into the cyclonic air stream.
  • Figure 1 is a side elevation of part of the apparatus according to the present invention showing the fan in part section;
  • Figure 2 is a part sectional side elevation of an alternative feed assembly of the apparatus according to the present invention.
  • Figure 3 is a transverse cross-section of the apparatus of Figure 1 taken along the line 3-3.
  • Figure 4 is a plan view of a vane of the fan of the present invention.
  • Figure 5 is a cross-section of the vane of Figure 4 taken along the line 5-5;
  • Figure 6 is a cross-section of the vane of Figure 4 taken along the line 6-6;
  • Figure 7 is a cross-section of the vane of Figure 4 taken along the line 7-7;
  • Figure 8 is a detailed plan view of a vane of the fan according the present invention.
  • Figure 9 is the profile of the vane of Figure 8.
  • Figure 10a is a side elevation of the interrupter according to the present invention.
  • Figure 10b is a plan view of the interrupter of Figure 10a.
  • Figure 1 1 is a perspective view showing an embodiment of the apparatus according to the present invention.
  • the apparatus comprises a conical impeller suction fan 71 and a cyclone chamber 70.
  • the cyclone chamber 70 is generally cylindrical and is arranged such that its longitudinal axis lies along the axis of rotation of the impeller suction fan 71.
  • the impeller suction fan 71 has an impeller 10 which typically has a diameter within the range 300 mm to 1220 mm Smaller impellers can also be utilised in the apparatus of the present invention for certain laboratory, domestic, cosmetic or pharmaceutical applications
  • the width of the impeller would be 196 mm
  • the impeller 10 is rotatably supported within a fan casing 19 To accommodate the impeller of diameter of 610 mm, the internal width of the fan casing would be approximately 203 mm.
  • the casing 19 has an opening 63 in one of the side walls 61 thereof
  • the impeller 10 has an inlet 14 which is an annular ring and partly extends out of the casing 19 via the opening 63.
  • the casing 19 is generally spiral in shape having an outlet 72
  • the inner surface of the casing 19 may be lined with a wear plate (not shown) formed of a high abrasion resistant plastics material.
  • the wear plate extends around approximately two-thirds of the circumferential area of the inner surface of the casing 19 from the point of minimum clearance 8-8.
  • the wear plate helps to minimise wear of the casing wall
  • a groove may he formed in the wear plate which extends circumferentially around the casing to define a space which conforms to the air flows experienced within the casing 19
  • the clearances between the outer edge of the impeller of the present invention are reduced by approximately 30% so that at least two-thirds of radial vanes provided on the impeller 10 of the present invention are fully pressurised. Of the remaining vanes, at least 90° of travel, the first of the vanes has begun to depressurise and the remaining vanes are fully depressurised with the final vane just entering the zone of minimum clearance.
  • the discharge area is designed to be within the range of 19 to 27%, preferably 24%, of the fan's circumferential outlet area, and the area of the inlet of the fan is within the range 28 to 35%, preferably 32%, of the fan's circumferential outlet area.
  • the discharge area is 457.2 mm multiplied by the width of the fan's discharge conduit 72.
  • the impeller 10 is keyed to one end of a shaft 16 which is supported by a bearing 17 mounted on the rear of the casing 19.
  • a drive pulley 18 is fastened to the other end of the shaft 16.
  • the pulley 18 is driven by a variable speed motor or internal combustion engine by means of at least one belt as shown in Figure 11.
  • the impeller is driven at typical speeds of 4,500 to 7,000 rpm.
  • the cyclone chamber 70 comprises a cylindrical conduit 20 which, for the particular impeller mentioned above, has an inner diameter of 203.2 mm and a length of approximately 1.83m, such that the cross-sectional area of the conduit 20 is within the range of 24 to 29%, preferably 26% of the cross-sectional area of the inlet 14 of the impeller 10.
  • One end of the conduit 20 is open to the atmosphere and is fitted with a cylindrical sleeve 24 in slidable engagement therewith.
  • a slot 26 and locking clamp 25 enables the position of the sleeve 24 to be adjusted and locked into position, thereby varying the length of the conduit 20 to finely tune the harmonic frequencies of the air stream within the conduit during operation.
  • the other end of the conduit 20 terminates in a frusto-conical section 21 which has an opening 62.
  • the optimum length of the conduit 20 is between 786 mm (i.e. the circumference of the inlet area of the impeller) and 931 mm.
  • the optimum length is 1298 mm (i.e. again the circumference of inlet area) up to 1851 mm.
  • the inlet tube length range would apply to an impeller speed range of between 5760 rpm to 6827 rpm.
  • the length of the conduit should not be less than 718 mm or more than 1150 mm, and for the impeller of diameter 610 mm, not less than 1 126 or more than 1851 mm.
  • the cyclone chamber 70 is secured, for example by welding, to one side of a common supporting bracket 22, the side wall 61 of the casing 19 being removably fitted to the other side so that the opening 63 of the casing 19 and the mouth 62 of the expander section 21 are coincident.
  • the inlet 14 of the impeller 10 extends partly into the expander section 21 of the cyclone chamber 70.
  • a hopper 23 for receiving the material to be granulated is mounted on the conduit 20 adjacent the open end thereof and partly extending into the conduit.
  • the hopper may be slidably mounted (not shown) on the conduit 20 so that its distance from the impeller may be adjusted. Such an arrangement allows the material to be introduced into the conduit 20 at a position which ensures the most efficient granulation.
  • FIG. 2 shows an alternative feed assembly 44 which comprises a hopper 40, an auger-driven conveyor formed by a conduit 43 in which a screw 41 is driven to rotate by a geared motor 42.
  • the conduit 43 of the feed assembly 44 extends partly into the conduit 20 of the cyclone chamber 70 so that the material fed into the hopper 40 is conveyed by rotation of the screw 42 into the path of the cyclonic air stream during operation.
  • Suitable supporting brackets (not shown) are provided for the feed assembly 44.
  • the auger-driven conveyor is mounted on the lower end 23a of the gravity hopper 23, discharge thereinto and from thence into the conduit 20 of the cyclone chamber 70.
  • An advantage of such an arrangement is that both feed assemblies may utilise the means for adjusting the distance of the feed assembly from the impeller.
  • the feed assembly may comprise an enlarged air inlet to increase the sir flow within the conduit.
  • feed assembly may also be utilised in the apparatus of the present apparatus, for example a pneumatic conveyor.
  • the impeller 10 comprises a plurality of radially extending vanes 11.
  • the number of vanes 1 1 number between 4 to 12 depending on the type of material to be granulated
  • the vanes 1 1 may be formed of and further may be coated with a layer of high abrasion resistant material to protect the vanes 11 against metal contamination as well as to provide a cushion to protect brittle particles such as diamonds which are released from ore such as kimberlite to allow large diamonds which would otherwise be crushed to emerge intact
  • Each of the vanes 1 1 are offset from the radius of the impeller by an angle within the range of 3 to 17°
  • the vanes 11 are equispaced about a hub 15.
  • the innermost edge 28 of each vane 1 1 is fitted into a corresponding axially aligned slot 29 in the hub 15.
  • the hub 15 is provided with a central bore 37 and keyway 30 for receiving and being secured to the shaft 16.
  • the spine 27 of each vane 11 is flat along both its chord and span, defining an isosceles triangle depicted by lines 80 and 81 and the innermost edge 28. The apex of the triangle coincides with the centre of the outermost edge of the vane 1 1.
  • the profile of the vane 11 on either side of the spine 27 is generally arcuate in cross-section
  • the vane further comprises vane extensions 31 which may be flat and are angled at approximately 20° relative to the surface of the spine 27, but is preferably curved with rounded leading edges as shown by the broken line 31a This curve induces laminar air flows over the surfaces thereby reducing drag and improving the efficiency of the fan.
  • Each vane 11 is generally concave, the concavity of each vane 11 facing the direction of rotation of the impeller 10
  • the curvature at the outermost edge of the vane is 1 to 3 mm
  • the vane extension 31 extends into the inlet 14 of the impeller 10 at which point a slot 100 is formed in the vane 1 1, see Figure 9
  • the slot extends in a direction substantially parallel to the axis of rotation of the impeller 10
  • the width of the slot is preferably 0 5 to 4% of the overall length 1 of the vane 11.
  • the width of the slot is 2 mm
  • the vane extension 31 extends forwardly from the hub 15 of the impeller 10 by an angle to the axis of rotation of the impeller 10
  • the angle ⁇ is within the range of 38 to 50°, for the particular vane of length 1 4 5 mm, the angle is 45°
  • the extension 31 extends in a forward direction at angle ⁇ to a point A to form a straight front edge 101
  • the point A is designed such that it extends at distance beyond the wall of the conduit 20 of the cyclone 70 by a distance of 1/24 1 of the overall diameter of the impeller 10
  • the front edge 73 which extends beyond the extension 31 is secured to an annulus 13, the inner peripheral margin of which provides an annular ring 14 which forms the inlet of the impeller 10
  • the internal diameter of the inlet 14 is approximately 406 mm
  • the rear edge 74 of each vane is secured to a plate 75 which comprises an outer annular ring 34 and a frusto-conical central portion 35 which, at its inner end, is secured to the hub 15 to provide a rigid structure
  • An interrupter 90 may be fitted into the central bore 37 at the front side of the hub 15 facing the inlet 14 of the impeller 10
  • the interrupter is shown in Figures 10a and 10b It comprises a disc 91 mounted on a central spine 92.
  • the spine 92 is screw- threaded so that the interrupter 90 can be screw-fitted into the central bore 37 of the hub 15
  • the interrupter 90 further comprises a diametrical ridge 93 which is raised at one end
  • a hole 94 is bored through the raised portion of the ridge 93 at an angle of 45°
  • the interrupter 90 disturbs the stationary air directly in front of the hub 15.
  • the interrupter has a diameter approximately equal to the diameter of the hub 15.
  • the orientation and design of the impeller vanes can be further optimised by computer-aided design and can be further adjusted dynamically to compensate for any wear of the vanes
  • the degree of curvature of the vanes can be adjusted by computational fluid dynamics analysing wear patterns created by a given product and redesigning the vane to give optimum freedom from abrasion.
  • the granulation and drying of a material may be further improved by introducing an externally generated frequency to the cyclonic air stream by means of a speaker or electrical feed, for example.
  • Typical frequencies may be 25 to 28 Hz, 57.6 Hz, 576 Hz for a fan running at 5760 rpm.
  • Disassociation of water can be enhanced by introduction of a frequency of approximately 42.7 Hz.
  • FIG. 1 1 A practical example of the apparatus according to the present invention is shown in Figure 1 1 It comprises a supportive framework 50 upon which is mounted the support bracket 22 to which the suction fan 71 and the cyclone chamber 70 are secured.
  • a variable speed motor 57 with a drive pulley 58 is also mounted on the framework 50 and a belt 59 connects the drive pulley 58 to the pulley 18 of the fan 71.
  • the means for varying the speed of the motor 57 are not shown.
  • a belt guard 60 provides protection from the moving parts
  • a conduit 51 connects the discharge conduit of the fan casing 19 to a cyclone separator 52 and receiving hopper 55 which are also mounted on the supportive framework 50
  • the lower end 54 of the separator 52 discharges the granulated material into the receiving hopper 55 from which it can be taken as required via a chute 56 by opening a shutter 77
  • the separated, clean air is then discharged from an exhaust conduit 53 into the atmosphere either directly or via filters for removal of any fine dust.
  • the motor 57 is run-up to speed and the length of the conduit 20 of the cyclone chamber 70 is adjusted by loosening the clamp 25 and moving the sleeve 24 axially until the optimum conditions are achieved for granulating a particular material by tuning the apparatus to the natural resonance frequency of the material.
  • the sleeve 24 is then locked in situ by the clamp 25.
  • the types of materials which may granulated by the apparatus of the present invention ranges from coal, lignite, petroleum coke, mezotrace, oil shale, glass, drywall, ash, manure, sewage sludge, salt crystal, mineral and ore bearing sand, black sand, grains such as soybeans, corn, oats, barley, milo and rice.
  • the apparatus of the present invention can be utilised to dry wet clay, paper pulp, fish and bones into a fine powder. It is also useful for drying pigmentation cake which contains upto 50% water. The drying process is accomplished at a reduced length of time which using conventional methods has typically required at least 16 hours. It is assumed that the 4°C temperature and the free N 2 generated in the air flow suppresses combustion which normally occurs when pigmentation feedstock is powdered. Sewage cake utilised for fuel in combustion type gassifiers can be dried and deodorised by the apparatus of the present invention.
  • Sewage slurry can be dewatered without pre-treatment, ideal for either fuel feedstock for plasma gassification and conversion into surplus town gas or chemical treatment processes for metal recovery and binding heavy metals against acid rain leachate as well as destroying all known pathogens in the process making it suitable for land reclamation. It can be utilised to process fish to fishmeal on ship providing a 20% saving.
  • the apparatus can also be utilised to dry ceramics and mineral compounds. Comminution of these can be avoided by slowing down the speed of the fan and feeding the material close to or in the expansion section in front of the fan inlet. Mining slurries can be dried either in powder form or dewatered sufficiently for chemical treatment for extraction of metals.
  • the material to be granulated is fed into the hopper 23 and is introduced into the path of the cyclonic air stream created by the suction fan 71 within the conduit 20 of the cyclone chamber 70.
  • the material is completely fragmented within the conduit 20 before entering the fan due to the tuned harmonics carried by the vortices within the cyclonic air stream and is drawn by the cyclonic air stream into the inlet 14 of the impeller 10.
  • the size of the exhaust ducting can be varied to adjust the air flow through the system.
  • a safety cut-off mechanism may be installed. During normal operation, there is virtually no load, particularly if a DC constant torque motor is utilised to drive the fan. Therefore sensors can be provided to detect any increase in load, for example due to a large particle hitting the fan, to activate a cut-off switch and brake.
  • the sensors may alternatively, detect particularly large particles in transit such as diamonds and perform the same function. Sensors may also be utilised to detect large particles in the exhaust ducting and increase the speed of the fan to ensure that the material is finely granulated. Alternatively, the feed rates or the cyclone separator can be adjusted upon detection of large particles.
  • the forces within the vortices of the cyclonic air stream may release hydrogen and oxygen gases from certain materials, for example sewage sludge, to at least partly dry the material.
  • it may be preferable to dry materials by heating the material for example by subjecting the material to microwaves, either as is fed into the conduit 20 of the cyclone chamber 70, within the conduit 20 itself or feed into the fan casing.
  • microwaves also promotes separation between metals and their ores.
  • disassociation of the water due to the result of shearing of the water at 4°C (its densest point) results in the formation of singlet oxygen such as 0 3 and 0 4 (ozone) which destroys odours in bacteria contaminated products such as sewage cake.
  • H 2 formed by the disassociation of water may recombine with some of the oxygen to form water which may be exhausted out via the fan or it may form around the inner surface of the conduit 20 and stream out of the open end of the conduit counter to the air stream within the conduit.
  • an impeller of 380 mm diameter having eight vanes running at a speed of 5760 rpm will dry 2.16 tons per hour of sewage (comprising 70% water, 30% solids), which has been diced into 4.5 cm cubes. Further such an arrangement can granulate rock of 15 cm at a rate of 5 tons per hour.
  • a 610 mm diameter impeller having eight vanes will dry 3.6 tons of sewage per hour (comprising 70% water, 30% solids), diced into 7.5 cm cubes or granulate rock of 25 cm at a rate of 8 tons per hour.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Toxicology (AREA)
  • Molecular Biology (AREA)
  • Cyclones (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Fertilizers (AREA)
  • Telephone Function (AREA)
  • Measurement And Recording Of Electrical Phenomena And Electrical Characteristics Of The Living Body (AREA)
  • Measuring Pulse, Heart Rate, Blood Pressure Or Blood Flow (AREA)
  • Threshing Machine Elements (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

Cet appareil permettant de traiter un matériau comprend une chambre (70) à cyclone, un ventilateur aspirant (71) à ailettes qui crée un écoulement d'air cyclonique à l'intérieur de la chambre (70) à cyclone, et comporte une entrée (14) et une sortie destinées à laisser passer l'écoulement d'air, et un ensemble alimentation (23) qui sert à introduire le matériau dans le parcours de l'écoulement d'air cyclonique, aux fins de traitement du matériau dans la chambre (70) à cyclone, ledit écoulement d'air cylconique intégrant les effets non antagonistes de tourbillons centripètes formant du vide, dont des parties circulent à des vitesses supersoniques; des séries d'harmoniques et de sous-harmoniques résultantes et inhérentes à l'appareil; la résonance supersonique; l'onde stationnaire; le choc thermique; des variations de pression; la cavitation; les contraintes combinées de ces effets transforment en énergie cinétique l'énergie potentielle du matériau véhiculée par l'écoulement d'air cyclonique.
PCT/GB1998/000422 1997-02-12 1998-02-11 Appareil de traitement d'un materiau et ventilateur associe WO1998035756A1 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
EP98903191A EP1039970B1 (fr) 1997-02-12 1998-02-11 Appareil de traitement d'un materiau
DE69826517T DE69826517D1 (de) 1997-02-12 1998-02-11 Materialbearbeitungsvorrichtung
AT98903191T ATE276833T1 (de) 1997-02-12 1998-02-11 Materialbearbeitungsvorrichtung
AU60009/98A AU742906B2 (en) 1997-02-12 1998-02-11 Apparatus for processing a material and fan therefor

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9702796.5 1997-02-12
GBGB9702796.5A GB9702796D0 (en) 1997-02-12 1997-02-12 Media communication apparatus

Publications (1)

Publication Number Publication Date
WO1998035756A1 true WO1998035756A1 (fr) 1998-08-20

Family

ID=10807445

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1998/000422 WO1998035756A1 (fr) 1997-02-12 1998-02-11 Appareil de traitement d'un materiau et ventilateur associe

Country Status (7)

Country Link
EP (1) EP1039970B1 (fr)
AT (1) ATE276833T1 (fr)
AU (1) AU742906B2 (fr)
DE (1) DE69826517D1 (fr)
GB (1) GB9702796D0 (fr)
WO (1) WO1998035756A1 (fr)
ZA (1) ZA981137B (fr)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024518A1 (fr) * 1998-10-28 2000-05-04 Douglas Forbes Dispositif et procede permettant de produire un materiau granulaire
WO2001019521A2 (fr) * 1999-09-13 2001-03-22 Mcgrath, Lee Systeme pneumatique de broyage et d'assechement
GB2357499A (en) * 1999-08-11 2001-06-27 Mark Youds Methods and apparatus for sewage processing and treatment
GB2358629A (en) * 2000-05-18 2001-08-01 Mark William Youds Cyclone apparatus for treating sewage, dissociating water, comminuting matter
GB2354232B (en) * 1999-08-03 2001-11-07 Mark William Youds Sewage processing treatment invention
EP1420886A2 (fr) * 2001-08-31 2004-05-26 Pulsewave, Inc. Procede de micronisation de matieres
GB2412655A (en) * 2004-03-29 2005-10-05 Otwoempower Corp Method and apparatus for dewatering sewage sludge
US7040557B2 (en) 2001-02-26 2006-05-09 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7059550B2 (en) 2001-02-26 2006-06-13 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7429008B2 (en) 2001-02-26 2008-09-30 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
WO2011049532A1 (fr) * 2009-10-20 2011-04-28 Musse Singapore Pte Ltd Appareil et procédé pour une réduction de dimension
US8057739B2 (en) 2003-11-12 2011-11-15 Pulverdryer Usa, Inc. Liquid purification system
US8448884B2 (en) 2010-05-10 2013-05-28 Taprogge Gesellschaft Mit Beschraenkter Haftung Eggshell membrane separation process
US8485459B2 (en) 2001-07-13 2013-07-16 Rodolfo Antonio M Gomez Intense vortex dryer, comminutor and reactor
CN107572258A (zh) * 2017-09-05 2018-01-12 余绍火 一种适用于粘性物料的输送装置
IT201900004321A1 (it) * 2019-03-25 2020-09-25 Gianmaria Barbotto Sistema cinetico, elettronico, cimatico, pneumatico, atto alla separazione di differenti sostanze contenute nelle polveri provenienti da impianti di frantumazione
WO2021226640A1 (fr) * 2020-05-07 2021-11-11 Vortex Industrial Solutions Ltd Appareil et procédé de traitement aéro-acoustique de matériaux

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109655271B (zh) * 2018-12-27 2019-12-20 南京航空航天大学 一种单对超声速流向旋涡发生装置
RU2758021C1 (ru) * 2020-11-25 2021-10-25 федеральное государственное бюджетное образовательное учреждение высшего образования "Ульяновский государственный технический университет" Устройство для автоматизированного осушения сыпучих веществ

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3255793A (en) * 1963-03-01 1966-06-14 Francis H Clute & Son Inc Vacuum comminutor
US4390131A (en) * 1981-02-09 1983-06-28 Pickrel Jack D Method of and apparatus for comminuting material
US4391411A (en) * 1980-12-18 1983-07-05 Process Development Corporation Method and apparatus for pulverizing materials by vacuum comminution
WO1986004527A1 (fr) * 1985-01-31 1986-08-14 Cp Coal Mills, Inc. Dispositif et procede de broyage pneumatique
US4892261A (en) * 1986-03-20 1990-01-09 The T.D.J. Co., Inc. Material communitor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3255793A (en) * 1963-03-01 1966-06-14 Francis H Clute & Son Inc Vacuum comminutor
US4391411A (en) * 1980-12-18 1983-07-05 Process Development Corporation Method and apparatus for pulverizing materials by vacuum comminution
US4390131A (en) * 1981-02-09 1983-06-28 Pickrel Jack D Method of and apparatus for comminuting material
WO1986004527A1 (fr) * 1985-01-31 1986-08-14 Cp Coal Mills, Inc. Dispositif et procede de broyage pneumatique
US4892261A (en) * 1986-03-20 1990-01-09 The T.D.J. Co., Inc. Material communitor

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024518A1 (fr) * 1998-10-28 2000-05-04 Douglas Forbes Dispositif et procede permettant de produire un materiau granulaire
GB2354232B (en) * 1999-08-03 2001-11-07 Mark William Youds Sewage processing treatment invention
GB2357499A (en) * 1999-08-11 2001-06-27 Mark Youds Methods and apparatus for sewage processing and treatment
GB2357499B (en) * 1999-08-11 2001-10-24 Mark Youds Methods and apparatus for sewage processing and treatment
WO2001012332A3 (fr) * 1999-08-11 2002-01-17 Helix Comminutions Ltd Procedes et dispositif pour le traitement et la transformation des eaux usees
WO2001019521A2 (fr) * 1999-09-13 2001-03-22 Mcgrath, Lee Systeme pneumatique de broyage et d'assechement
WO2001019521A3 (fr) * 1999-09-13 2002-01-31 Mcgrath Lee Systeme pneumatique de broyage et d'assechement
US6530534B1 (en) 1999-09-13 2003-03-11 Lee McGrath Pneumatic comminution and drying system
GB2358629A (en) * 2000-05-18 2001-08-01 Mark William Youds Cyclone apparatus for treating sewage, dissociating water, comminuting matter
GB2358629B (en) * 2000-05-18 2001-12-19 Mark William Youds Formulae, methods and apparatus for the: treatment of; processing of; pasteurisation; dissociating water in; and the communication of: materials;
US7429008B2 (en) 2001-02-26 2008-09-30 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7040557B2 (en) 2001-02-26 2006-05-09 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7059550B2 (en) 2001-02-26 2006-06-13 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7137580B2 (en) 2001-02-26 2006-11-21 Power Technologies Investment Ltd. System and method for pulverising and extracting moisture
US7374113B2 (en) 2001-02-26 2008-05-20 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7500830B2 (en) 2001-02-26 2009-03-10 Power Technologies Investment Ltd. System and method for pulverizing and extracting moisture
US7909577B2 (en) 2001-02-26 2011-03-22 Pulverdryer Usa, Inc. System and method for pulverizing and extracting moisture
US8485459B2 (en) 2001-07-13 2013-07-16 Rodolfo Antonio M Gomez Intense vortex dryer, comminutor and reactor
EP1420886A2 (fr) * 2001-08-31 2004-05-26 Pulsewave, Inc. Procede de micronisation de matieres
EP1420886A4 (fr) * 2001-08-31 2009-01-21 Pulsewave Llc Procede de micronisation de matieres
US8057739B2 (en) 2003-11-12 2011-11-15 Pulverdryer Usa, Inc. Liquid purification system
GB2412655A (en) * 2004-03-29 2005-10-05 Otwoempower Corp Method and apparatus for dewatering sewage sludge
CN102844120A (zh) * 2009-10-20 2012-12-26 缪斯股份有限公司 用于减小尺寸的装置和方法
JP2013508141A (ja) * 2009-10-20 2013-03-07 ミュゼ・インコーポレイテッド サイズリダクションのための装置及び方法
WO2011049532A1 (fr) * 2009-10-20 2011-04-28 Musse Singapore Pte Ltd Appareil et procédé pour une réduction de dimension
US8602331B2 (en) 2009-10-20 2013-12-10 Musse Singapore Pte Ltd Apparatus and method for size reduction
US8448884B2 (en) 2010-05-10 2013-05-28 Taprogge Gesellschaft Mit Beschraenkter Haftung Eggshell membrane separation process
CN107572258A (zh) * 2017-09-05 2018-01-12 余绍火 一种适用于粘性物料的输送装置
CN107572258B (zh) * 2017-09-05 2024-01-09 余绍火 一种适用于粘性物料的输送装置
IT201900004321A1 (it) * 2019-03-25 2020-09-25 Gianmaria Barbotto Sistema cinetico, elettronico, cimatico, pneumatico, atto alla separazione di differenti sostanze contenute nelle polveri provenienti da impianti di frantumazione
WO2021226640A1 (fr) * 2020-05-07 2021-11-11 Vortex Industrial Solutions Ltd Appareil et procédé de traitement aéro-acoustique de matériaux
CN115605293A (zh) * 2020-05-07 2023-01-13 漩涡工业解决方案有限责任公司（Gb） 气动声学式材料处理设备和处理方法
EP4146400A4 (fr) * 2020-05-07 2024-10-23 Vortex Ind Solutions Ltd Appareil et procédé de traitement aéro-acoustique de matériaux

Also Published As

Publication number Publication date
AU6000998A (en) 1998-09-08
ZA981137B (en) 1998-08-11
EP1039970B1 (fr) 2004-09-22
AU742906B2 (en) 2002-01-17
DE69826517D1 (de) 2004-10-28
EP1039970A1 (fr) 2000-10-04
GB9702796D0 (en) 1997-04-02
ATE276833T1 (de) 2004-10-15

Similar Documents

Publication Publication Date Title
EP1039970B1 (fr) Appareil de traitement d'un materiau
US8485459B2 (en) Intense vortex dryer, comminutor and reactor
US4390131A (en) Method of and apparatus for comminuting material
JP4989059B2 (ja) 粉砕装置
JP2002524232A (ja) 粉砕機および粉砕方法
WO2001012332A2 (fr) Procedes et dispositif pour le traitement et la transformation des eaux usees
KR100720286B1 (ko) 곡류 등의 분쇄분류방법 및 곡류 등의 분쇄분류기
US5769332A (en) Efficient production of landplaster by collecting and classsifying gypsum fines
TW445175B (en) Apparatus for granulating a material
MXPA97002608A (en) Efficient production of gypsum calcinated by collection and classification of fine and
JPS62168556A (ja) 遠心空気分離機
JP2010201289A (ja) 微粉砕装置
JP2823099B2 (ja) 微粉砕設備
RU2106199C1 (ru) Роторно-вихревой аппарат
AU2002317626B2 (en) Intense vortex dryer, comminutor and reactor
AU2021266807A1 (en) Aero-acoustic materials processing apparatus and method
GB2354232A (en) Cyclone apparatus for treating sewage
JP2019150764A (ja) 分級機能付き粉砕装置及び被処理物の粉砕方法
AU2002317626A1 (en) Intense vortex dryer, comminutor and reactor
JP7514952B2 (ja) 排気ガイド及び排気方法
SU1079289A2 (ru) Сепарационное устройство струйной мельницы
JPH02207852A (ja) 微粉砕機
KR20070018810A (ko) 분쇄와 수분 추출 시스템 및 방법
CA1236809A (fr) Broyeur de noir de carbone
SU1643080A1 (ru) Центробежна многоступенчата мельница

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AL AM AT AU AZ BA BB BG BR BY CA CH CN CU CZ DE DK EE ES FI GB GE GH GM GW HU ID IL IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT UA UG US UZ VN YU ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW SD SZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN ML MR NE SN TD TG

DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 1998903191

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 60009/98

Country of ref document: AU

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

NENP Non-entry into the national phase

Ref country code: JP

Ref document number: 1998535463

Format of ref document f/p: F

WWP Wipo information: published in national office

Ref document number: 1998903191

Country of ref document: EP

WWG Wipo information: grant in national office

Ref document number: 60009/98

Country of ref document: AU

WWG Wipo information: grant in national office

Ref document number: 1998903191

Country of ref document: EP