AU574922B2 - Creation of Inventions and Patents with Artificial Intelligence

AU574922B2 – Pneumatic classifying procedure and means
– Google Patents

AU574922B2 – Pneumatic classifying procedure and means
– Google Patents
Pneumatic classifying procedure and means

Info

Publication number
AU574922B2

AU574922B2
AU58647/86A
AU5864786A
AU574922B2
AU 574922 B2
AU574922 B2
AU 574922B2
AU 58647/86 A
AU58647/86 A
AU 58647/86A
AU 5864786 A
AU5864786 A
AU 5864786A
AU 574922 B2
AU574922 B2
AU 574922B2
Authority
AU
Australia
Prior art keywords
classifying
coarse product
fluid
passage
centrifugal field
Prior art date
1985-05-03
Legal status (The legal status 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 status listed.)

Ceased

Application number
AU58647/86A
Other versions

AU5864786A
(en

Inventor
Pertti Ovaskainen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Outotec Filters Oy

Original Assignee
Larox Oyj
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.)
1985-05-03
Filing date
1986-05-05
Publication date
1988-07-14

1986-05-05
Application filed by Larox Oyj
filed
Critical
Larox Oyj

1986-12-04
Publication of AU5864786A
publication
Critical
patent/AU5864786A/en

1988-07-14
Application granted
granted
Critical

1988-07-14
Publication of AU574922B2
publication
Critical
patent/AU574922B2/en

2006-05-05
Anticipated expiration
legal-status
Critical

Status
Ceased
legal-status
Critical
Current

Links

Espacenet

Global Dossier

Discuss

238000000034
method
Methods

0.000
title
claims
description
24

239000012530
fluid
Substances

0.000
claims
description
37

239000002245
particle
Substances

0.000
claims
description
13

239000011236
particulate material
Substances

0.000
claims
description
11

239000000463
material
Substances

0.000
claims
description
6

230000001105
regulatory effect
Effects

0.000
claims
description
3

238000007664
blowing
Methods

0.000
claims
1

238000000926
separation method
Methods

0.000
description
11

230000005484
gravity
Effects

0.000
description
2

239000004020
conductor
Substances

0.000
description
1

239000000470
constituent
Substances

0.000
description
1

230000001276
controlling effect
Effects

0.000
description
1

238000001035
drying
Methods

0.000
description
1

239000000428
dust
Substances

0.000
description
1

230000000694
effects
Effects

0.000
description
1

230000008030
elimination
Effects

0.000
description
1

238000003379
elimination reaction
Methods

0.000
description
1

238000001914
filtration
Methods

0.000
description
1

230000001771
impaired effect
Effects

0.000
description
1

239000007787
solid
Substances

0.000
description
1

239000007921
spray
Substances

0.000
description
1

Classifications

B—PERFORMING OPERATIONS; TRANSPORTING

B07—SEPARATING SOLIDS FROM SOLIDS; SORTING

B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL

B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents

B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force

B07B7/083—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by rotating vanes, discs, drums, or brushes

B—PERFORMING OPERATIONS; TRANSPORTING

B07—SEPARATING SOLIDS FROM SOLIDS; SORTING

B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents

B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force

B—PERFORMING OPERATIONS; TRANSPORTING

B07—SEPARATING SOLIDS FROM SOLIDS; SORTING

B07B9/00—Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets

B07B9/02—Combinations of similar or different apparatus for separating solids from solids using gas currents

Description

PNEUMATIC CLASSIFYING PROCEDURE AND MEANS
The present invention concerns a pneumatic classifying procedure wherein particulate material is with the aid of centrifugal force divided into a fines product consisting of lighter particles and a coarse product consisting of heavier particles and wherein the fines product is removed from the central part of the centrifugal field and the coarse product from its outer margin.
In pneumatic classifying of particulate material, prior art has employed, towards producing a centrifugal field causing classification, blowers setting the material in rotary motion, and mechanical rotors. The separation limit of such classification, that is the limiting size between fines particles and coarse product particles has usually been controlled by the aid of the rotational speed of the centrifugal field.
The coarse product can be separated, and removed from the centrifugal field, utilizing gravity when the separation limit of classification is large enough, about 50 μm. When the separation limit goes down, what happens is that gravity is no longer sufficient to separate the coarse product from the classifying fluid rotating in the centrifugal field. In such cases the coarse product has been separated by removing, together with the product, the part of the classifying fluid accompanying it, to a separate coarse product cyclone. However, this method is embarrassed by the drawback that at the same time part of the fines contained in the material will be entrained with the coarse product. Therefore the sharpness of separation will be poor in such classification; and it is progressively impaired, the finer the adjustment of the separation limit is made by increasing the proportion of fluid flow going along with the coarse product.
The object of the present invention is to eliminate the drawback mentioned, by devising a classifying procedure by which better sharpness of separation than before is achieved and which is superior to procedures of prior art also as regards controllability of

the process. The classifying process of the invention is characterized in that the coarse product is removed from the centrifugal field with the aid of a separate gas flow tangential to the centrifugal field.
The advantageous effect of the principle taught by the invention, i.e., of employing a separate gas flow which does not participate in the classifying process, is substantially based on the fact that said pure gas flow totally or partly replaces, in the coarse product removal, the classifying fluid rotating in the centrifugal field and containing fines constituents of the material which is being classified. Thereby the entraining of fines with the flow removing coarse product is minimized or entirely inhibited.
The gas employed towards removing the coarse product, from which the coarse product is separated in a cyclone, may advantageously be returned, after said process, to the classifying process to serve as fluid in the classification taking place in the centrifugal field.
The invention also concerns a means for classifying particulate material pneumatically, by the procedure just described. The means comprises, in a manner known in itself in the art, a classifying space in which a centrifugal field can be established; at least one feed passage for conducting material to be classified, and gas serving as fluid medium, into the classifying space; and exit apertures for removal of the fines product, consisting of lighter particles, from the central part of the classifying space and for removal of the coarse product, consisting of heavier particles, on the outer margin of the classifying space, and the means is characterized in that it has been provided with a passage which is tangential to the classifying space adjacent to the coarse product removal aperture so that the coarse product can be removed with the aid of a gas flow conducted through said passage.
In an advantageous embodiment of the invention, the size of the coarse product aperture opening into the passage which is tangential to the classifying space has been arranged to be adjustable.

It is possible with the aid of the removal aperture’s size to regulate the separation limit of classification, and in combination with control of the strength of the centrifugal field this endows the entire process with a wide, and easily controlled, range of regulation.
The invention is described, in the following, more in detail with the aid of examples, reference being made to the attached drawings, wherein: –
Fig. 1 presents a classifying apparatus according to the invention wherein the centrifugal field is produced with the aid of a blower supplying gaseous classifying fluid into the classifying space,
Fig. 2 presents another classifying apparatus according to the invention wherein the centrifugal field is produced with the aid of a blower supplying gaseous classifying fluid into the classifying space,
Fig. 3 shows a vertical section through a classifying apparatus according to the invention wherein the centrifugal field is produced with the aid of a rotor disposed within the classifying space, and
Fig. 4 shows the apparatus of Fig. 3, in top view.
In Fig. 1 is depicted a pneumatic classifying apparatus which divides particulate material composed of varioussized solid particles into a fines product consisting of lighter particles and a coarse product consisting of heavier particles. Classification takes place with the aid of centrifugal force in the centrifugal field established in a substantially cylindrical classifying space 1 with horizontal axis. The centrifugal field is created, and maintained, by tangential supply into the classifying space 1 of the particulate material to be classified and of a gaseous classifying fluid. The particulate material and the fluid are set in rotary motion in the classifying space 1, where the fines become separated to reside in the centre of the classifying space and the coarse

product, on its outer margin.
The supply of particulate material and of gaseous fluid into the classifying space is through feed passages 2,3 joining the classifying space tangentially and of which the passage 3 supplying fluid has been provided with a blower 4. The fines removal aperture 5 is loacted roughly on the horizontal central axis of the classifying space 1 and it leads to a cyclone 6, which separates the fines product from the fluid escaping together with it. From the cyclone 6, the fluid is returned by a connecting passage 7 to the blower 4, to be reused as fluid for the classifying process. The intake aperture 8 of the blower 4 has been provided with a guide vane control, with a speed of rotation control or equivalent for controlling the separation limit in classification. The coarse product removal aperture 9 is located on the outer margin of the classifying space 1, having been formed in the substantially cylindrical shell confining the classifying space. The wall sections 10 of the classifying space on either side of the removal aperture 9 have been arranged to be movable so that it is possible with their aid to regulate the size of the removal aperture. The extreme position of the sections 10, in which the size of the removal aperture 9 is at its minimum, has been indicated with dotted lines in Fig. 1. For removal of the coarse product, a passage 11 has been conducted past the classifying space 1, its direction conforming to the direction of the flow in progress in the marginal part of the classifying space and the coarse product removal aperture 9 opening into this passage. Through the passage 11, gaseous fluid can be introduced, this fluid transporting the coarse product emerging from the classifying space 1 through the removal aperture 9 to a cyclone 12, which separates the coarse product from the fluid flow. From the cyclone 12, the fluid departs to a connecting passage 13, which joins the connecting passage 7 coming from the fines cyclone 6 and thereby returns the fluid through the blower 4 to the classifying prrocess, to serve as fluid in the classifying taking place in the centrifugal field. In order to maintain a balance between the material flows introduced into the classifying process and those removed therefrom, part of the fluid coming from the blower 4 is separated and directed into the passage 14 which conducts it

through dust elimination apparatus (not depicted) and out from the process.
The purpose with the pure fluid flow conducted through the passage 11 and which does not participate in the classifying taking place in the centrifugal field in the classifying space 1 is to make the classification limit sharper by reducing the entrainment of fines with the coarse product. The separation limit of the classification process, and its sharpness, can be regulated by means of the size of the removal aperture 9, the quantity of gaseous fluid conduc ted through the passage 11, the quantity of fluid escaping through the passage 14 and the power input of the blower 4. Regulation of the flow in the passage 11 is effected with the aid of a valve 15 disposed in this passage.
The classifying apparatus depicted in Fig. 2 differs from that of Fig. 1, in the first place, regarding the processing of the fines removed from the classifying space I. The fines product removal apertue 5 has been connected through a filter 16, and further through a passage 17, to a blower 18. The filter 16 retains the fines departing from the classifying space 1, while at the same time the blower 18 draws the fluid accompanying the fines, through the filter, and removing it from the process. The separation of the coarse product with the aid of the fluid introduced by the passage 11 is equivalent to that which has been presented in connection with Fig. 1. The apparatus of Fig. 2 is intended to be used in particular in connection with those grinding and drying processes (e.g. spray grinding) where the material to be classified which the process produces contains part of the classifying fluid, which requires filtering.
In Figs 3 and 4 is depicted a classifying apparatus wherein the cylindrical, vertical classifying space 1 has been provided with a rotating rotor 19 producing a centrifugal field. The rotor 19 comprises a vertical shaft 20 and a plurality of vanes 21 projecting radially therefrom. Supply of the particulate material to be classified and of classifying fluid is through the passage 22 to the axis of the classifying space 1. The coarse product becomes sepa

rated, in the centrifugal field produced by the rotary motion of the rotor 19, to the outer margin of the classifying space 1 and the fines product, to its centre, similarly as in the embodiments of the invention already described, and for removal of the coarse product there has been carried past the lower margin of the classifying space, a straight passage 23, substantially tangential in relation to the classifying space, through which gaseous fluid can be conducted. The fluid flow takes the coarse product along with itself, and the fines product separating in the centre of the classifying space 1 escapes into the axial removal passage 24. The separation limit of the apparatus of Figs 3 and 4 can be regulated by means of the fluid flow conducted through the passage 23 and the speed of rotation of the rotor 19.
It is obvious to a person skilled in the art that different embodiments of the invention are not confined to the examples presented and that they may vary within the scope of the claims following below.

Claims (8)

1. A pneumatic classifying procedure wherein particulate material is divided with the aid αf centrifugal force into a fines product consisting of lighter particles and a coarse product consisting of heavier particles and wherein the fines product is removed from the central part of the centrifugal field and the coarse product from its outer margin, characterized in that the coarse product is removed with the aid of a separate gas flow which is tangential to the centrifugal field.

2. Procedure according to claim 1, characterized in that the coarse product is separated from said gas flow in a cyclone (12), whereafter the gas flow is returned to the classifying process to serve as fluid in the classification taking place in the centrifugal field.

3. Procedure according to claim 1 or 2, characterized in that the particulate material to be classified and the gas serving as fluid are blown into the centrifugal field tangentially so that the blowing maintains the centrifugal field effecting classification.

4. Means for classifying particulate material according to any one of the preceding claims, said means comprising a classifying space (1) in which a centrifugal field can be established; at least one supply passage (2,3,22) for conducting the material to be classified and the gas serving as fluid into the classifying space; and removal apertures (5,9,24) for removing the fines product consisting of lighter particles from the central part of the classifying space and for removal of the coarse product consisting of heavier particles from the outer margin of the classifying space, characterized in that the means is provided with a passage (11,23) which is tangential to the classifying space (1) at the coarse product removal aperture (9) so that the coarse product can be removed by the aid of a gas flow conducted through the passage.

5. Means according tα claim 4, characterized in that the size of the coarse product removal aperture (9) opening into the passage (11) which is tangential to the classifying space (1) has been arranged to be adjustable.

6. Means according to claim 5, characterized in that the walls (10) confining the classifying space (1) have on both sides of the coarse product removal aperture (9) been arranged to be movable so that the size αf the removal aperture can be regulated by moving said walls.

7. Means according to any one of claims 4-6, characterized in that the passage (11) tangential to the classifying space (1) and which removes the coarse product has been connected to a cyclone (12) which separates the coarse product from the gas flow, and that the cyclone has been connected over a connecting passage (13,7) and a blower (4) to the set of supply passages (3) of the classifying space so that the gas can be returned to the classifying process to serve as fluid in the classification taking place in the centrifugal field.

8. Means according to claim 7, characterized in that the supply passage (3) for gas serving as fluid, leading from the blower (4) to the classifying space (1), has been connected to the classifying space tangentially so that the centrifugal field effecting classification can be maintained by the aid of the blower.

AU58647/86A
1985-05-03
1986-05-05
Pneumatic classifying procedure and means

Ceased

AU574922B2
(en)

Applications Claiming Priority (2)

Application Number
Priority Date
Filing Date
Title

FI851762

1985-05-03

FI851762A

FI78241C
(en)

1985-05-03
1985-05-03

Pneumatic grading method and device

Publications (2)

Publication Number
Publication Date

AU5864786A

AU5864786A
(en)

1986-12-04

AU574922B2
true

AU574922B2
(en)

1988-07-14

Family
ID=8520769
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

AU58647/86A
Ceased

AU574922B2
(en)

1985-05-03
1986-05-05
Pneumatic classifying procedure and means

Country Status (10)

Country
Link

US
(1)

US4784756A
(en)

EP
(1)

EP0222802B1
(en)

JP
(1)

JPS62502734A
(en)

AU
(1)

AU574922B2
(en)

DE
(1)

DE3662756D1
(en)

DK
(1)

DK157980C
(en)

FI
(1)

FI78241C
(en)

HU
(1)

HU199318B
(en)

SU
(1)

SU1528333A3
(en)

WO
(1)

WO1986006660A1
(en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

DE3912077C2
(en)

1989-04-13
1993-11-04
Happle Gmbh & Co Maschf

CLEANING MACHINE FOR GRAINY CLEANING GOODS

US6910585B1
(en)

2000-08-31
2005-06-28
Fisher-Klosterman, Inc.
Dynamic centrifugal gas classifier and method of classifying performed therewith

US20070023328A1
(en)

2005-07-29
2007-02-01
Flora Jonathan J
Recycling horizontal cyclonic segregator for processing harvested nuts and fruits

DE102005053617A1
(en)

2005-11-10
2007-06-14
Khd Humboldt Wedag Gmbh

Classifying device for sifting granular material

US8016117B2
(en)

2009-07-31
2011-09-13
Mac Process Inc.
System and method for eliminating emissions from an air classification device

UA111922C2
(en)

2015-05-25
2016-06-24
Олена Іванівна Кострубяк

AERODYNAMIC RECIRCULATION BULLING MATERIALS

Citations (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU520238B2
(en)

1977-07-09
1982-01-21

Kennedy Van Saun Corp.

Pneumatic classifier

Family Cites Families (2)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US1832256A
(en)

1929-05-24
1931-11-17
Albert H Stebbins
Air classifier

FI54681C
(en)

1971-09-27
1979-02-12
Insinoeoeritoimisto Engineerin

PNEUMATIC CLASSIFICATION FOR OVERFLOWER FUEL

1985

1985-05-03
FI
FI851762A
patent/FI78241C/en
not_active
IP Right Cessation

1986

1986-05-05
HU
HU863118A
patent/HU199318B/en
unknown

1986-05-05
US
US07/019,793
patent/US4784756A/en
not_active
Expired – Fee Related

1986-05-05
WO
PCT/FI1986/000044
patent/WO1986006660A1/en
active
IP Right Grant

1986-05-05
AU
AU58647/86A
patent/AU574922B2/en
not_active
Ceased

1986-05-05
EP
EP86902837A
patent/EP0222802B1/en
not_active
Expired

1986-05-05
JP
JP61502740A
patent/JPS62502734A/en
active
Pending

1986-05-05
DE
DE8686902837T
patent/DE3662756D1/en
not_active
Expired

1986-12-18
DK
DK614986A
patent/DK157980C/en
not_active
IP Right Cessation

1987

1987-01-04
SU
SU874028935A
patent/SU1528333A3/en
active

Patent Citations (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU520238B2
(en)

1977-07-09
1982-01-21
Kennedy Van Saun Corp.
Pneumatic classifier

Also Published As

Publication number
Publication date

DK157980C
(en)

1990-08-27

DE3662756D1
(en)

1989-05-18

JPS62502734A
(en)

1987-10-22

WO1986006660A1
(en)

1986-11-20

FI78241C
(en)

1989-07-10

DK157980B
(en)

1990-03-12

AU5864786A
(en)

1986-12-04

FI851762A0
(en)

1985-05-03

DK614986A
(en)

1987-01-20

HUT45929A
(en)

1988-09-28

EP0222802B1
(en)

1989-04-12

DK614986D0
(en)

1986-12-18

SU1528333A3
(en)

1989-12-07

EP0222802A1
(en)

1987-05-27

FI851762L
(en)

1986-11-04

HU199318B
(en)

1990-02-28

US4784756A
(en)

1988-11-15

FI78241B
(en)

1989-03-31

Contact information