专利摘要:
A separator for sorting particulate material has a rotor (1) with vanes (3); static, separately adjustable guide vanes (8,9); a casing (14) defining an inlet duct for material suspended in a conveying gas; an outlet (7) for a suspended fine fraction; and a hopper (12) for collecting a coarse fraction.
公开号:SU1436859A3
申请号:SU864027580
申请日:1986-06-02
公开日:1988-11-07
发明作者:Фольсберг Ян
申请人:Ф.Л. Смидт Энд Ко А/С (Фирма);
IPC主号:
专利说明:

.
18
18
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ABOUT)
P
four
WITH
but
00
ate

 CM
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14
16, Caldai set 8.9 L 10.11 has a drive of the most effective movement in the form of gear wheels 18, 19, mounted on one end of the shafts 15, 17 and driven in rotation through the gear crown 20, 21 , 11 a funnel 12 is installed with P 13 for unloading the core fraction. The senarator is equipped with a P for supplying the carrier gas and the source material. Suspended material in the gas flow enters the working zone L 10, 11, is reflected from them and moves

in the direction of rotation P 1. In the case of s. On the inside of L 10, 11, the first separation of the suspension is carried out. Large particles move outwards again towards L 10, 11, are reflected from them, enter funnel 12 and are discharged through P 13. Leaving the suspension enters working zone L 3, where large particles move from P 1 towards L 10, 11 and enter the funnel 12. The small fraction is discharged through P 7, 1 Il.
one
This invention relates to the field of mineral processing.
The aim of the invention is to improve the accuracy of separation,
The drawing shows a separator, axial section.
The separator has a rotor 1 mounted rotatably around a vertical axis YU. The rotor 1 is driven by a PO1-SUS engine (not shown) through shaft 2, the rotor 1 is equipped
blades 3 mounted on ring nga: neck 4 and top 5 plates. Top plate 5. Equipped with a central hole 6, communicating with the nozzle
com 7 for discharging the separated fine fraction suspended in the gas. Along the perimeter of the rotor 1, there are two sets of 8.9 guide vanes 10 and 11, installed with the possibility of independent movement,
Under the rotor 1 and the blades 10 and 11 directed by them, there is placed a funnel 12 equipped with a nozzle 13 for discharging the coarse fraction. The separator is enclosed in housing 14, which may be the upper part of the housing of a vertical roller mill.
The guide blades 10 are provided with shafts 15 mounted with the possibility of rotation on the upper part of the housing 14 and in the fixed ring 16 placed between the total sets 8.9, and the guide blades 11 are equipped with the shafts 17 mounted with the possibility of rotation on the upper parts of the funnel 12 and in the ring 16.
0
five
0
five
ABOUT
Each set 8.9 of the guide vanes 10 and 11 is provided with an independent movement drive, made in the form of gear wheels 18 and 19 mounted on one end of the shafts 15 and 17 and driven in rotation through the gear ring 20, 21.
The separator works as follows.
Pa; the material suspended in the separator suspended in the gas stream is fed up into the housing 14 to the zone of the rotor 1 (indicated by arrows). Then the material enters the working area of the guide blades 10 and 11 of both sets 8, 9, and as a result of the inclination of the guide blades 10 and 11, the suspension is reflected and moved in the direction of rotation of the rotor 1. Thus, both the guide blades 10 and 11 and the rotor 1 provides rotation of the slurry and, due to the centrifugal force generated by the rotation, the first separation already takes place on the inside of the guide blades 10 and It. Just inside the guide blades 10 and 11, large particles of the suspension move outwards again towards the guide blades 10 and 11, where the particles are reflected, as a result they fall into the funnel 12. The rest of the suspension containing fine particles of the starting material enters the working area of the blades 3, where another particle separation process takes place. The remaining coarse particles also move as a result of centrifugal force from the rotor 1 to the outside towards the guide vanes 10 and 11 and then fall into the funnel 12, from where the coarse particles are released for their intended purpose.
The separated fine fraction, which is still suspended in the gas stream, moves with the gas through the rotor and as the desired product is withdrawn through the nozzle 7, made in the upper part of the separator.
权利要求:
Claims (1)
[1]
Invention Formula
Separator for the separation of particles of the material into large and small fractions, including a housing with a rotor in it, equipped with a vertical
five
20
axis of the blade, and guide vanes located around the rotor, pipes for supplying carrier gas and the source material, pipe for unloading the separated small fraction suspended in the gas, located at least at one end of the separator, and pipe for unloading the separated coarse fractions located under the rotor and guide blades, characterized in that, in order to improve the separation accuracy, the guide blades are combined into several sets, with the guide blades of each set The ras are installed one above the other in a fixed ring and are equipped with independent rotation of the blades of each set.
类似技术:
公开号 | 公开日 | 专利标题
SU1436859A3|1988-11-07|Separator for separating material particles into fine and large fractions
US3234716A|1966-02-15|Apparatus for separating dust and other particles from suspension in a gas
US4528091A|1985-07-09|Particle classifier
SU1528334A3|1989-12-07|Separator for dividing material particles into fine and coarse fractions
GB1488642A|1977-10-12|Classifying apparatus for classifying particulate materia
EP0210729A2|1987-02-04|Separator for sorting particulate material
EP0149221B1|1989-08-16|Classifier
GB1391256A|1975-04-16|Apparatus for separating and classifying mixtures of particulate materials
EP0519535A1|1992-12-23|Dynamic separator for pulverulent materials, in particular cement, and a plant incorporating it
US3036709A|1962-05-29|Centrifugal air classifier
SU1641474A2|1991-04-15|Centrifugal classifier
SU1510961A1|1989-09-30|Centrifugal classifier
RU2067900C1|1996-10-20|Centrifugal apparatus for fractionation of loose materials
SU959846A1|1982-09-23|Separator for powdered materials
SU1158228A1|1985-05-30|Apparatus for grinding materials
SU780908A1|1980-11-23|Pneumatic classifier
RU2007230C1|1994-02-15|Separator
SU1007758A1|1983-03-30|Separator with multichannel circulation
SU1175547A1|1985-08-30|Apparatus for crushing materials
SU506440A1|1976-03-15|Pneumatic separator
SU1632516A1|1991-03-07|Centrifugal countercurrent separator
SU1036401A1|1983-08-23|Separator for powdered materials
JP2707021B2|1998-01-28|Crushed sand dust removal equipment
SU933128A1|1982-06-07|Powdered material classifier
SU1554994A2|1990-04-07|Separator for separating pulverulent materials
同族专利:
公开号 | 公开日
GB2176134A|1986-12-17|
CN86103352A|1986-12-31|
KR870000091A|1987-02-16|
ES8707122A1|1987-07-01|
ZA864103B|1987-01-28|
AU5650586A|1986-12-11|
CN86103352B|1988-10-26|
US4689141A|1987-08-25|
EP0204412A2|1986-12-10|
BR8602528A|1987-01-27|
DK153697B|1988-08-22|
IN166869B|1990-07-28|
JPS61278387A|1986-12-09|
EP0204412B1|1990-07-25|
KR890002072B1|1989-06-16|
EP0204412B2|1993-09-15|
ES555578A0|1987-07-01|
DE3672901D1|1990-08-30|
AU579466B2|1988-11-24|
DK248486D0|1986-05-28|
MX163738B|1992-06-18|
GB8513968D0|1985-07-03|
DK153697C|1988-12-27|
DK248486A|1986-12-04|
EP0204412A3|1987-10-14|
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法律状态:
优先权:
申请号 | 申请日 | 专利标题
GB08513968A|GB2176134A|1985-06-03|1985-06-03|Separator for sorting particulate material|
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