CN103567028A - Stirring ball mill - Google Patents

Stirring ball mill Download PDF

Info

Publication number
CN103567028A
CN103567028A CN201310328674.XA CN201310328674A CN103567028A CN 103567028 A CN103567028 A CN 103567028A CN 201310328674 A CN201310328674 A CN 201310328674A CN 103567028 A CN103567028 A CN 103567028A
Authority
CN
China
Prior art keywords
fluid
grinding
stirring ball
ball mill
exit region
Prior art date
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.)
Granted
Application number
CN201310328674.XA
Other languages
Chinese (zh)
Other versions
CN103567028B (en
Inventor
U·恩德勒
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.)
Netzsch Feinmahltechnik GmbH
Original Assignee
Netzsch Feinmahltechnik GmbH
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 Netzsch Feinmahltechnik GmbH filed Critical Netzsch Feinmahltechnik GmbH
Publication of CN103567028A publication Critical patent/CN103567028A/en
Application granted granted Critical
Publication of CN103567028B publication Critical patent/CN103567028B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/18Details
    • B02C17/183Feeding or discharging devices
    • B02C17/186Adding fluid, other than for crushing by fluid energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/16Mills in which a fixed container houses stirring means tumbling the charge
    • B02C17/163Stirring means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/18Details
    • B02C17/183Feeding or discharging devices
    • B02C17/186Adding fluid, other than for crushing by fluid energy
    • B02C17/1875Adding fluid, other than for crushing by fluid energy passing gas through crushing zone
    • B02C17/188Adding fluid, other than for crushing by fluid energy passing gas through crushing zone characterised by point of gas entry or exit or by gas flow path

Abstract

The present invention relates to a stirring ball mill used for grinding dry or non-dry substances. The stirring ball mill is provided with a grinding vessel. The grinding vessel is provided with an inlet of the material to be milled, a fluid inlet and a material outlet, wherein the outlet is provided with a sieve. A stirring shaft extends in the center or near the center of the grinding vessel, a plurality of grinding elements are arranged on stirring shaft. The grinding vessel is at least partially filled with grinding aids.

Description

Stirring ball mill
Technical field
The present invention relates to a kind of stirring ball mill for preferred mill-drying or non-dry matter, and relate to a kind of for the method at stirring ball mill mill-drying or non-dry matter.By of the present invention, for the stirring ball mill of mill-drying or non-dry matter, be provided with grinding container.This grinding container is equipped with for the entrance of material to be ground and material outlet, and wherein, exit region is equipped with sieve.Shaft extends near the central or central authorities of grinding container, and a plurality of grinding elements are arranged on this shaft.This grinding container is filled by grinding auxiliary body at least partly.
Background technology
Germany Patent document DE3642320C2 discloses a kind of for grinding, be particularly useful for dry type ground ground pigment, it has columniform container, abrasive body is arranged in this container, and this container is equipped with for the entrance of material to be ground with for the outlet of abrasive material.Drivable agitator is arranged on the axis of this container, and the acting surface of this agitator and the distance between container inner wall are less than the diameter of abrasive body.Exist at least two acting surfaces, they extend and in axial expansion direction, surround this container completely along the outer cover line of container.
In German patent document DE1288890, disclose a kind of for the dry very fine of the stirring ball mill at high speed operation pulverize the method for solid matter.The grinding container of the vertical setting of stirring ball mill is filled by abrasive body and partly by gas percolation.This abrasive material stream and always directly and the air-flow that is almost only guided through abrasive body-abrasive material-particle controlled like this, 10% of free space between abrasive body is filled by abrasive material to 60%.This agitator consists of the smooth whole disk being medially arranged on shaft.
German patent application DE102010049827 discloses a kind of stirring ball mill for mill-drying or non-dry matter.This stirring ball mill is equipped with grinding container.This grinding container is provided with the entrance for material to be ground, independent fluid intake and material outlet, and wherein, this exit region is equipped with screen.Shaft extends near the central or central authorities of grinding container, and a plurality of grinding elements are arranged on this shaft.This grinding container is filled by grinding auxiliary body at least partly.The entrance area of stirring ball mill is equipped with the first retainer, and this exit region is equipped with the second retainer.
Summary of the invention
The object of the invention is, provide a kind of, for economical and reliable, dry or non-dry material are ground to form to the method for the abrasive material of very fine, and optimize pumped (conveying) medium (fluid) flowing in grinding container.
Above-mentioned purpose reaches by having the method for the feature of claim 1.Other favourable feature can be drawn by dependent claims.
In addition, the present invention also aims to create a kind of stirring ball mill, by this stirring ball mill, dry or non-dry material can be ground to form to the abrasive material of very fine, also can economical and reliable ground mill-drying or non-dry material.
Above-mentioned purpose is achieved by having the stirring ball mill of the feature of claim 8.Other favourable feature can be drawn by dependent claims.
Disclose a kind of for moving stirring ball mill and for the method for mill-drying or non-dry material.By the fluid passage being arranged in shaft, fluid is incorporated in grinding container.This fluid is introduced near the space of last grinding element, and this last grinding element is connected to the upstream of the exit region of stirring ball mill.In a kind of preferred form of implementation, fluid is introduced in stirring ball mill between grinding element and last grinding element.In another kind of form of implementation, fluid in the end sprays into, is blown into or be drawn in grinding container between grinding element and the exit region of stirring ball mill.According to the parameter of stirring ball mill operation, change the mode that fluid enters stirring ball mill.If stirring ball mill is overvoltage (vacuum) operation to bear for example, fluid is inhaled in grinder.
Fluid moves at grinding container with 0 speed to 50m/s after entering or injecting.Fluid preferably with 0 and the speed of 5m/s in grinding container, move.How the to flow through mode of grinding container of this speed and fluid depends on the free cross section in grinding container.Compare with the grinding container with a small amount of member/grinding element, in the situation that the speed that is blown into is identical, due to less free cross section, in having the grinding container of many member/grinding elements, flowing velocity is higher.Flowing through of consisting of fluid and abrasive material exported from grinding container by separator.Another separation assembly for separating of fluid and abrasive material is connected to this separator downstream.
When mill-drying material, preferably adopt air, inert gas or steam as fluid.In order to ensure dry grinding, adopt overheated dry steam as fluid.Can regulate as required fluid to the addition in the grinding container of stirring ball mill and/or add frequency.
In addition, the invention also discloses a kind of stirring ball mill for mill-drying or non-dry matter.This stirring ball mill comprises grinding container, and this grinding container is at least local is filled by abrasive body.This grinding container has for the entrance of material to be ground with for the outlet of the abrasive material that ground.Separator is arranged in the exit region of stirring ball mill.Shaft extends in the central authorities of grinding container, and a plurality of grinding elements are arranged on this shaft.Fluid passage extends through this shaft, and fluid can import in grinding container by this fluid passage.Last grinding element being arranged on before the exit region of stirring ball mill is equipped with at least one for the tap of fluid near space.One in these taps is configured to nozzle.
At least one tap is arranged between grinding element and last grinding element.In another embodiment, at least one tap is arranged between last grinding element and exit region.At least one separation assembly for separating of abrasive material and fluid is connected to this exit region and is arranged on the separator downstream in this exit region.This at least one separation assembly is wind separator.
Accompanying drawing explanation
By accompanying drawing, embodiments of the invention and advantage thereof have at length been set forth below.Each element size in the accompanying drawings is not always equivalent to real size, because some shape simplification, but another shape is in order better to show and to compare and expanded with other element.
Fig. 1 shows by stirring ball mill of the present invention;
Fig. 2 shows by stirring ball mill of the present invention, and wherein, tap is arranged between last grinding element and exit region.
List of numerals
10 stirring ball mills
12 shafts
14 fluids
16 grinding containers
18 grinding elements
19 last grinding element
20 separators
22 separation assemblies
24 entrances
26 outlets
28 exit regions
30 fluid passages
32 taps/nozzle
The specific embodiment
Fig. 1 shows by stirring ball mill 10 of the present invention.This stirring ball mill 10 comprises grinding container 16 and shaft 12.A plurality of grinding elements 18 are set on this shaft 12.Separator 20 is positioned on the end of shaft 12, and grinding auxiliary body (not shown) and abrasive material can be by this separator separately.Material to be ground is provided in grinding container 16 by entrance 24.The abrasive material having ground leaves grinding container 16 by exporting 26.The end of shaft 12 forms like this, makes separator 20 be arranged on the inside of exit region 28.Fluid passage 30 is positioned at the inside of shaft 12, and various fluids 14 can be introduced in the grinding container 16 of stirring ball mill 10 by this fluid passage.This fluid 14 leaves fluid passage 30 by tap 32, and this tap 32 is configured to nozzle in a preferred embodiment.Tap 32 be arranged on last grinding element 19 near.
In Fig. 1, tap 32 is arranged between grinding element 18 and last grinding element 19.The mixture consisting of fluid 14 and abrasive material leaves stirring ball mill 10 by exporting 26, and separation assembly 22 is connected to the downstream of this outlet.Fluid 14 and abrasive material are separated from each other in this separation assembly 22.
It will be apparent to those skilled in the art that and can adopt different fluid 14 or separation assembly 22.When dry grinding, adopt air, inert gas or overheated steam as fluid 14.In the Fig. 1 illustrating herein, adopt wind separator as separation assembly 22.Above done enumerating is not the enclosed restriction to the present invention.
Fig. 2 shows by stirring ball mill 10 of the present invention, and wherein, tap 32 is arranged between last grinding element 19 and exit region 28.Fluid passage 30 extends past the shaft 12 of stirring ball mill 10, and fluid 14 imports in tap 32 by this fluid passage.
The present invention is described with reference to preferred embodiment.But can imagine for a person skilled in the art, can the present invention is out of shape or be changed, and can not depart from the protection domain of following claim.

Claims (13)

1. one kind for moving the method for stirring ball mill (10), this stirring ball mill is for mill-drying or non-dry material, wherein, fluid (14) is introduced in grinding container (16) via shaft (12), it is characterized in that, described fluid (14) is introduced near the space of last grinding element (19) that is connected to exit region (28) upstream.
2. method according to claim 1, is characterized in that, described fluid (14) is introduced between grinding element (18) and described last grinding element (19).
3. method according to claim 1, is characterized in that, described fluid (14) is introduced between described last grinding element (19) and described exit region (28).
4. according to the method described in any one of claims 1 to 3, it is characterized in that, described fluid (14) is with 0 to 50m/s speed, preferably mobile in described grinding container (16) with 0 to 5m/s speed.
5. according to the method described in any one of claim 1 to 4, it is characterized in that, flowing through of consisting of fluid (14) and abrasive material exported from grinding container (16) by separator (20), and at least one is connected to the downstream of described separator (20) for separating of another separation assembly (22) of fluid (14) and abrasive material.
6. according to the method described in any one of claim 1 to 5, it is characterized in that, adopt air, inert gas or steam as fluid (14).
7. according to the method described in any one of claim 1 to 6, it is characterized in that, regulate the addition of described fluid (14) and/or add frequency.
8. the stirring ball mill for mill-drying or non-dry matter (10), it has
-grinding container (16), this grinding container is at least local fills by grinding auxiliary body;
-for material to be ground or the entrance of abrasive material (24) and outlet (26);
-be arranged on the separator (20) in exit region (28);
-extend past the central shaft (12) of grinding container (16);
-a plurality of grinding elements (18) that are arranged on described shaft (12);
-extend past the fluid passage (30) of described shaft (12); And
-fluid (14) can guide by described fluid passage (30),
It is characterized in that, be arranged on exit region (28) last grinding element (19) before and near space, be equipped with at least one tap for fluid (14) (32).
9. stirring ball mill according to claim 8 (10), is characterized in that, at least one in tap (32) is nozzle.
10. stirring ball mill (10) according to claim 8 or claim 9, is characterized in that, at least one tap (32) is arranged between described grinding element (18) and described last grinding element (19).
11. stirring ball mills (10) according to claim 8 or claim 9, is characterized in that, at least one tap (32) is arranged between described last grinding element (19) and exit region (28).
Stirring ball mill described in any one of 12. according to Claim 8 to 11 (10), it is characterized in that, for separating of at least one separation assembly (22) of abrasive material and fluid (14), be connected to the downstream of described exit region (28) and described separator (20).
13. stirring ball mills according to claim 12 (10), is characterized in that, described at least one separation assembly (22) is wind separator.
CN201310328674.XA 2012-07-31 2013-07-31 Stirring ball mill and the method being used for running stirring ball mill Active CN103567028B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102012107005.9 2012-07-31
DE102012107005.9A DE102012107005A1 (en) 2012-07-31 2012-07-31 stirred ball mill

Publications (2)

Publication Number Publication Date
CN103567028A true CN103567028A (en) 2014-02-12
CN103567028B CN103567028B (en) 2016-10-19

Family

ID=48906081

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310328674.XA Active CN103567028B (en) 2012-07-31 2013-07-31 Stirring ball mill and the method being used for running stirring ball mill

Country Status (3)

Country Link
EP (1) EP2692445A3 (en)
CN (1) CN103567028B (en)
DE (1) DE102012107005A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106040374A (en) * 2015-04-16 2016-10-26 耐驰精细研磨技术有限公司 Agitator ball mill
CN110385175A (en) * 2019-07-29 2019-10-29 成都利君实业股份有限公司 One kind can quantity-produced cement grog grinding implementation equipment

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112808393A (en) * 2020-12-31 2021-05-18 生态环境部南京环境科学研究所 Vertical continuous stirring ball milling equipment and working method thereof

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85107966A (en) * 1984-11-09 1986-05-10 奥姆亚有限公司 Mixer grinder
CN1119557A (en) * 1994-09-09 1996-04-03 Evv财产管理有限公司 Stirring mill
JPH09122519A (en) * 1995-10-31 1997-05-13 Mitsubishi Heavy Ind Ltd Horizontal wet mill
JP2001259452A (en) * 2000-03-16 2001-09-25 Masumi Kusunoki Circulating grinding system and grinding method
JP2004188835A (en) * 2002-12-12 2004-07-08 Chuo Kakoki Kk Woody material grinder
CN1583277A (en) * 2004-06-03 2005-02-23 袁运法 Non-powdered spiral feeding method and device for ball mill
CN202113904U (en) * 2011-05-31 2012-01-18 陈波 Novel grinding device

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1288890B (en) 1964-04-10 1969-02-06 Draiswerke Gmbh Method and device for the dry fine comminution of solids
SU594294A2 (en) * 1974-11-05 1978-02-25 Всесоюзный научно-исследовательский институт по креплению скважин и буровым растворам Bead mill
DE3642320A1 (en) 1986-12-11 1988-06-23 Thomson Brandt Gmbh Video recorder
FR2650198B1 (en) * 1989-07-26 1995-02-17 Chauveau Jean Marie PROCESS AND CRUSHER FOR THE MANUFACTURE OF A PRODUCT FORMED BY A SUSPENSION OF SOLID PARTICLES IN A FAT VEHICLE
DE102010049827A1 (en) 2010-10-27 2012-05-03 Netzsch-Feinmahltechnik Gmbh stirred ball mill

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85107966A (en) * 1984-11-09 1986-05-10 奥姆亚有限公司 Mixer grinder
CN1119557A (en) * 1994-09-09 1996-04-03 Evv财产管理有限公司 Stirring mill
JPH09122519A (en) * 1995-10-31 1997-05-13 Mitsubishi Heavy Ind Ltd Horizontal wet mill
JP2001259452A (en) * 2000-03-16 2001-09-25 Masumi Kusunoki Circulating grinding system and grinding method
JP2004188835A (en) * 2002-12-12 2004-07-08 Chuo Kakoki Kk Woody material grinder
CN1583277A (en) * 2004-06-03 2005-02-23 袁运法 Non-powdered spiral feeding method and device for ball mill
CN202113904U (en) * 2011-05-31 2012-01-18 陈波 Novel grinding device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106040374A (en) * 2015-04-16 2016-10-26 耐驰精细研磨技术有限公司 Agitator ball mill
CN110385175A (en) * 2019-07-29 2019-10-29 成都利君实业股份有限公司 One kind can quantity-produced cement grog grinding implementation equipment

Also Published As

Publication number Publication date
DE102012107005A1 (en) 2014-05-22
EP2692445A2 (en) 2014-02-05
EP2692445A3 (en) 2017-06-14
CN103567028B (en) 2016-10-19

Similar Documents

Publication Publication Date Title
CN103298561B (en) For the dynamic element of the separator of stirring ball mill
US8033399B2 (en) Centrifugal separator
US8118247B2 (en) Agitator ball mill
KR102154690B1 (en) Agitator ball mill
US8453846B2 (en) Method for classifying a ground material-fluid mixture and mill classifier
WO2012009450A3 (en) Pulverizer classifier
CN106423420B (en) A kind of dry type multistage intelligent agitating ball mill
CN103657801B (en) Stirring-type grinds separator and lapping device
CN105073221B (en) Gas desander
CN103567028A (en) Stirring ball mill
JP2011530404A5 (en) Method for classifying pulverized product-fluid mixture and pulverizing classifier
CN206642897U (en) The used manifold type mill separator of rotation
CN106573257A (en) Separator
CN105772235B (en) A kind of cyclone separator
CN209663527U (en) For separating the cyclone separator and dip-tube of gas
CN104741253A (en) Direct current guide vane type cyclone dust collector
CN105358265A (en) Powder classifying apparatus
CN105188948A (en) Device and method for separating foreign particles out of a gas stream
DE2012797C3 (en) Device for the sifting of bulk goods
CN203695426U (en) Ultrafine powder airflow classifier
US9144826B2 (en) Separator for granular materials
JP6561120B2 (en) Cyclone separation device comprising two cyclones connected by an optimized piping unit
CN108339642A (en) A kind of high-shear colloid mill
CN208302964U (en) A kind of airslide disintegrating mill with variable cross-section cylinder
CN108126808B (en) High pressure liquid flow powder making method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C53 Correction of patent of invention or patent application
CB02 Change of applicant information

Address after: German selbe

Applicant after: Netzsch Feinmahltechnik GmbH

Address before: German selbe

Applicant before: Netzsch Feinmahltechnik

COR Change of bibliographic data

Free format text: CORRECT: APPLICANT; FROM: NETZSCH FEINMAHLTECHNIK TO: NETZSCH FEINMAHLTECHNIK GMBH

SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant