EP3613508B1 - Verfahren zur ausschleusung schwer mahlbarer partikel aus einer spiralstrahlmühle - Google Patents

Verfahren zur ausschleusung schwer mahlbarer partikel aus einer spiralstrahlmühle Download PDF

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Publication number
EP3613508B1
EP3613508B1 EP19190424.2A EP19190424A EP3613508B1 EP 3613508 B1 EP3613508 B1 EP 3613508B1 EP 19190424 A EP19190424 A EP 19190424A EP 3613508 B1 EP3613508 B1 EP 3613508B1
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EP
European Patent Office
Prior art keywords
grinding
discharge nozzle
process space
feed
ground
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.)
Active
Application number
EP19190424.2A
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German (de)
English (en)
French (fr)
Other versions
EP3613508A1 (de
Inventor
Hermann Sickel
Frank Winter
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 Trockenmahltechnik GmbH
Original Assignee
Netzsch Trockenmahltechnik GmbH
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Application filed by Netzsch Trockenmahltechnik GmbH filed Critical Netzsch Trockenmahltechnik GmbH
Priority to SI201930679T priority Critical patent/SI3613508T1/sl
Publication of EP3613508A1 publication Critical patent/EP3613508A1/de
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Publication of EP3613508B1 publication Critical patent/EP3613508B1/de
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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
    • B02C19/061—Jet mills of the cylindrical type
    • 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
    • B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/02—Feeding devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
    • B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C25/00—Control arrangements specially adapted for crushing or disintegrating

Definitions

  • the present invention relates to methods for removing particles that are difficult to grind from a spiral steel mill according to the features of claim 1.
  • jet mills such as those from WO9601694 or DE 44 31 534 A1 known. These jet mills are used to crush various materials. The particles to be comminuted are accelerated using gas jets in order to be comminuted by mutual impact. Furthermore, shear forces occur at the points where the particles are accelerated by the gas jets, which additionally contribute to the size reduction process.
  • feed material consists of different components, it may happen that only some of them can be ground using the steel mill.
  • the sufficiently comminuted particles leave the grinding chamber in which the sufficiently comminuted particles, also referred to as fines, pass through a classifying device, for example a classifier wheel, and then leave the jet mill via a fines outlet.
  • a classifying device for example a classifier wheel
  • Components that have other properties, such as ductile behavior or higher hardness can remain in the grinding chamber.
  • These difficult-to-grind components, or even coarse particles accumulate in the grinding chamber as the grinding process continues and thus reduce the volume of the grinding chamber that should actually be available for grinding, thereby significantly reducing the throughput of the jet mill.
  • the object of the present invention is to optimize the grinding process in such a way that residues which remain within the grinding chamber during a grinding process can be removed from it more quickly and efficiently than is the case in the prior art.
  • the invention relates to a method for grinding, separating and discharging difficult-to-grind components of a mixture of components with different grindability from a process space of a jet mill. Due to the different properties of the components contained in the good mixture, the sufficiently comminuted particles, also described as fines, leave the process room after classification via the fines outlet.
  • the classification is carried out, for example, using a classifier wheel.
  • the components that are difficult to grind, also described as coarse particles are unable to overcome the classifying device and are therefore retained in the process space.
  • the coarse particles are discharged using a fluid via at least one discharge nozzle. The opening of the discharge nozzle and the interruption of the feed of the regrind are carried out in a synchronized manner.
  • the fluid which removes the coarse particles from the process space is made available through the grinding nozzles protruding into the process space. During the grinding process, these nozzles provide the gas jets through which the particles of the feed material are comminuted. Due to the excess pressure or negative pressure that prevails in the process space, the coarse particles are discharged from the process space via the at least one discharge nozzle using the grinding gas.
  • the discharge nozzle is closed to the process space during the grinding process and is only opened manually or automatically during a coarse fraction discharge phase.
  • Another advantage of the method according to the invention is the manual or automatic interruption of the regrind feed. This prevents unground material from being fed into the grinding chamber via the ground material inlet during the emptying of the grinding chamber or during the discharge of the difficult-to-grind components from the grinding chamber.
  • the feed of regrind via the regrind feed into the process space is carried out using a dosing unit, for example via a rotary valve, or a dosing pump.
  • the discharge nozzle and the feed of the ground material can be closed from the process space using closure elements.
  • the closure elements can be designed, for example, as a flap, slide or rotary valve.
  • At least one operating parameter of the method is recorded via the at least one sensor.
  • Important operating parameters include, for example, the filling level of the mill, the amount and speed of the grinding material feed, and the amount, pressure and speed of the grinding fluid used, the speed of the classifier wheel and the power consumption of the motor that drives the classifier wheel, as well as the grinding material throughput.
  • the various parameters interact with each other, in particular the degree of filling of the mill and the feed of the milled material.
  • the filling level of the The mill is controlled via the power consumption of the classifying wheel. If ground material leaves the process space via the classifier wheel and the fine material outlet, there is less material to be ground in the process room, which means there are fewer collisions of particles of the material to be ground with the classifier wheel. As a result, the power required to maintain a constant speed of the classifier wheel decreases, and the power consumption of the motor that drives the classifier wheel decreases.
  • regrind is fed into the process room via the regrind feed until the current consumption of the motor that drives the classifier wheel is reached, due to the now increasing number of collisions with ground material has again reached a defined maximum value, for example 65% of the maximum power of the motor that drives the classifier wheel.
  • a defined maximum value for example 65% of the maximum power of the motor that drives the classifier wheel.
  • the limits for the power consumption of the motor that drives the classifier wheel can vary. For example, values for the minimum value between 30% and 80%, in particular between 40% and 60%, are possible.
  • the maximum value for the power consumption of the motor that drives the classifier wheel can be between 50% and 100%, in particular between 60% and 80%.
  • the process for feeding the regrind explained in the paragraph above is expressed as a constant interval for regrind that does not contain any components that are difficult or impossible to grind. This means that the intervals between the stop of the regrind feed and the start of the regrind feed, as well as the duration of the regrind feed, behave almost periodically. This is not the case for ground material with components that are difficult or impossible to grind.
  • the enrichment of the components of the ground material that are difficult or impossible to grind means that fewer particles leave the process area than usual. For this reason, the current consumption of the motor that drives the classifier wheel does not fall below the defined minimum value so quickly, which is accompanied by a delay in the feed of the regrind.
  • the components of the regrind that are difficult or impossible to grind and remain in the process space continue to put stress on the classifier wheel, but without passing through it.
  • the power consumption of the motor that drives the classifier wheel does not decrease as with normal regrind without components that are difficult or impossible to grind, and the intervals between stopping the grinding material feed do not decrease and start of the regrind feed increase.
  • the duration of the regrind feed is reduced because once the current consumption of the motor that drives the classifier wheel falls below the defined minimum value, the corresponding maximum value is reached more quickly because a higher number of particles remain in the process space.
  • This reduction in throughput can preferably be used as a control value for the discharge of the components that are difficult or impossible to grind from the mill.
  • the feed of the regrind is automatically stopped.
  • the opening and closing of the Discharge nozzle can be controlled.
  • the interruption or start of the regrind feed and the opening or closing of the discharge nozzle can also be coordinated with one another. For example, it is possible to control only the regrind feed via at least one operating parameter. If at least one operating parameter, e.g. the throughput or the interval duration of the material supply, leaves the value range defined for it, the grinding material feed is interrupted. Depending on this, the opening of the discharge nozzle can be triggered at the same time or at a different time.
  • the opening time of the discharge nozzle and the interruption of the feed of the material to be ground are set individually.
  • the opening time of the discharge nozzle is preferably 1 - 10 seconds.
  • the interruption of the feed of the ground material is preferably 1 - 10 seconds.
  • the opening of the discharge nozzle and the interruption of the regrind feed, as well as the closure of the discharge nozzle and the start of the regrind feed are carried out in a coordinated manner.
  • the feeding of the ground material is interrupted before the discharge nozzle is opened. In this way, feed material that has not yet been ground can be ground and the particles still in the process space that have been ground to the target size can be discharged.
  • some of the process steps described above have a defined duration.
  • the grinding and discharge of the portion of grindable portions of the ground material still in the process space takes between one second and five minutes, in particular between 1 and 60 seconds.
  • the opening time of the discharge nozzle is between one second and one minute, in particular between 1 and 10 seconds.
  • the time between these two process steps can be between 0.5 and 60 seconds, in particular between 0.5 and 5 seconds.
  • the process according to the invention is carried out by a spiral jet mill to act on material that can be partially comminuted and classified.
  • Such spiral steel mills have a process space that is surrounded by a housing. At least two grinding nozzles protrude into the process space; the grinding fluid is passed into the process space through these grinding nozzles during the grinding process.
  • the process space is rotationally symmetrical, flat and round, with a radial housing wall that is delimited by a circular surface at the top and bottom, with the height of the cylinder being smaller than the diameter.
  • the grinding nozzles are arranged tangentially on the housing wall. Furthermore, the grinding nozzles are arranged on the same level as the classifier wheel, which is located in the middle of the process space.
  • the classifier wheel is also rotationally symmetrical, flat and round, with radially extending slats, each of which is delimited at the top and bottom by a plate that forms a circular surface, whereby the height of the cylinder body is also smaller than the diameter.
  • the set pressure at which the grinding fluid is fed through the grinding nozzles into the process space varies between 0.1 and 40 bar(g).
  • Typical grinding fluids are air, nitrogen, water vapor and noble gases such as argon and helium.
  • the ground material introduced via a ground material inlet connected to the process space is captured by the grinding fluid jets, accelerated and comminuted by particle-particle collisions. It is therefore an autogenous grinding of the ground material.
  • the stressed particles are transported from the grinding fluid to the classifier wheel, which is driven by a motor, for example a frequency-controlled motor.
  • the desired target fineness of the fine material is preset via the speed of the classifier wheel. After passing the classifier wheel, the fine material is discharged from the machine via the fine material outlet. Particles that are too coarse or have not yet been ground sufficiently are rejected by the classifier wheel and thus find their way back into the product-laden grinding fluid jets for renewed stress. This creates a circular movement of the ground material in the process space.
  • a discharge nozzle connected to the process space is provided. This discharge nozzle can be closed manually or automatically from the process space and is closed during the grinding process.
  • the machine which acts on partially shredded and classifiable goods, has measuring instruments that record the operating parameters of the grinding process. Relevant operating parameters include, for example, the throughput of regrind per unit of time, the quantity and speed of the regrind feed, and the amount, pressure and speed of the grinding fluid used, the speed of the classifier wheel and the power consumption of the motor that drives the classifier wheel.
  • the machine also includes a device with which the dosage of the ground material into the process space can be recorded and controlled.
  • the method may include one or more features and/or properties of the previously described device.
  • the device can also alternatively or additionally have individual or multiple features and/or properties of the methods described.
  • Figure 1 shows a sectional view of a spiral jet mill (1), having a regrind feed (2) through which the regrind (10) is guided into the process space (3).
  • the dosing i.e. the feeding of the ground material (10), takes place via a dosing unit (not shown), for example a rotary valve or a pump device.
  • Grinding nozzles (4) which are positioned at a suitable distance from one another, protrude into the process space (3). This suitable distance varies depending on the number of grinding nozzles (4) and should be chosen so that the grinding nozzles (4) are evenly distributed over the circular path that describes the housing (5) which encloses the process space (3), in the example Figure 1
  • the grinding nozzles (4) are each arranged 90° offset and their respective longitudinal axes (41) close with an im
  • the tangent (13) created in the area of the respective grinding nozzle attachment in the housing (5) forms an angle alpha ( ⁇ ) which should be in the range of 10° and 60°.
  • the grinding nozzles (4) can also be arranged irregularly on the housing (5).
  • the grinding nozzles (4) supply the grinding fluid (6) to the process space (3).
  • This grinding fluid (6) is used to stress and shred the ground material (10) that is dispensed.
  • the parameters such as pressure, quantity, temperature and spray angle for the grinding fluid (6) must be adjusted.
  • gases come into consideration as grinding fluid (6), in particular protective gases such as argon and helium and nitrogen.
  • the fine material outlet (7) is located in the middle of the process space (3). This leads particles out of the process space (3) through the lid or bottom of the housing (5).
  • the particles that have achieved the necessary fineness through grinding in the process space (3), i.e. the ground portions of the ground material (11), are removed through the fine material outlet (7).
  • a classifier wheel (8) is positioned around the fine material outlet (7) so that only particles with the necessary fineness can leave the process space (3).
  • the classifier wheel (8) rotates and is operated at a variable speed. The necessary fineness for the ground portions of the ground material (11) can thus be set. If a particle that is too large wants to pass through the rotating classifier wheel (8), it is thrown back into the process space (3) by the safety wheel (8) and stressed again. If the particle is ground finely enough, i.e. it has a sufficiently small particle or grain size, it can leave the process space (3) through the fine material outlet (7) with the fluid flow of the ground parts of the ground material (11).
  • the regrind feed (2) is closed relative to the process space (3).
  • the discharge nozzle (9) opens. This is closed during the grinding process by a closure element (14), for example a flap, or a slide relative to the process space (3).
  • This closure element (14) can be positioned anywhere in the discharge nozzle (9), for example the closure element (14) can rest flush against the outer shell of the housing (5), or can be mounted inside the housing (5) and be flush with the process space (3). . Due to the overpressure or negative pressure of -500 mbar(g) to +600 mbar(g) prevailing in the process space (3), all particles located in the process space (3) are now flushed out of the process space (3) via the discharge nozzle (9).
  • the discharge nozzle (9 ) After a period of, for example, 1 to 60 seconds or a message from a sensor that monitors the degree of filling in the process space (3) and thus checks whether all parts of the ground material (12) that are difficult or impossible to grind have been discharged from the process space, the discharge nozzle (9 ), closed again by means of the closure element (14). The grinding material feed (2) is then opened or started again and the grinding process is continued.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Disintegrating Or Milling (AREA)
  • Crushing And Grinding (AREA)
EP19190424.2A 2018-08-23 2019-08-07 Verfahren zur ausschleusung schwer mahlbarer partikel aus einer spiralstrahlmühle Active EP3613508B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SI201930679T SI3613508T1 (sl) 2018-08-23 2019-08-07 Postopek odstranjevanja slabo mlevnih delcev iz spiralnega mešalnika

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102018120596.1A DE102018120596A1 (de) 2018-08-23 2018-08-23 Verfahren und Vorrichtung zur Ausschleusung schwer mahlbarer Partikel aus einer Spiralstrahlmühle

Publications (2)

Publication Number Publication Date
EP3613508A1 EP3613508A1 (de) 2020-02-26
EP3613508B1 true EP3613508B1 (de) 2023-09-27

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US (1) US11235337B2 (fi)
EP (1) EP3613508B1 (fi)
JP (1) JP6934491B2 (fi)
KR (1) KR102277738B1 (fi)
CN (1) CN110856830B (fi)
DE (1) DE102018120596A1 (fi)
DK (1) DK3613508T3 (fi)
ES (1) ES2966925T3 (fi)
FI (1) FI3613508T3 (fi)
LT (1) LT3613508T (fi)
PL (1) PL3613508T3 (fi)
RU (1) RU2732837C1 (fi)
SI (1) SI3613508T1 (fi)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4088818A1 (de) 2021-05-14 2022-11-16 LANXESS Deutschland GmbH Spiralstrahlmühle und verfahren zum vermahlen von mahlgütern in einer spiralstrahlmühle

Family Cites Families (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3425638A (en) * 1965-10-04 1969-02-04 Grace W R & Co Fluid energy mill
US3602439A (en) * 1969-07-25 1971-08-31 Nippon Pneumatic Mfg Pneumatic mill for extra-fine powder
DE2063635C3 (de) * 1970-12-30 1980-01-03 Daikin Kogyo Co. Ltd., Tokio Verfahren zur Herstellung eines nicht faserigen ultrafeinen Polytetrafluoräthylen-Formpulvers
US3726484A (en) * 1971-10-15 1973-04-10 Du Pont Stepped fluid energy mill
US4502641A (en) * 1981-04-29 1985-03-05 E. I. Du Pont De Nemours And Company Fluid energy mill with differential pressure means
DE4431534B4 (de) * 1994-02-10 2006-12-28 Nied, Roland, Dr. Ing. Maschine zur Einwirkung auf zerkleinerbares und klassierbares Rohgut, sowie Verfahren zum Betrieb der Maschine
AU2873195A (en) * 1994-07-11 1996-02-09 Pmt Gesteinsvermahlungstechnik Powder Maker Technologies Gmbh Spiral jet mill
JPH0824702A (ja) * 1994-07-20 1996-01-30 Hosokawa Micron Corp 原液から微粉末を製造する方法及びその装置
JP3831102B2 (ja) * 1997-12-25 2006-10-11 日本ニューマチック工業株式会社 ジェット粉砕機
RU2199397C2 (ru) * 2000-11-16 2003-02-27 Белгородская государственная технологическая академия строительных материалов Устройство для вихревого измельчения материалов
JP4205888B2 (ja) * 2001-12-20 2009-01-07 ホソカワミクロン株式会社 粉体処理装置および粉体処理方法
KR20040073116A (ko) * 2003-02-13 2004-08-19 (주)디자인메카 복수개의 분쇄물 출구와 와류발생기를 갖는 유체에너지밀 분쇄장치 및 분쇄방법
JP4922760B2 (ja) * 2004-07-09 2012-04-25 サンレックス工業株式会社 ジェットミル
DE102006001937A1 (de) * 2006-01-14 2007-09-27 Lehigh Technologies, LLC, Naples Trennen von Mineralien
DE102006017472A1 (de) * 2006-04-13 2007-10-18 Nied, Roland, Dr. Ing. Verfahren zur Erzeugung feinster Partikel mittels einer Strahlmühle
WO2009008965A1 (en) * 2007-07-09 2009-01-15 Unimin Corporation Nepheline syenite powder with controlled particle size and novel method of making same
KR101063545B1 (ko) * 2008-11-11 2011-09-07 (주) 알앤에이 분급장치
CN102430380B (zh) * 2010-09-29 2014-08-06 张小丁 流体激波反应器
US9914132B2 (en) * 2011-09-15 2018-03-13 Michael J. Pilgrim Devices, systems, and methods for processing heterogeneous materials
US9931639B2 (en) * 2014-01-16 2018-04-03 Cold Jet, Llc Blast media fragmenter
EP3307440A1 (de) * 2015-06-15 2018-04-18 NETZSCH Trockenmahltechnik GmbH Verfahren zum zerkleinern von mahlgut und mühle dafür
DE102015118858B3 (de) * 2015-11-04 2017-02-09 Netzsch-Feinmahltechnik Gmbh Zerkleinerungsvorrichtung und Verfahren zum Zerkleinern von Rohstoffen
CN205236215U (zh) * 2015-12-31 2016-05-18 江苏博迁新材料有限公司 一种高速导流气旋打散分级机
IT201600098452A1 (it) * 2016-09-30 2018-03-30 Micro Macinazione Sa Apparecchiatura per la micronizzazione di materiale polveroso con capacita’ di prevenire incrostazioni
CN106955774A (zh) * 2017-05-10 2017-07-18 成都赋阳技术开发有限公司 一种采用气流冲击方式进行分料的超微粉碎机
CN207169926U (zh) * 2017-08-04 2018-04-03 池州特乃博先进材料有限公司 一种流化床气流粉碎机

Also Published As

Publication number Publication date
SI3613508T1 (sl) 2024-03-29
DK3613508T3 (da) 2023-12-18
US20200061631A1 (en) 2020-02-27
CN110856830B (zh) 2022-04-15
US11235337B2 (en) 2022-02-01
LT3613508T (lt) 2023-12-27
FI3613508T3 (fi) 2023-12-19
JP6934491B2 (ja) 2021-09-15
EP3613508A1 (de) 2020-02-26
KR20200023208A (ko) 2020-03-04
ES2966925T3 (es) 2024-04-25
PL3613508T3 (pl) 2024-03-04
CN110856830A (zh) 2020-03-03
RU2732837C1 (ru) 2020-09-23
DE102018120596A1 (de) 2020-02-27
KR102277738B1 (ko) 2021-07-16
JP2020028877A (ja) 2020-02-27

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