EP2874750B1 - Procédé et installation de comminution de matière à broyer à l'aide d'un broyeur à cylindres - Google Patents
Procédé et installation de comminution de matière à broyer à l'aide d'un broyeur à cylindres Download PDFInfo
- Publication number
- EP2874750B1 EP2874750B1 EP13736838.7A EP13736838A EP2874750B1 EP 2874750 B1 EP2874750 B1 EP 2874750B1 EP 13736838 A EP13736838 A EP 13736838A EP 2874750 B1 EP2874750 B1 EP 2874750B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- grinding
- drives
- mass flow
- power
- rollers
- 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.)
- Not-in-force
Links
- 238000000034 method Methods 0.000 title claims description 13
- 239000000463 material Substances 0.000 claims description 21
- 239000000654 additive Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000015556 catabolic process Effects 0.000 claims 1
- 238000009434 installation Methods 0.000 description 4
- 239000003245 coal Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 239000012615 aggregate Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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
- B02C25/00—Control arrangements specially adapted for crushing or disintegrating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/007—Mills with rollers pressed against a rotary horizontal disc
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/02—Centrifugal pendulum-type 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
Definitions
- the invention relates to a method and a plant for the comminution of ground material with a roller mill, wherein a grinding table cooperates with at least two, driven by their own drive grinding rollers and crushed in the mass flow material is comminuted between the grinding table and grinding roller.
- the compensation control is formed by a power compensation control, wherein the power of the drives is controlled in a predetermined ratio to each other by controlling the speed of at least one drive.
- a regulation of the grinding pressure is used to regulate the power of the drives in a predetermined relationship to one another.
- the EP 0 180 814 A2 discloses a roller mill with a control system to operate the mill over a wide flow range, ensuring a satisfactory air-to-solid ratio and degree of fineness.
- the invention was based on the object to develop a new concept of power balancing.
- a grinding table cooperates with at least two grinding rollers, whereby the millbase supplied in the mass flow is comminuted between the grinding plate and the grinding roller.
- At least two grinding rollers are driven by their own drives, whereby a power compensation control for the drives of the grinding rollers is performed, so that the performance of the drives is controlled in a predetermined ratio to each other.
- the power control is carried out by changing the mass flow of at least one of the grinding rollers supplied grinding material.
- the inventive plant for the comminution of ground material with a roller mill has a grinding table and at least two cooperating with the grinding table grinding rollers, wherein the mass flow supplied grinding material is comminuted between the grinding table and grinding roller, and wherein at least two grinding rollers have their own drive and a power compensation for the Drives of the grinding rollers for controlling the power of the drives in one predetermined ratio is provided to each other.
- the power balancing control cooperates with at least one actuator to change the mass flow of at least one of the grinding rollers supplied grinding material.
- mass flow is understood to mean the mass flow or mass flow which is usually applied centrally via a feed device to the grinding plate and then conducted to the grinding rollers. While the power compensation regulation known from the prior art acts directly on the grinding rollers by regulation of the rotational speed or the grinding pressure, the concept according to the invention for power compensation control proposes influencing the mass flow.
- the power compensation control preferably uses the torque and / or the speed of the drives as a controlled variable.
- the change in the mass flow can be effected in particular by influencing the orientation of the mass flow with respect to the grinding roller and / or influencing the width of the mass flow and / or influencing the height of the mass flow and / or influencing the quantity supplied.
- it can be provided to precompress or loosen up the ground material supplied in the mass flow.
- the power compensation control device is expediently with torque sensors for detecting the torque of the drives of the grinding rollers and / or with speed sensors for detecting the rotational speed of the drives Grinding rollers in operative connection, then depending on the measurement result, at least one actuator to control the mass flow to control.
- actuators can be formed for example by guide elements, adjustable chutes, adjustable height limits and metering devices.
- the drives of the grinding rollers are in particular unregulated three-phase electrical asynchronous motors in question.
- the performance of the drives can basically be controlled so that the operating torques of the drives are between zero and the overturning moment of the drives. In this way, the drives of the grinding rollers can be adapted to the respective grinding requirements in a wide range.
- Fig. 1 shown plant for crushing regrind with a roller mill has a grinding table 1 and at least two with the grinding table cooperating grinding rollers 2, 3, wherein the mass flow in a feed device 4 supplied grinding material 5 is comminuted between grinding plate and grinding roller.
- Each of the two grinding rollers 2, 3 has its own drive 6, 7, while the grinding table in the illustrated embodiment on the grinding rollers 2 and 3 and the material to be ground 5 is driven and thus no own drive is assigned. In the context of the invention, however, the grinding table can also be driven.
- a power compensation control device 8 is provided, which interacts with measuring members 9, 10 and at least one actuator 11.
- the measuring members 9, 10 are formed for example by torque sensors for detecting the torque M1, M2 of the drives 6 and 7 and / or by speed sensors for detecting the rotational speed n1, n2 of the drives 6, 7. With the measured values, the power compensation control device 8 can determine the power of the two drives 6, 7.
- the aim is to divide the total power of all drives in a given ratio to the individual drives. It can be provided, for example, that all drives are operated with the same power. However, it is quite conceivable that the services evaluate differently divided, which may be the case for example with different sized grinding rollers.
- the power compensation control device regulates the power of the individual drives so that the powers are within a predetermined target range. If it is ascertained via the measured values (rotational speed, torque) that the power of one or the other drive is outside the setpoint range, a targeted influencing of the mass flow of the grinding material 5 supplied to at least one of the grinding rollers 2, 3 is undertaken via the actuator 11. This may, for example, be such that the grinding roller, the drive of which has increased power, is supplied with less material to be ground than the grinding roller, whose drive consumes a power that is too low. In this way, the power of the two drives 6, 7 can be influenced in a targeted manner via the change in the mass flow in order to regulate the power of the two drives in the predetermined ratio of, for example, 50% in each case.
- drives 6, 7 are equipped with expensive control devices, such as frequency converters.
- control devices such as frequency converters.
- three-phase electrical asynchronous motors are used as drives 6, 7.
- the plant described above is particularly suitable for the comminution of regrind, such as limestone, binder and coal.
- the roller mill can be designed, for example, as follows: Diameter of the grinding table 1: 2 m to 8 m Diameter of the grinding roller 2, 3: 1 m to 4 m Rated power of the drives 6, 7: 100 kW to 4000 kW
- the actuator is formed by a provided at the lower end of the task device 4, pivotable chute 11a, which is pivotable via an actuator 11b.
- the power compensation control device 8 will therefore correspondingly control the actuator 11b as a function of the measured values determined by the measuring members 9, 10 if the powers of the two drives 6, 7 are outside their predetermined control ranges.
- the actuator is formed by an adjustable guide plate 11c with associated actuator 11b.
- this baffle 11c in particular, the orientation of the mass flow with respect to the grinding roller and / or the width of the mass flow and / or the amount supplied.
- Fig. 4 shows the variant in which the mass flow is changed by influencing its height.
- the actuator is formed by a height limiting element 11e that can be adjusted by an elevation 11f in height by the power compensation control device 8.
- the mass flow is influenced by changing its composition.
- the actuator is formed by a metering device 11g with associated actuator 11h, 11g additives are added to the material to be ground via the metering device 11g, such as fresh, circulating or finished good, coal, aggregates, water or grinding aids. If this addition occurs specifically before a grinding roller, the power consumption of the associated drive can be influenced in a targeted manner.
- each grinding roller can be preceded by a so-called slave roller, which enables a pre-compression of the grinding bed and thus influencing the power consumption of the drives associated grinding roller via a variable contact pressure.
- a loosening of the grinding bed for example by fluidizing air, is conceivable.
- the power compensation control described above is on the one hand very effective and considerably cheaper compared to the known from the prior art speed control.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Claims (12)
- Procédé de broyage de matière à broyer (5) à l'aide d'un broyeur à cylindres, dans lequel un plateau de broyage (1) coopère avec au moins deux cylindres de broyage (2, 3) et la matière à broyer (5) amenée en un flux massique est broyée entre le plateau de broyage (1) et les cylindres de broyage (2, 3), dans lequel au moins deux cylindres de broyage (2, 3) sont entraînés par des entraînements propres (6, 7) et on effectue une régulation de l'équilibre de puissance pour les entraînements (6, 7) des cylindres de broyage (2, 3), de telle manière que la puissance des entraînements (6, 7) soit régulée l'une par rapport à l'autre dans un rapport prédéterminé, caractérisé en ce que l'on effectue la régulation de puissance par la variation du flux massique de la matière à broyer (5) amenée à au moins un des cylindres de broyage (2, 3).
- Procédé selon la revendication 1, caractérisé en ce que l'on utilise le couple de rotation (M1, M2) et/ou le nombre de tours (n1, n2) des entraînements (6, 7) comme grandeur de réglage de la régulation de l'équilibre de puissance.
- Procédé selon la revendication 1, caractérisé en ce que l'on effectue la variation du flux massique en influençant l'orientation du flux massique par rapport au cylindre de broyage (2, 3) et/ou en influençant la largeur du flux massique et/ou en influençant la hauteur du flux massique et/ou en influençant la quantité amenée.
- Procédé selon la revendication 1, caractérisé en ce que l'on pré-comprime la matière à broyer (5) amenée dans le flux massique.
- Procédé selon la revendication 1, caractérisé en ce que l'on désagrège la matière à broyer (5) amenée dans le flux massique.
- Procédé selon la revendication 1, caractérisé en ce que l'on régule la puissance des entraînements (6, 7) des cylindres de broyage (2, 3) de telle manière que les couples de fonctionnement des entraînements (6, 7) se situent entre zéro et le couple de décrochage des entraînements.
- Procédé selon la revendication 1, caractérisé en ce que l'on effectue la variation du flux massique en faisant varier la composition de la matière à broyer (5).
- Procédé selon la revendication 7, caractérisé en ce que l'on fait varier le flux massique par l'addition d'auxiliaires de broyage et/ou d'eau et/ou de substances d'addition.
- Procédé selon la revendication 7, caractérisé en ce que l'on fait varier le flux massique par addition de matière grossière et/ou de matière fraîche et/ou de matière de retour et/ou de gravier et/ou de matière terminée.
- Installation pour le broyage de matière à broyer (5) avec un broyeur à cylindres, qui présente un plateau de broyage (1) et au moins deux cylindres de broyage (2, 3) qui coopèrent avec le plateau de broyage (1), dans laquelle la matière à broyer (5) amenée en un flux massique est broyée entre le plateau de broyage (1) et les cylindres de broyage (2, 3), et dans laquelle au moins deux cylindres de broyage présentent un entraînement propre (6, 7) et il est prévu un dispositif de régulation de l'équilibre de puissance pour les entraînement (6, 7) des cylindres de broyage (2, 3) pour la régulation de la puissance des entraînements (6, 7) dans un rapport prédéterminé l'une par rapport à l'autre, caractérisée en ce que le dispositif de régulation de l'équilibre de puissance (8) coopère avec au moins un organe de réglage (11) pour faire varier le flux massique de la matière à broyer (5) amenée à au moins un des cylindres de broyage (2, 3).
- Installation selon la revendication 10, caractérisée en ce que le dispositif de régulation de l'équilibre de puissance (8) est en liaison active avec des capteurs de couple de rotation pour la détection du couple de rotation des entraînements (6, 7) des cylindres de broyage et/ou avec des capteurs de nombre de tours pour la détection du nombre de tours des entraînements (6, 7) des cylindres de broyage (2, 3).
- Installation selon la revendication 10, caractérisée en ce que les entraînements (6, 7) des cylindres de broyage (2, 3) sont des moteurs électriques asynchrones à courant triphasé non régulés.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102012106554.3A DE102012106554A1 (de) | 2012-07-19 | 2012-07-19 | Verfahren und Anlage zur Zerkleinerung von Mahlgut mit einer Rollenmühle |
PCT/EP2013/064043 WO2014012792A2 (fr) | 2012-07-19 | 2013-07-03 | Procédé et installation de comminution de matière à broyer à l'aide d'un broyeur à cylindres |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2874750A2 EP2874750A2 (fr) | 2015-05-27 |
EP2874750B1 true EP2874750B1 (fr) | 2018-01-10 |
Family
ID=48790393
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP13736838.7A Not-in-force EP2874750B1 (fr) | 2012-07-19 | 2013-07-03 | Procédé et installation de comminution de matière à broyer à l'aide d'un broyeur à cylindres |
Country Status (7)
Country | Link |
---|---|
US (1) | US10464072B2 (fr) |
EP (1) | EP2874750B1 (fr) |
JP (1) | JP6278527B2 (fr) |
CN (1) | CN105102130B (fr) |
DE (1) | DE102012106554A1 (fr) |
DK (1) | DK2874750T3 (fr) |
WO (1) | WO2014012792A2 (fr) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012106554A1 (de) * | 2012-07-19 | 2014-05-15 | Thyssenkrupp Resource Technologies Gmbh | Verfahren und Anlage zur Zerkleinerung von Mahlgut mit einer Rollenmühle |
CN108318362B (zh) * | 2018-02-05 | 2023-07-25 | 西华大学 | 一种滚压状态下的固态颗粒性能测定系统 |
JP7205690B2 (ja) * | 2018-12-12 | 2023-01-17 | Ubeマシナリー株式会社 | 竪型粉砕機 |
US10758912B1 (en) * | 2019-04-11 | 2020-09-01 | Gene P. Guthmiller | Material processing system |
DE102019210047B3 (de) * | 2019-07-08 | 2020-06-18 | Thyssenkrupp Ag | Vertikal-Rollenmühle |
WO2021226651A2 (fr) * | 2020-05-13 | 2021-11-18 | Rubble Master Hmh Gmbh | Procédé pour régler un concasseur |
CN111732894B (zh) * | 2020-07-01 | 2021-08-31 | 青岛美尔高科技开发有限公司 | 一种高稳定性水性涂料的制备工艺 |
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DE102008036784C5 (de) * | 2008-08-07 | 2013-06-20 | Thyssenkrupp Polysius Ag | Rollenmühle und Verfahren zur Zerkleinerung von Mahlgut |
KR101092370B1 (ko) * | 2009-06-24 | 2011-12-09 | 한국생산기술연구원 | 금속 절삭칩 재생장치 |
DE102010016011A1 (de) * | 2010-03-18 | 2011-09-22 | Polysius Ag | Rollenmühle |
DE102010016472C5 (de) * | 2010-04-16 | 2017-11-23 | Thyssenkrupp Industrial Solutions Ag | Wälzmühle |
DE102010038197B4 (de) * | 2010-10-14 | 2012-08-30 | Thyssenkrupp Polysius Ag | Wälzmühle zur Zerkleinerung von sprödem Mahlgut |
US8602338B2 (en) * | 2010-11-22 | 2013-12-10 | Alstom Technology Ltd | Oscillation monitor for pulverizer journal assembly |
FR2977170B1 (fr) * | 2011-06-29 | 2013-08-09 | Cie Engrenages Et Reducteurs Messian Durand | Dispositif d'entrainement pour broyeur, et broyeur correspondant |
DE102012106553B4 (de) * | 2012-07-19 | 2014-05-22 | Thyssenkrupp Resource Technologies Gmbh | Zerkleinerung von Mahlgut in einer Vertikalrollenmühle |
DE102012106554A1 (de) * | 2012-07-19 | 2014-05-15 | Thyssenkrupp Resource Technologies Gmbh | Verfahren und Anlage zur Zerkleinerung von Mahlgut mit einer Rollenmühle |
DE102012107043B4 (de) * | 2012-08-01 | 2017-08-17 | Thyssenkrupp Industrial Solutions Ag | Rollenmühle und Verfahren zum Zerkleinern von Mahlgut mit einer Rollenmühle |
-
2012
- 2012-07-19 DE DE102012106554.3A patent/DE102012106554A1/de not_active Withdrawn
-
2013
- 2013-07-03 WO PCT/EP2013/064043 patent/WO2014012792A2/fr active Application Filing
- 2013-07-03 US US14/415,606 patent/US10464072B2/en not_active Expired - Fee Related
- 2013-07-03 EP EP13736838.7A patent/EP2874750B1/fr not_active Not-in-force
- 2013-07-03 DK DK13736838.7T patent/DK2874750T3/en active
- 2013-07-03 CN CN201380038381.6A patent/CN105102130B/zh active Active
- 2013-07-03 JP JP2015522032A patent/JP6278527B2/ja active Active
Also Published As
Publication number | Publication date |
---|---|
CN105102130B (zh) | 2019-01-11 |
WO2014012792A3 (fr) | 2014-04-17 |
JP6278527B2 (ja) | 2018-02-14 |
CN105102130A (zh) | 2015-11-25 |
EP2874750A2 (fr) | 2015-05-27 |
US10464072B2 (en) | 2019-11-05 |
US20150224512A1 (en) | 2015-08-13 |
JP2015522414A (ja) | 2015-08-06 |
DK2874750T3 (en) | 2018-04-23 |
DE102012106554A1 (de) | 2014-05-15 |
WO2014012792A2 (fr) | 2014-01-23 |
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