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
  • B02C4/00—Crushing or disintegrating by roller mills
  • B02C4/28—Details
  • B02C4/32—Adjusting, applying pressure to, or controlling the distance between, milling members
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
  • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
  • B02C4/00—Crushing or disintegrating by roller 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
  • 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
  • B02C4/00—Crushing or disintegrating by roller mills
  • B02C4/28—Details
  • B02C4/286—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
  • B02C4/00—Crushing or disintegrating by roller mills
  • B02C4/28—Details
  • B02C4/32—Adjusting, applying pressure to, or controlling the distance between, milling members
  • B02C4/36—Adjusting, applying pressure to, or controlling the distance between, milling members in mills specially adapted for paste-like materials
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
  • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
  • B02C4/00—Crushing or disintegrating by roller mills
  • B02C4/28—Details
  • B02C4/42—Driving mechanisms; Roller speed control

Definitions

• the present invention relates to an apparatus and a method and to a calibration method for a control unit of an apparatus for comminuting particles in a flowable material according to the preamble of the independent claims.
• the following process parameters can be set: nip, roll contact pressure, roll temperature, millbase temperature as well as roll speed or roll speed.
• EP 2103223 discloses a method and an apparatus for reducing the particle size in a material insbesonde re ⁇ a chocolate mass, with a gap between two rollers is varied depending on the image taken by a driving motor of the rolls electric power.
• EP 0953291 describes a process for producing chocolate, wherein the nip between two rollers ge measure ⁇ and is compared with a reference value. Due to the difference detected, the rotational speed of one of the rollers is changed.
• An object of the present invention is to provide a device for comminuting particles in a flowable material, which prevents the disadvantages of the known and wel ⁇ che in particular allows a constant degree of comminution even with changing properties of the ground material. This object is achieved with a device according to claim 1.
• the device according to the invention for comminuting particles in a flowable material comprises at least one pair of rollers for which at least one process parameter, in particular the roller contact pressure of the rollers and / or the rotational speed of at least one of the rollers, can be set.
• the number of roller pairs is defined by the number of roller nips between the rollers.
• a pair of rollers usually consists of two rollers.
• the device comprises more than one Wal ⁇ zencru so, one and the same roller belong to different pairs of rollers. So it does not necessarily have twice as many rolls as pairs of rolls to be present.
• a roller pair may comprise only one roller, namely when the nip between a roller and a wall is formed.
• the apparatus further comprises a level gauge for measuring the level height of the flowable material in a nip or a roll trough upstream of the rolls.
• the level gauge can measure the level in the nip of the pair of rolls for which one process parameter is adjustable or in another upstream or downstream nip. Alternatively, the level can be measured in an upstream roller trough.
• the apparatus further has a control unit comprising at least one process parameter changes in dependence on the measured filling level of flowable ⁇ Ma terials.
• the device is particularly suitable for comminuting particles in a powder or a semi-liquid to produce a chocolate mass.
• the device is preferably a roller mill.
• the device has at least two rollers, which are arranged as a pair of rollers and are pressed against each other by ei ⁇ NEN contact pressure.
• further rollers may be arranged in the device.
• the device according to the invention may have four or five rollers.
• the number of rolls that are actively used during the crushing process can be variable.
• the number of activated rollers can be made dependent on the desired film thickness and / or on the mass to be comminuted. Thus, for example, only two or three rolls can be used at the beginning of a comminution process, and later, for example in the case of renewed passes of the flowable material through the device, further rolls can be added.
• Rollers which are to be deactivated can be designed so liftable that they do not come in the off-hook state with the flowable mass.
• a roller trough is preferably preceded by a roller trough, ie the roller trough is arranged in front of the rollers in the processing direction of the flowable material.
• the flowable mate rial is zenspalt ⁇ via a feed device, such as a storage bin or a feed belt, first in the Wal ⁇ or transported the roller trough.
• a feed device such as a storage bin or a feed belt
• the feed of the grinding stock under ei ⁇ nem constant mass flow takes place. That is, the supplied amount of the ground material per unit time is always the same during operation of the device.
• the supplied amount can be adjusted exactly ⁇ means of an appropriate delivery device.
• the rotation of the rolls advances the flowable material through the nip located between the rolls. Due to the contact pressure of the rollers and the shear forces generated by the rotational movement, the comminution of the particles contained in the flowable material takes place.
• These particles are, for example, sugar crystals, kaaaibs, milk powder or the like.
• At least one of the rollers of the roller pair is pressed against the second roller via a pressure device .
• both rollers have a pressure device, wherein both rollers are pressed against each other.
• the pressure device is for example a hydraulic piston or the like.
• a roller may also be arranged rigidly, while the second roller of the roller pair is pressed against the rigid roller.
• the rollers can also be arranged such that a different contact pressure can be set at both ends of the rollers.
• the rotational speed can be individually adjusted for each of the rollers of the roller pair. This can ⁇ example, via a separate speed control of the drive motors of the rolls take place or, alternatively, via variable transmission between a common drive motor and the individual rollers.
• the apparatus preferably has at least one sensor which zenspalt the filling level of flowable material in Wal ⁇ and / or measures in the roller trough. In order to improve the measurement accuracy, the device may also have several sensors that measure the level height. Preferably, these are contactless sensors.
• Measurement of the fill level in the nip in the sense of this application means measuring the fill level of a mill deposit above the nip.
• the millbase collecting in front of the nip forms this millbase depot.
• the control unit changes at least one process parameter in dependence on the measured filling ⁇ standing height of the flowable material in the nip or in the roller trough.
• the control unit is preferably a microcontroller unit.
• the control unit can be adjusted to a desired value for the Hugheshal ⁇ tend filling level, for example via a entranc ⁇ before direction preferred.
• the control unit is preferably madestal ⁇ tet, that at a predetermined deviation of the target value of the level, for example, by 5cm, the change at least one process variable by a certain value, for example, the rotational speed of the rollers is reduced by 50 revolutions per minute.
• the control unit in this case has an additional storage unit, in which, for example, level setpoints for various grinding material and / or Ge, for ver ⁇ different to be achieved degrees of comminution of the particles are ⁇ stores. Furthermore, specific change values of the process parameters may be stored for different grinding properties and / or for different degrees of reduction to be achieved.
• the control unit changes the contact pressure of the rollers and / or the rotational speed of at least one of the rollers.
• further process parameters by the control unit could be changed as beispielswei ⁇ se of the roll gap or the feed rate of fliessfä- ELIGIBLE material into the nip or in the rolling pan. The feed rate can be adjusted, for example, via the pumping power to convey the flowable material.
• Changes in the mechanical, physicochemical or structural properties of a flowable material affect the throughput of the material between the rolls.
• ⁇ rate of the material By measuring the filling level of flowable material in the nip or in the roller trough of this can be calculated by ⁇ rate of the material at any time. Either the change in filling height per unit time is then calculated or it is checked via ⁇ whether the level at constant introduction of fliessfä- higem material into the nip or in the roller trough remains the same height, ie, the amount corresponding to of supplied material that amount which is drawn in between the rollers in the same time unit.
• the throughput through a nip can also be determined by a comparison of inflowing and outflowing quantities, which are each determined, for example, with a flow meter.
• the material to be ground is introduced into a roller trough or into the nip at a constant mass flow rate by means of a feed device. If a constant fill level in the roll trough or in the nip is changed by changing the contact pressure of the rolls and / or the rotational speed min. adhered to at least one roller, the throughput and thus the degree of comminution can be kept constant.
• the throughput can be measured by means of a direct measurement in the feed device, the discharge device or in the device.
• the feeding device can be configured such that the amount of ground material introduced into the nip or the roller trough can be adjusted.
• the device according to the invention thus enables the comminution of particles in a flowable material at a constant throughput and at a constant degree of comminution of the particles, even if the properties of the flowable material supplied to the pair of rollers change.
• the level meter preferably comprises an optical or acoustic sensor.
• the sensor can measure, for example, by means of a laser beam, infrared rays or ultrasonic waves level in the nip or in the roller trough.
• the use of such sensors allows a contactless measurement of the level height of the flowable material in the nip or in the roll trough.
• the measurement can be done at a certain point, one-dimensional or multi-dimensional. As eindi ⁇ dimensional measurement, the determination is understood in only one spatial direction, ie, in this case, a filling level measurement along one spatial direction.
• a multi-dimensional measurement can be used, for example, to determine the filling level volume or other geometric quantities. With the inventive device can be selectively measured, single and multi-dimensional filling ⁇ stand heights determine in a short time to real time.
• the level meter preferably comprises a camera directed onto the nip and an image evaluation unit which is used for Calculation of the level height based on a camera image is suitable.
• an image evaluation unit which is used for Calculation of the level height based on a camera image is suitable.
• the image analysis unit preferably has a corresponding evaluation software, which allows the gleichzei ⁇ term determining the filling level at various points within the roll gap or the roller trough.
• the evaluation unit Before ⁇ geous enough, the evaluation unit also has a ⁇ An see showing the captured by the camera in real time to ⁇ so that it is possible for the operator to check the level optically.
• the control unit is preferably configured such that, when to ⁇ guidance of the flowable material with a constant volume flow in the roll nips or in the roller trough the filling ⁇ standing height of the flowable material in the nip or in the roller trough by varying the pressing pressure and / or the rotational speed of at least one of Rolls to a terme ⁇ agreed or predeterminable value is maintained.
• This can ensure that, despite changing own sheep ⁇ th of the flowable material, particularly when the flowable material passes by means of a recirculation ⁇ a plurality of through passages through the same rolling mill, that a constant flow is ensured.
• This throughput can also be kept constant only during time-defined periods on a value or a range of values.
• the time periods can be adjusted, for example, based on empirical values or these are defined based on changes in the fill level.
• Constant volume flow in the sense of the present application, it is understood that the same volume of flowable material is supplied and / or conveyed per unit of time.
• a feed device for feeding the flowable material into the nip or in the roll trough is arranged in the material flow direction in front of the rollers. This allows light ⁇ feeding flowable material into the nip or in the roller trough, particularly preferably with a ⁇ an adjustable and / or constant flow.
• the device may be equipped with a return means leading at least part of the already ge through the rollers ⁇ feed material again by the at least one pair of rolls.
• the nips can be traversed by the crowd so often ⁇ until the desired film thickness is reached.
• multiple passes through the rollers for example, with a two- or three-roll mill, the same result can be achieved as with a Bookwal zwerk.
• the device preferably also has a measuring device for determining the particle thickness in the millbase, in particular a fineness measuring device or a film thickness gauge. It may be an electro-magnetic, opto-electronic, akusti ⁇ specific or mechanical measuring means.
• the measuring device is mounted in the vicinity of a grinding roller and the fineness or film thickness on the grinding roller is measured. Al ⁇ tively, the measuring device may be mounted on a separate roller discharge and the fineness or layer thickness are measured on this.
• a fineness measuring device using light in the near-infrared range is used for the fineness measurement.
• the wavelength is ist ⁇ agrees to the material to be measured, so that the amount of de-defined ⁇ product ingredients, such as sugar and fat can be determined from the absorbed radiation, which correlates with the fineness of the product.
• the correlation relationship is product-specific and must first be determined by calibration.
• the device emits infrared light onto a product layer on a roller, measures the amount of light reflected and calculates the fineness of the product in microns.
• a purge air protects the measuring device ⁇ window from contamination.
• the device has a control unit, which ensures that at least a portion of the material is passed into the return device when the fineness, or the film thickness has not yet reached the desired size.
• control unit is designed such that the desired size is adjustable according to customer requirements.
• Ultra-fine chocolate as is often required for example in the Asian Chicks rule ⁇ market, requires film thicknesses from 12 to 18 microns. As a rule, however, chocolates with film thicknesses between 18 and 30 microns are perceived as fine chocolates, since smaller structures can not be resolved by the receptors of the tongue.
• the invention also relates to a device, in particular as described above, for comminuting particles in a flowable material, in particular a powder or a semi-liquid for producing a chocolate mass.
• the pre ⁇ direction comprises at least one roll pair for which Minim ⁇ least one process parameter, in particular, the roll pressure, the temperature and / or the rotational speed of at least one of the rollers is adjustable, and means for detecting the flow rate of the flowable material through a nip.
• the device further comprises a control unit, wel ⁇ che depending on the measured flow rate of the flowable material in the nip or in response to the change ⁇ tion of throughput at least one process parameters, in particular ⁇ special selected from the roll contact pressure, the nip and the rolling speed of at least one the rollers, as well as combinations thereof, changed.
• a control unit wel ⁇ che depending on the measured flow rate of the flowable material in the nip or in response to the change ⁇ tion of throughput at least one process parameters, in particular ⁇ special selected from the roll contact pressure, the nip and the rolling speed of at least one the rollers, as well as combinations thereof, changed.
• the process parameters are adjustable.
• the device for detecting the throughput preferably comprises at least one measuring device for a parameter, on the basis of which the throughput can be determined.
• the measuring device may be a level gauge.
• the throughput can also be determined by means of a flow meter or from the Mengendiffe ⁇ ence of outflowing and inflowing mass, which can be determined by a volume or weight measurement.
• the control unit is preferably designed so that fixed constant throughput is achieved.
• the invention also relates to a plant for comminuting particles in a flowable material, in particular in powders or semi-liquids for producing a chocolate mass, in which a plurality of devices for comminuting, as described above, are arranged one behind the other in the material flow direction.
• the respective devices can preferably be coupled into the material flow, so that the number of devices involved in the comminution process can be selected.
• a further aspect of the present invention relates to a method for comminuting particles in a flowable material.
• the particles are comminuted between at least one pair of rollers.
• the process parameters of at least one pair of rollers are adjustable.
• the throughput of the flowable material is detected by a nip or a level height of the flowable material in a nip or in a roller trough, which is ei ⁇ nem roller pair upstream, measured.
• the throughput is measured through a nip or level in the nip of the pair of rolls whose process parameters are adjustable.
• At least one process parameter in particular a process parameter of a Roller pair, further in particular the roll contact pressure and / or the rolling speed of at least one of the Wal ⁇ zen changed.
• the temperature of at least one roller can be changed.
• the roll nip or roll trough kontinuier ⁇ Lich flowable material is preferably fed, for example via a loading ⁇ schickungsband.
• the level is particularly preferably continuously measure ⁇ ge.
• the level height of the flowable material in the nip and / or in the roller trough is preferably measured without contact, in particular with an acoustic or optical sensor.
• Non-contact sensors have the advantage that the measured data are falsified by sticky material. In addition, these only need to be cleaned a lens, which reduces the maintenance.
• the throughput can be determined by level measurement.
• the throughput can also be a flow measurement or a difference of outflowing and zufliessender amount, ie for Example of volume or weight measurements of the inflowing and / or outflowing mass, are determined.
• a target value or a target value range for the flow rate and / or the fill level is preferably determined and the Minim ⁇ least one process parameter is automatically changed such that the flow rate and / or the measured filling level corresponds to the specified differently set point or is within the desired value range.
• a set point range in this application is an area within which the throughput or the fill level can be ⁇ place without a control intervention takes place. That is, for example, small variations in the liquid level cause even not attempt to modify ⁇ tion of the process parameters, but only leaving the standard value by the measured liquid level.
• the material to be ground is additionally comminuted with preset process parameters by the at least one pair of rollers until a stationary state has set.
• the process parameters are preferably changed automatically by a control unit.
• the control unit is preferably set or adjustable such that a change in the fill level height by a specific value causes the change of at least one process parameter by a defined value.
• a minimum gap width can be set in the device which at least during operation is set to a minimum width. can not be exceeded during the startup of the device.
• the minimum gap width may preferably be an ent ⁇ speaking mechanics. The specification of a minimum gap width simplifies the approach of the roll mill, since the material to be ground is drawn in better than when the rolls are pressed together completely.
• the pressure for a certain time can be reduced even when starting the roll mill until a entspre ⁇ chender throughput of material is achieved.
• a calibration step may initially be carried out in which the relationship between the degree of comminution and at least one process parameter is determined.
• the associated degree of comminution is then determined and it can be created a process variable map, which can be deposited accordingly in the control unit or in a control device and used for control.
• a calibration step takes place in which the nominal value or the nominal value range of the fill level height is determined.
• the relationships between the process parameters, the fill level, the throughput and the degree of comminution of the particles can be determined.
• the film thickness is preferably measured on at least one roller, in particular with a film thickness meter which has a sensor for detecting the film thickness.
• the inventive method again ⁇ obtained, so the composition is more preferably further crushed by the at least one roller pair.
• the method comprises a step test in which it is determined whether a test variable reaches the special ⁇ a measured fineness or film thickness, a target value and / or exceeded or dropped below.
• the method comprises a control step, wherein the preceding method steps are repeated as long as the test variable, in particular the measured fineness or film thickness, the desired value has not yet been reached.
• the method comprises a control step, wherein one or more additional rollers are activated so ⁇ soon the test quantity has reached a desired value.
• the method includes a setting step, with which at least one target variable, in particular a ge ⁇ desired fineness or film thickness, or a sequence of target sizes is specified.
• a further aspect of the present invention relates to a device for comminuting particles in a flowable material, in particular a powder or a semi-liquid for producing a chocolate mass, which allows a substantial increase in throughput, in particular for a device as described above.
• the inventive device comprises at least one rolling ⁇ few.
• the device further comprises at least ei ⁇ ne further roller, which is pressed against the roller pair. More preferably, the device may also have further rollers, which are arranged sequentially one behind the other and are pressed against each other.
• At least one process parameter of the at least one roller pair or the at least one to ⁇ sharmlichen roller can be changed, in particular the contact pressure and / or the roll rotational speed at least ei ⁇ ner of the rolls.
• at least one roller of the roller pair and / or at least one further roller is embodied as bom ⁇ b istslose roller.
• the crownless roller has a stiff Kernman ⁇ tel, preferably made of steel, and a thin wall. Between the core shell and the wall is also an elastic
• the core sheath can be designed as a hollow roll with stei ⁇ fem roll shell.
• Such rolls are, for example, in EP 0712469 ⁇ be written and allow a constant reduction ratio over the entire roll length, even with changing pressure in the nip.
• the advantage over the commonly incorporated ⁇ translated cambered rollers is that at any pressure in the roll gap that always has a constant width over the entire length.
• the at least one process parameter is at ⁇ basis of a measured value, in particular a filling level of the ground material in the nip or in a said at least one pair of rolls upstream rolling pan, changed.
• the device allows a well controllable and rapid flow of the rolling process, which leads to a defined degree of shredding ⁇ degree of the particles and thus guarantees a good product quality.
• Fig. 1 a schematic representation of a first example of an inventive device
• FIG. 2 shows a schematic representation of a second example of an apparatus according to the invention
• FIG. 3 is a schematic representation of a third example of a device according to the invention.
• FIG. 4 shows a schematic representation of a fourth example of a device according to the invention.
• Fig. 5 a schematic representation of a fifth example of an inventive device.
• FIG. 1 shows a schematic representation of a device 1 according to the invention.
• the device 1 has at least two rollers 2, 3 arranged as roller pairs. Zwi ⁇ tween the rollers 2,3 a nip 14 is present.
• Each of the two rollers 2, 3 of the roller pair is driven by a separate, speed-controlled motor 6, 7.
• the contact pressure between the rollers 2, 3 is adjusted via a pressure regulator 8. provides.
• a roller trough 4 is arranged, the flowable material 13 by a feed device 9 is ⁇ leads.
• the level 5 of the flowable material 13 in the roll trough 4 is measured by a level gauge 11.
• the direction of measurement of the gauge 11 is such that the filling height ⁇ stand 5 of the flowable material can be gemes ⁇ sen in the roller trough. 4
• the measured filling level is forwarded to a re ⁇ gel unit 10th
• at least one process parameter is changed by the control unit 10.
• the rotational speed of at least one roller 2, 3 is changed via the rotational speed of the associated motor 6, 7.
• the contact pressure of the rollers 2, 3 can be changed via the pressure regulator 8.
• a high contact pressure is required, e.g. 35 bar, which results in a correspondingly smaller throughput of the flowable material. Therefore, by increasing the roller speeds at a constant high pressure, the throughput can be increased.
• a material to be ground is milled at a set starting pressure in the nip of 28 bar and rolling speeds of 50 rpm for a first roller and 100 rpm for the second roller of the pair of rollers. This results in a throughput of 800 kg / h at a degree of comminution of particles in the material to be ground to 30 ⁇ .
• the throughput is reduced to 600 kg / h, the degree of comminution of the particles falling to 20 ⁇ .
• the flow rate can be set to the original 800 kg / h with a degree of crushing of the Particles of 20 ⁇ .
• a continuous process is achieved, when the filling ⁇ standing height of the millbase in the nip or in the Minim a ⁇ least a pair of rolls upstream rolling pan remains constant. In this state, the process parameters are set such that the supplied amount of ground material of the discharged amount ent ⁇ speaks, so a preselected throughput is reached.
• Figure 2 shows a schematic representation of a second case ⁇ game for a device of the invention one hundred and first
• a roller 102 forms a nip 114 with a fixed wall 115.
• a process parameter of the roller 102 e.g. the roll contact pressure or the rotational speed can be controlled.
• Figure 3 shows a schematic representation of a third case ⁇ game for a device of the invention two hundred and first
• Two equal size rollers 202, 203 form a first pair of rollers 220 for which a process parameter, e.g. the roll contact pressure or the rotational speed of at least one of the rollers 202, 203 is adjustable.
• a process parameter e.g. the roll contact pressure or the rotational speed of at least one of the rollers 202, 203 is adjustable.
• rollers 202, 203 is preceded by a further roller 216 with a smaller diameter, which serves as an applicator roll and with ei ⁇ ner of the rollers 203 forms another pair of rollers.
• the applicator roll 216 forms a trough wall 218 a whale ⁇ zentrog 204th
• a process parameter of the roller pair 220 for example, the roll pressure or the rotational speed Minim ⁇ least a roller 202, 203, are regulated.
• Figure 4 shows a schematic representation of a fourth ⁇ In the game for an inventive device 301 in the form of another example of a three-roll mill.
• a smaller diameter roll 316 is downstream of a pair of rolls 320 with two larger rolls 302, 303.
• a process parameter of the rolling pair 320 e.g. the roll contact pressure or the rotational speed of at least one roller 302, 303, or the second roller pair 321, e.g. the roll contact pressure or the rotational speed of at least one roller 303, 316, are regulated.
• Figure 5 shows a schematic illustration of a fifth game for a ⁇ In inventive apparatus 401, in the form of another example of a three-roll mill.
• the three-roll mill also has two pairs of rollers 420, 421.
• a process parameter of the rolling pair 420 for example the roll contact pressure or the rotational speed of at least one roll 402, 403 or the second roller pair 421, for example, the roller contact pressure or the rotational speed of at least one roller 403, 416 are controlled.
• a fineness measuring device which is not explicitly shown in the figure, can be provided, which determines the fineness of the product located on the discharge roller 416. Has not yet reached a specified setpoint fine ⁇ ness, the product can be returned to the first nip 414th

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• 2012
  • 2012-05-14 EP EP12721829.5A patent/EP2707138A2/de not_active Withdrawn
  • 2012-05-14 CA CA2835799A patent/CA2835799A1/en not_active Abandoned
  • 2012-05-14 UA UAA201312891A patent/UA113169C2/uk unknown
  • 2012-05-14 BR BR112013028738A patent/BR112013028738A2/pt not_active Application Discontinuation
  • 2012-05-14 WO PCT/EP2012/058945 patent/WO2012152951A2/de active Application Filing
  • 2012-05-14 JP JP2014509770A patent/JP2014512958A/ja active Pending
  • 2012-05-14 RU RU2013155179/13A patent/RU2603727C2/ru active
  • 2012-05-14 US US14/116,431 patent/US10159985B2/en not_active Expired - Fee Related
  • 2012-05-14 CN CN201280022924.0A patent/CN103547372B/zh not_active Expired - Fee Related

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