EP3546625A1 - Feeding device of a carding machine - Google Patents
Feeding device of a carding machine Download PDFInfo
- Publication number
- EP3546625A1 EP3546625A1 EP19162734.8A EP19162734A EP3546625A1 EP 3546625 A1 EP3546625 A1 EP 3546625A1 EP 19162734 A EP19162734 A EP 19162734A EP 3546625 A1 EP3546625 A1 EP 3546625A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- feed
- fiber
- feed channel
- fan
- control
- 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
Links
- 238000009960 carding Methods 0.000 title claims abstract description 31
- 239000000835 fiber Substances 0.000 claims abstract description 164
- 239000002657 fibrous material Substances 0.000 claims abstract description 40
- 238000000034 method Methods 0.000 claims abstract description 13
- 238000009530 blood pressure measurement Methods 0.000 claims abstract description 4
- 238000012937 correction Methods 0.000 claims description 8
- 238000004260 weight control Methods 0.000 claims description 8
- 230000008859 change Effects 0.000 claims description 7
- 238000012546 transfer Methods 0.000 claims description 5
- 238000005259 measurement Methods 0.000 description 9
- 230000033228 biological regulation Effects 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 7
- 230000006835 compression Effects 0.000 description 6
- 238000007906 compression Methods 0.000 description 6
- 238000013461 design Methods 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005056 compaction Methods 0.000 description 3
- 244000144992 flock Species 0.000 description 3
- 230000001965 increasing effect Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 229920000742 Cotton Polymers 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 241000123589 Dipsacus Species 0.000 description 1
- 229920000297 Rayon Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 230000003827 upregulation Effects 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G15/00—Carding machines or accessories; Card clothing; Burr-crushing or removing arrangements associated with carding or other preliminary-treatment machines
- D01G15/02—Carding machines
- D01G15/12—Details
- D01G15/40—Feeding apparatus
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
- D01G23/00—Feeding fibres to machines; Conveying fibres between machines
- D01G23/02—Hoppers; Delivery shoots
- D01G23/04—Hoppers; Delivery shoots with means for controlling the feed
Definitions
- the present invention relates to a device for feeding of fiber material to a carding machine with a hopper, a Basschachtaustrag, a feed channel and a fan for compacting the fiber material to a fiber wadding with a specific fiber wadding weight in the feed channel, and a method for controlling the fiber wadding weight.
- the carding machine produces a card sliver from the fiber material which is subsequently processed into a yarn.
- a card is usually associated with a hopper which is supplied by a conveyor system with fibers from a blowroom.
- the fibers are transported in the form of fiber flakes.
- the hopper is filled with fiber flakes from a transport system continuously or demand-controlled. In most cases, pneumatic transport systems are used. From the hopper, the fiber flakes are introduced by means of a feed device in the form of a fiber wadding in the card.
- the uniformity of the fiber wadding entering the card plays an important role with regard to the service life of the working elements of the card and the demands on carding quality. Also, the uniformity of the tape or web produced by the card is affected by the uniformity of the fiber wadding entering the card.
- Another important technological factor in the carding process is the weight of the fiber wadding entering the card. The size of the fiber wadding weight and the entry speed of the fiber wadding into the carding machine essentially determine the production quantity of a card and are jointly responsible for achieving a specific carding quality. The fiber wadding weight which can be processed by the carding machine is also determined by the product to be processed.
- feed roller for the continuous withdrawal of the fiber flock from the hopper is arranged.
- the extracted from the feed roller from the hopper fiber flakes are over a Opening roller for additional opening and homogenization fed to a feed channel.
- the fiber flakes are formed by means of compressed air to form a homogeneous fiber wadding template, which is suitable for feeding the card.
- a fan is provided in addition to the feed device, which allows an increase in pressure in the feed channel and thereby a compression of the fiber flakes to a fiber wadding. Due to the fan induced pressure in the feed channel, the fiber flakes are compressed to a fiber wadding.
- the air flowing into the feed channel through the fan is withdrawn via an air-permeable wall from the feed channel at its end and returned to the fan.
- Another type of filling shaft discloses, for example, the CH 706 658 A1 , This shows a two-part hopper consisting of an upper shaft and a lower shaft.
- the upper shaft is filled with fiber flakes, then the fiber flakes are passed from the upper shaft via a feed device to the lower shaft.
- the fiber flakes are discharged in the form of a fiber wadding and fed to the fiber wadding in the sequence via a feed channel of the card, with no devices are provided in the feed channel for influencing the fiber wadding.
- the feed channel is used only for transporting the fiber wadding from the lower shaft to the card.
- a disadvantage of this design is that a uniform automatic regulation of the density of the fiber mass or the filling level in the feed channel immediately before the transfer of the fiber wadding to the card is not possible.
- Object of the present invention is therefore to provide a feeding device with an automatic regulation of the compaction of the fiber wadding and the filling level in the feed channel and thus to achieve a feeding of the carding machine with a uniform fiber wadding.
- Another object of the invention is to achieve a regulation of the level in the feed channel over the working width of the carding constant and uniform feeding of the fiber wadding to the card.
- Proposed is a device for feeding fiber material to a card with a hopper, a Bashamachtaustrag, a feed channel and a fan for compression of the fiber material in the feed channel to a specific fiber wadding weight.
- the filling duct discharge has a feed roller driven by a frequency converter with a feed trough for metering the fiber material out of the feed hopper and an opening roller for transferring the fiber material from the feed roll to the feed duct.
- a control is provided, in which a desired volume flow of the fan and a desired pressure in the feed channel are assigned for different fiber wadding weights each to a specific fiber wadding weight. In the feed channel a pressure measurement is provided.
- the introduced by the fan in the feed channel air is discharged through an air-permitting part of the feed channel at the end of this.
- the air introduced by the fan must pass through the fiber material to the air-permeable part at the end of the feed channel.
- the fiber material is compressed by the air. The higher the compression of the fiber material becomes, the more resistance the air flow experiences from the fan.
- the size of the compaction determines the fiber wadding weight of the fiber material compacted into a fiber wadding. This will be the fiber wadding weight determined by the inflowing air opposing resistance of the fiber material.
- the densification of the fiber material is decisive, which depends on the pending on the fiber mass pressure of the air introduced by the fan. Due to this dependence, a specification of the air flow to be introduced by the fan into the feed duct is provided with respect to its pressure.
- the air By changing the filling level in the feed channel, the air is forced to flow through a larger mass of fiber material to reach the air-permeable wall of the feed channel.
- the level in the feed channel is significantly influenced by the air flow.
- the filling level in the feed duct is determined accordingly.
- various types of fibers and fiber blends are processed. These differ by their specific properties such as material (cotton, synthetic fibers, viscose, etc.) or fiber lengths (for example, short or medium stacks) or the proportions of different fibers in a fiber blend.
- material cotton, synthetic fibers, viscose, etc.
- fiber lengths for example, short or medium stacks
- proportions of different fibers in a fiber blend Due to the fiber material to be processed, a production volume to be achieved and requirements for carding quality, a corresponding fiber wadding weight is determined for feeding the card. The determination of the fiber wadding weight of the fiber material to be fed takes place on the basis of operational experience of the spinning industry personnel.
- setpoint values for the pressure in the feed duct and the volumetric flow of the fan are stored for the various fiber mat weights.
- the arranged in the feed channel pressure measurement allows compliance with the predetermined target pressure by controlling the speed of the feed roller and thus the amount of reaching into the feed channel fiber material.
- a fiber wadding weight control is provided in the control.
- the controller determines an actual value of the fiber wadding weight. Determinations of the actual fiber wadding weight are known from the prior art, for example, describes the EP 2 867 392 A1 such a procedure. If a deviation now results between the predetermined desired fiber wadding weight, as a result of which the nominal values for volume flow and pressure of the fan have been assigned, and the actual fiber wadding weight, the setpoint values for the pressure are corrected while maintaining the setpoint value for the volumetric flow of the fan. This is due to the fact that a correction of the fiber wadding weight requires a change in the pressure in the feed channel. However, the filling height of the feed channel determined by the volume flow can be left.
- the determination of the actual value of the fiber wadding weight is carried out by a calculation of a weight of the produced card sliver or fleece, a total delay of the card and a deposited leaving quantity.
- the individual fibers of the fiber material are parallelized in the card and leave the card in the form of a fleece or card sliver.
- the fiber wadding is pulled apart so that the produced card sliver leaves the carding machine at a higher discharge speed than the entry speed of the fiber wadding into the carding machine. This process is called delay.
- delay occurs over several arranged in the carding rollers. The occurring individual delays from roller to roller can be added together in a so-called total delay of the card.
- the total delay of a card corresponds to the ratio of the delivery speed of the card sliver or web to Infeed speed of the fiber wadding.
- the machine control system determines the speed of the motors from the output values output to the corresponding motors and, correspondingly, the peripheral speeds of the rollers driven by the motors.
- Other means for determining the inlet velocity or the outlet velocity are, for example, speed measurements of the rollers or shafts.
- the output quantity can be determined via an outgoing function depending on the production quantity.
- the determination of the outgoing function is usually carried out for a machine type and a fiber product to be processed once by an empirical measurement of the output quantity at different production ratios and different fiber material.
- the measurement of the band weight at the card runout takes place, for example, via the measurement of a disk roll spacing or radiometric measuring systems for the measurement of a nonwoven.
- the fan has a drive with a frequency converter for speed control.
- a control element may be provided to a drive with a frequency control.
- the determination of a new setpoint for the speed is necessary to achieve a uniform distribution of the fiber material over the entire width of the feed channel. An uneven distribution of the fiber material leads to a non-uniform fiber wadding seen in the feed channel over the working width of the carding machine.
- the fiber wadding weight in this case would not be equal over the entire width of the carding machine by the creation of holes or tearing of the edges of the fiber wadding at the outer ends of the feed channel.
- the volume flow of the air in the feed channel has an influence on the filling level.
- An excessively high volume flow can be Due to the formation of exhaust ducts in the fiber wadding from the feed channel to the air-permeable region of the wall of the feed channel cause uneven compression of the fiber wadding.
- a sensor for measuring an opening of the feed trough is provided.
- the density or compactness of the fiber flakes taken from the feed chute through the feed roll also has an effect on the fiber wadding to be formed in the feed chute.
- the air permeability of the fiber material is reduced and it is achieved with the same setpoint for the pressure of a lower filling level in the feed channel.
- a compensation of this phenomenon via the regulation of the pressure in the feed channel is not always satisfactory, since a sluggish control has too long a reaction time result and thus a short-term increase in the filling level, a blockage of the feed channel may result.
- the feed trough is resiliently held and is opened or closed by the fiber fluff according to need.
- the sensor which detects the position of the feed trough a change in the density of the fiber flakes is noticed early and can be incorporated into the control of the speed of the feed roller accordingly. This makes it possible to reduce the supply when dense fiber flakes and to avoid clogging of the feed channel.
- the design of the sensor can be an embodiment of the feed trough or the movement of a distance sensor or a distance measurement (for example, inductive or capacitive mode of action) or a rotation angle sensor.
- the device for feeding fiber material to a carding machine comprises a feed channel and a fan for compressing the fiber material in the feed channel to a specific fiber wadding weight.
- the fan has a drive with a frequency converter for speed control or a control device for controlling the flow rate.
- a filling sensor is provided for measuring a filling level.
- the filling sensor can be designed as a single or multiple sensors. The uniformity of the filling level must be ensured over the entire working width of the card. As types of the sensor, for example, optical or transmitted light sensors are conceivable. Due to the design, a specified fill level (setpoint) is the same for all types of applications due to the geometry for a specific design of a feed channel.
- a volume flow control which calculates a correction of the speed of the fan or the position of the control element from a comparison of the measured filling height with a desired filling level.
- the nominal filling level can be present as a fixed value due to the built-in supply channel in the controller. Alternatively, this fixed value can also be determined by the installation location of the fill sensor, so that the measurement of the fill level results in a direct measurement of the difference to the desired fill level.
- a method for feeding a card is proposed, with a certain amount of fiber, from a hopper with a feed roller which cooperates with a feed trough, brought the fiber via a feed roller downstream Auflensewalze in a feed channel and in the feed channel with a fan to a Fiber wadding is compacted with a fiber wadding weight.
- a selected volume of cotton wool to be fed is assigned a nominal volumetric flow rate of the fan and a nominal pressure in the feed duct.
- an actual pressure is measured with a pressure sensor and a drive of the feed roller via a Frequency converter regulated due to a target-actual adjustment of the pressure in the feed channel while maintaining the target volume flow.
- the assignment of the desired pressure due to the selected fiber wadding weight is influenced by a fiber wadding weight control while maintaining the desired volume flow. Too high a volume flow of air in the feed channel can result in uneven compression of the fiber wadding through the formation of exhaust air ducts through the fiber wadding from the feed channel to the air-permeable region of the wall of the feed channel.
- a change in the desired pressure due to the fiber wadding weight control is compensated for a constant desired volume flow by a corresponding adjustment of the speed of the feed roller.
- the speed is adjusted via a drive associated with the drive or a variable speed drive. Further, it is advantageous if it is compensated to maintain a level by a corresponding adjustment of the speed of the fan or a position of the control element.
- an opening of the feed trough is measured with a sensor.
- the measured opening of the feed trough can act as a correction factor on the regulation of the feed roll. This serves to prevent blockages or undersupplies in the feed channel due to a changing density of the fiber flakes in the feed chute.
- FIG. 1 shows a carding machine 1 equipped with a hopper 2, a Medschachtaustrag 5 and a feed channel 3.
- Fiber flakes 4 arrive after they have passed through the various stages of a blowroom in the hopper 2.
- the fiber flakes 4 are through the Golfschachtaustrag 5, comprising a feed roller 6 and an opening roller 7 and a supply of air 8, passed to the feed channel 3.
- a supply of air 8 is provided to support the flock transfer of the opening roller 7 to the feed channel 3 and to ensure a compaction of the fiber wadding 11 in front of a feed device 10 of the carding machine 1.
- the air supply blows air 8 tangentially to the opening roller 7 along in the feed channel 3 and thereby compresses the fiber flakes to a fiber wadding 11 with a necessary for further processing in the carding machine 1 high fiber wadding weight.
- the blown through the air supply air 8 flows through the fiber flakes which are discharged from the opening roller 7 in the feed channel 3. This air flow leaves the feed channel 3 through the air-permeable region 9 of the wall at the end of the feed channel.
- a feed device 10 following the feed channel 3 feeds the fiber flakes, now in the form of a homogeneous fiber wadding template 11, to the licker-in module 12 of the carding machine 1.
- a Kardenspeisewalze with a feed trough for metering the fiber wadding 11 is provided for the feed device 10.
- the fiber flakes discharged from the feed device 10 from the fiber wadding template 11 are further opened by the lickerins contained in the licker-in module 12 and at the same time freed from a portion of the impurities contained therein.
- the last licker-in roller of the licker-in module 12 finally transfers the fibers to the card drum 13, which completely dissolves and parallelizes the fibers.
- the carding drum 13 cooperates with the cover unit 14.
- FIG. 2 shows a schematic representation of an inventive device in a first embodiment. From a hopper 2 fiber flakes 4 are removed with a feed roller 6. The feed roller 6 cooperates with a feed trough 25. The feed trough 25 is provided with a spring delivery 26 which presses the feed trough 25 against the feed roller 6. The feed trough 25 is thereby opened more or less against the spring delivery 26 by the fiber flakes 4 extracted from the feed roller 6 from the feed hopper 2 in accordance with the density of the fiber flakes 4. The feed roller 6 transmits the fiber flakes 4 to an opening roller 7. The opening roller 7 transfers the fiber flakes 4 from the feed roller 6 into a feed channel 3, in which the fiber flakes 4 are further transported to the carding machine.
- air 8 is introduced into the feed channel 3 by an air supply duct 19 by a fan 18 with a drive.
- the introduced through the fan 18 in the feed channel 3 8 air is discharged through an air-permeable region 9 in a wall of the feed channel 3 at the end again from the feed channel 3 and brought back to the fan 18 via a return line 28.
- a false air opening 29 is provided in the return line 28. The false air opening 29 serves to compensate for losses of air at possibly leaking points of the entire air flow from and to the fan 18.
- a fiber wadding 11 is formed at the end of the feed channel 3 from the fiber flakes and this compressed by the air pressure.
- the pressure arises due to a resistance which the air 8 must overcome by flowing through the fiber wadding 11 to pass through the air-permeable region 9 from the feed channel 3 in the return line 28.
- a fiber wadding 11 is formed with a certain level 34.
- a pressure sensor 24 for measuring an actual pressure of the air 8 in the feed channel 3 is provided in the feed channel 3.
- the pressure in the feed channel 3 is decisive for the density of the fiber wadding 11 and thus a yardstick for a fiber wadding weight W to be achieved at the end of the feed channel 3.
- a controller 31 is shown.
- characteristic curves for a desired volume flow V and a target pressure P for the air 8 are stored.
- a desired fiber wadding weight W is input to the controller 31 via the input 33.
- the controller 31 of this fiber wadding weight W the corresponding desired volume flow V and the target pressure P are assigned.
- Via the pressure sensor 24, an actual pressure in the feed channel 3 is measured.
- a target-actual-value comparison of the pressure a corresponding correction of the speed of the feed roller 6 is calculated in the controller and via a frequency converter 23 which acts on the drive 22 of the feed roller 6, the speed of the feed roller 6 is corrected.
- a constant pressure and a constant volume flow in the feed channel 3 is ensured.
- FIG. 3 shows a schematic representation of an inventive device in a further embodiment.
- the present arrangement of the device comprising a hopper 2, a feed roller 6, a feed trough 25 with a spring load 26, an opening roller 7 and a feed channel 3 and a fan 18 with an air supply channel 19 and a return line 28 are identical to the arrangement according to FIG FIG. 2 ,
- a pressure sensor 24 for measuring an actual pressure of the air 8 in the feed channel 3 is provided in the feed channel 3.
- the pressure in the feed channel 3 is decisive for the density of the fiber wadding 11 and thus a yardstick for a fiber wadding weight W to be achieved at the end of the feed channel 3.
- a controller 31 is shown.
- characteristic curves for a desired volume flow V and a target pressure P for the air 8 are stored.
- a desired fiber wadding weight W is input to the controller 31 via the input 33.
- the controller 31 of this fiber wadding weight W the corresponding desired volume flow V and the target pressure P are assigned.
- Via the pressure sensor 24, an actual pressure in the feed channel 3 is measured.
- a desired-actual-value comparison of the pressure in the control a corresponding correction of the speed of the feed roller. 6 calculated and a frequency converter 23 which acts on the drive 22 of the feed roller 6, the speed of the feed roller 6 is corrected.
- a constant pressure and a constant volume flow in the feed channel 3 is ensured.
- the controller 31 is associated with a fiber wadding weight control 30.
- a desired fiber wadding weight which corresponds to the input 33 of the fiber wadding weight, compared with an actual fiber wadding weight at the Karde.
- the speed of the drive 22 of the feed roller 6 is changed by the controller 31 via a frequency converter 23.
- the speed of the drive 20 of the fan 18 via a frequency converter 21 or alternatively, instead of the speed of the fan 18 in the return line 28, a control element Be provided 32, which also allows a change in the flow rate.
- An excessively high volume flow of the air 8 in the feed channel 3 can result in uneven compression of the fiber wadding 11 as a result of the formation of exhaust air channels through the fiber wadding 11 from the feed channel 3 to the air-permeable region 9 of the wall of the feed channel 3.
- an opening sensor 27 is additionally provided on the feed trough 25.
- the opening sensor 27 measures the opening state of the feed trough 25 and thereby provides information about the density of the currently extracted by the feed roller 6 from the hopper 2 fiber flakes 4. By the controller 31, this information is processed and as a correction factor to the control of the speed of the drive 22nd the feed trough 6 switched.
- FIG. 4 shows a schematic representation of an inventive device with a control of the filling level 34.
- the present arrangement of the device with respect to a hopper 2 with fiber flakes 4, a feed roller 6, a feed trough 25, an opening roller 7 and a partially filled with a fiber wadding 11 feed channel. 3 and a fan 18 with an air supply channel 19 and a return line 28 are identical to the arrangement according to FIG. 2 , Next is also the description of the false air opening 29, the air-permeable area 9 and the filling level 34 of FIG. 2 refer to.
- the fan 18 conveys air 8 with a certain volume flow through the air supply channel 19 and the feed channel 3 to the fiber wadding 11.
- a filling level 34 which denotes the area filled with fiber wadding 11 of the feed channel 3.
- a filling sensor 35 is arranged in the area of the desired filling level.
- the volume flow control 36 controls via a corresponding control signal, the speed of the fan 18 and the drive 20 by means of a frequency converter 21.
- the flow control 36 in the supply or discharge line of the fan 18 existing Control element 32 are changed in its position accordingly.
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Abstract
Die vorliegende Erfindung betrifft ein Verfahren und eine Vorrichtung zur Speisung von Fasergut (4) zu einer Karde (1). Die Vorrichtung umfasst einen Füllschacht (2), einen Füllschachtaustrag (5), einen Speisekanal (3) und einen Ventilator (18) zur Verdichtung des Fasergutes (4) im Speisekanal (3) zu einem bestimmten Faserwattegewicht. Der Füllschachtaustrag (5) weist eine über einen Frequenzumrichter (23) angetriebene Speisewalze (6) mit einer Speisemulde (25) zur Dosierung des Fasergutes (4) aus dem Füllschacht (2) und eine Auflösewalze (7) zur Übergabe des Fasergutes (4) von der Speisewalze (6) zum Speisekanal (3) auf. Es ist eine Steuerung (31) vorgesehen, in welcher für verschiedene Faserwattegewichte jeweils einem bestimmten Faserwattegewicht ein Soll-Volumenstrom (V) des Ventilators (18) und ein Soll-Druck (P) im Speisekanal (3) zugewiesen sind. Im Speisekanal (3) ist eine Druckmessung (24) vorgesehen. The present invention relates to a method and a device for feeding fiber material (4) to a carding machine (1). The apparatus comprises a filling shaft (2), a filling shaft discharge (5), a feed channel (3) and a fan (18) for compressing the fiber material (4) in the feed channel (3) to a specific fiber wadding weight. The Füllschachtaustrag (5) has a via a frequency converter (23) driven feed roller (6) with a feed trough (25) for metering the fiber material (4) from the hopper (2) and an opening roller (7) for transferring the fiber material (4) from the feed roller (6) to the feed channel (3). A controller (31) is provided, in which a desired volume flow (V) of the fan (18) and a desired pressure (P) in the feed channel (3) are assigned for different fiber wadding weights each to a specific fiber wadding weight. In the feed channel (3) a pressure measurement (24) is provided.
Description
Die vorliegende Erfindung betrifft eine Vorrichtung zur Speisung von Fasergut zu einer Karde mit einem Füllschacht, einem Füllschachtaustrag, einem Speisekanal und einem Ventilator zur Verdichtung des Fasergutes zu einer Faserwatte mit einem bestimmten Faserwattegewicht im Speisekanal, sowie ein Verfahren zur Regelung des Faserwattegewichtes.The present invention relates to a device for feeding of fiber material to a carding machine with a hopper, a Füllschachtaustrag, a feed channel and a fan for compacting the fiber material to a fiber wadding with a specific fiber wadding weight in the feed channel, and a method for controlling the fiber wadding weight.
Die Karde produziert aus dem eingespeisten Fasergut ein Kardenband, welches in der Folge zu einem Garn weiter verarbeitet wird. Anstelle eines Kardenbandes kann jedoch auch ein Vlies hergestellt werden. Dabei ist einer Karde in der Regel ein Füllschacht zugeordnet welcher durch ein Fördersystem mit Fasern aus einer Putzerei versorgt wird. Die Fasern werden dabei in Form von Faserflocken transportiert. Der Füllschacht wird mit Faserflocken aus einem Transportsystem kontinuierlich oder bedarfsgesteuert befüllt. Zumeist kommen pneumatische Transportsysteme zum Einsatz. Aus dem Füllschacht werden die Faserflocken mit Hilfe einer Speisevorrichtung in Form einer Faserwatte in die Karde eingebracht. Dabei spielt die Gleichmässigkeit der in die Karde einlaufenden Faserwatte eine wichtige Rolle bezüglich der Lebensdauer der Arbeitselemente der Karde und den Anforderungen an die Kardierqualität. Auch wird die Gleichmässigkeit des durch die Karde produzierten Bandes oder Vlieses durch die Gleichmässigkeit der in die Karde einlaufenden Faserwatte beeinflusst. Eine ebenfalls wichtige technologische Grösse im Kardierprozess ist das Gewicht der in die Karde einlaufenden Faserwatte. Die Grösse des Faserwattegewichts und die Einlaufgeschwindigkeit der Faserwatte in die Karde bestimmen wesentlich die Produktionsmenge einer Karde und sind mitverantwortlich für das Erreichen einer bestimmten Kardierqualität. Dabei wird das Faserwattegewicht welches durch die Karde verarbeitet werden kann auch durch das zu verarbeitende Produkt bestimmt.The carding machine produces a card sliver from the fiber material which is subsequently processed into a yarn. Instead of a card sliver, however, it is also possible to produce a nonwoven. In this case, a card is usually associated with a hopper which is supplied by a conveyor system with fibers from a blowroom. The fibers are transported in the form of fiber flakes. The hopper is filled with fiber flakes from a transport system continuously or demand-controlled. In most cases, pneumatic transport systems are used. From the hopper, the fiber flakes are introduced by means of a feed device in the form of a fiber wadding in the card. In this case, the uniformity of the fiber wadding entering the card plays an important role with regard to the service life of the working elements of the card and the demands on carding quality. Also, the uniformity of the tape or web produced by the card is affected by the uniformity of the fiber wadding entering the card. Another important technological factor in the carding process is the weight of the fiber wadding entering the card. The size of the fiber wadding weight and the entry speed of the fiber wadding into the carding machine essentially determine the production quantity of a card and are jointly responsible for achieving a specific carding quality. The fiber wadding weight which can be processed by the carding machine is also determined by the product to be processed.
Im unteren Teil des Füllschachtes oder in einer alternativen Bauart im unteren Teil des Oberschachtes ist eine mit einer Speisemulde zusammen arbeitende Speisewalze für den kontinuierlichen Abzug der Faserflocken aus dem Füllschacht angeordnet. Die von der Speisewalze aus dem Füllschacht abgezogenen Faserflocken werden über eine Auflösewalze zur zusätzlichen Öffnung und Homogenisierung einem Speisekanal zugeführt. Im Speisekanal werden die Faserflocken mit Hilfe von komprimierter Luft zu einer homogenen Faserwattenvorlage geformt, welche für die Speisung der Karde geeignet ist. Ebenfalls ist zugehörig zur Speisevorrichtung ein Ventilator vorgesehen, welcher eine Druckerhöhung im Speisekanal und dadurch eine Verdichtung der Faserflocken zu einer Faserwatte ermöglicht. Durch den mit dem Ventilator herbeigeführten Druck im Speisekanal werden die Faserflocken zu einer Faserwatte verdichtet. Die durch den Ventilator in den Speisekanal einströmende Luft wird über eine luftdurchlässige Wand aus dem Speisekanal an dessen Ende wieder abgezogen und zum Ventilator zurückgeführt.In the lower part of the hopper or in an alternative design in the lower part of the upper shaft with a feed trough working together feed roller for the continuous withdrawal of the fiber flock from the hopper is arranged. The extracted from the feed roller from the hopper fiber flakes are over a Opening roller for additional opening and homogenization fed to a feed channel. In the feed channel, the fiber flakes are formed by means of compressed air to form a homogeneous fiber wadding template, which is suitable for feeding the card. Also, a fan is provided in addition to the feed device, which allows an increase in pressure in the feed channel and thereby a compression of the fiber flakes to a fiber wadding. Due to the fan induced pressure in the feed channel, the fiber flakes are compressed to a fiber wadding. The air flowing into the feed channel through the fan is withdrawn via an air-permeable wall from the feed channel at its end and returned to the fan.
Aus dem Stand der Technik ist eine Speisung einer Karde nach der
Eine weitere Bauart eines Füllschachtes offenbart beispielsweise die
Eine weitere Aufgabe der Erfindung besteht darin, durch eine Regulierung der Füllhöhe im Speisekanal eine über die Arbeitsbreite der Karde konstante und gleichmässige Speisung der Faserwatte zur Karde zu erreichen.Another object of the invention is to achieve a regulation of the level in the feed channel over the working width of the carding constant and uniform feeding of the fiber wadding to the card.
Die Aufgaben werden gelöst durch eine Speisevorrichtung mit den Merkmalen der unabhängigen Patentansprüche.The objects are achieved by a feed device having the features of the independent claims.
Vorgeschlagen wird eine Vorrichtung zur Speisung von Fasergut zu einer Karde mit einem Füllschacht, einem Füllschachtaustrag, einem Speisekanal und einem Ventilator zur Verdichtung des Fasergutes im Speisekanal zu einem bestimmten Faserwattegewicht. Der Füllschachtaustrag weist eine über einen Frequenzumrichter angetriebene Speisewalze mit einer Speisemulde zur Dosierung des Fasergutes aus dem Füllschacht und eine Auflösewalze zur Übergabe des Fasergutes von der Speisewalze zum Speisekanal auf. Eine Steuerung ist vorgesehen, in welcher für verschiedene Faserwattegewichte jeweils einem bestimmten Faserwattegewicht ein Soll-Volumenstrom des Ventilators und ein Soll-Druck im Speisekanal zugewiesen sind. Im Speisekanal ist eine Druckmessung vorgesehen. Da die Gleichmässigkeit der in die Karde einlaufenden Faserwatte eine wichtige Rolle spielt ist eine Steuerung der Faserwatteeigenschaften am Ende des Speisekanals massgebend. Die durch den Ventilator in den Speisekanal eingebrachte Luft wird über einen luftdurchlässig ausgeführten Teil des Speisekanals an dessen Ende aus diesem abgeführt. Wird nun der Speisekanal durch das Fasergut angefüllt, muss die vom Ventilator eingeführte Luft durch das Fasergut zum luftdurchlässigen Teil am Ende des Speisekanals gelangen. Dabei wird das Fasergut durch die Luft verdichtet. Umso höher die Verdichtung des Fasergutes wird, desto mehr Widerstand erfährt der Luftstrom vom Ventilator. Die Grösse der Verdichtung bestimmt das Faserwattegewicht des zu einer Faserwatte verdichteten Fasergutes. Damit wird das Faserwattegewicht bestimmt durch den der einströmenden Luft entgegenstehenden Widerstand des Fasergutes. Für das zu erreichende Faserwattegewicht ist die Verdichtung des Fasergutes massgebend ist, welche vom an der Fasermasse anstehenden Druck der vom Ventilator eingebrachten Luft abhängig ist. Aufgrund dieser Abhängigkeit ist eine Vorgabe der durch den Ventilator in den Speisekanal einzubringenden Luftströmung in Bezug auf deren Druck vorgesehen.Proposed is a device for feeding fiber material to a card with a hopper, a Füllschachtaustrag, a feed channel and a fan for compression of the fiber material in the feed channel to a specific fiber wadding weight. The filling duct discharge has a feed roller driven by a frequency converter with a feed trough for metering the fiber material out of the feed hopper and an opening roller for transferring the fiber material from the feed roll to the feed duct. A control is provided, in which a desired volume flow of the fan and a desired pressure in the feed channel are assigned for different fiber wadding weights each to a specific fiber wadding weight. In the feed channel a pressure measurement is provided. Since the uniformity of the fiber wadding entering the carding machine plays an important role, control of the fiber wadding properties at the end of the feed channel is decisive. The introduced by the fan in the feed channel air is discharged through an air-permitting part of the feed channel at the end of this. Now, if the feed channel is filled by the fiber material, the air introduced by the fan must pass through the fiber material to the air-permeable part at the end of the feed channel. The fiber material is compressed by the air. The higher the compression of the fiber material becomes, the more resistance the air flow experiences from the fan. The size of the compaction determines the fiber wadding weight of the fiber material compacted into a fiber wadding. This will be the fiber wadding weight determined by the inflowing air opposing resistance of the fiber material. For the fiber wadding weight to be achieved, the densification of the fiber material is decisive, which depends on the pending on the fiber mass pressure of the air introduced by the fan. Due to this dependence, a specification of the air flow to be introduced by the fan into the feed duct is provided with respect to its pressure.
Durch eine Änderung der Füllhöhe im Speisekanal ist die Luft gezwungen durch eine grössere Masse an Fasergut zu strömen um die luftdurchlässige Wandung des Speisekanals zu erreichen. Damit wird die Füllhöhe im Speisekanal wesentlich durch den Luftvolumenstrom beeinflusst. Durch eine Regelung des Luftvolumenstromes wird demnach die Füllhöhe im Speisekanal bestimmt.By changing the filling level in the feed channel, the air is forced to flow through a larger mass of fiber material to reach the air-permeable wall of the feed channel. Thus, the level in the feed channel is significantly influenced by the air flow. By regulating the air volume flow, the filling level in the feed duct is determined accordingly.
In der Karde werden verschiedene Arten von Fasern und Fasermischungen verarbeitet. Diese unterscheiden sich durch ihre spezifischen Eigenschaften wie beispielsweise Material (Baumwolle, synthetische Fasern, Viskose, etc.) oder Faserlängen (beispielsweise Kurz- oder Mittelstapel) oder die Anteile an unterschiedlichen Fasern in einer Fasermischung. Aufgrund des zu verarbeitenden Fasergutes, einer zu erreichenden Produktionsmenge und Anforderungen an die Kardierqualität wird für die Speisung der Karde ein entsprechendes Faserwattegewicht festgelegt. Die Bestimmung des Faserwattegewichts des zu speisenden Fasergutes erfolgt dabei aufgrund von betrieblichen Erfahrungen des Spinnereifachpersonals. In der Steuerung sind für die verschiedenen Faserwattegewichte Sollwerte für den Druck im Speisekanal und den Volumenstrom des Ventilators hinterlegt. Die im Speisekanal angeordnete Druckmessung ermöglicht eine Einhaltung des vorgegebenen Soll-Druckes durch eine Regelung der Drehzahl der Speisewalze und damit der Menge des in den Speisekanal gelangenden Fasergutes. Die Füllhöhe im Speisekanal hingegen wird durch eine Beeinflussung des Volumenstromes bestimmt.In the carding various types of fibers and fiber blends are processed. These differ by their specific properties such as material (cotton, synthetic fibers, viscose, etc.) or fiber lengths (for example, short or medium stacks) or the proportions of different fibers in a fiber blend. Due to the fiber material to be processed, a production volume to be achieved and requirements for carding quality, a corresponding fiber wadding weight is determined for feeding the card. The determination of the fiber wadding weight of the fiber material to be fed takes place on the basis of operational experience of the spinning industry personnel. In the control system, setpoint values for the pressure in the feed duct and the volumetric flow of the fan are stored for the various fiber mat weights. The arranged in the feed channel pressure measurement allows compliance with the predetermined target pressure by controlling the speed of the feed roller and thus the amount of reaching into the feed channel fiber material. The filling level in the feed channel, however, is determined by influencing the volume flow.
Bei einer Veränderung der Produktionsmenge, beispielsweise einer Steigerung der Produktion der Karde, wird mehr Faserwatte aus dem Speisekanal in die Karde abgeführt, was zu einer Verringerung der Füllhöhe im Speisekanal führt. Diesem Umstand wird normalerweise durch eine direkte Steuerung der Lieferleistung der Speisewalze ausgeglichen. Erfolgt trotz der direkten Steuerung eine Verringerung der Füllhöhe wird der Widerstand verkleinert, welcher der Luft vom Ventilator entgegensteht und damit einhergehend der Druck im Speisekanal unter den Soll-Druck abgesenkt. Die Regelung reagiert darauf durch eine Erhöhung der Drehzahl der Speisewalze um den Soll-Druck wieder herzustellen.With a change in the production quantity, for example, an increase in the production of the card, more fiber wadding is discharged from the feed channel into the card, resulting in a reduction of the level in the feed channel. This circumstance is normally compensated by direct control of the feed rate of the feed roll. If, despite the direct control, a reduction in the filling level, the resistance is reduced, which opposes the air from the fan and, consequently, the pressure in the feed channel is lowered below the desired pressure. The control responds by increasing the speed of the feed roller to restore the setpoint pressure.
Vorteilhafterweise ist in der Steuerung eine Faserwattegewichtsregelung vorgesehen. Zur Regelung des Faserwattegewichts wird durch die Steuerung ein Ist-Wert des Faserwattegewichts bestimmt. Bestimmungen des Ist-Faserwattegewichts sind aus dem Stand der Technik bekannt, beispielsweise beschreibt die
Dabei erfolgt die Ermittlung des Istwertes des Faserwattegewichtes durch eine Berechnung aus einem Gewicht des hergestellten Kardenbandes oder Vlieses, einem Totalverzug der Karde und einer abgeschiedenen Abgangsmenge. Die einzelnen Fasern des Fasergutes werden in der Karde parallelisiert und verlassen die Karde in Form eines Vlieses oder Kardenbandes. In diesem Prozess wird die Faserwatte auseinandergezogen, sodass das hergestellte Kardenband mit einer höheren Auslaufgeschwindigkeit die Karde verlässt als die Einlaufgeschwindigkeit der Faserwatte in die Karde. Diesen Vorgang nennt man Verzug. Ein derartiger Verzug geschieht über mehrere in der Karde angeordnete Walzen. Die dabei auftretenden einzelnen Verzüge von Walze zu Walze können in einem sogenannten Totalverzug der Karde zusammengerechnet werden. Aufgrund des Betriebszustandes einer Karde ist deren Totalverzug bekannt und wird durch die Maschinensteuerung selbst ermittelt. Der Totalverzug einer Karde entspricht dem Verhältnis von der Auslaufgeschwindigkeit des Kardenbandes oder Vlieses zur Einlaufgeschwindigkeit der Faserwatte. Über die Ansteuerung der Antriebe im Einlauf und Auslauf der Karde ermittelt die Maschinensteuerung aus den, an die entsprechenden Motoren, ausgegebenen Stellwerten die Drehzahl der Motoren und entsprechend die Umfangsgeschwindigkeiten der durch die Motoren angetriebenen Walzen. Andere Mittel zu Bestimmung der Einlaufgeschwindigkeit oder der Auslaufgeschwindigkeit sind beispielsweise Drehzahlmessungen der Walzen oder Wellen. Durch die Reinigung und Parallelisierung des Fasergutes werden in der Karde aus dem Fasergut Verunreinigungen und Kurzfasern ausgeschieden. Die dem Fasergut entnommenen Bestandeile werden zusammenfassend als Abgang bezeichnet. Die Abgangsmenge kann über eine Abgangsfunktion in Abhängigkeit der Produktionsmenge bestimmt werden. Die Ermittlung der Abgangsfunktion erfolgt in der Regel für einen Maschinentyp und ein zu verarbeitendes Fasergut einmal durch ein empirisches Messen der Abgangsmenge bei verschiedenen Produktionsverhältnissen und unterschiedlichem Fasergut. Die Messung des Bandgewichts am Kardenauslauf erfolgt beispielsweise über die Messung eines Scheibenwalzenabstands oder radiometrische Messsysteme für die Messung eines Vlieses.In this case, the determination of the actual value of the fiber wadding weight is carried out by a calculation of a weight of the produced card sliver or fleece, a total delay of the card and a deposited leaving quantity. The individual fibers of the fiber material are parallelized in the card and leave the card in the form of a fleece or card sliver. In this process, the fiber wadding is pulled apart so that the produced card sliver leaves the carding machine at a higher discharge speed than the entry speed of the fiber wadding into the carding machine. This process is called delay. Such a delay occurs over several arranged in the carding rollers. The occurring individual delays from roller to roller can be added together in a so-called total delay of the card. Due to the operating state of a card whose total delay is known and is determined by the machine control itself. The total delay of a card corresponds to the ratio of the delivery speed of the card sliver or web to Infeed speed of the fiber wadding. By controlling the drives in the infeed and outfeed of the card, the machine control system determines the speed of the motors from the output values output to the corresponding motors and, correspondingly, the peripheral speeds of the rollers driven by the motors. Other means for determining the inlet velocity or the outlet velocity are, for example, speed measurements of the rollers or shafts. By cleaning and parallelization of the fiber material impurities and short fibers are excreted in the card from the fiber. The components taken from the fiber material are collectively referred to as the departure. The output quantity can be determined via an outgoing function depending on the production quantity. The determination of the outgoing function is usually carried out for a machine type and a fiber product to be processed once by an empirical measurement of the output quantity at different production ratios and different fiber material. The measurement of the band weight at the card runout takes place, for example, via the measurement of a disk roll spacing or radiometric measuring systems for the measurement of a nonwoven.
Bevorzugterweise weist der Ventilator einen Antrieb mit einem Frequenzumrichter zur Drehzahlsteuerung auf. Dadurch kann der Ventilator auf die neuen Sollwerte durch die Steuerung direkt eingestellt werden. Alternativ zu einem Antrieb mit einer Frequenzsteuerung kann ein Regelgetriebe oder in einem Lufteintritts- oder einem Luftaustrittskanal des Ventilators ein Regelorgan vorgesehen sein. Die Festlegung eines neuen Sollwertes für die Drehzahl ist notwendig um eine gleichmässige Verteilung des Fasergutes auf der gesamten Breite des Speisekanals zu erreichen. Eine ungleichmässige Verteilung des Fasergutes führt zu einer über die Arbeitsbreite der Karde gesehenen ungleichförmigen Faserwatte im Speisekanal. Das Faserwattegewicht wäre in diesem Fall nicht über die gesamte Breite der Karde gleich durch ein Entstehen von Löchern oder einem Einreissen der Ränder der Faserwatte an den äusseren Enden des Speisekanals. Dies kann auch zu einer Reduktion der möglichen Produktionsmenge oder bei einer Hochregulierung des Faserwattegewichts zu einem überhöhten Faserwattegewicht im zentralen Bereich des Speisekanals führen. Der Volumenstrom der Luft im Speisekanal hat einen Einfluss auf die Füllhöhe. Ein zu hoher Volumenstrom kann unter Umständen eine ungleichmässige Verdichtung der Faserwatte zur Folge haben durch die Bildung von Abluftkanälen in der Faserwatte vom Speisekanal zum luftdurchlässigen Bereich der Wandung des Speisekanals.Preferably, the fan has a drive with a frequency converter for speed control. This allows the fan to be set directly to the new setpoints by the controller. Alternatively to a drive with a frequency control, a control gear or in a Lufteintritts- or an air outlet duct of the fan, a control element may be provided. The determination of a new setpoint for the speed is necessary to achieve a uniform distribution of the fiber material over the entire width of the feed channel. An uneven distribution of the fiber material leads to a non-uniform fiber wadding seen in the feed channel over the working width of the carding machine. The fiber wadding weight in this case would not be equal over the entire width of the carding machine by the creation of holes or tearing of the edges of the fiber wadding at the outer ends of the feed channel. This can also lead to a reduction of the possible production amount or upregulation of the fiber batting weight to an excessive fiber batt weight in the central region of the feed channel. The volume flow of the air in the feed channel has an influence on the filling level. An excessively high volume flow can be Due to the formation of exhaust ducts in the fiber wadding from the feed channel to the air-permeable region of the wall of the feed channel cause uneven compression of the fiber wadding.
Weiterhin ist es vorteilhaft, wenn ein Sensor zur Messung einer Öffnung der Speisemulde vorgesehen ist. Die Dichte oder Kompaktheit welche die Faserflocken aufweisen die durch die Speisewalze dem Füllschacht entnommen werden, haben ebenfalls eine Auswirkung auf die zu bildende Faserwatte im Speisekanal. Bei einer hohen Dichte verringert sich die Luftdurchlässigkeit des Fasergutes und es wird mit dem gleichen Sollwert für den Druck eine geringere Füllhöhe im Speisekanal erreicht. Ein Ausgleich dieses Phänomens über die Regelung des Druckes im Speisekanal ist jedoch nicht in jedem Fall zufriedenstellend, da eine träge Regelung eine zu lange Reaktionszeit zur Folge hat und dadurch bei einem kurzfristigen Anstieg der Füllhöhe eine Verstopfung des Speisekanals die Folge sein kann. Bei einer hohen Dichte der Faserflocken im Füllschacht ergibt sich durch die Entnahme der Faserflocken mit der Speisewalze eine Öffnung der Speisemulde. Die Speisemulde ist federnd gehalten und wird durch die Faserflocken entsprechend dem Bedarf geöffnet oder geschlossen. Durch den Sensor welcher die Stellung der Speisemulde feststellt wird eine Veränderung der Dichte der Faserflocken frühzeitig bemerkt und kann in die Steuerung der Drehzahl der Speisewalze entsprechend einfliessen. Dadurch wird es möglich, Bei Auftreten dichter Faserflocken die Speisung zu reduzieren und eine Verstopfung des Speisekanals zu vermeiden. Die Bauart des Sensors kann einer Ausführung der Speisemulde respektive dessen Bewegung ein Abstandssensor oder eine Wegmessung (beispielsweise induktiver oder kapazitiver Wirkungsweise) oder ein Drehwinkelsensor sein.Furthermore, it is advantageous if a sensor for measuring an opening of the feed trough is provided. The density or compactness of the fiber flakes taken from the feed chute through the feed roll also has an effect on the fiber wadding to be formed in the feed chute. At a high density, the air permeability of the fiber material is reduced and it is achieved with the same setpoint for the pressure of a lower filling level in the feed channel. However, a compensation of this phenomenon via the regulation of the pressure in the feed channel is not always satisfactory, since a sluggish control has too long a reaction time result and thus a short-term increase in the filling level, a blockage of the feed channel may result. With a high density of the fiber flakes in the hopper results from the removal of the fiber flakes with the feed roller an opening of the feed trough. The feed trough is resiliently held and is opened or closed by the fiber fluff according to need. By the sensor which detects the position of the feed trough a change in the density of the fiber flakes is noticed early and can be incorporated into the control of the speed of the feed roller accordingly. This makes it possible to reduce the supply when dense fiber flakes and to avoid clogging of the feed channel. The design of the sensor can be an embodiment of the feed trough or the movement of a distance sensor or a distance measurement (for example, inductive or capacitive mode of action) or a rotation angle sensor.
Im umgekehrten Fall, wenn eine Verringerung der Dichte der Faserflocken auftritt, kann eine Erhöhung der Speisung durch Steigerung der Drehzahl der Speisewalze vorgenommen werden und es entsteht kein Leerlaufen des Speisekanals durch eine Unterversorgung. Durch die Berücksichtigung der Dichte der Faserflocken über die Messung der Öffnung der Speisemulde wird eine kurze Bauweise des Speisekanals ermöglicht. Weiterhin wird eine Vorrichtung vorgeschlagen, welche eine Regelung der Füllhöhe im Speisekanal unabhängig von der Faserwattedichte ermöglicht. Die Vorrichtung zur Speisung von Fasergut zu einer Karde umfasst einen Speisekanal und einen Ventilator zur Verdichtung des Fasergutes im Speisekanal zu einem bestimmten Faserwattegewicht. Der Ventilator weist einen Antrieb mit einem Frequenzumrichter zur Drehzahlsteuerung oder ein Regelorgan zur Regelung des Volumenstroms auf. Im Speisekanal ist ein Füllsensor zur Messung einer Füllhöhe vorgesehen. Der Füllsensor kann dabei als einzelner oder mehrere Sensoren ausgebildet sein. Die Gleichmässigkeit der Füllhöhe ist über die gesamte Arbeitsbreite der Karde sicherzustellen. Als Bauarten des Sensors sind beispielsweise optische oder auch Durchlichtsensoren denkbar. Konstruktionsbedingt ist für eine bestimmte Ausführung eines Speisekanals eine festgelegte Füllhöhe (Sollwert) aufgrund der Geometrie für alle Anwendungsarten gleich.Conversely, if there is a reduction in the density of the fiber flakes, an increase in feed can be made by increasing the speed of the feed roller and there is no emptying of the feed channel by a shortage. By taking into account the density of the fiber flakes on the measurement of the opening of the feed trough a short construction of the feed channel is made possible. Furthermore, a device is proposed which allows a regulation of the filling level in the feed channel, regardless of the fiber wadding density. The device for feeding fiber material to a carding machine comprises a feed channel and a fan for compressing the fiber material in the feed channel to a specific fiber wadding weight. The fan has a drive with a frequency converter for speed control or a control device for controlling the flow rate. In the feed channel, a filling sensor is provided for measuring a filling level. The filling sensor can be designed as a single or multiple sensors. The uniformity of the filling level must be ensured over the entire working width of the card. As types of the sensor, for example, optical or transmitted light sensors are conceivable. Due to the design, a specified fill level (setpoint) is the same for all types of applications due to the geometry for a specific design of a feed channel.
Vorteilhafterweise ist eine Volumenstromsteuerung, welche aus einem Vergleich der gemessenen Füllhöhe mit einer Soll-Füllhöhe eine Korrektur der Drehzahl des Ventilators oder der Stellung des Regelorgans errechnet, vorgesehen. Die Soll-Füllhöhe kann als Festwert aufgrund des eingebauten Speisekanals in der Steuerung vorhanden sein. Alternativ kann dieser Festwert auch durch den Einbauort des Füllsensors festgelegt sein, sodass sich aus der Messung der Füllhöhe eine direkte Messung der Differenz zur Soll-Füllhöhe ergibt.Advantageously, a volume flow control, which calculates a correction of the speed of the fan or the position of the control element from a comparison of the measured filling height with a desired filling level, is provided. The nominal filling level can be present as a fixed value due to the built-in supply channel in the controller. Alternatively, this fixed value can also be determined by the installation location of the fill sensor, so that the measurement of the fill level results in a direct measurement of the difference to the desired fill level.
Weiter wird eine Karde mit einer Vorrichtung zur Speisung von Fasergut vorgeschlagen, wobei die Vorrichtung nach der obigen Beschreibung ausgebildet ist.Further, a card with a device for feeding of fiber material is proposed, wherein the device is designed according to the above description.
Weiter wird ein Verfahren zur Speisung einer Karde vorgeschlagen, mit einer bestimmten Menge an Fasergut, wobei aus einem Füllschacht mit einer Speisewalze welche mit einer Speisemulde zusammenarbeitet, das Fasergut über eine der Speisewalze nachgeordnete Auflösewalze in einen Speisekanal gebracht und im Speisekanal mit einem Ventilator zu einer Faserwatte mit einem Faserwattegewicht verdichtet wird. Einem gewählten zu speisenden Faserwattegewicht werden ein Soll-Volumenstrom des Ventilators und ein Soll-Druck im Speisekanal zugeordnet. Im Speisekanal wird mit einem Drucksensor ein Ist-Druck gemessen und ein Antrieb der Speisewalze über einen Frequenzumrichter aufgrund eines Soll-Ist-Abgleichs des Druckes im Speisekanal unter Beibehaltung des Soll-Volumenstromes geregelt.Next, a method for feeding a card is proposed, with a certain amount of fiber, from a hopper with a feed roller which cooperates with a feed trough, brought the fiber via a feed roller downstream Auflösewalze in a feed channel and in the feed channel with a fan to a Fiber wadding is compacted with a fiber wadding weight. A selected volume of cotton wool to be fed is assigned a nominal volumetric flow rate of the fan and a nominal pressure in the feed duct. In the feed channel, an actual pressure is measured with a pressure sensor and a drive of the feed roller via a Frequency converter regulated due to a target-actual adjustment of the pressure in the feed channel while maintaining the target volume flow.
Vorteilhafterweise wird die Zuordnung des Soll-Druckes aufgrund des gewählten Faserwattegewichtes durch eine Faserwattegewichtsregelung bei einer Beibehaltung des Soll-Volumenstromes beeinflusst. Ein zu hoher Volumenstrom der Luft im Speisekanal kann eine ungleichmässige Verdichtung der Faserwatte zur Folge haben durch die Bildung von Abluftkanälen durch die Faserwatte vom Speisekanal zum luftdurchlässigen Bereich der Wandung des Speisekanals. Bevorzugterweise wird eine Änderung des Soll-Druckes aufgrund der Faserwattegewichtsregelung bei gleichbleibendem Soll-Volumenstrom durch eine entsprechende Anpassung der Drehzahl der Speisewalze kompensiert. Dabei wird die Drehzahl über einen dem Antrieb zugehörigen Frequenzumrichter oder ein Regelgetriebe verstellt. Weiter ist es vorteilhaft, wenn zur Beibehaltung einer Füllhöhe durch eine entsprechende Anpassung der Drehzahl des Ventilators oder einer Stellung des Regelorgans kompensiert wird.Advantageously, the assignment of the desired pressure due to the selected fiber wadding weight is influenced by a fiber wadding weight control while maintaining the desired volume flow. Too high a volume flow of air in the feed channel can result in uneven compression of the fiber wadding through the formation of exhaust air ducts through the fiber wadding from the feed channel to the air-permeable region of the wall of the feed channel. Preferably, a change in the desired pressure due to the fiber wadding weight control is compensated for a constant desired volume flow by a corresponding adjustment of the speed of the feed roller. In this case, the speed is adjusted via a drive associated with the drive or a variable speed drive. Further, it is advantageous if it is compensated to maintain a level by a corresponding adjustment of the speed of the fan or a position of the control element.
Weiter ist es vorteilhaft, wenn eine Öffnung der Speisemulde mit einem Sensor gemessen wird. Dadurch kann bevorzugterweise die gemessene Öffnung der Speisemulde als Korrekturfaktor auf die Regelung der Speisewalze wirken. Dies dient dazu Verstopfungen oder Unterversorgungen im Speisekanal aufgrund einer sich ändernden Dichte der Faserflocken im Füllschacht zu verhindern.Further, it is advantageous if an opening of the feed trough is measured with a sensor. As a result, preferably the measured opening of the feed trough can act as a correction factor on the regulation of the feed roll. This serves to prevent blockages or undersupplies in the feed channel due to a changing density of the fiber flakes in the feed chute.
Weitere Vorteile der Erfindung sind in den nachfolgenden Ausführungsbeispielen beschrieben. Es zeigen:
-
Figur 1 - eine schematische Seitenansicht einer Karde nach dem Stand der Technik;
-
Figur 2 - eine schematische Darstellung einer erfindungsgemässen Vorrichtung in einer ersten Ausführungsform;
-
Figur 3 - eine schematische Darstellung einer erfindungsgemässen Vorrichtung in einer weiteren Ausführungsform und
-
Figur 4 - eine schematische Darstellung einer erfindungsgemässen Vorrichtung mit einer Regelung der Füllhöhe.
- FIG. 1
- a schematic side view of a card according to the prior art;
- FIG. 2
- a schematic representation of an inventive device in a first embodiment;
- FIG. 3
- a schematic representation of an inventive device in a further embodiment and
- FIG. 4
- a schematic representation of an inventive device with a control of the level.
Eine auf den Speisekanal 3 nachfolgende Speisevorrichtung 10 speist die Faserflocken, nunmehr in Form einer homogenen Faserwattenvorlage 11 dem Vorreissermodul 12 der Karde 1 zu. Dabei ist für die Speisevorrichtung 10 eine Kardenspeisewalze mit einer Speisemulde zur Dosierung der Faserwatte 11 vorgesehen. Die von der Speisevorrichtung 10 abgegebenen Faserflocken aus der Faserwattenvorlage 11 werden durch die im Vorreissermodul 12 enthaltenen Vorreisser weiter geöffnet und gleichzeitig von einem Teil der darin enthaltenen Verunreinigungen befreit. Die letzte Vorreisserwalze des Vorreissermoduls 12 übergibt die Fasern schliesslich an die Kardentrommel 13, welche die Fasern vollständig auflöst und parallelisiert. Die Kardentrommel 13 arbeitet dazu mit dem Deckelaggregat 14 zusammen. Nachdem die Fasern zum Teil mehrere Umläufe auf der Kardentrommel 13 durchgeführt haben, werden sie von der Abnehmerwalze 15 von der Kardentrommel 13 abgenommen, einer bandbildenden Einheit 16 zugeführt und schliesslich in Form eines Kardenbandes 17 in eine Kanne abgelegt (nicht gezeigt).
Unterhalb der Auflösewalze 7 wird durch einen Luftzuführkanal 19 von einem Ventilator 18 mit einem Antrieb 20 Luft 8 in den Speisekanal 3 eingeführt. Durch die Luft werden die Faserflocken im Speisekanal 3 gegen die Karde transportiert und zu einer Faserwatte 11 am Ende des Speisekanals 3 verdichtet. Die durch den Ventilator 18 in den Speisekanal 3 eingebrachte Luft 8 wird über einen luftdurchlässiger Bereich 9 in einer Wandung des Speisekanals 3 an dessen Ende wieder aus dem Speisekanal 3 abgeführt und über eine Rückführleitung 28 wieder zum Ventilator 18 zurück gebracht. In der Rückführleitung 28 ist eine Falschluftöffnung 29 vorgesehen. Die Falschluftöffnung 29 dient dazu Verluste von Luft an möglicherweise undichten Stellen der gesamten Luftführung vom und zum Ventilator 18 auszugleichen. Durch die Luft 8 wird am Ende des Speisekanals 3 aus den Faserflocken eine Faserwatte 11 gebildet und diese durch den Luftdruck verdichtet. Der Druck entsteht dabei aufgrund eines Widerstandes welche die Luft 8 durch ein Durchströmen der Faserwatte 11 überwinden muss um durch den luftdurchlässigen Bereich 9 vom Speisekanal 3 in die Rückführleitung 28 zu gelangen. Im Speisekanal 3 wird dabei eine Faserwatte 11 mit einer bestimmten Füllhöhe 34 gebildet.Below the
Im Speisekanal 3 ist ein Drucksensor 24 zur Messung eines Ist-Druckes der Luft 8 im Speisekanal 3 vorgesehen. Der Druck im Speisekanal 3 ist massgeblich für die Dichte der Faserwatte 11 und damit ein Massstab für ein zu erreichendes Faserwattegewicht W am Ende des Speisekanals 3.In the
Weiter ist eine Steuerung 31 gezeigt. In der Steuerung 31 sind Kennlinien für einen Soll-Volumenstrom V und einen Soll-Druck P für die Luft 8 hinterlegt. Über die Eingabe 33 wird ein gewünschtes Faserwattegewicht W in die Steuerung 31 eingegeben. Durch die Steuerung 31 werden diesem Faserwattegewicht W der entsprechende Soll-Volumenstrom V und der Soll-Druck P zugewiesen. Über den Drucksensor 24 wird ein Ist-Druck im Speisekanal 3 gemessen. Durch einen Soll-Ist-Wert-Vergleich des Druckes wird in der Steuerung eine entsprechende Korrektur der Drehzahl der Speisewalze 6 errechnet und über einen Frequenzumrichter 23 welcher auf den Antrieb 22 der Speisewalze 6 wirkt wird die Drehzahl der Speisewalze 6 korrigiert. Dadurch wird ein konstanter Druck und ein gleichbleibender Volumenstrom im Speisekanal 3 gewährleistet.Further, a
Im Speisekanal 3 ist ein Drucksensor 24 zur Messung eines Ist-Druckes der Luft 8 im Speisekanal 3 vorgesehen. Der Druck im Speisekanal 3 ist massgeblich für die Dichte der Faserwatte 11 und damit ein Massstab für ein zu erreichendes Faserwattegewicht W am Ende des Speisekanals 3.In the
Weiter ist eine Steuerung 31 gezeigt. In der Steuerung 31 sind Kennlinien für einen Soll-Volumenstrom V und einen Soll-Druck P für die Luft 8 hinterlegt. Über die Eingabe 33 wird ein gewünschtes Faserwattegewicht W in die Steuerung 31 eingegeben. Durch die Steuerung 31 werden diesem Faserwattegewicht W der entsprechende Soll-Volumenstrom V und der Soll-Druck P zugewiesen. Über den Drucksensor 24 wird ein Ist-Druck im Speisekanal 3 gemessen. Durch einen Soll-Ist-Wert-Vergleich des Druckes wird in der Steuerung eine entsprechende Korrektur der Drehzahl der Speisewalze 6 errechnet und über einen Frequenzumrichter 23 welcher auf den Antrieb 22 der Speisewalze 6 wirkt wird die Drehzahl der Speisewalze 6 korrigiert. Dadurch wird ein konstanter Druck und ein gleichbleibender Volumenstrom im Speisekanal 3 gewährleistet.Further, a
Weiter ist in der gezeigten Ausführung nach
In der gezeigten Ausführungsform ist zudem ein Öffnungssensor 27 an der Speisemulde 25 vorgesehen. Der Öffnungssensor 27 misst den Öffnungszustand der Speisemulde 25 und gibt dadurch eine Information über die Dichte der momentan durch die Speisewalze 6 aus dem Füllschacht 2 entnommenen Faserflocken 4. Durch die Steuerung 31 wird diese Information verarbeitet und als Korrekturfaktor auf die Regelung der Drehzahl des Antriebs 22 der Speisemulde 6 aufgeschaltet.In the embodiment shown, an
Die vorliegende Erfindung ist nicht auf die dargestellten und beschriebenen Ausführungsbeispiele beschränkt. Abwandlungen im Rahmen der Patentansprüche sind ebenso möglich wie eine Kombination der Merkmale, auch wenn diese in unterschiedlichen Ausführungsbeispielen dargestellt und beschrieben sind.The present invention is not limited to the illustrated and described embodiments. Variations within the scope of the claims are also possible as a combination of features, even if they are shown and described in different embodiments.
- 11
- Kardeteasel
- 22
- Füllschachthopper
- 33
- Speisekanalfeeding channel
- 44
- Faserflockenfiber flocks
- 55
- FüllschachtaustragFüllschachtaustrag
- 66
- Speisewalzefeed roll
- 77
- Auflösewalzeopening roller
- 88th
- Luftair
- 99
- Luftdurchlässiger Bereich der WandungAir permeable area of the wall
- 1010
- Speisevorrichtungfeeder
- 1111
- Faserwattefiber wadding
- 1212
- VorreissermodulVorreissermodul
- 1313
- Kardentrommelcarding drum
- 1414
- Deckelaggregatflat unit
- 1515
- Abnehmerwalzedoffer
- 1616
- Bandbildende EinheitBand-building unit
- 1717
- KardenbandKardenband
- 1818
- Ventilatorfan
- 1919
- Luftzuführkanalair supply duct
- 2020
- Antrieb VentilatorDrive fan
- 2121
- Frequenzumrichter VentilatorFrequency converter fan
- 2222
- Antrieb SpeisewalzeDrive feed roller
- 2323
- Frequenzumrichter SpeisewalzeFrequency converter feed roller
- 2424
- Drucksensorpressure sensor
- 2525
- Speisemuldefeed trough
- 2626
- Federzustellungspring delivery
- 2727
- Öffnungssensoropening sensor
- 2828
- RückführleitungReturn line
- 2929
- FalschluftöffnungAir opening
- 3030
- FaserwattegewichtsregelungFiber wadding weight control
- 3131
- Steuerungcontrol
- 3232
- Regelorganregulating element
- 3333
- Eingabe FaserwattegewichtInput fiber batting weight
- 3434
- Füllhöhe SpeisekanalFilling level feed channel
- 3535
- Füllsensorfill sensor
- 3636
- VolumenstromsteuerungFlow control
- WW
- FaserwattegewichtFiber wadding weight
- VV
- Soll-VolumenstromSet volume flow
- PP
- Soll-DruckTarget pressure
Claims (14)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH00420/18A CH714843A1 (en) | 2018-03-29 | 2018-03-29 | Feed device to a card. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3546625A1 true EP3546625A1 (en) | 2019-10-02 |
EP3546625B1 EP3546625B1 (en) | 2021-08-25 |
Family
ID=65812149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19162734.8A Active EP3546625B1 (en) | 2018-03-29 | 2019-03-14 | Feeding device for a carding machine |
Country Status (3)
Country | Link |
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EP (1) | EP3546625B1 (en) |
CN (1) | CN110318124B (en) |
CH (1) | CH714843A1 (en) |
Cited By (1)
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CN116837497A (en) * | 2023-07-07 | 2023-10-03 | 浙江中超新材料股份有限公司 | Variable-frequency speed-regulating cotton feeder and application method thereof |
Families Citing this family (2)
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CN111101242A (en) * | 2019-12-02 | 2020-05-05 | 莫永献 | High-efficient edulcoration carding machine is used in weaving |
CN111793861B (en) * | 2020-07-26 | 2022-04-01 | 潍坊驼王实业有限公司 | Carding device for manufacturing polypropylene short fiber non-woven geotextile |
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Also Published As
Publication number | Publication date |
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CN110318124A (en) | 2019-10-11 |
EP3546625B1 (en) | 2021-08-25 |
CN110318124B (en) | 2023-02-24 |
CH714843A1 (en) | 2019-09-30 |
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