EP2508659A1 - System for collecting and recovering spooling scraps - Google Patents
System for collecting and recovering spooling scraps Download PDFInfo
- Publication number
- EP2508659A1 EP2508659A1 EP12162025A EP12162025A EP2508659A1 EP 2508659 A1 EP2508659 A1 EP 2508659A1 EP 12162025 A EP12162025 A EP 12162025A EP 12162025 A EP12162025 A EP 12162025A EP 2508659 A1 EP2508659 A1 EP 2508659A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- collecting
- spooling
- filtering
- spooler
- scraps
- 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
- 239000000463 material Substances 0.000 claims abstract description 24
- 239000000428 dust Substances 0.000 claims abstract description 14
- 230000000717 retained effect Effects 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims description 38
- 239000012535 impurity Substances 0.000 claims description 12
- 238000007599 discharging Methods 0.000 claims description 10
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 230000001174 ascending effect Effects 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims 1
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 238000004804 winding Methods 0.000 description 10
- 239000002699 waste material Substances 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 208000012886 Vertigo Diseases 0.000 description 3
- 238000009960 carding Methods 0.000 description 3
- 238000005304 joining Methods 0.000 description 3
- 238000009987 spinning Methods 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01H—SPINNING OR TWISTING
- D01H11/00—Arrangements for confining or removing dust, fly or the like
- D01H11/005—Arrangements for confining or removing dust, fly or the like with blowing and/or suction devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H54/00—Winding, coiling, or depositing filamentary material
- B65H54/70—Other constructional features of yarn-winding machines
- B65H54/702—Arrangements for confining or removing dust
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H54/00—Winding, coiling, or depositing filamentary material
- B65H54/70—Other constructional features of yarn-winding machines
- B65H54/707—Suction generating system
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H67/00—Replacing or removing cores, receptacles, or completed packages at paying-out, winding, or depositing stations
- B65H67/08—Automatic end-finding and material-interconnecting arrangements
- B65H67/081—Automatic end-finding and material-interconnecting arrangements acting after interruption of the winding process, e.g. yarn breakage, yarn cut or package replacement
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65H—HANDLING THIN OR FILAMENTARY MATERIAL, e.g. SHEETS, WEBS, CABLES
- B65H2701/00—Handled material; Storage means
- B65H2701/30—Handled filamentary material
- B65H2701/31—Textiles threads or artificial strands of filaments
Definitions
- the present invention refers to a device for collecting and recovering the scraps produced during the spooling process by the units that constitute the automatic spooler.
- Spoolers indeed consist of a plurality of spooling units aligned along the front of the machine and provided with common control and service equipments. Among such common service equipments there are the devices for preparing the spools to be unwound in the spooling units.
- both the non continuous and high head suction service, for recovering the ends through the mouths 9 and 10, and the continuous low head service, for dust removal through the mouths 20 are carried out through an individual aspirator 22, one for each of the winding units aligned along the front of the machine.
- an aspirator consists of a rotary aspirator with a centrifugal impeller 25 actuated through a "brushless" electric motor 26 controlled in frequency by the control unit 16 of the winding unit.
- the mouth 20 of the "dust removal" service with continuous low vacuum suction is connected through a duct 30 to the suction unit of the winding unit, intercepted through a gate valve 31, controlled by the control unit 16 of the winding unit and normally kept open during the normal winding process.
- the mouths 9 and 10 work discontinuously with high vacuum suction during the interruptions to normal winding. They are respectively connected through a duct 34 to the suction unit 22 of the winding unit, intercepted through a gate valve 35, controlled by the control unit 16 of the winding unit and normally kept closed during the normal winding process.
- the gate valve 35 is only opened on occasion of the joining interventions.
- the individual suction unit 22 that equips the single winding unit 23 serves either the duct 30 of the low vacuum "dust removal" service or the duct 34 of the high vacuum suction.
- the different vacuum values required for the two alternative suction services are obtained by actuating the centrifugal aspirator 22 at different speeds, which has characteristic curves of the suction vacuum ⁇ P that varies inversely to the flow rate in volume, according to a band of curves parallel and increasing with the increase in rotation speed, as already described in the cited application IT 2009A2013 in the name of the same Applicant.
- the two ducts 30 and 34 of each spooling station are connected to a common filter 50, individual for each spooling station, which has the function of retaining the material picked up and transported through the suction and in particular it retains both the impurities of the "dust removal” collected through the spooling while functioning and the pieces of yarn, the so-called “fluff”, removed by the suctioning of the aspirator 22, when it is connected to the mouths 9 and 10 and actuated at high depression when the spooling is interrupted.
- the individual filter 50 can be equipped with a single fine mesh filtering sect that retains all of the material: both the impurities and the fluff.
- the individual filter 50 consists of two filtering chambers in series, of a hopper 55 below for collecting the separated fluff.
- the first filtering chamber is equipped with a rougher mesh filtering sect 51 that retains the "fluff", which is removed by the high-depression suction by the aspirator 22, when it is connected to the mouths 9 and 10 and actuated at high depression.
- the second filtering chamber downstream of the first, is equipped with a fine mesh filtering sect 52 for the impurities, consisting of hair and fibres, which on the other hand pass freely through the rougher filtering sect 51 that constitutes the first filtering chamber, both during filtering and during cleaning of the filter.
- the rougher mesh filtering sect has a hole dimension of the order of 20 mesh
- the fine mesh filtering sect has a hole dimension of the order of 800 mesh.
- the filtering sects of the filter 50 are preferably arranged to receive, from below, the flow of fluid containing the material to be separated, so that, when the suction flow at high depression stops, most of the rough material intercepted and retained by the filtering sect 51 falls spontaneously downwards into the hopper 55 below, freeing the first of the filtering sects.
- the amount of material to be retained mainly consists of fluff.
- the linear size of the fluff can indeed range from a few centimetres, in the normal preparation of the join of the yarn, up to ten or even more metres, for long defects of the count of the yarn detected through the slubcatcher.
- the impurities of the "dust removal” have an average size of about a millimetre or slightly more.
- the material separated and recovered through the filters is generally recycled to carding, in order to recover the fibres that constitute the fluff.
- the impurities and the short fibres possibly present in the recovered material are separated and removed, keeping just the fibres of acceptable length being processed.
- the realization of the filter with a double filtering chamber in series, shown in figure 2 allows a greater accumulation of material before the overall load loss of the filter requires the discharging operation of the material.
- the fluff is substantially stopped by the rough filtering sect and, when the suction at high depression stops, it mostly falls and accumulates on the bottom of the filter.
- the filters 50 From the bottom of the filters 50, which the spooling stations are equipped with, the accumulated material is periodically discharged, respectively, through ducts 53, intercepted through a shutter 54, which gather in a common discharge collector 70.
- the filters 50 are equipped with a waste valve 57, which is opened for the discharge operations of the material accumulated in the filters 50. The opening of such waste valves 57 preferably isolates the filter 50 from its aspirator 22.
- Figure 3 illustrates the assembly of the collection system of spooling scraps. All of the individual discharges 53 of the spooling units 23 are connected to a common collector 70, which collects all of the material separated in the respective filters 50.
- the devices 63 for preparing the spools can also be advantageously connected to the collector 70, for example as described in patent application IT 2009 A 2011 and herein shown schematically. Such devices generate a significant amount of residuals of yarn pieces, suctioned through an individual aspirator 64, deposited in mesh filters 65 and discharged through a duct 68, through a scheme equipped with discharging shutters 66 and with waste valves 67 totally analogous to that of the filters 50 of the spooling units according to figure 1 .
- All of the filters 50 and 65 are connected through the collector 70 to a collective system for collecting their scraps, consisting of a duct having a small size that is arranged along the machine and that receives the flow coming from all of the spooling units 23 and, preferably, also from the devices 63 for preparing the spools.
- the collector 70 is served by a high-depression aspirator 71, which provides for periodically discharging the material of the filters through pneumatic transportation to a general filter 80 that is described in greater details in figures 4 and 5 . In order to avoid clogging, the transportation speed in the duct 70 is kept around 20 m/sec.
- the discharging needs of the material retained by the filters are very variable, according to the yarns treated in the spooler.
- the greater discharging frequency is required by the devices 63 for preparing the spools, which require cleaning of their filters 65 even every 10-20 minutes, in the order of magnitude of a few hundred spools prepared.
- the filters 50 which the spooling stations 23 are equipped with in general require cleaning with a period of the order of magnitude of an hour, in the case of filters having a single fine mesh filtering sect that retains all of the material: both dust and fluff.
- the filters 50 are realized with a double filtering chamber in series, as shown in figure 2 , such a cleaning frequency is reduced, increasing the intervals between one cycle and the other by about 40-50%, unless very hairy yarns are processed.
- Such cleaning is preferably carried out for one filter 50 at a time while its spooling unit 23 is operating.
- the operation requires a few seconds and is carried out, for the spooling units 23, firstly by opening their waste valves 57, preferably isolating their filter 50 from the aspirator 22, closing the valves 31,35 towards the spooling unit 23 and then opening the discharge valve 54 on the duct 53, with the aspirator 71 in action.
- the cleaning of the filter is thus prevented from affecting the spooling in its normal operation.
- the suctioning through the aspirator 71 draws air from the waste valves 57 and empties the filters 50 of the material accumulated bringing it into the general filter 80 through the collector 70.
- the general filter 80 can be a conventional filter that separates and indistinctly discharges the fluff together with the fine impurities, recycling them to carding. In the carding process of dust, tufts, "neps" and short fibres are eliminated from the production cycle.
- the general filter 80 is made to obtain a classification of the material in a double cyclone system, illustrated in greater details in figure 4 as an overall scheme; in figures 5A,B the cyclones are shown in section to describe their operation.
- the filtering system 80 consists of a pair of cyclones in series placed in depression through the aspirator 71.
- the first cyclone 81 is fed by the duct 70 through a suctioned air flow containing both fluff and other impurities coming from the filters 50 and 65 that are gradually cleaned, opening their waste valves 57 and 67 and their shutters 54 and 66.
- the flow to be filtered is introduced into the cyclone 81 in the upper part and with tangential direction, generating a spiral motion descending downwards.
- the particulate of greater dimensions, the fluff comes out of the flow and by inertia comes into contact with and slows down against the inner conical walls of the cyclone: as a result of the effect of gravity, the particulate slides and accumulates at the bottom of the conical hopper 82, from which it is periodically discharged through the shutter 83.
- Such a particulate essentially consists of fluff that can be recycled.
- the cyclone 81 works discontinuously and operates as a separator of the fluff from the particulate, unlike what is described in the cited EP 2.045.378 .
- the flow of the duct 87 is introduced into the second cyclone 91, in particular in its lower conical part 92 and with tangential direction into the opening 94.
- a spiral motion descending downwards is generated.
- the medium-sized particulate comes out of the flow, by inertia comes into contact with and slows down against the inner conical walls of the cyclone: as a result of the effect of gravity the medium-sized particulate slides and accumulates at the bottom of the conical hopper 92, from which it is periodically discharged through the shutter 95.
- the air flow containing the finer particulate inverts the sense of its motion and rises spiralling upwards to the upper part 93 of the second cyclone 91.
- Such an upper part 93 is cylinder-shaped and, in its central part, it is occupied by a filtering cartridge 96, which intercepts the ascending flow and sorts and retains the residual particulate.
- the hole dimension of the filtering cartridge is of the order of 15 ⁇ m.
- Such a filtering cartridge is preferably cylindrical, in a common axis with the cyclone 91, equipped with a blind hole 97 and with a blind upper crown 98, so as to force the air flow to pass through its cylindrical filtering surface, with the flows indicated with the arrows, and then to come out of the upper opening 100 towards the aspirator 71 and its release into the atmosphere.
- a diffuser 102 of compressed air for washing the cartridge is placed, connected to the service compressed air.
- the load loss i.e. the differential pressure
- the aspirator 71 is stopped and its discharge is closed.
- the cartridge 96 is cleaned, simultaneously opening the solenoid valve 104 and the shutter 95 of the hopper 92 and injecting compressed air through the diffuser 102. In this way a "counter-washing" is carried out from inside to outside that frees the particulate retained on the outer surface of the cartridge 96.
- the individual filters 50 are cleaned one at a time by opening their valves 54 and their respective waste valves 57 in sequence.
- the procedure is totally analogous.
- a suctioning depression of 10-13 kPa, or 1000-1300 mm of water column is applied.
- Such depression values refer to the depression exerted in the filters 50 and 65 to be cleaned, whereas the depression values in the members downstream are affected by the load losses of the overall circuit.
- the discharging device of the spooling scraps according to the present invention also allows such discharging to be carried out through a single duct, and furthermore one with a small diameter, and through low suctioning powers installed, since it is provided for discharging one filter at a time.
- the number of filters installed for the spooling units and the relative intercepting shutters is reduced to the minimum, as well as the relative command and control members.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Cyclones (AREA)
- Spinning Or Twisting Of Yarns (AREA)
- Adjustment Of Camera Lenses (AREA)
- Treating Waste Gases (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
- The present invention refers to a device for collecting and recovering the scraps produced during the spooling process by the units that constitute the automatic spooler.
- In industral practice, it is common to use the technique of producing yarns in a spinning stage followed by a spooling stage wherein the yarn is unwound from its spool, purified of its defects and rewound in a reel. Spoolers indeed consist of a plurality of spooling units aligned along the front of the machine and provided with common control and service equipments. Among such common service equipments there are the devices for preparing the spools to be unwound in the spooling units.
- As already described in the previous Italian patent application
IT 2009A2013 figure 1 that shows the path of theyarn 2 from thelower spool 1 to theupper collecting reel 12, as follows: - 3. group of members for guiding the yarn,
- 4. the sensor for detecting the presence of the yarn,
- 5.
thread tightener 5, - 6. end joining device, known as thread joiner, served by
- 9,10. suction mouths for catching and delivering the ends,
- 11. slubcatcher,
- 12. collection reel, actuated in rotation by the
- 13. roller, and rests supported by
- 14. the reel-carrying arm,
- 15.
spool positioning pin 1, - 20. one or more suction mouths by the
spool 1 in order to eliminate the impurities, substantially consisting of hair and fluff that develop while the spooling is in function, commonly called "dust removal". - Again according to the cited application
IT 2009A2013 mouths mouths 20 are carried out through anindividual aspirator 22, one for each of the winding units aligned along the front of the machine. Such an aspirator consists of a rotary aspirator with acentrifugal impeller 25 actuated through a "brushless"electric motor 26 controlled in frequency by thecontrol unit 16 of the winding unit. - The
mouth 20 of the "dust removal" service with continuous low vacuum suction is connected through aduct 30 to the suction unit of the winding unit, intercepted through agate valve 31, controlled by thecontrol unit 16 of the winding unit and normally kept open during the normal winding process. Themouths duct 34 to thesuction unit 22 of the winding unit, intercepted through agate valve 35, controlled by thecontrol unit 16 of the winding unit and normally kept closed during the normal winding process. Thegate valve 35 is only opened on occasion of the joining interventions. Basically, theindividual suction unit 22 that equips the single windingunit 23 serves either theduct 30 of the low vacuum "dust removal" service or theduct 34 of the high vacuum suction. - The different vacuum values required for the two alternative suction services are obtained by actuating the
centrifugal aspirator 22 at different speeds, which has characteristic curves of the suction vacuum ΔP that varies inversely to the flow rate in volume, according to a band of curves parallel and increasing with the increase in rotation speed, as already described in the cited applicationIT 2009A2013 - In the prior art, for example in patent application
EP 2.045.378 to Murata , just the "dust removal" service for spinning units is described, for retaining "fly waste". Such a service is carried out by continuously suctioning such "fly waste" through a collector from one or more spinning units and then separating it from the transportation air through a cyclone separator. Such a prior art document does not consider the technical problem of alternately collecting dust and fluff through the same filtering device, jointly discharging them and then separating them to recover the fluff, nor the cyclones present in documentEP 2.045.378 would be able to work the two materials. - According to the present invention the two
ducts common filter 50, individual for each spooling station, which has the function of retaining the material picked up and transported through the suction and in particular it retains both the impurities of the "dust removal" collected through the spooling while functioning and the pieces of yarn, the so-called "fluff", removed by the suctioning of theaspirator 22, when it is connected to themouths - In each spooling station, the
individual filter 50 can be equipped with a single fine mesh filtering sect that retains all of the material: both the impurities and the fluff. - According to a preferred embodiment of the present invention, shown in the detail of
figure 2 in an axonometric view, theindividual filter 50 consists of two filtering chambers in series, of ahopper 55 below for collecting the separated fluff. The first filtering chamber is equipped with a roughermesh filtering sect 51 that retains the "fluff", which is removed by the high-depression suction by theaspirator 22, when it is connected to themouths mesh filtering sect 52 for the impurities, consisting of hair and fibres, which on the other hand pass freely through therougher filtering sect 51 that constitutes the first filtering chamber, both during filtering and during cleaning of the filter. The rougher mesh filtering sect has a hole dimension of the order of 20 mesh, whereas the fine mesh filtering sect has a hole dimension of the order of 800 mesh. - The filtering sects of the
filter 50, both in the embodiment with a single filtering chamber and in the embodiment with a double filtering chamber in series, are preferably arranged to receive, from below, the flow of fluid containing the material to be separated, so that, when the suction flow at high depression stops, most of the rough material intercepted and retained by thefiltering sect 51 falls spontaneously downwards into thehopper 55 below, freeing the first of the filtering sects. - In general, the amount of material to be retained mainly consists of fluff. The linear size of the fluff can indeed range from a few centimetres, in the normal preparation of the join of the yarn, up to ten or even more metres, for long defects of the count of the yarn detected through the slubcatcher. Again in general, the impurities of the "dust removal" have an average size of about a millimetre or slightly more.
- In industrial practice, the material separated and recovered through the filters is generally recycled to carding, in order to recover the fibres that constitute the fluff. In such a processing, the impurities and the short fibres possibly present in the recovered material are separated and removed, keeping just the fibres of acceptable length being processed.
- The realization of the filter with a double filtering chamber in series, shown in
figure 2 , allows a greater accumulation of material before the overall load loss of the filter requires the discharging operation of the material. In the first filtering chamber, during the filtering of the fluff deriving from the search for the ends for joining the yarn, the fluff is substantially stopped by the rough filtering sect and, when the suction at high depression stops, it mostly falls and accumulates on the bottom of the filter. - From the bottom of the
filters 50, which the spooling stations are equipped with, the accumulated material is periodically discharged, respectively, throughducts 53, intercepted through ashutter 54, which gather in acommon discharge collector 70. On the opposite upper side, thefilters 50 are equipped with awaste valve 57, which is opened for the discharge operations of the material accumulated in thefilters 50. The opening ofsuch waste valves 57 preferably isolates thefilter 50 from itsaspirator 22. -
Figure 3 illustrates the assembly of the collection system of spooling scraps. All of theindividual discharges 53 of the spoolingunits 23 are connected to acommon collector 70, which collects all of the material separated in the respective filters 50. - The
devices 63 for preparing the spools can also be advantageously connected to thecollector 70, for example as described in patent applicationIT 2009 A 2011 duct 68, through a scheme equipped with dischargingshutters 66 and withwaste valves 67 totally analogous to that of thefilters 50 of the spooling units according tofigure 1 . - All of the
filters collector 70 to a collective system for collecting their scraps, consisting of a duct having a small size that is arranged along the machine and that receives the flow coming from all of the spoolingunits 23 and, preferably, also from thedevices 63 for preparing the spools. Thecollector 70 is served by a high-depression aspirator 71, which provides for periodically discharging the material of the filters through pneumatic transportation to ageneral filter 80 that is described in greater details infigures 4 and5 . In order to avoid clogging, the transportation speed in theduct 70 is kept around 20 m/sec. - The discharging needs of the material retained by the filters are very variable, according to the yarns treated in the spooler. In general, the greater discharging frequency is required by the
devices 63 for preparing the spools, which require cleaning of theirfilters 65 even every 10-20 minutes, in the order of magnitude of a few hundred spools prepared. - The
filters 50 which thespooling stations 23 are equipped with, on the other hand, in general require cleaning with a period of the order of magnitude of an hour, in the case of filters having a single fine mesh filtering sect that retains all of the material: both dust and fluff. In case thefilters 50 are realized with a double filtering chamber in series, as shown infigure 2 , such a cleaning frequency is reduced, increasing the intervals between one cycle and the other by about 40-50%, unless very hairy yarns are processed. - Such cleaning is preferably carried out for one
filter 50 at a time while itsspooling unit 23 is operating. The operation requires a few seconds and is carried out, for the spoolingunits 23, firstly by opening theirwaste valves 57, preferably isolating theirfilter 50 from theaspirator 22, closing thevalves unit 23 and then opening thedischarge valve 54 on theduct 53, with theaspirator 71 in action. The cleaning of the filter is thus prevented from affecting the spooling in its normal operation. The suctioning through theaspirator 71 draws air from thewaste valves 57 and empties thefilters 50 of the material accumulated bringing it into thegeneral filter 80 through thecollector 70. - The
general filter 80 can be a conventional filter that separates and indistinctly discharges the fluff together with the fine impurities, recycling them to carding. In the carding process of dust, tufts, "neps" and short fibres are eliminated from the production cycle. - According to a preferred embodiment of the invention the
general filter 80 is made to obtain a classification of the material in a double cyclone system, illustrated in greater details infigure 4 as an overall scheme; infigures 5A,B the cyclones are shown in section to describe their operation. - With reference to
figures 4 and5A , thefiltering system 80 consists of a pair of cyclones in series placed in depression through theaspirator 71. Thefirst cyclone 81 is fed by theduct 70 through a suctioned air flow containing both fluff and other impurities coming from thefilters waste valves shutters cyclone 81 in the upper part and with tangential direction, generating a spiral motion descending downwards. As a result of the effect of the centrifugal force, the particulate of greater dimensions, the fluff, comes out of the flow and by inertia comes into contact with and slows down against the inner conical walls of the cyclone: as a result of the effect of gravity, the particulate slides and accumulates at the bottom of theconical hopper 82, from which it is periodically discharged through theshutter 83. Such a particulate essentially consists of fluff that can be recycled. - The
cyclone 81 works discontinuously and operates as a separator of the fluff from the particulate, unlike what is described in the citedEP 2.045.378 . - As a result of the effect of the pressure difference between the
tangential inlet opening 85 and the upper outlet opening 86, the air flow inverts the sense of its motion and rises in a tight spiral upwards to thedischarge opening 86 in axis with thecyclone 81, also taking the smaller sized residual particulate with it in theduct 87. - As also illustrated in
figure 5B , the flow of theduct 87 is introduced into thesecond cyclone 91, in particular in its lowerconical part 92 and with tangential direction into theopening 94. Like for thecyclone 81, also here a spiral motion descending downwards is generated. As a result of the effect of the centrifugal force, the medium-sized particulate comes out of the flow, by inertia comes into contact with and slows down against the inner conical walls of the cyclone: as a result of the effect of gravity the medium-sized particulate slides and accumulates at the bottom of theconical hopper 92, from which it is periodically discharged through theshutter 95. Also here, the air flow containing the finer particulate inverts the sense of its motion and rises spiralling upwards to theupper part 93 of thesecond cyclone 91. Such anupper part 93 is cylinder-shaped and, in its central part, it is occupied by afiltering cartridge 96, which intercepts the ascending flow and sorts and retains the residual particulate. - Unlike what is described by document
EP 2.045.378 , the finer particulate consisting of the "fly" - the dust and hair lost by the processed yarn - cannot be significantly separated through just the cyclone configuration of thesecond separator 91, especially when operating discontinuously like in the device according to the present invention. - The hole dimension of the filtering cartridge is of the order of 15 µm. Such a filtering cartridge is preferably cylindrical, in a common axis with the
cyclone 91, equipped with ablind hole 97 and with a blindupper crown 98, so as to force the air flow to pass through its cylindrical filtering surface, with the flows indicated with the arrows, and then to come out of theupper opening 100 towards theaspirator 71 and its release into the atmosphere. - Above the cartridge 96 a
diffuser 102 of compressed air for washing the cartridge is placed, connected to the service compressed air. During the cleaning operations of theindividual filters cartridge 96, is constantly checked, for example through thedifferential manometer 103. When such a measurement reaches a predetermined value, at the end of the cleaning cycle theaspirator 71 is stopped and its discharge is closed. Then thecartridge 96 is cleaned, simultaneously opening thesolenoid valve 104 and theshutter 95 of thehopper 92 and injecting compressed air through thediffuser 102. In this way a "counter-washing" is carried out from inside to outside that frees the particulate retained on the outer surface of thecartridge 96. - The individual filters 50 are cleaned one at a time by opening their
valves 54 and theirrespective waste valves 57 in sequence. For thefilters 65 of thepreparation devices 63 the procedure is totally analogous. Through the aspirator 71 a suctioning depression of 10-13 kPa, or 1000-1300 mm of water column is applied. Such depression values refer to the depression exerted in thefilters - The discharging device of the spooling scraps according to the present invention also allows such discharging to be carried out through a single duct, and furthermore one with a small diameter, and through low suctioning powers installed, since it is provided for discharging one filter at a time. The number of filters installed for the spooling units and the relative intercepting shutters is reduced to the minimum, as well as the relative command and control members.
Claims (10)
- A device for collecting the scraps produced by a spooler, consisting of a plurality of spooling units (23) aligned and served by a suctioning system consisting of a plurality of individual aspirators (22) which individually equip each spooling unit (23), wherein each single spooler (22) alternately provides a low depression continuous suction, while the spooling is in function, either for the removal service of impurities and of the hair of the yarn, i.e. a "dust removal service", or a high depression discontinuous suction, for eliminating pieces of yarn, i.e. fluff, deriving from the catching and junction operations of the yarn, while the spooling is interrupted, characterized in that each individual aspirator (22) is provided with a separating filter (50) of the suctioned material, such filter alternately receiving and retaining impurities and fluff, and in that all filters (50) of the spooling stations (23) forming the spooler are connected through a common duct (70) to a common general filter (80) for collecting scraps that it periodically discharges and it receives the material retained by such filters (50), one at a time and for both materials.
- The device for collecting scraps produced by a spooler according to claim 1, characterized in that the individual filter (50) is realized with two filtering chambers in series, of which the first filtering chamber is provided with a rougher mesh filtering sect (51) which retains the fluff, suctioned by the high depression aspirator by the aspirator (22), and the second filtering chamber, placed downstream of the first one, is provided with a fine mesh filtering sect (52) which retains the impurities.
- The device for collecting the scraps produced by a spooler according to claim 2, characterized in that the two filtering chambers in series are realized with the rougher mesh having a dimension of the holes of the order of 20 mesh and with the fine mesh having a dimension of the order of 800 mesh.
- The device for collecting the scraps produced by a spooler according to claim 1, characterized in that spool preparation devices (63) which equip the spooler are also connected to it, in order to discharge the respective filters (65) which collect a significant amount of residuals of yarn pieces.
- The device for collecting the scraps produced by a spooler according to claim 1, characterized in that the common general filter (80) for collecting spooling scraps is realized to obtain a classification of the material in a double cyclone system, formed by a pair of cyclones (81,91) in series, placed in depression with the aspirator (71) and fed by the duct (70) with a suctioned air flow, containing both fluff and impurities, of which the first cyclone (81) sorts out the fluff and the second cyclone (91) sorts out the residual particulate, such cyclones being provided in their lower part with conical hoppers and discharging shutters (83,95).
- The device for collecting the scraps produced by a spooler according to claim 5, characterized in that the upper part (93) of the second cyclone (91) is occupied by a filtering cartridge (96) which intercepts the ascending flow and sorts and retains the residual particulate.
- The device for collecting the scraps produced by a spooler according to claim 6, characterized in that the dimension of the pores of the filtering cartridge (96) is of the order of 15 µm.
- The device for collecting the scraps produced by a spooler according to claim 6, characterized in that the filtering cartridge (96) is cylindrical, with a common axis with the cyclone (91) and disposed so that it forces the air flow to pass through its cylindrical surface and thus to exit from the upper opening (100) towards the aspirator (71) and its discharge to the atmosphere.
- The device for collecting the scraps produced by a spooler according to claim 6, characterized in that over the filtering cartridge (96) a diffuser (102) for compressed air is placed, for washing the cartridge, connected to the service compressed air.
- The device for collecting the scraps produced by a spooler according to claim 6, characterized in that between the upstream and downstream of the cartridge (96) a differential manometer (103) is installed, in order to measure the loss of charge in the cartridge itself.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT000585A ITMI20110585A1 (en) | 2011-04-08 | 2011-04-08 | SYSTEM FOR THE COLLECTION AND RECOVERY OF ROCKING SFRIDES |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2508659A1 true EP2508659A1 (en) | 2012-10-10 |
EP2508659B1 EP2508659B1 (en) | 2014-03-12 |
Family
ID=44553940
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20120162025 Active EP2508659B1 (en) | 2011-04-08 | 2012-03-29 | System for collecting and recovering spooling scraps |
Country Status (3)
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EP (1) | EP2508659B1 (en) |
CN (1) | CN102861740B (en) |
IT (1) | ITMI20110585A1 (en) |
Cited By (7)
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EP2653423B1 (en) * | 2012-04-18 | 2015-07-15 | Savio Macchine Tessili S.p.A. | Separation device of dust from pieces of yarn for the collection and recovery of winding waste and winding machine wih such device |
CN106516877A (en) * | 2016-12-13 | 2017-03-22 | 苏州市朗润纺织科技有限公司 | Cotton cloth attachment anti-adhesion yarn winding device |
CN107503007A (en) * | 2017-10-24 | 2017-12-22 | 青岛金汇丰机械有限公司 | Dust exhaust apparatus and fly frame |
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EP3489398A1 (en) * | 2017-11-22 | 2019-05-29 | Savio Macchine Tessili S.p.A. | Open-end spinning machine with improved yarn waste discharge device and related yarn waste discharge method |
CN113893635A (en) * | 2021-11-16 | 2022-01-07 | 江苏精亚环境科技有限公司 | Secondary dust, pile and dust separating method and equipment for dust filter unit |
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JP2016079526A (en) * | 2014-10-16 | 2016-05-16 | 村田機械株式会社 | Yarn winding machine |
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ITMI20012421A1 (en) * | 2001-11-16 | 2003-05-16 | Savio Macchine Tessili Spa | DEVICE AND PROCEDURE FOR DEPURING THE WIRE OF THE SUPPLY COIL TO AN AUTOMATIC SPOOLER FROM ITS DEFECTIVE TERMINAL SECTIONS |
ITMI20070133A1 (en) * | 2007-01-29 | 2008-07-30 | Savio Macchine Tessili Spa | SUCTION SYSTEM FOR ROCKERS |
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DE19908378A1 (en) * | 1999-02-26 | 2000-08-31 | Schlafhorst & Co W | Filter assembly at an open-end spinner has a filter chamber divided into main and reserve chambers with controlled shut-offs at their air outlet openings to increase the intervals between filter cleaning |
DE102008040992A1 (en) * | 2007-09-12 | 2009-03-19 | Rieter Ingolstadt Gmbh | Suction system for sucking spinning air from spinning aggregates of rotor spinning machine, has controller designed to produce regulating signal that is provided for regulating primary low pressure to control secondary low pressure |
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Cited By (9)
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EP2653423B1 (en) * | 2012-04-18 | 2015-07-15 | Savio Macchine Tessili S.p.A. | Separation device of dust from pieces of yarn for the collection and recovery of winding waste and winding machine wih such device |
CN106516877A (en) * | 2016-12-13 | 2017-03-22 | 苏州市朗润纺织科技有限公司 | Cotton cloth attachment anti-adhesion yarn winding device |
CN107503007A (en) * | 2017-10-24 | 2017-12-22 | 青岛金汇丰机械有限公司 | Dust exhaust apparatus and fly frame |
EP3489398A1 (en) * | 2017-11-22 | 2019-05-29 | Savio Macchine Tessili S.p.A. | Open-end spinning machine with improved yarn waste discharge device and related yarn waste discharge method |
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CN107844109B (en) * | 2017-12-11 | 2023-09-08 | 保定市尤里卡电气设备有限公司 | Down washing control system |
CN113893635A (en) * | 2021-11-16 | 2022-01-07 | 江苏精亚环境科技有限公司 | Secondary dust, pile and dust separating method and equipment for dust filter unit |
CN113893635B (en) * | 2021-11-16 | 2023-07-21 | 江苏精亚环境科技有限公司 | Method and equipment for separating secondary dust and velvet dust of dust filtering unit |
EP4345199A1 (en) * | 2022-09-30 | 2024-04-03 | TMT Machinery, Inc. | False-twisting machine and fiber waste collection device |
Also Published As
Publication number | Publication date |
---|---|
CN102861740B (en) | 2016-12-28 |
ITMI20110585A1 (en) | 2012-10-09 |
CN102861740A (en) | 2013-01-09 |
EP2508659B1 (en) | 2014-03-12 |
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