WO2011070639A1 - Powder adding device and adding method thereof - Google Patents
Powder adding device and adding method thereof Download PDFInfo
- Publication number
- WO2011070639A1 WO2011070639A1 PCT/JP2009/070474 JP2009070474W WO2011070639A1 WO 2011070639 A1 WO2011070639 A1 WO 2011070639A1 JP 2009070474 W JP2009070474 W JP 2009070474W WO 2011070639 A1 WO2011070639 A1 WO 2011070639A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- web material
- air
- transfer path
- powder
- addition
- Prior art date
Links
- 239000000843 powder Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims description 16
- 239000000463 material Substances 0.000 claims abstract description 75
- 239000007921 spray Substances 0.000 claims abstract description 32
- 239000008187 granular material Substances 0.000 claims description 52
- 239000002245 particle Substances 0.000 claims description 47
- 238000011144 upstream manufacturing Methods 0.000 claims description 14
- 235000019504 cigarettes Nutrition 0.000 claims description 9
- 230000035699 permeability Effects 0.000 claims description 7
- 239000000654 additive Substances 0.000 claims 1
- 230000000996 additive effect Effects 0.000 claims 1
- 239000003054 catalyst Substances 0.000 abstract description 3
- 239000002304 perfume Substances 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000000428 dust Substances 0.000 description 6
- 239000000835 fiber Substances 0.000 description 6
- 239000004014 plasticizer Substances 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- 239000000779 smoke Substances 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 239000003205 fragrance Substances 0.000 description 2
- 239000005022 packaging material Substances 0.000 description 2
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 description 2
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 235000013773 glyceryl triacetate Nutrition 0.000 description 1
- 239000001087 glyceryl triacetate Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229960002715 nicotine Drugs 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 229960002622 triacetin Drugs 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
- B05B7/14—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas designed for spraying particulate materials
- B05B7/1481—Spray pistols or apparatus for discharging particulate material
- B05B7/1486—Spray pistols or apparatus for discharging particulate material for spraying particulate material in dry state
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24D—CIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
- A24D3/00—Tobacco smoke filters, e.g. filter-tips, filtering inserts; Filters specially adapted for simulated smoking devices; Mouthpieces for cigars or cigarettes
- A24D3/02—Manufacture of tobacco smoke filters
- A24D3/0204—Preliminary operations before the filter rod forming process, e.g. crimping, blooming
- A24D3/0212—Applying additives to filter materials
- A24D3/0225—Applying additives to filter materials with solid additives, e.g. incorporation of a granular product
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B14/00—Arrangements for collecting, re-using or eliminating excess spraying material
- B05B14/10—Arrangements for collecting, re-using or eliminating excess spraying material the excess material being particulate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B14/00—Arrangements for collecting, re-using or eliminating excess spraying material
- B05B14/20—Arrangements for collecting, re-using or eliminating excess spraying material from moving belts, e.g. filtering belts or conveying belts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
- B05B5/08—Plant for applying liquids or other fluent materials to objects
- B05B5/14—Plant for applying liquids or other fluent materials to objects specially adapted for coating continuously moving elongated bodies, e.g. wires, strips, pipes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
- B05B1/14—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with multiple outlet openings; with strainers in or outside the outlet opening
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B5/00—Electrostatic spraying apparatus; Spraying apparatus with means for charging the spray electrically; Apparatus for spraying liquids or other fluent materials by other electric means
- B05B5/025—Discharge apparatus, e.g. electrostatic spray guns
- B05B5/03—Discharge apparatus, e.g. electrostatic spray guns characterised by the use of gas, e.g. electrostatically assisted pneumatic spraying
- B05B5/032—Discharge apparatus, e.g. electrostatic spray guns characterised by the use of gas, e.g. electrostatically assisted pneumatic spraying for spraying particulate materials
Definitions
- the present invention relates to an addition apparatus for adding a granular material to a web material having air permeability, and an addition method thereof, and more particularly, an addition of a granular material suitable for a filter manufacturing machine for manufacturing a filter for a filter cigarette.
- the present invention relates to an apparatus and an addition method.
- the filter manufacturing machine has a filter tow supply path as a web material, and this filter tow is supplied to the wrapping apparatus along the supply path.
- the filter tow is formed from filter fibers and is in the form of a web.
- the filter tow is squeezed into a rod shape, and is wrapped by a packaging material and formed into a continuous rod. After this, the continuous rod is cut into individual filter rods, which have multiple times the length of the filters used in the individual filter cigarettes.
- the original function required for the above-mentioned filter is to remove nicotine and tar in the mainstream smoke of the cigarette when smoking the filter cigarette, but in addition to the original function, in recent years other functions have been added to the filter. It is desired to add. As such other additional functions, it is conceivable to add a fragrance to the mainstream smoke, or to oxidize CO in the mainstream smoke to CO 2. It is necessary to add a granular material such as a catalyst.
- the filter manufacturing machine disclosed in Patent Document 1 is provided with an adding device for adding the above-described powder particles.
- the adding device includes a sealed chamber, that is, a powder chamber, and this powder chamber is disposed in the supply path of the filter tow. Therefore, the filter tow passes through the powder chamber and is conveyed toward the wrapping device. Further, a powder particle ejection nozzle is disposed in the powder chamber, and this ejection nozzle ejects the powder particle toward the filter tow passing through the powder chamber, thereby adding the powder particle to the filter tow.
- a suction fan and a pair of rod-shaped chargers are indispensable for the adding device of Patent Document 1.
- the suction fan keeps the powder chamber in a vacuum state, thereby discharging the suspended powder particles from the powder chamber, and the charger uniformly charges the filter tow upstream of the powder chamber. While aiming at reduction of a granular material, adhesion of the granular material to a filter tow is promoted.
- the above-described suction fan and charger increase the size and complexity of the entire addition device.
- the discharge of the floating granular material from the powder chamber by the suction fan wastes a part of the granular material ejected from the ejection nozzle and makes it impossible to effectively attach the granular material to the filter tow.
- the addition apparatus of patent document 1 is not only the amount of the granular material ejected from an ejection nozzle but the charge level of the filter tow by a charger. Control is also required, and the amount of powder added cannot be easily adjusted.
- the object of the present invention is to allow the powder material to be effectively added to the web material without the need for a closed chamber such as a powder chamber or a suction fan for exhausting the sealed chamber.
- An object of the present invention is to provide an apparatus for adding a granular material and an addition method thereof, the amount of which can be easily adjusted.
- the granular material addition apparatus of the present invention is provided with a transfer path for transferring a web material having air permeability, and a powder disposed toward the web material, disposed above the transfer path.
- the spray unit ejects the powder and the granular material together with the air toward the web material transferred on the sieve member of the fixing unit.
- air passes through the web material and the sieve member, but the granular material is prevented from passing through the web material by the sieve member and remains in the web material. Therefore, the granular material does not float above the web material, and the granular material is effectively fixed to the web material.
- the fixing unit is the above-described sieve member, and extends below the transfer path along the transfer path and allows the passage of air, and an upper conveyor extends above the transfer path along the transfer path.
- the upper conveyor has a downstream end that sandwiches the web material in cooperation with the lower conveyor.
- the above-mentioned spray unit can include a plurality of electrostatic nozzles that charge and eject the powder particles, and in this case, the charged powder particles are effectively attached to the web material.
- the lower conveyor has an endless mesh belt. Such a mesh belt allows only air to escape from the web material, leaving a granular material in the web material.
- the above-described upper conveyor is inclined with respect to the transfer path and has an upstream end positioned above the transfer path.
- the upper conveyor can adjust the height level of the upstream end from the transfer path.
- the upper conveyor may extend along the transfer path in parallel with the lower conveyor. In this case, the upper conveyor presses the web material on the entire lower surface thereof.
- the fixing unit can further comprise a suction source arranged below the lower conveyor, which sucks the air escaped through the web material and the lower conveyor.
- the present invention also provides a method for adding powder particles.
- the addition method of the present invention transfers a web material having air permeability along a transfer path, and the powder particles are applied to the web material from above the web material. Out of the powder and air blown onto the web material, and using the sieving member to leave the powder material in the web material, while letting the air escape from the web material, the powder on the web material Fix the body.
- the addition method presses the web material after the air is released from the web material, while sucking the air released from the web material and the sieve member.
- the web material processed by the addition apparatus and the addition method is a filter material for cigarettes, for example.
- the granular material addition apparatus and the addition method of the present invention effectively fix the granular material in the web material without floating the granular material above the web material by the function of the sieving member of the fixing unit. be able to. Therefore, the above-described sealed chamber and suction fan are not necessary for fixing the granular material to the web material. Moreover, the addition amount of the granular material to a web material is determined only by the ejection amount of a granular material, and adjustment of the additional amount of a granular material becomes easy. Furthermore, if the fixing unit includes a lower conveyor and an upper conveyor, these conveyors can uniformly transfer the filter tow along the transfer path toward the wrapping device even if the web material is a filter tow. Therefore, when the filter rod is formed from the filter tow by the lapping apparatus as described above, the packing density of the filter tow in the filter rod becomes uniform, and a high quality filter rod can be obtained.
- FIG. 1 schematically shows an upstream section 10 of a filter maker.
- the upstream section 10 includes a supply path 12 for the filter tow T as a web material, and the supply path 12 extends horizontally.
- An upstream end of the supply path 12 is connected to a filter tow supply source (not shown), and a downstream end thereof is connected to a downstream section, that is, a wrapping section 14.
- the filter tow T is formed from a filter material for cigarettes, i.e., filter fibers, and has air permeability.
- the filter tow T is transferred along the supply path 12 toward the wrapping section 14.
- a pair of extension rollers 16 and a pair of guide rollers 18 are disposed in the upstream portion of the supply path 12, while a trumpet guide 20 is disposed immediately upstream of the wrapping section 14.
- a plasticizer addition device (not shown) is disposed downstream of the guide roller 18 in the supply path 12, and this addition device adds liquid triacetin as a plasticizer to the filter tow.
- the filter tow T passes the trumpet guide 20
- the filter tow T is squeezed into a rod shape and fed to the wrapping section 14.
- the wrapping section 14 further squeezes the supplied filter tow T, wraps it with a packaging material and forms it into continuous rods (not shown), and then cuts the continuous rods into individual filter rods FR. Is sent out.
- the filter rod FR is packed in a box and shipped to a filter cigarette manufacturing factory.
- the supply passage 12 is further provided with the powder material adding device 22 of the first embodiment.
- This adding device 22 is provided between the plasticizer adding device and the trumpet guide 20 described above. Arranged upstream.
- the addition device 22 includes a spray unit 24, which is disposed above the supply path 12 and connected to a powder quantitative supply device 26.
- the powder fixed amount supply device 26 has a hopper 28 in which powder particles such as a fragrance and a catalyst are stored.
- the powder fixed quantity supply device 26 can supply the powder particles in the hopper 28 to the spray unit 24 in a fixed quantity, and the supply amount can be varied.
- the spray unit 24 injects the granular material supplied from the powder quantitative supply device 26 toward the filter tow T on the supply path 12. As is apparent from FIG. 1, the spray direction of the granular material from the spray unit 24 is inclined downstream and downward of the supply path 12. In FIG. 1, the reference symbol P is attached to the position where the powder particles sprayed from the spray unit 24 reach the filter tow T.
- the spray unit 24 has a large number of electrostatic nozzles 30, and these electrostatic nozzles 30 are arranged at regular intervals in the width direction of the filter tow T.
- the powdered particles are ejected together with compressed air. Therefore, the powder particles are uniformly added to the filter tow T, and the added powder particles adhere to the filter fibers of the filter tow T based on the adsorption action by static electricity.
- the adding device 22 further includes a fixing unit 32.
- the fixing unit 32 is disposed downstream of the spray unit 24, and the granular material adhered to the filter tow T or above the filter tow T. In addition, the granular material floating in the vicinity is fixed to the filter tow T.
- the fixing unit 32 includes a lower and upper conveyors 34 and 36.
- the lower conveyor 34 is disposed immediately below the supply path 12, and extends downstream from the position directly below the spray unit 24 beyond the position P along the supply path 12.
- the lower conveyor 34 has a width sufficiently wider than the width of the filter tow T (see FIG. 2).
- the lower conveyor 34 has a driving roller 38 and a driven roller 40, and these rollers 38, 40 are separated from each other along the supply path 12.
- the driving roller 38 is positioned downstream of the driven roller 40, and an endless air permeable belt as a sieving member, that is, a mesh belt 42 is attached to the rollers 38 and 40.
- the mesh of the mesh belt 42 is, for example, smaller than the average particle diameter of the granular material.
- the upper conveyor 36 has the same width as that of the lower conveyor 34 and is disposed above the supply path 12.
- the upper conveyor 36 extends along the supply path 12 like the lower conveyor 34, but is not parallel to the supply path 12 but is inclined with respect to the supply path 12.
- the upper conveyor 36 also has a driving roller 44, a driven roller 46, and an endless fixing belt 48 attached to these rollers 44 and 46.
- the driving roller 44 is arranged so as to be able to sandwich the filter tow T on the supply path 12 in cooperation with the driving roller 38, while the driven roller 46 is upstream of the driving roller 44, specifically, the driving roller 38 and the driven roller. 40 and above the supply path 12.
- the fixing belt 48 does not have air permeability.
- the fixing unit 32 described above defines an inlet 50 between the upstream end (driven roller 46) of the upper conveyor 36 and the supply path 12, and the height of the inlet 50, that is, the upper conveyor 36 with respect to the supply path 12. Can be adjusted according to the spray angle ⁇ of the granular material from the spray unit 24.
- the upper conveyor 36 is supported so as to be rotatable up and down around a roller shaft (not shown) of the driving roller 44, while the roller shaft (not shown) of the driven roller 46 is
- the lift actuator 52 is supported.
- the elevating actuator 52 is an air cylinder, and adjusts the inclination angle ⁇ , that is, the height of the inlet 50 by bringing the upstream end of the upper conveyor 36 into and out of contact with the supply path 12.
- the roller shafts of the drive rollers 38 and 44 are connected to a drive unit 56 through a common power transmission path 54, and the drive unit 56 includes a drive source 58 such as an electric motor and a speed controller 60. Therefore, when the driving force of the driving source 58 is transmitted to the driving rollers 38 and 44 via the power transmission path 54, the driving roller 38 is rotated counterclockwise as viewed in FIG. It is rotated at the same peripheral speed in the direction. Therefore, the upper surface of the mesh belt 42 and the lower surface of the fixing belt 48 travel in the same direction as the transfer direction of the filter tow T, and the traveling speed of these belts 42 and 48 depends on the transfer speed of the filter tow T. 60.
- a cover 62 may be disposed between the inlet 50 and the spray unit 24 as necessary.
- the cover 62 extends from the inlet 50 to the spray unit 24 and covers the transfer path 12. The cover 62 does not hinder the ejection of powder from the spray unit 24.
- a dust collecting unit 64 as a suction source is arranged below the fixing unit 32, that is, the lower conveyor 34.
- the dust collection unit 64 has a mesh sheet 66 on its upper surface, and the mesh sheet 66 extends along the lower conveyor 34.
- the dust collection unit 64 sucks air through the mesh sheet 66, and the mesh of the mesh sheet 66 is also preferably smaller than the average particle diameter of the granular material.
- each electrostatic nozzle 30 of the spray unit 24 ejects the charged granular material together with air toward the filter toe T just before entering the inlet 50 of the fixing unit 32.
- the air passes through the filter tow T and the mesh belt 42 of the lower conveyor 34 and escapes from the filter tow T.
- the powder particles are contained in the filter tow T. And separated from the air.
- the mesh of the mesh belt 42 is smaller than the average particle diameter of the powder particles, the powder particles do not pass through the mesh belt 42. Further, since the powder particles are charged and the plasticizer is already added to the filter tow T, the powder particles are effectively attached to the filter fibers of the filter tow T, that is, fixed. On the other hand, the generation of the air passing through the filter tow T and the mesh belt 42, that is, the air flow A indicated by the reference symbol A in FIGS. To reduce. Therefore, the floating of the granular material due to the rebound of the air flow is effectively suppressed.
- the floating particles are prevented from being scattered by the fixing belt 48 of the upper conveyor 36, and a part of the floating particles adheres to the lower surface of the fixing belt 48 or is fixed. After colliding with the lower surface of the belt 48, it is dropped on the filter tow T. Since the downstream ends of the lower and upper conveyors 34 and 36 cooperate with each other to sandwich the filter tow T on the supply path 12, when the filter tow T is sent out from the fixing unit 32, the filter tow T is moved to the lower conveyor 34. And the upper conveyor 36. Therefore, the granular material adhering to the lower surface of the fixing belt 48 and the granular material exposed on the upper surface of the filter tow T are pushed between the filter fibers of the filter tow T.
- the lower conveyor 34 cooperates with the upper conveyor 36, so that not only can the powder particles be well fixed on the filter tow T as described above, but also the filter tow T on which the powder particles are fixed can be used in the next process. It also plays the role of continuously feeding into the wrapping section 14. Therefore, the lower conveyor 34 greatly contributes to uniforming the density of the filter fibers and the distribution of the powder particles of the filter tow T to be supplied to the wrapping section 14.
- the addition device 22 can effectively add the granular material to the filter tow T in a state in which the floating and scattering of the granular material is prevented, a sealed chamber for adding the granular material, A suction fan for exhausting the room becomes unnecessary. Furthermore, since the cover 62 is disposed between the spray unit 24 and the upper conveyor 36, even if there is a powder that jumps upward from the main jet flow of the powder from the spray unit 24, it jumped out. The powder particles are captured by the cover 62, and the powder particles are not scattered around the fixing unit 32.
- the dust collection unit 64 is disposed below the lower conveyor 34, the dust collection unit 64 can suck the air flow A described above through the mesh sheet 66 therein. Therefore, even if the airflow A contains powder particles that have passed through the mesh belt 42, these passing powder particles are captured on the mesh sheet 66 and the passing powder particles are not scattered around. .
- the addition device 22 only adjusts the amount of powder and particles ejected from the spray unit 24, that is, the amount of powder and particles supplied from the powder fixed amount supply device 26 to the spray unit 24. The amount of powder added can be easily and easily controlled.
- FIG. 3 shows the addition apparatus of the second embodiment.
- the addition device of the second embodiment is such that the upper conveyor 36 extends in parallel with the transfer path 12 and is between the entire lower surface of the fixing belt 48 and the upper surface of the mesh belt 42. The only difference is that the filter tow T is sandwiched.
- FIG. 4 shows the addition apparatus of the third embodiment.
- the addition apparatus of the third embodiment is different only in that the transfer path 12 is not horizontal but is inclined downward toward the downstream side.
- the spray unit 24 preferably ejects the powder particles toward the position immediately before the entrance of the fixing unit 32.
- FIG. 5 shows the addition apparatus of the fourth embodiment.
- the addition apparatus of the fourth embodiment is different only in that the transfer path 12 is not horizontal but is inclined downward toward the downstream side.
- 3 to 5 show the downstream ends of the lower conveyor 34 and the upper conveyor 36 in a state where they are separated from the transfer path 12, this is for the convenience of drawing.
- Any of the addition apparatuses of the first to fourth embodiments described above is applied to a filter manufacturing machine.
- the addition apparatus of the present invention can be used in the same manner for adding powder particles to a web material other than the filter tow T.
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- Cigarettes, Filters, And Manufacturing Of Filters (AREA)
Abstract
Disclosed is a powder adding device which has: a transfer path (12) for transferring a filter tow (T) as webbing material; a spray unit (24) for spraying air together with a perfume, catalyst, or other such powder toward the transfer path (12); and a fixing unit (32) for separating inside the filter tow (T) the air and the powder which is blown onto the filter tow (T), and for fixing the powder to the filter tow (T).
Description
本発明は、空気透過性を有するウエブ材に粉粒体を含ませるための添加装置及びその添加方法に係わり、特に、フィルタシガレットのためのフィルタを製造するフィルタ製造機に好適した粉粒体添加装置及び添加方法に関する。
TECHNICAL FIELD The present invention relates to an addition apparatus for adding a granular material to a web material having air permeability, and an addition method thereof, and more particularly, an addition of a granular material suitable for a filter manufacturing machine for manufacturing a filter for a filter cigarette. The present invention relates to an apparatus and an addition method.
フィルタ製造機はウエブ材としてのフィルタトウの供給経路を備え、このフィルタトウは供給経路に沿い、ラッピング装置に向けて供給される。フィルタトウはフィルタ繊維から形成され、ウエブの形態をなしている。フィルタトウがラッピング装置に供給されたとき、フィルタトウはロッド状に絞り込まれながら、包材により包み込まれ、連続ロッドに成形される。この後、連続ロッドは個々のフィルタロッドに切断され、このフィルタロッドは、個々のフィルタシガレットに使用されるフィルタの複数倍の長さを有する。
The filter manufacturing machine has a filter tow supply path as a web material, and this filter tow is supplied to the wrapping apparatus along the supply path. The filter tow is formed from filter fibers and is in the form of a web. When the filter tow is supplied to the wrapping device, the filter tow is squeezed into a rod shape, and is wrapped by a packaging material and formed into a continuous rod. After this, the continuous rod is cut into individual filter rods, which have multiple times the length of the filters used in the individual filter cigarettes.
上述のフィルタに要求される本来の機能は、フィルタシガレットの喫煙時、シガレットの主流煙中のニコチンやタールを除去することにあるが、本来の機能に加えて、近年、フィルタに他の機能を付加することが望まれている。このような他の付加機能として、主流煙に香気を付加したり又は主流煙中のCOをCO2に酸化させたりすることが考えられ、このためにはフィルタトウに香気を発生する香料や酸化触媒等の粉粒体を添加する必要がある。
The original function required for the above-mentioned filter is to remove nicotine and tar in the mainstream smoke of the cigarette when smoking the filter cigarette, but in addition to the original function, in recent years other functions have been added to the filter. It is desired to add. As such other additional functions, it is conceivable to add a fragrance to the mainstream smoke, or to oxidize CO in the mainstream smoke to CO 2. It is necessary to add a granular material such as a catalyst.
例えば、特許文献1に開示されたフィルタ製造機は上述の粉粒体を添加するための添加装置を備えている。具体的には、添加装置は密閉室、即ち、パウダ室を含み、このパウダ室はフィルタトウの供給経路に配置されている。それ故、フィルタトウはパウダ室を通過し、ラッピング装置に向けて搬送される。更に、パウダ室内には粉粒体の噴出ノズルが配置され、この噴出ノズルはパウダ室内を通過するフィルタトウに向けて粉粒体を噴出し、これにより、フィルタトウに粉粒体を添加する。
For example, the filter manufacturing machine disclosed in Patent Document 1 is provided with an adding device for adding the above-described powder particles. Specifically, the adding device includes a sealed chamber, that is, a powder chamber, and this powder chamber is disposed in the supply path of the filter tow. Therefore, the filter tow passes through the powder chamber and is conveyed toward the wrapping device. Further, a powder particle ejection nozzle is disposed in the powder chamber, and this ejection nozzle ejects the powder particle toward the filter tow passing through the powder chamber, thereby adding the powder particle to the filter tow.
特許文献1の添加装置によれば、粉粒体がパウダ室内にてフィルタトウに添加されるため、粉粒体がパウダ室外に飛散することはないと考えられる。しかしながら、パウダ室内には噴出ノズルから噴出された粉粒体が多量に浮遊し、このような浮遊粉粒体はフィルタトウへの粉粒体の一様な添加を阻害する大きな要因となる。
According to the addition apparatus of Patent Document 1, it is considered that the granular material is not scattered outside the powder chamber because the granular material is added to the filter tow in the powder chamber. However, a large amount of powder particles ejected from the ejection nozzle float in the powder chamber, and such suspended powder particles are a major factor that hinders uniform addition of powder particles to the filter tow.
このため、特許文献1の添加装置には吸引ファンや一対のロッド形状の帯電器が必要不可欠となる。詳しくは、吸引ファンはパウダ室内を真空状態に維持することで、パウダ室から浮遊粉粒体の排出し、帯電器はパウダ室の上流にてフィルタトウを一様に帯電させることで、浮遊粉粒体の低減を図る一方、フィルタトウへの粉粒体の付着を促進する。
For this reason, a suction fan and a pair of rod-shaped chargers are indispensable for the adding device of Patent Document 1. Specifically, the suction fan keeps the powder chamber in a vacuum state, thereby discharging the suspended powder particles from the powder chamber, and the charger uniformly charges the filter tow upstream of the powder chamber. While aiming at reduction of a granular material, adhesion of the granular material to a filter tow is promoted.
しかしながら、上述の吸引ファンや帯電器は添加装置全体の構造を大掛かりし且つ複雑にする。
また、吸引ファンによるパウダ室からの浮遊粉粒体の排出は、噴出ノズルから噴出された粉粒体の一部を無駄にし、フィルタトウへの粉粒体の効果的な付着を不能にする。 However, the above-described suction fan and charger increase the size and complexity of the entire addition device.
In addition, the discharge of the floating granular material from the powder chamber by the suction fan wastes a part of the granular material ejected from the ejection nozzle and makes it impossible to effectively attach the granular material to the filter tow.
また、吸引ファンによるパウダ室からの浮遊粉粒体の排出は、噴出ノズルから噴出された粉粒体の一部を無駄にし、フィルタトウへの粉粒体の効果的な付着を不能にする。 However, the above-described suction fan and charger increase the size and complexity of the entire addition device.
In addition, the discharge of the floating granular material from the powder chamber by the suction fan wastes a part of the granular material ejected from the ejection nozzle and makes it impossible to effectively attach the granular material to the filter tow.
更に、フィルタトウへの粉粒体の添加量を増加又は減少させる場合、特許文献1の添加装置は、噴出ノズルからの粉粒体の噴出量のみならず、帯電器によるフィルタトウの帯電レベルの制御をも要求され、粉粒体の添加量を容易に調整することができない。
Furthermore, when increasing or decreasing the addition amount of the granular material to the filter tow, the addition apparatus of patent document 1 is not only the amount of the granular material ejected from an ejection nozzle but the charge level of the filter tow by a charger. Control is also required, and the amount of powder added cannot be easily adjusted.
本発明の目的は、パウダ室等の密閉室やこの密閉室内を排気する吸引ファンを必要とせずに、ウエブ材に粉粒体を効果的に添加させることができ、しかも、粉粒体の添加量を容易に調整することができる粉粒体添加装置及びその添加方法を提供することにある。
The object of the present invention is to allow the powder material to be effectively added to the web material without the need for a closed chamber such as a powder chamber or a suction fan for exhausting the sealed chamber. An object of the present invention is to provide an apparatus for adding a granular material and an addition method thereof, the amount of which can be easily adjusted.
上記の目的を達成するため、本発明の粉粒体添加装置は、空気透過性を有したウエブ材を移送するための移送経路と、この移送経路の上方に配置され、ウエブ材に向けて粉粒体を空気とともに噴出するスプレーユニットと、移送経路にスプレーユニットの下流に位置して配置され、ウエブ材に粉粒体を定着させる定着ユニットであって、ウエブ材の移送を案内する一方、ウエブ材に吹き付けられた粉粒体及び空気のうち、粉粒体をウエブ材内に残す一方、空気をウエブ材内から下方に逃がす篩部材を含む、定着ユニットとを備える。
In order to achieve the above object, the granular material addition apparatus of the present invention is provided with a transfer path for transferring a web material having air permeability, and a powder disposed toward the web material, disposed above the transfer path. A spray unit that ejects particles together with air, and a fixing unit that is positioned downstream of the spray unit in the transfer path and fixes the particles to the web material, and guides the transfer of the web material, A fixing unit including a sieving member for leaving the granular material in the web material out of the granular material and air sprayed on the material, while allowing the air to escape downward from the web material;
上述の添加装置によれば、スプレーユニットは、定着ユニットの篩部材上を移送されるウエブ材に向け、空気とともに粉粒体を噴出する。ウエブ材に吹き付けられた粉粒体及び空気のうち、空気はウエブ材及び篩部材を通過するが、粉粒体は篩部材によってウエブ材の通過を阻止されてウエブ材内に残る。それ故、粉粒体がウエブ材の上方にて浮遊することはなく、粉粒体はウエブ材に効果的に定着される。
According to the above-described addition apparatus, the spray unit ejects the powder and the granular material together with the air toward the web material transferred on the sieve member of the fixing unit. Of the granular material and air sprayed on the web material, air passes through the web material and the sieve member, but the granular material is prevented from passing through the web material by the sieve member and remains in the web material. Therefore, the granular material does not float above the web material, and the granular material is effectively fixed to the web material.
具体的には、定着ユニットは前述の篩部材として、移送経路の下側を移送経路に沿って延び、空気の通過を許容するロアコンベアと、移送経路の上側を移送経路に沿って延びるアッパコンベアとを含み、このアッパコンベアはロアコンベアと協働してウエブ材を挟み込む下流端を有する。
Specifically, the fixing unit is the above-described sieve member, and extends below the transfer path along the transfer path and allows the passage of air, and an upper conveyor extends above the transfer path along the transfer path. The upper conveyor has a downstream end that sandwiches the web material in cooperation with the lower conveyor.
ウエブ材がアッパコンベアの下流端を通過する際、ウエブ材はアッパコンベアの下流端とロアコンベアとの間にてプレスされ、ウエブ材の上面に露出する粉粒体はウエブ材内に押し込められる。
この場合、前述したスプレーユニットは、粉粒体を帯電させて噴出する複数の静電ノズルを含むことができ、この場合、帯電された粉粒体はウエブ材内に効果的に付着される。
更に具体的には、ロアコンベアは無端状のメッシュベルトを有する。このようなメッシュベルトは、ウエブ材内から空気のみを逃がし、ウエブ材内に粉粒体を残す。 When the web material passes the downstream end of the upper conveyor, the web material is pressed between the downstream end of the upper conveyor and the lower conveyor, and the granular material exposed on the upper surface of the web material is pushed into the web material.
In this case, the above-mentioned spray unit can include a plurality of electrostatic nozzles that charge and eject the powder particles, and in this case, the charged powder particles are effectively attached to the web material.
More specifically, the lower conveyor has an endless mesh belt. Such a mesh belt allows only air to escape from the web material, leaving a granular material in the web material.
この場合、前述したスプレーユニットは、粉粒体を帯電させて噴出する複数の静電ノズルを含むことができ、この場合、帯電された粉粒体はウエブ材内に効果的に付着される。
更に具体的には、ロアコンベアは無端状のメッシュベルトを有する。このようなメッシュベルトは、ウエブ材内から空気のみを逃がし、ウエブ材内に粉粒体を残す。 When the web material passes the downstream end of the upper conveyor, the web material is pressed between the downstream end of the upper conveyor and the lower conveyor, and the granular material exposed on the upper surface of the web material is pushed into the web material.
In this case, the above-mentioned spray unit can include a plurality of electrostatic nozzles that charge and eject the powder particles, and in this case, the charged powder particles are effectively attached to the web material.
More specifically, the lower conveyor has an endless mesh belt. Such a mesh belt allows only air to escape from the web material, leaving a granular material in the web material.
更に、前述したアッパコンベアは移送経路に対して傾斜し、移送経路よりも上方に位置付けられた上流端を有する。この場合、アッパコンベアは移送経路からの前記上流端の高さレベルを調整可能であるのが好ましい。
一方、アッパコンベアは移送経路に沿い、ロアコンベアと平行に延びていてもよく、この場合、アッパコンベアはその下面全面にてウエブ材をプレスする。
更に、定着ユニットは、ロアコンベアの下方に配置されたサクション源を更に備えることができ、このサクション源はウエブ材及びロアコンベアを通じて逃がされた空気を吸引する。 Furthermore, the above-described upper conveyor is inclined with respect to the transfer path and has an upstream end positioned above the transfer path. In this case, it is preferable that the upper conveyor can adjust the height level of the upstream end from the transfer path.
On the other hand, the upper conveyor may extend along the transfer path in parallel with the lower conveyor. In this case, the upper conveyor presses the web material on the entire lower surface thereof.
Furthermore, the fixing unit can further comprise a suction source arranged below the lower conveyor, which sucks the air escaped through the web material and the lower conveyor.
一方、アッパコンベアは移送経路に沿い、ロアコンベアと平行に延びていてもよく、この場合、アッパコンベアはその下面全面にてウエブ材をプレスする。
更に、定着ユニットは、ロアコンベアの下方に配置されたサクション源を更に備えることができ、このサクション源はウエブ材及びロアコンベアを通じて逃がされた空気を吸引する。 Furthermore, the above-described upper conveyor is inclined with respect to the transfer path and has an upstream end positioned above the transfer path. In this case, it is preferable that the upper conveyor can adjust the height level of the upstream end from the transfer path.
On the other hand, the upper conveyor may extend along the transfer path in parallel with the lower conveyor. In this case, the upper conveyor presses the web material on the entire lower surface thereof.
Furthermore, the fixing unit can further comprise a suction source arranged below the lower conveyor, which sucks the air escaped through the web material and the lower conveyor.
本発明は、粉粒体の添加方法をも提供し、本発明の添加方法は、空気透過性を有したウエブ材を移送経路に沿って移送し、ウエブ材の上方からウエブ材に粉粒体を空気とともに噴出し、ウエブ材に吹き付けられた粉粒体及び空気のうち、篩部材を使用して粉粒体をウエブ材内に残す一方、空気をウエブ材内から逃がし、ウエブ材に粉粒体を定着させる。
好ましくは、添加方法は、空気がウエブ材から逃がされた後、ウエブ材をプレスし、一方、ウエブ材及び篩部材から逃がされた空気を吸引する。
なお、添加装置及び添加方法により処理されるウエブ材は例えば、シガレットのためのフィルタ材料であるのが好ましい。 The present invention also provides a method for adding powder particles. The addition method of the present invention transfers a web material having air permeability along a transfer path, and the powder particles are applied to the web material from above the web material. Out of the powder and air blown onto the web material, and using the sieving member to leave the powder material in the web material, while letting the air escape from the web material, the powder on the web material Fix the body.
Preferably, the addition method presses the web material after the air is released from the web material, while sucking the air released from the web material and the sieve member.
In addition, it is preferable that the web material processed by the addition apparatus and the addition method is a filter material for cigarettes, for example.
好ましくは、添加方法は、空気がウエブ材から逃がされた後、ウエブ材をプレスし、一方、ウエブ材及び篩部材から逃がされた空気を吸引する。
なお、添加装置及び添加方法により処理されるウエブ材は例えば、シガレットのためのフィルタ材料であるのが好ましい。 The present invention also provides a method for adding powder particles. The addition method of the present invention transfers a web material having air permeability along a transfer path, and the powder particles are applied to the web material from above the web material. Out of the powder and air blown onto the web material, and using the sieving member to leave the powder material in the web material, while letting the air escape from the web material, the powder on the web material Fix the body.
Preferably, the addition method presses the web material after the air is released from the web material, while sucking the air released from the web material and the sieve member.
In addition, it is preferable that the web material processed by the addition apparatus and the addition method is a filter material for cigarettes, for example.
本発明の粉粒体添加装置及びその添加方法は、定着ユニットの篩部材の働きにより、ウエブ材の上方に粉粒体を浮遊させることなく、粉粒体をウエブ材内に効果的に定着させることができる。それ故、ウエブ材への粉粒体の定着にあたり、前述した密閉室や吸引ファンは不要である。また、ウエブ材への粉粒体の添加量は、粉粒体の噴出量のみによって決定され、粉粒体の添加量の調整は容易となる。
更に、定着ユニットがロア及びアッパコンベアを含んでいれば、これらコンベアはウエブ材がフィルタトウであっても、このフィルタトウを移送経路に沿いラッピング装置に向けて一様に移送することができる。それ故、前述したようにラッピング装置にて、フィルタトウからフィルタロッドが形成された場合、フィルタロッド内におけるフィルタトウの充填密度は均一になり、高品質なフィルタロッドが得られる。 The granular material addition apparatus and the addition method of the present invention effectively fix the granular material in the web material without floating the granular material above the web material by the function of the sieving member of the fixing unit. be able to. Therefore, the above-described sealed chamber and suction fan are not necessary for fixing the granular material to the web material. Moreover, the addition amount of the granular material to a web material is determined only by the ejection amount of a granular material, and adjustment of the additional amount of a granular material becomes easy.
Furthermore, if the fixing unit includes a lower conveyor and an upper conveyor, these conveyors can uniformly transfer the filter tow along the transfer path toward the wrapping device even if the web material is a filter tow. Therefore, when the filter rod is formed from the filter tow by the lapping apparatus as described above, the packing density of the filter tow in the filter rod becomes uniform, and a high quality filter rod can be obtained.
更に、定着ユニットがロア及びアッパコンベアを含んでいれば、これらコンベアはウエブ材がフィルタトウであっても、このフィルタトウを移送経路に沿いラッピング装置に向けて一様に移送することができる。それ故、前述したようにラッピング装置にて、フィルタトウからフィルタロッドが形成された場合、フィルタロッド内におけるフィルタトウの充填密度は均一になり、高品質なフィルタロッドが得られる。 The granular material addition apparatus and the addition method of the present invention effectively fix the granular material in the web material without floating the granular material above the web material by the function of the sieving member of the fixing unit. be able to. Therefore, the above-described sealed chamber and suction fan are not necessary for fixing the granular material to the web material. Moreover, the addition amount of the granular material to a web material is determined only by the ejection amount of a granular material, and adjustment of the additional amount of a granular material becomes easy.
Furthermore, if the fixing unit includes a lower conveyor and an upper conveyor, these conveyors can uniformly transfer the filter tow along the transfer path toward the wrapping device even if the web material is a filter tow. Therefore, when the filter rod is formed from the filter tow by the lapping apparatus as described above, the packing density of the filter tow in the filter rod becomes uniform, and a high quality filter rod can be obtained.
図1はフィルタ製造機の上流セクション10を概略的に示す。
上流セクション10はウエブ材としてのフィルタトウTの供給経路12を含み、この供給経路12は水平に延びている。供給経路12の上流端はフィルタトウの供給源(図示しない)に接続され、その下流端は下流セクション、即ち、ラッピングセクション14に接続されている。 FIG. 1 schematically shows anupstream section 10 of a filter maker.
Theupstream section 10 includes a supply path 12 for the filter tow T as a web material, and the supply path 12 extends horizontally. An upstream end of the supply path 12 is connected to a filter tow supply source (not shown), and a downstream end thereof is connected to a downstream section, that is, a wrapping section 14.
上流セクション10はウエブ材としてのフィルタトウTの供給経路12を含み、この供給経路12は水平に延びている。供給経路12の上流端はフィルタトウの供給源(図示しない)に接続され、その下流端は下流セクション、即ち、ラッピングセクション14に接続されている。 FIG. 1 schematically shows an
The
フィルタトウTはシガレットのためのフィルタ材料、即ち、フィルタ繊維から形成されて、空気透過性を有する。フィルタトウTは供給経路12に沿い、ラッピングセクション14に向けて移送される。供給経路12の上流部分には一対の伸長ローラ16及び一対のガイドローラ18が配置され、一方、ラッピングセクション14の直上流にはトランペットガイド20が配置されている。
更に、供給経路12にはガイドローラ18の下流に可塑剤添加装置(図示しない)が配置され、この添加装置はフィルタトウに可塑剤として液状のトリアセチンを添加する。 The filter tow T is formed from a filter material for cigarettes, i.e., filter fibers, and has air permeability. The filter tow T is transferred along thesupply path 12 toward the wrapping section 14. A pair of extension rollers 16 and a pair of guide rollers 18 are disposed in the upstream portion of the supply path 12, while a trumpet guide 20 is disposed immediately upstream of the wrapping section 14.
Further, a plasticizer addition device (not shown) is disposed downstream of theguide roller 18 in the supply path 12, and this addition device adds liquid triacetin as a plasticizer to the filter tow.
更に、供給経路12にはガイドローラ18の下流に可塑剤添加装置(図示しない)が配置され、この添加装置はフィルタトウに可塑剤として液状のトリアセチンを添加する。 The filter tow T is formed from a filter material for cigarettes, i.e., filter fibers, and has air permeability. The filter tow T is transferred along the
Further, a plasticizer addition device (not shown) is disposed downstream of the
フィルタトウTがトランペットガイド20を通過するとき、フィルタトウTはロッド形状に絞り込まれ、そして、ラッピングセクション14に供給される。
ラッピングセクション14は、供給されたフィルタトウTを更に絞り込みながら、包材により包み込んで連続ロッド(図示しない)に成形し、この後、連続ロッドを個々のフィルタロッドFRに切断し、これらフィルタロッドFRを送出する。なお、フィルタロッドFRは箱詰めされ、フィルタシガレットの製造工場に出荷される。 As the filter tow T passes thetrumpet guide 20, the filter tow T is squeezed into a rod shape and fed to the wrapping section 14.
Thewrapping section 14 further squeezes the supplied filter tow T, wraps it with a packaging material and forms it into continuous rods (not shown), and then cuts the continuous rods into individual filter rods FR. Is sent out. The filter rod FR is packed in a box and shipped to a filter cigarette manufacturing factory.
ラッピングセクション14は、供給されたフィルタトウTを更に絞り込みながら、包材により包み込んで連続ロッド(図示しない)に成形し、この後、連続ロッドを個々のフィルタロッドFRに切断し、これらフィルタロッドFRを送出する。なお、フィルタロッドFRは箱詰めされ、フィルタシガレットの製造工場に出荷される。 As the filter tow T passes the
The
供給経路12には第1実施例の粉粒体添加装置22が更に備えられており、この添加装置22は前述した可塑剤添加装置とトランペットガイド20との間、詳しくは、トランペットガイド20の直上流に配置されている。添加装置22はスプレーユニット24を含み、このスプレーユニット24は供給経路12の上方に配置され、粉体定量供給装置26に接続されている。この粉体定量供給装置26は、ホッパ28を有し、このホッパ28内には香料や触媒等の粉粒体が蓄えられている。粉体定量供給装置26はホッパ28内の粉粒体をスプレーユニット24に向けて定量供給することができ、また、その供給量を可変可能である。
The supply passage 12 is further provided with the powder material adding device 22 of the first embodiment. This adding device 22 is provided between the plasticizer adding device and the trumpet guide 20 described above. Arranged upstream. The addition device 22 includes a spray unit 24, which is disposed above the supply path 12 and connected to a powder quantitative supply device 26. The powder fixed amount supply device 26 has a hopper 28 in which powder particles such as a fragrance and a catalyst are stored. The powder fixed quantity supply device 26 can supply the powder particles in the hopper 28 to the spray unit 24 in a fixed quantity, and the supply amount can be varied.
スプレーユニット24は、粉体定量供給装置26から供給された粉粒体を供給経路12上のフィルタトウTに向けて噴射する。図1から明らかなように、スプレーユニット24からの粉粒体の噴射方向は供給経路12の下流且つ下向きに傾斜している。図1中、スプレーユニット24から噴射された粉粒体がフィルタトウTに達する位置には参照符号Pが付されている。
The spray unit 24 injects the granular material supplied from the powder quantitative supply device 26 toward the filter tow T on the supply path 12. As is apparent from FIG. 1, the spray direction of the granular material from the spray unit 24 is inclined downstream and downward of the supply path 12. In FIG. 1, the reference symbol P is attached to the position where the powder particles sprayed from the spray unit 24 reach the filter tow T.
より詳しくは、図2に示されているようにスプレーユニット24は多数の静電ノズル30を有し、これら静電ノズル30はフィルタトウTの幅方向に一定の間隔を存して並び、帯電された粉粒体を圧縮空気とともに噴出する。それ故、フィルタトウTには粉粒体が均一に添加され、添加された粉粒体は静電気による吸着作用に基づき、フィルタトウTのフィルタ繊維に付着される。
More specifically, as shown in FIG. 2, the spray unit 24 has a large number of electrostatic nozzles 30, and these electrostatic nozzles 30 are arranged at regular intervals in the width direction of the filter tow T. The powdered particles are ejected together with compressed air. Therefore, the powder particles are uniformly added to the filter tow T, and the added powder particles adhere to the filter fibers of the filter tow T based on the adsorption action by static electricity.
図1に示されるように、添加装置22は定着ユニット32を更に備え、この定着ユニット32はスプレーユニット24の下流に配置され、フィルタトウTに付着された粉粒体や、フィルタトウTの上方且つ近傍を浮遊する粉粒体をフィルタトウTに定着させる。
As shown in FIG. 1, the adding device 22 further includes a fixing unit 32. The fixing unit 32 is disposed downstream of the spray unit 24, and the granular material adhered to the filter tow T or above the filter tow T. In addition, the granular material floating in the vicinity is fixed to the filter tow T.
詳しくは、定着ユニット32はロア及びアッパコンベア34,36を含む。ロアコンベア34は供給経路12の直下に配置され、供給経路12に沿い、スプレーユニット24の直下から前記位置Pを越えて下流に延びている。また、ロアコンベア34はフィルタトウTの幅よりも十分に広い幅を有する(図2参照)。ロアコンベア34は駆動ローラ38及び従動ローラ40を有し、これらローラ38,40は供給経路12に沿って互いに離間している。駆動ローラ38は従動ローラ40よりも下流に位置付けられ、これらローラ38,40に篩部材としての無端状の空気透過ベルト、即ち、メッシュベルト42が取付けられている。このメッシュベルト42の網目は例えば、粉粒体の平均粒径よりも小さい。
Specifically, the fixing unit 32 includes a lower and upper conveyors 34 and 36. The lower conveyor 34 is disposed immediately below the supply path 12, and extends downstream from the position directly below the spray unit 24 beyond the position P along the supply path 12. The lower conveyor 34 has a width sufficiently wider than the width of the filter tow T (see FIG. 2). The lower conveyor 34 has a driving roller 38 and a driven roller 40, and these rollers 38, 40 are separated from each other along the supply path 12. The driving roller 38 is positioned downstream of the driven roller 40, and an endless air permeable belt as a sieving member, that is, a mesh belt 42 is attached to the rollers 38 and 40. The mesh of the mesh belt 42 is, for example, smaller than the average particle diameter of the granular material.
一方、アッパコンベア36はロアコンベア34との幅と同一の幅を有し、供給経路12の上方にて配置されている。アッパコンベア36はロアコンベア34と同様に供給経路12に沿って延びているものの、供給経路12に対して平行ではなく、供給経路12に対して傾斜されている。
On the other hand, the upper conveyor 36 has the same width as that of the lower conveyor 34 and is disposed above the supply path 12. The upper conveyor 36 extends along the supply path 12 like the lower conveyor 34, but is not parallel to the supply path 12 but is inclined with respect to the supply path 12.
即ち、アッパコンベア36もまた、駆動ローラ44、従動ローラ46及びこれらローラ44,46に取り付けられた無端状の定着ベルト48を有する。駆動ローラ44は駆動ローラ38と協働して供給経路12上のフィルタトウTを挟み込み可能に配置され、一方、従動ローラ46は駆動ローラ44の上流、具体的には、駆動ローラ38と従動ローラ40との間で、且つ、供給経路12の上方に配置されている。定着ベルト48はメッシュベルト42とは異なり、空気透過性を有していない。
That is, the upper conveyor 36 also has a driving roller 44, a driven roller 46, and an endless fixing belt 48 attached to these rollers 44 and 46. The driving roller 44 is arranged so as to be able to sandwich the filter tow T on the supply path 12 in cooperation with the driving roller 38, while the driven roller 46 is upstream of the driving roller 44, specifically, the driving roller 38 and the driven roller. 40 and above the supply path 12. Unlike the mesh belt 42, the fixing belt 48 does not have air permeability.
上述した定着ユニット32は、アッパコンベア36の上流端(従動ローラ46)と供給経路12との間に入口50を規定しており、この入口50の高さ、即ち、供給経路12に対するアッパコンベア36の傾斜角αはスプレーユニット24からの粉粒体の噴出角βに応じて調整可能である。
The fixing unit 32 described above defines an inlet 50 between the upstream end (driven roller 46) of the upper conveyor 36 and the supply path 12, and the height of the inlet 50, that is, the upper conveyor 36 with respect to the supply path 12. Can be adjusted according to the spray angle β of the granular material from the spray unit 24.
傾斜角αの調整を可能にするため、アッパコンベア36は駆動ローラ44のローラ軸(図示しない)を中心して上下に回動自在に支持され、一方、従動ローラ46のローラ軸(図示しない)は昇降アクチュエータ52に支持されている。具体的には、昇降アクチュエータ52はエアシリンダであり、供給経路12に対してアッパコンベア36の上流端を接離させることで、傾斜角α、即ち、入口50の高さを調整する。
In order to enable adjustment of the inclination angle α, the upper conveyor 36 is supported so as to be rotatable up and down around a roller shaft (not shown) of the driving roller 44, while the roller shaft (not shown) of the driven roller 46 is The lift actuator 52 is supported. Specifically, the elevating actuator 52 is an air cylinder, and adjusts the inclination angle α, that is, the height of the inlet 50 by bringing the upstream end of the upper conveyor 36 into and out of contact with the supply path 12.
一方、駆動ローラ38,44のローラ軸は共通の動力伝達経路54を介して駆動ユニット56に接続され、この駆動ユニット56は、電動モータ等の駆動源58及び速度コントローラ60を含む。それ故、駆動源58の駆動力が動力伝達経路54を介して駆動ローラ38,44に伝達されたとき、図1でみて駆動ローラ38は反時計方向に回転され、そして、駆動ローラ44は時計方向に同一の周速で回転される。それ故、メッシュベルト42の上面及び定着ベルト48の下面はフィルタトウTの移送方向と同一の方向に走行し、これらベルト42,48の走行速度はフィルタトウTの移送速度に応じて、速度コントローラ60によって制御される。
On the other hand, the roller shafts of the drive rollers 38 and 44 are connected to a drive unit 56 through a common power transmission path 54, and the drive unit 56 includes a drive source 58 such as an electric motor and a speed controller 60. Therefore, when the driving force of the driving source 58 is transmitted to the driving rollers 38 and 44 via the power transmission path 54, the driving roller 38 is rotated counterclockwise as viewed in FIG. It is rotated at the same peripheral speed in the direction. Therefore, the upper surface of the mesh belt 42 and the lower surface of the fixing belt 48 travel in the same direction as the transfer direction of the filter tow T, and the traveling speed of these belts 42 and 48 depends on the transfer speed of the filter tow T. 60.
図1から明らかなように、定着ユニット32の入口50及び前述したスプレーユニット24は供給経路12に沿って互いに離間している。それ故、入口50とスプレーユニット24との間には必要に応じてカバー62が配置されていてもよい。このカバー62は入口50からスプレーユニット24まで延び、移送経路12の上方を覆っている。なお、カバー62がスプレーユニット24からの粉粒体の噴出を妨げることはない。
As is clear from FIG. 1, the inlet 50 of the fixing unit 32 and the spray unit 24 described above are separated from each other along the supply path 12. Therefore, a cover 62 may be disposed between the inlet 50 and the spray unit 24 as necessary. The cover 62 extends from the inlet 50 to the spray unit 24 and covers the transfer path 12. The cover 62 does not hinder the ejection of powder from the spray unit 24.
更に、定着ユニット32、即ち、そのロアコンベア34の下方にはサクション源としての集塵ユニット64が配置されている。この集塵ユニット64はその上面にメッシュシート66を有し、このメッシュシート66はロアコンベア34に沿って延びている。集塵ユニット64はメッシュシート66を通じて空気を吸引し、メッシュシート66の網目もまた粉粒体の平均粒径よりも小さい方が好ましい。
Further, a dust collecting unit 64 as a suction source is arranged below the fixing unit 32, that is, the lower conveyor 34. The dust collection unit 64 has a mesh sheet 66 on its upper surface, and the mesh sheet 66 extends along the lower conveyor 34. The dust collection unit 64 sucks air through the mesh sheet 66, and the mesh of the mesh sheet 66 is also preferably smaller than the average particle diameter of the granular material.
次に、上述した添加装置22による粉粒体の添加方法を説明する。
フィルタトウTの移送中、ロア及びアッパコンベア34,36はフィルタトウTの移送速度に応じた速度で走行されている。このような状態にて、スプレーユニット24の各静電ノズル30は、定着ユニット32の入口50に進入する直前のフィルタトウTに向けて、帯電された粉粒体を空気とともに噴出する。フィルタトウTに吹き付けられた粉粒体及び空気のうち、空気はフィルタトウT及びロアコンベア34のメッシュベルト42を通過してフィルタトウT内から逃がされるが、しかしながら、粉粒体はフィルタトウT内に残され、空気から分離される。 Next, the addition method of the granular material by theaddition apparatus 22 mentioned above is demonstrated.
During the transfer of the filter tow T, the lower and upper conveyors 34 and 36 are traveling at a speed corresponding to the transfer speed of the filter tow T. In such a state, each electrostatic nozzle 30 of the spray unit 24 ejects the charged granular material together with air toward the filter toe T just before entering the inlet 50 of the fixing unit 32. Of the powder particles and air sprayed on the filter tow T, the air passes through the filter tow T and the mesh belt 42 of the lower conveyor 34 and escapes from the filter tow T. However, the powder particles are contained in the filter tow T. And separated from the air.
フィルタトウTの移送中、ロア及びアッパコンベア34,36はフィルタトウTの移送速度に応じた速度で走行されている。このような状態にて、スプレーユニット24の各静電ノズル30は、定着ユニット32の入口50に進入する直前のフィルタトウTに向けて、帯電された粉粒体を空気とともに噴出する。フィルタトウTに吹き付けられた粉粒体及び空気のうち、空気はフィルタトウT及びロアコンベア34のメッシュベルト42を通過してフィルタトウT内から逃がされるが、しかしながら、粉粒体はフィルタトウT内に残され、空気から分離される。 Next, the addition method of the granular material by the
During the transfer of the filter tow T, the lower and
詳しくは、メッシュベルト42の網目は粉粒体の平均粒径よりも小さいので、粉粒体がメッシュベルト42を通過することはない。また、粉粒体が帯電されており、しかも、フィルタトウTには可塑剤が既に添加されているので、粉粒体はフィルタトウTのフィルタ繊維に効果的に付着、即ち、定着される。
一方、フィルタトウT及びメッシュベルト42を通過する空気、即ち、図1及び図2中、参照符号Aで示された空気流Aの発生は、フィルタトウTの上面にて跳ね返る空気の流れを大幅に低減する。それ故、このような空気流の跳ね返りに起因する粉粒体の浮遊は効果的に抑制される。 Specifically, since the mesh of themesh belt 42 is smaller than the average particle diameter of the powder particles, the powder particles do not pass through the mesh belt 42. Further, since the powder particles are charged and the plasticizer is already added to the filter tow T, the powder particles are effectively attached to the filter fibers of the filter tow T, that is, fixed.
On the other hand, the generation of the air passing through the filter tow T and themesh belt 42, that is, the air flow A indicated by the reference symbol A in FIGS. To reduce. Therefore, the floating of the granular material due to the rebound of the air flow is effectively suppressed.
一方、フィルタトウT及びメッシュベルト42を通過する空気、即ち、図1及び図2中、参照符号Aで示された空気流Aの発生は、フィルタトウTの上面にて跳ね返る空気の流れを大幅に低減する。それ故、このような空気流の跳ね返りに起因する粉粒体の浮遊は効果的に抑制される。 Specifically, since the mesh of the
On the other hand, the generation of the air passing through the filter tow T and the
更に、たとえ浮遊粉粒体が発生しても、浮遊粉粒体の飛散はアッパコンベア36の定着ベルト48により阻止され、浮遊粉粒体の一部は定着ベルト48の下面に付着するか、定着ベルト48の下面に衝突した後、フィルタトウTに落下される。
ロア及びアッパコンベア34,36の下流端は互いに協働して供給経路12上のフィルタトウTを挟み付けているので、フィルタトウTが定着ユニット32から送出されるとき、フィルタトウTはロアコンベア34とアッパコンベア36との間にてプレスされる。それ故、定着ベルト48の下面に付着した粉粒体や、フィルタトウTの上面に露出した粉粒体はフィルタトウTのフィルタ繊維間に押し込められる。 Further, even if floating particles are generated, the floating particles are prevented from being scattered by the fixingbelt 48 of the upper conveyor 36, and a part of the floating particles adheres to the lower surface of the fixing belt 48 or is fixed. After colliding with the lower surface of the belt 48, it is dropped on the filter tow T.
Since the downstream ends of the lower and upper conveyors 34 and 36 cooperate with each other to sandwich the filter tow T on the supply path 12, when the filter tow T is sent out from the fixing unit 32, the filter tow T is moved to the lower conveyor 34. And the upper conveyor 36. Therefore, the granular material adhering to the lower surface of the fixing belt 48 and the granular material exposed on the upper surface of the filter tow T are pushed between the filter fibers of the filter tow T.
ロア及びアッパコンベア34,36の下流端は互いに協働して供給経路12上のフィルタトウTを挟み付けているので、フィルタトウTが定着ユニット32から送出されるとき、フィルタトウTはロアコンベア34とアッパコンベア36との間にてプレスされる。それ故、定着ベルト48の下面に付着した粉粒体や、フィルタトウTの上面に露出した粉粒体はフィルタトウTのフィルタ繊維間に押し込められる。 Further, even if floating particles are generated, the floating particles are prevented from being scattered by the fixing
Since the downstream ends of the lower and
更にまた、ロアコンベア34はアッパコンベア36と協働することで、前述したようにフィルタトウTに粉粒体を良好に定着させるばかりでなく、粉粒体が定着されたフィルタトウTを次工程のラッピングセクション14に連続的に送り込む役割をも担う。それ故、ロアコンベア34は、ラッピングセクション14に供給されるべきフィルタトウTのフィルタ繊維の密度や粉粒体の分布を一様にするうえで大きく貢献する。
Furthermore, the lower conveyor 34 cooperates with the upper conveyor 36, so that not only can the powder particles be well fixed on the filter tow T as described above, but also the filter tow T on which the powder particles are fixed can be used in the next process. It also plays the role of continuously feeding into the wrapping section 14. Therefore, the lower conveyor 34 greatly contributes to uniforming the density of the filter fibers and the distribution of the powder particles of the filter tow T to be supplied to the wrapping section 14.
上述したように添加装置22は粉粒体の浮遊や飛散を阻止した状態で、フィルタトウTに粉粒体を効果的に添加できることから、粉粒体の添加をなすための密閉室や、密閉室内の排気する吸引ファンが不要となる。
更に、スプレーユニット24とアッパコンベア36との間にはカバー62が配置されているので、スプレーユニット24からの粉粒体の主噴出流から上方に飛び出す粉粒体が存在しても、飛び出した粉粒体はカバー62により捕獲され、粉粒体が定着ユニット32の周囲に飛散することはない。 As described above, since theaddition device 22 can effectively add the granular material to the filter tow T in a state in which the floating and scattering of the granular material is prevented, a sealed chamber for adding the granular material, A suction fan for exhausting the room becomes unnecessary.
Furthermore, since thecover 62 is disposed between the spray unit 24 and the upper conveyor 36, even if there is a powder that jumps upward from the main jet flow of the powder from the spray unit 24, it jumped out. The powder particles are captured by the cover 62, and the powder particles are not scattered around the fixing unit 32.
更に、スプレーユニット24とアッパコンベア36との間にはカバー62が配置されているので、スプレーユニット24からの粉粒体の主噴出流から上方に飛び出す粉粒体が存在しても、飛び出した粉粒体はカバー62により捕獲され、粉粒体が定着ユニット32の周囲に飛散することはない。 As described above, since the
Furthermore, since the
更にまた、ロアコンベア34の下方には集塵ユニット64が配置されているので、この集塵ユニット64はその内部にメッシュシート66を通じて前述した空気流Aを吸い込むことができる。それ故、空気流A中にメッシュベルト42を通過した粉粒体が含まれていても、これら通過粉粒体はメッシュシート66上に捕獲され、通過粉粒体が周囲に飛散することはない。
一方、添加装置22は、スプレーユニット24からの粉粒体の噴出量、即ち、粉体定量供給装置26からスプレーユニット24への粉粒体の供給量を調整するだけで、フィルタトウTへの粉粒体の添加量を容易且つ簡単に制御することができる。 Furthermore, since thedust collection unit 64 is disposed below the lower conveyor 34, the dust collection unit 64 can suck the air flow A described above through the mesh sheet 66 therein. Therefore, even if the airflow A contains powder particles that have passed through the mesh belt 42, these passing powder particles are captured on the mesh sheet 66 and the passing powder particles are not scattered around. .
On the other hand, theaddition device 22 only adjusts the amount of powder and particles ejected from the spray unit 24, that is, the amount of powder and particles supplied from the powder fixed amount supply device 26 to the spray unit 24. The amount of powder added can be easily and easily controlled.
一方、添加装置22は、スプレーユニット24からの粉粒体の噴出量、即ち、粉体定量供給装置26からスプレーユニット24への粉粒体の供給量を調整するだけで、フィルタトウTへの粉粒体の添加量を容易且つ簡単に制御することができる。 Furthermore, since the
On the other hand, the
本発明は、上述した第1実施例の添加装置に制約されるものではなく、種々の変形が可能である。
図3は第2実施例の添加装置を示す。
第1実施例の添加装置と対比したとき、第2実施例の添加装置は、アッパコンベア36が移送経路12と平行に延び、定着ベルト48の下面全体とメッシュベルト42の上面との間にてフィルタトウTが挟み込まれている点のみで相違する。 The present invention is not limited to the addition apparatus of the first embodiment described above, and various modifications are possible.
FIG. 3 shows the addition apparatus of the second embodiment.
When compared with the addition device of the first embodiment, the addition device of the second embodiment is such that theupper conveyor 36 extends in parallel with the transfer path 12 and is between the entire lower surface of the fixing belt 48 and the upper surface of the mesh belt 42. The only difference is that the filter tow T is sandwiched.
図3は第2実施例の添加装置を示す。
第1実施例の添加装置と対比したとき、第2実施例の添加装置は、アッパコンベア36が移送経路12と平行に延び、定着ベルト48の下面全体とメッシュベルト42の上面との間にてフィルタトウTが挟み込まれている点のみで相違する。 The present invention is not limited to the addition apparatus of the first embodiment described above, and various modifications are possible.
FIG. 3 shows the addition apparatus of the second embodiment.
When compared with the addition device of the first embodiment, the addition device of the second embodiment is such that the
図4は第3実施例の添加装置を示す。
第2実施例の添加装置と対比したとき、第3実施例の添加装置は移送経路12が水平ではなく、下流側に向けて下方に傾斜している点のみで相違する。
第2及び第3実施例の場合、スプレーユニット24は、定着ユニット32の入口の直前位置に向けて粉粒体を噴出するのが好ましい。 FIG. 4 shows the addition apparatus of the third embodiment.
When compared with the addition apparatus of the second embodiment, the addition apparatus of the third embodiment is different only in that thetransfer path 12 is not horizontal but is inclined downward toward the downstream side.
In the case of the second and third embodiments, thespray unit 24 preferably ejects the powder particles toward the position immediately before the entrance of the fixing unit 32.
第2実施例の添加装置と対比したとき、第3実施例の添加装置は移送経路12が水平ではなく、下流側に向けて下方に傾斜している点のみで相違する。
第2及び第3実施例の場合、スプレーユニット24は、定着ユニット32の入口の直前位置に向けて粉粒体を噴出するのが好ましい。 FIG. 4 shows the addition apparatus of the third embodiment.
When compared with the addition apparatus of the second embodiment, the addition apparatus of the third embodiment is different only in that the
In the case of the second and third embodiments, the
図5は第4実施例の添加装置を示す。
第1実施例の添加装置と対比したとき、第4実施例の添加装置は移送経路12が水平ではなく、下流側に向けて下方に傾斜している点のみで相違する。
なお、図3~図5はロアコンベア34及びアッパコンベア36の下流端を移送経路12から離した状態で示しているが、これは作図上の都合による。
前述した第1~第4実施例の添加装置は何れもフィルタ製造機に適用されている。しかしながら、本発明の添加装置はフィルタトウT以外のウエブ材に粉粒体を添加するためにも同様に使用可能である。 FIG. 5 shows the addition apparatus of the fourth embodiment.
When compared with the addition apparatus of the first embodiment, the addition apparatus of the fourth embodiment is different only in that thetransfer path 12 is not horizontal but is inclined downward toward the downstream side.
3 to 5 show the downstream ends of thelower conveyor 34 and the upper conveyor 36 in a state where they are separated from the transfer path 12, this is for the convenience of drawing.
Any of the addition apparatuses of the first to fourth embodiments described above is applied to a filter manufacturing machine. However, the addition apparatus of the present invention can be used in the same manner for adding powder particles to a web material other than the filter tow T.
第1実施例の添加装置と対比したとき、第4実施例の添加装置は移送経路12が水平ではなく、下流側に向けて下方に傾斜している点のみで相違する。
なお、図3~図5はロアコンベア34及びアッパコンベア36の下流端を移送経路12から離した状態で示しているが、これは作図上の都合による。
前述した第1~第4実施例の添加装置は何れもフィルタ製造機に適用されている。しかしながら、本発明の添加装置はフィルタトウT以外のウエブ材に粉粒体を添加するためにも同様に使用可能である。 FIG. 5 shows the addition apparatus of the fourth embodiment.
When compared with the addition apparatus of the first embodiment, the addition apparatus of the fourth embodiment is different only in that the
3 to 5 show the downstream ends of the
Any of the addition apparatuses of the first to fourth embodiments described above is applied to a filter manufacturing machine. However, the addition apparatus of the present invention can be used in the same manner for adding powder particles to a web material other than the filter tow T.
12 移送経路
24 スプレーユニット
30 静電ノズル
22 添加装置
26 粉体定量供給装置
32 定着ユニット
34 ロアコンベア
36 アッパコンベア
42 メッシュベルト
48 定着ベルト
52 昇降アクチュエータ
56 駆動ユニット
62 カバー
64 集塵ユニット(サクション源)
T フィルタトウ(ウエブ材) DESCRIPTION OFSYMBOLS 12 Transfer route 24 Spray unit 30 Electrostatic nozzle 22 Adder 26 Powder fixed quantity supply device 32 Fixing unit 34 Lower conveyor 36 Upper conveyor 42 Mesh belt 48 Fixing belt 52 Lifting actuator 56 Drive unit 62 Cover 64 Dust collection unit (suction source)
T Filter tow (web material)
24 スプレーユニット
30 静電ノズル
22 添加装置
26 粉体定量供給装置
32 定着ユニット
34 ロアコンベア
36 アッパコンベア
42 メッシュベルト
48 定着ベルト
52 昇降アクチュエータ
56 駆動ユニット
62 カバー
64 集塵ユニット(サクション源)
T フィルタトウ(ウエブ材) DESCRIPTION OF
T Filter tow (web material)
Claims (13)
- 空気透過性を有したウエブ材を移送するための移送経路と、
前記移送経路の上方に配置され、前記ウエブ材に向けて粉粒体を空気とともに噴出するスプレーユニットと、
前記移送経路に前記スプレーユニットの下流に位置して配置され、前記ウエブ材に前記粉粒体を定着させる定着ユニットであって、前記ウエブ材の移送を案内する一方、前記ウエブ材に吹き付けられた前記粉粒体及び前記空気のうち、前記粉粒体を前記ウエブ材内に残す一方、前記空気を前記ウエブ材内から下方に逃がす篩部材を有する、定着ユニットと
を備える、粉粒体添加装置。 A transfer path for transferring a web material having air permeability;
A spray unit that is disposed above the transfer path, and sprays the granular material together with air toward the web material;
A fixing unit that is disposed downstream of the spray unit in the transfer path and fixes the granular material to the web material, and guides the transfer of the web material, and is sprayed on the web material Of the powder and the air, the powder and granule adding apparatus, comprising: a fixing unit having a sieve member that leaves the powder in the web material and allows the air to escape downward from the web material. . - 前記定着ユニットは、
前記篩部材として前記移送経路の下側を前記移送経路に沿って延び、前記空気の通過を許容するロアコンベアと、
前記移送経路の上側を前記移送経路に沿って延び、前記ロアコンベアと協働して前記ウエブ材を挟み込む下流端を有する、アッパコンベアと
を含む、請求項1に記載の添加装置。 The fixing unit includes:
A lower conveyor that extends below the transfer path as the sieve member along the transfer path and allows the passage of the air;
The addition apparatus according to claim 1, further comprising: an upper conveyor that extends along the transfer path along the transfer path and has a downstream end that sandwiches the web material in cooperation with the lower conveyor. - 前記スプレーユニットは、前記粉粒体を帯電させて噴出する複数の静電ノズルを含む、請求項2に記載の添加装置。 The addition device according to claim 2, wherein the spray unit includes a plurality of electrostatic nozzles that charge and eject the powder particles.
- 前記ロアコンベアは無端状のメッシュベルトを有する、請求項2に記載の添加装置。 The additive device according to claim 2, wherein the lower conveyor has an endless mesh belt.
- 前記アッパコンベアは前記移送経路に対して傾斜し、前記移送経路よりも上方に位置付けられた上流端を有する、請求項2に記載の添加装置。 The addition apparatus according to claim 2, wherein the upper conveyor has an upstream end that is inclined with respect to the transfer path and is positioned above the transfer path.
- 前記アッパコンベアは、前記移送経路からの前記上流端の高さレベルを調整可能である、請求項5に記載の添加装置。 The addition device according to claim 5, wherein the upper conveyor is capable of adjusting a height level of the upstream end from the transfer path.
- 前記アッパコンベアは前記移送経路に沿い、前記ロアコンベアと平行に延びている、請求項2に記載の添加装置。 The addition apparatus according to claim 2, wherein the upper conveyor extends along the transfer path in parallel with the lower conveyor.
- 前記定着ユニットは、前記ロアコンベアの下方に配置され、前記ウエブ材及び前記ロアコンベアから逃がされた前記空気を吸引するサクション源を更に備える、請求項2に記載の添加装置。 The addition device according to claim 2, wherein the fixing unit further includes a suction source that is disposed below the lower conveyor and sucks the web material and the air released from the lower conveyor.
- 前記ウエブ材は、シガレットのためのフィルタ材料である、請求項3に記載の添加装置。 The addition device according to claim 3, wherein the web material is a filter material for cigarette.
- 空気透過性を有したウエブ材に粉粒体を添加する添加方法であって、
前記ウエブ材を移送経路に沿って移送し、
前記ウエブ材の上方から前記ウエブ材に粉粒体を空気とともに噴出し、
前記ウエブ材に吹き付けられた前記粉粒体及び前記空気のうち、篩部材を使用して前記粉粒体を前記ウエブ材内に残す一方、前記空気を前記ウエブ材内から逃がし、前記ウエブ材に前記粉粒体を定着させる、粉粒体の添加方法。 It is an addition method of adding a granular material to a web material having air permeability,
Transporting the web material along a transport path;
A powder body is ejected from above the web material to the web material together with air,
Of the powder particles and the air sprayed on the web material, a sieve member is used to leave the powder particles in the web material, while letting the air escape from the web material. A method for adding a granular material, wherein the granular material is fixed. - 前記空気が前記ウエブ材から逃がされた後、前記ウエブ材をプレスする、請求項10に記載の添加方法。 The addition method according to claim 10, wherein the web material is pressed after the air has escaped from the web material.
- 前記ウエブ材及び前記篩部材から逃がされた前記空気を吸引する、請求項11に記載の添加方法。 The addition method according to claim 11, wherein the air released from the web material and the sieve member is sucked.
- 前記ウエブ材は、シガレットためのフィルタ材料である、請求項10に記載の添加方法。 The addition method according to claim 10, wherein the web material is a filter material for cigarette.
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PCT/JP2009/070474 WO2011070639A1 (en) | 2009-12-07 | 2009-12-07 | Powder adding device and adding method thereof |
Applications Claiming Priority (1)
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PCT/JP2009/070474 WO2011070639A1 (en) | 2009-12-07 | 2009-12-07 | Powder adding device and adding method thereof |
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Cited By (2)
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CN103894325A (en) * | 2014-03-28 | 2014-07-02 | 苏州市建诚装饰材料有限公司 | Electrostatic spraying device |
EP3488711A4 (en) * | 2016-07-26 | 2020-03-18 | Japan Tobacco, Inc. | Filter manufacturing device and filter manufacturing method |
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JPH11239472A (en) * | 1997-10-30 | 1999-09-07 | Brown & Williamson Tobacco Corp | Addition of medicine to filter material and method therefor |
JPH11243939A (en) * | 1998-02-27 | 1999-09-14 | Japan Tobacco Inc | Filter for tobacco product |
JP2000118128A (en) * | 1998-10-13 | 2000-04-25 | Dainippon Printing Co Ltd | Manufacture of thermal transfer image receiving sheet |
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JPS5391199A (en) * | 1976-11-02 | 1978-08-10 | Cigarette Components Ltd | Smoke filtering rod and method and apparatus for producing same |
JPH0272856A (en) * | 1988-07-13 | 1990-03-13 | Koerber Ag | Method and apparatus for producing filter rod for rod-shaped smoking article |
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CN103894325A (en) * | 2014-03-28 | 2014-07-02 | 苏州市建诚装饰材料有限公司 | Electrostatic spraying device |
EP3488711A4 (en) * | 2016-07-26 | 2020-03-18 | Japan Tobacco, Inc. | Filter manufacturing device and filter manufacturing method |
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