WO2014080516A1 - Method for producing filter cigarette, filter, and filter cigarette - Google Patents
Method for producing filter cigarette, filter, and filter cigarette Download PDFInfo
- Publication number
- WO2014080516A1 WO2014080516A1 PCT/JP2012/080465 JP2012080465W WO2014080516A1 WO 2014080516 A1 WO2014080516 A1 WO 2014080516A1 JP 2012080465 W JP2012080465 W JP 2012080465W WO 2014080516 A1 WO2014080516 A1 WO 2014080516A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filter
- sheath
- core
- hollow filter
- cigarette
- Prior art date
Links
Images
Classifications
-
- 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
- A24D3/0275—Manufacture of tobacco smoke filters for filters with special features
- A24D3/0291—Manufacture of tobacco smoke filters for filters with special features for hollow tipped filters, e.g. recess filters
-
- 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
-
- 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
- A24D3/0229—Filter rod forming processes
- A24D3/0233—Filter rod forming processes by means of a garniture
-
- 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
- A24D3/0275—Manufacture of tobacco smoke filters for filters with special features
- A24D3/0279—Manufacture of tobacco smoke filters for filters with special features with tubes
-
- 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
- A24D3/0275—Manufacture of tobacco smoke filters for filters with special features
- A24D3/0287—Manufacture of tobacco smoke filters for filters with special features for composite filters
-
- 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
- A24D3/04—Tobacco smoke filters characterised by their shape or structure
Definitions
- the present invention relates to a filter cigarette manufacturing method, a filter, and a filter cigarette.
- a filter manufacturing machine that manufactures a hollow filter having a through hole formed in the axial direction is known (see, for example, Patent Document 1).
- a filter in which such through-holes are formed has a heavier weight of cellulose acetate tow than a normal filter, and further has a high proportion of plasticizer added to cellulose acetate tow. Thereby, sufficient hardness is given to the filter and the shape of the through hole is maintained.
- the manufactured hollow filter needs to be conveyed while being crushed in a passage narrower than the diameter of the filter in the subsequent process, for example, the process of winding the chip paper to connect with the cigarette.
- the shape of the through hole at the end of the filter may change.
- the filter mounting device for winding the chip paper is provided with a convex portion protruding toward the passage in order to give a trigger of rotation for the purpose of reliably sending the filter to the passage.
- the present invention has been made in consideration of the above-mentioned problems, and a filter cigarette manufacturing method capable of reducing a through-hole shape change even when the hollow filter is crushed in a subsequent process of manufacturing a filter cigarette using a hollow filter.
- An object of the present invention is to provide a filter and a filter cigarette.
- a core fiber processing step in which a plasticizer is added to a core fiber having a total fineness of 23,000 denier to 70000 denier to an addition rate of 13% to 40%, and a total fineness of 10,000 denier to 47,000 denier.
- the core fiber is cured to form a core portion having a hole extending from one end surface toward the other end surface, and the outer portion of the core portion is covered with the sheath fiber to form a hollow filter as a sheath portion.
- the hollow filter is narrower than the diameter of the hollow filter and is equal to the diameter of the core part. Conveyed by passing also large narrow portion, to provide a filter cigarette manufacturing method comprising the subsequent step.
- the addition rate of the plasticizer to the core fiber is 13% to 35%, and the addition rate of the plasticizer to the sheath fiber is about 3% to 12%.
- the post-process is directed toward the inside of the rolling passage in order to provide an opportunity to roll the hollow filter and the cigarette when the hollow filter and the cigarette are introduced into the rolling passage.
- the present invention also includes a cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed, and an adsorption filter continuously connected to the hollow filter in the longitudinal direction.
- the hollow filter has a core portion in which a hole extending from one end face toward the other end face is formed, and a sheath portion covering the outside of the core portion, and between the core portion and the sheath portion.
- the core portion has a total fineness of 23,000 denier to 70000 denier, a plasticizer addition rate of 13% to 40%, and the sheath portion has a total fineness of 10,000 denier to 47,000.
- a filter having a plasticizer addition rate of 0% to 15%.
- the present invention includes a cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed, and an adsorption filter continuously connected to the hollow filter in the longitudinal direction.
- the hollow filter has a core portion in which a hole extending from one end face toward the other end face is formed, and a sheath portion covering the outside of the core portion, and between the core portion and the sheath portion.
- the core portion has a hardness of 0 mm / 10 or more and less than 5 mm / 10
- the sheath portion has a hardness of 5 mm / 10 or more and 10 mm / 10 or less.
- the core portion has a total fineness of 23000 denier to 70000 denier and a plasticizer addition rate of 13% to 40%, and the sheath portion has a total fineness of 10,000 denier to 47000 denier.
- the addition rate is 0% to 15%.
- the present invention provides a filter cigarette comprising the filter, a cigarette in which chopped cigarettes are wrapped with a wrapping paper, and chip paper that wraps the filter and the cigarettes and connects them in the longitudinal direction.
- the shape change of the through-hole can be reduced.
- the filter cigarette manufacturing machine 1 used for filter manufacturing will be described.
- the filter cigarette making machine 1 has first and second feeding paths 2 and 3 in which the core fiber 4 and the sheath fiber 5 are continuously drawn out in the direction of the arrow in the figure and travel. Yes.
- the arrows shown along the feeding paths 2 and 3 in FIG. 1 indicate the traveling directions of the core fiber 4 and the sheath fiber 5.
- a core fiber 4 and a sheath fiber 5 made of cellulose acetate fiber are bundled at the start ends of the feeding paths 2 and 3, respectively, as a tow bail 28.
- Each feeding path 2, 3 is guided by a guide 36 or a guide roller 6.
- the first unwinding path 2 is provided with a first fiber opening and plasticizer addition device 7.
- the core fiber 4 traveling on the first feeding path 2 is opened using a known banding jet, a pair of pretension rollers, a pair of blooming rollers, and the like. Then, a plasticizer is added to the opened core fiber 4 using a known spray spray or the like.
- a second opening and plasticizer addition device 8 having the same function as the first opening and plasticizer addition device 7 is also provided in the second feeding path 3 along which the sheath fiber 5 travels.
- the first and second feeding paths 2 and 3 are connected to the hole forming device 9.
- the hole forming device 9 (see FIG. 2) will be described later.
- the hollow filter intermediate 54 in which the through holes 10 are formed in the longitudinal direction is manufactured.
- the hollow filter intermediate 54 is sent to the paper winding device 13 through the conveyance path 12.
- the hollow filter intermediate body 54 is manufactured by passing through the trumpet guide 18 provided on the inlet side of the paper winding device 13.
- the trumpet guide 18 is handled as a part of the hole forming device 9 for convenience.
- the hollow filter intermediate 54 is wrapped with the web 30 (see FIG. 4) to become the hollow filter 11 (see FIG. 3).
- the hollow filter 11 is cut by the paper winding device 13, the entire outer periphery is wrapped with the forming paper 32 (see FIG. 4) in a state of being arranged in the longitudinal direction with the adsorption filter 31 that adsorbs the components in the smoke. Then, the hollow filter 11 and the adsorption filter 31 wrapped with the molding paper 32 become the filter 22 (see FIG. 4), and are sent to the filter mounting device 14 and connected to the cigarette 16 via the chip paper 15.
- the hollow filter 11 may adsorb
- the hollow filter intermediate 54 is manufactured by the hole forming apparatus 9.
- the hole forming device 9 includes a forming tube 17, a trumpet guide 18, and a mandrel 19.
- One end of the mandrel 19 is supported by the support base 20 and extends into the forming tube 17 from the inlet side of the core fiber 4.
- the forming tube 17 has a hollow cylindrical shape
- the trumpet guide 18 has a hollow cylindrical shape with an enlarged diameter on the inlet side, and allows the sheath fiber 5 to pass along with the core fiber 4 while narrowing down.
- the core fiber 4 that has passed through the first fiber opening and plasticizer addition device 7 enters the forming tube 17.
- the core fiber 4 passes through a passage formed by the molding tube 17 and the mandrel 19 in cooperation with each other.
- the core fiber 4 is heat-treated in the molding tube 17 and has a through hole 10 along the outer shape of the mandrel 19 in the longitudinal direction. It becomes the hollow cylindrical core part 11a.
- the heat treatment unit 50 is provided as a hole 51 that penetrates the peripheral wall of the molded tube 17, and steam is blown into the molded tube 17 through the hole 51.
- the core fiber 4 is plasticized and hardened in the process of passing through the molding tube 17.
- a new heat source such as microwave, high-temperature air, or heating wire may be used.
- tube 17 is expanded gradually.
- the inlet side of the first molded tube 17 is curved.
- a plasticizer may be added from the inside before the core fiber 4 enters the forming tube 17.
- a part of the support 20 can be made into a spray nozzle, and a plasticizer can be added from this nozzle (arrow S in FIG. 2).
- the plasticizer is supplied toward the portion to be the surface of the through-hole 10, so that the surface of the through-hole 10 can be appropriately cured.
- the core fiber 4 can be sufficiently cured with a small amount of plasticizer. If the surface of the through hole 10 is cured in this way, for example, when the hollow filter 11 is cut, the through hole 10 can be prevented from being crushed by the cut surface.
- a trumpet guide 18 having the same axis as the forming tube 17 is disposed on the outlet side of the forming tube 17.
- the core portion 11 a formed by the forming tube 17 is drawn out as it is and flows into the trumpet guide 18.
- the sheath fiber 5 that has passed through the second opening and plasticizer addition device 8 enters the trumpet guide 18. Since the sheath fiber 5 passes through a passage formed by the trumpet guide 18 and the core portion 11a in cooperation, the sheath fiber 5 becomes a sheath portion 11b that covers the outside of the core portion 11a.
- the hollow filter intermediate 54 is wrapped with the web 30 on the ganiche belt 55 to become the hollow filter 11.
- the web 30 on the ganiche belt 55 is not shown in FIG.
- the hollow filter 11 thus formed has a two-layer structure having a core portion 11a as an inner cylinder and a sheath portion 11b as an outer cylinder.
- the core portion 11 a and the sheath portion 11 b are clearly separated by a boundary line 21 in the cross section of the hollow filter 11.
- the diameter can be 7.4 mm to 8.0 mm
- the diameter of the core portion 11a can be 4.6 mm to 5.2 mm.
- the diameter may be 5.0 mm to 7.3 mm
- the diameter of the core portion 11a may be 2.4 mm to 4.7 mm.
- the diameter of the core portion 11a of the hollow filter 11 having a diameter of 7.4 mm to 8.0 mm can be set to 2.4 mm to 4.7 mm.
- Such a hollow filter 11 is manufactured through the following manufacturing method (see FIG. 5).
- a core fiber processing step is performed (step S1).
- the core fiber processing step is performed using the first fiber opening and plasticizer addition device 7.
- the total fineness of the core fiber 4 is set to 23000 denier to 70000 denier (2555.3 tex to 7777 tex).
- a cellulose acetate fiber etc. can be used for a fiber.
- the core fiber 4 fed to the first feeding path 2 is opened, and a plasticizer is added at an addition rate of 13% to 40% (preferably 15 to 35%, most preferably 17 to 30%).
- the addition rate of the plasticizer is a value determined by the sum of the first fiber opening and the addition by the plasticizer addition device and the local addition from the support base 20.
- a sheath fiber processing step is performed (step S2).
- the sheath fiber processing step is performed using the second fiber opening and plasticizer addition device 8.
- the total fineness of the sheath fiber 5 is set to 10,000 denier to 47,000 denier (1888.7 tex to 2999.7 tex).
- a cellulose acetate fiber etc. can be used for a fiber.
- the sheath fiber 5 fed to the second feeding path 3 is opened, and a plasticizer is added at an addition rate of 15% or less (preferably 3 to 12%, most preferably 6 to 9%). Alternatively, a plasticizer may not be added.
- step S3 a hollow filter formation process is performed (step S3).
- This hollow filter forming step is performed using the hole forming apparatus 9.
- the core fiber 4 is a cylindrical core portion 11a in which the through hole 10 is formed in the longitudinal direction, and the outside of the core portion 11a is covered with the sheath fiber 5 to form a sheath portion 11b.
- the hollow filter 11 is formed by wrapping with a web 30.
- Such a hollow filter 11 is subjected to a filter mounting step (step S4) as an example of a post-process.
- a filter mounting device 14 used in this step will be described. That is, in order to manufacture the filter cigarette 27 using the hollow filter 11, a filter mounting device 14 as shown in FIG. 6 is used.
- a filter plug 37 is first disposed between two cigarettes 16. This filter plug 37 is formed with a length of two filters 22 with the adsorption filter 31 positioned on both sides. Thereby, the intermediate product 25 of the double filter cigarette 49 is formed. Thereafter, the chip paper 15 having an adhesive applied on one side is wound around the intermediate product 25 to form a double filter cigarette 49.
- the filter mounting device 14 includes a transport path 39 formed by the first transport drum 38 and the second transport drum 23. That is, the transport path 39 for the intermediate product 25 is formed by the first transport drum 38 rotating in the direction of arrow R1 and the second transport drum 23 rotating in the direction of arrow R2.
- the conveyance path 39 is a path along which the intermediate product 25 is conveyed.
- the first transport drum 38 forms an upstream portion of the transport path 39, and the second transport drum 23 forms a downstream portion.
- the first transport drum 38 is also called a swash plate drum.
- the second transport drum 23 is also called a rolling drum. Both the first conveyance drum 38 and the second conveyance drum 23 have a plurality of adsorption grooves (not shown) that adsorb while accommodating a part of the intermediate product 25 on the outer periphery. The intermediate products 25 are accommodated one by one in the suction grooves and conveyed in the circumferential direction of the first conveyance drum 38 and the second conveyance drum 23.
- a supply drum 40 that rotates in the direction of arrow R3 is disposed adjacent to the first transport drum 38.
- the chip paper 15 is unwound from the supply drum 40, and one side edge of the chip paper 15 is affixed to the intermediate product 25 that is transported along the first transport drum 38.
- a guide member 24 is disposed adjacent to the second transport drum 23 along the circumferential direction thereof. The guide member 24 rolls the intermediate product 25 in cooperation with the second transport drum 23 and winds the chip paper 15 around the intermediate product 25.
- the filter mounting process (step S4) as an example of a post-process for actually winding the chip paper 15 around the intermediate product 25 using the filter mounting apparatus 14 having the above structure will be described in order.
- the double cigarette DS having a length corresponding to two cigarettes manufactured by a known means is cut into two cigarettes 16 in the process of transporting the cigarette DS (arrow F1 in FIG. 6). Thereafter, these two cigarettes 16 are separated in the axial direction to form a cigarette row (arrow F2 in FIG. 6). Then, the cigarette row is supplied to the first transport drum 38 (arrow F3 in FIG. 6).
- the above-described filter plugs 37 are aligned in a row through a grading process in the transport direction, and then supplied to a first transport drum (swash plate drum) 38 through an acceleration drum 41 that rotates in the direction of arrow R4.
- the above-described cigarette row has an interval in which the filter plug 37 can be received between the cigarettes 16 and is supplied to the first transport drum 38 while maintaining this interval.
- the first transport drum 38 is provided with a pair of floating disks (not shown) on both sides. As the first transport drum 38 rotates, each cigarette 16 is sandwiched between the floating disks on both sides, and the distance between them in the axial direction. Packed. Thereby, the intermediate product 25 of the double filter cigarette in which the filter plug 37 is positioned between the two cigarettes 16 is formed.
- a tip paper web W is fed out from a tip paper roll (not shown) (in the direction of arrow E in FIG. 6).
- the web W is guided to a supply drum (coke drum) 40.
- An adhesive glue
- An adhesive roller 42 is disposed at a position in front of the supply drum 40, and the adhesive roller 42 rotates with its lower half immersed in the adhesive liquid 43.
- a transmission roller 44 is disposed adjacently above the adhesive roller 42, and the adhesive adhering to the outer peripheral surface of the adhesive roller 42 is transferred to the outer peripheral surface of the transmission roller 44 with a predetermined layer thickness. As the web W passes, the transmission roller 44 rolls on one side and applies an adhesive according to a predetermined application pattern.
- the supply drum 40 has a suction surface on its outer periphery, and rotates while holding the web W on this suction surface.
- a bladed drum 45 is disposed adjacent to the supply drum 40.
- the bladed drum 45 has a number of coke knives (not shown) on its outer periphery. These coke knives are arranged at regular intervals, and rotate in synchronization with the supply drum 40 as the bladed drum 45 rotates.
- the web W is cut into chip paper 15 on the suction surface of the supply drum 40 by these rotating coke knives.
- the chip paper 15 rotates while being sucked and held by the supply drum 40 and is supplied to the intermediate product 25 on the first transport drum 38.
- a gap between the supply drum 40 and the first transport drum 38 is formed as a pasting passage 46.
- the chip paper 15 is attached to the outer surface of the intermediate product 25 from the leading portion thereof, and is conveyed on the first conveyance drum 38 together with the intermediate product 25.
- the intermediate product 25 is transferred from the first transport drum 38 to the second transport drum (rolling drum) 23 with the chip paper 15 attached.
- a transfer passage 47 is formed between the first transfer drum 38 and the second transfer drum 23.
- the intermediate product 25 is transported between the guide member 24 as the second transport drum 23 rotates.
- the guide member 24 extends along the rotation direction of the second transport drum 23.
- a rolling passage 26 of the intermediate product 25 is formed between the outer periphery of the second transport drum 23 and the guide member 24, and the rolling passage 26 is curved along the outer periphery of the second transport drum 23. Yes.
- the chip paper 15 is wound around the intermediate product 25, and the double filter cigarette 49 is manufactured.
- the filter cigarette 27 in which the hollow filter 11 is positioned on the end surface on the mouth end side is manufactured by cutting the double filter cigarette 49 at the location of the hollow filter 11.
- a narrow portion 48 (for example, affixed to the conveyance path 39) is narrower than the diameter of the filter plug 37, that is, the hollow filter 11, which is conveyed as a part of the intermediate product 25, and larger than the diameter of the core portion 11a.
- the chip paper 15 needs to be a little compressed in the radial direction and affixed, and the drums 38 and 23 adsorb the intermediate product 25 by air suction. It is necessary to ensure the delivery of the intermediate product 25 without causing air leakage by compressing the intermediate product 25 in the radial direction.
- the rolling passage 26 it is necessary to roll the tip paper 15 securely by rolling the intermediate product 25 while compressing the intermediate product 25 in a radial direction to some extent.
- the narrow portion 48 is required in the transport path 39 for some purpose.
- a convex portion 29 is provided so as to project the rolling of the intermediate product 25 to the rolling passage 26 side.
- the chip paper 15 of the intermediate product 25 is wound, and a double filter cigarette 49 using the hollow filter 11 is manufactured.
- the filter cigarette 27 using the hollow filter 11 has a filter 22, and the hollow filter 11 is used on the mouth end side of the filter 22.
- An adsorption filter 31 is continuously connected in the longitudinal direction of the hollow filter 11.
- the hollow filter 11 and the adsorption filter 31 are each wrapped in a web 30.
- the hollow filter 11 and the adsorption filter 31 are both integrated with a molding paper 32.
- the cigarette 16 is formed by wrapping a cigarette 33 with a wrapping paper 34. As described above, the filter 22 and the cigarette 16 are connected via the chip paper 15 and integrated.
- the core portion 11a has a hardness of 0 mm / 10 to 5 mm / 10
- the sheath portion 11b has a hardness of 5 mm / 10 to 10 mm / 10. That is, the core portion 11a has a high hardness, and the sheath portion 11b has a low hardness.
- the diameter of the core part 11a is smaller than the width
- the post-process is a filter mounting process using the filter mounting device 14.
- the portion provided with the convex portion 29 in the introduction portion of the rolling passage 26 described above has a narrow passage width, but the diameter of the core portion 11a is smaller than the width of the conveyance passage in the portion where the convex portion 29 is provided. .
- the core portion 11a and the sheath portion 11b are set so that the core portion 11a is hardened and the sheath portion 11b is softened by changing the total fineness and the addition rate of the plasticizer. Even if the sheath portion 11b is crushed during passage, the sheath portion 11b absorbs external pressure, and the pressure applied to the core portion 11a is reduced. Therefore, the shape change of the through hole 10 can be reduced. Further, since at least the diameter of the core portion 11a is smaller than the width of the narrow portion 48, the through hole 10 is not directly crushed. For example, as shown in FIG. 7, when the hollow filter 11 passes through the intermediate product 25, that is, the rolling passage 26 (narrow portion 48) whose width is narrower than the diameter of the hollow filter 11, the sheath portion 11 b is directly crushed. However, the core portion 11a is not directly crushed.
- This effect is particularly useful when passing through the convex portion 29 provided in the introduction portion of the rolling passage 26 of the filter mounting device 14. This is because this portion is particularly narrow in the narrow portion 48 narrower than the diameter of the hollow filter 11. Further, the core portion 11 a and the sheath portion 11 b are clearly separated via a boundary line 21 in a cross-sectional view of the hollow filter 11. Therefore, compared with the so-called gradation layer in which the core fiber 4 and the sheath fiber 5 are mixed and the ratio of the core fiber 4 and the sheath fiber 5 changes stepwise depending on the radial direction of the hollow filter 11, The pressure from the outside can be cut off at 21 to effectively protect the core portion 11a from the external pressure, and it becomes easy to manufacture a filter of the same quality.
- the core portion 11a becomes hard when the plasticizer addition rate and the total fineness value are increased, and the core portion 11a is soft when the plasticizer addition rate and the total fineness value are decreased. And if the core part 11a is too soft, fluff will occur and it will become difficult to maintain the shape of a through-hole.
- the core fiber 4 for forming the core portion 11a preferably has a total fineness of 23,000 denier to 70000 denier, more preferably 26000 denier to 60000 denier, and 30000 denier to 50000 denier. Most preferably.
- the plasticizer addition rate of the core fiber 4 is preferably 13% to 40%, more preferably 15% to 35%, and most preferably 17% to 30%. And it is preferable that the hardness of the core part 11a shall be 0 mm / 10 or more and less than 5 mm / 10 by such a total fineness and a plasticizer addition rate.
- the smell of the plasticizer becomes strong. If the total fineness is too small, the circumference of the hollow filter 11 tends to be thinner than a desired value when the sheath fiber 11b is used. If the total fineness is too large, the circumference of the hollow filter 11 tends to be thicker than a desired value.
- the core portion 11a becomes hard when the plasticizer addition rate and the total fineness value are increased, and the core portion 11a is soft when the plasticizer addition rate and the total fineness value are decreased. And if the sheath fiber 11b is too soft, it becomes difficult to maintain the position of the core part at a desired position, and the cut surface is likely to fluff.
- the core fiber 4 for forming the sheath fiber 11b preferably has a total fineness of 10,000 denier to 47,000 denier, more preferably 10,000 denier to 40000 denier, and 12000 denier to 30000 denier. Most preferably.
- the plasticizer addition rate of the sheath fiber 11b is preferably 0% to 15%, more preferably 3% to 12%, and most preferably 6% to 9%. And it is preferable that the hardness of the sheath fiber 11b shall be 5 mm / 10 or more and 10 mm / 10 or less by such a total fineness and a plasticizer addition rate.
- the cross-sectional shapes of the through hole 10 and the core portion 11a are both circular and concentric with the axis of the hollow filter 11 as shown in FIG.
- the center of the through hole 10 may not be on the axis of the hollow filter 11.
- the cross-sectional shape of the through hole 10 may be a star shape as shown in FIG.
- various shapes such as a cross shape and a heart shape may be used.
- the cross-sectional shape of the core part 11a may be a rectangle.
- a polygon such as a triangle may be used.
- the through hole 10 is provided as the hole provided in the core part 11 a
- the hole provided in the core part 11 a does not need to pass through, and from one end surface to the other What is necessary is just to extend toward an end surface.
- a hole 35 extending partway from one end surface of the hollow filter 11 toward the other end surface may be formed.
- the hole 35 can be prevented from being crushed or deformed.
- Such a hole 35 can be formed by introducing the core fiber 4 into the first forming tube while inserting and removing the mandrel 19 by the hole forming device 9.
- the pressurization test was conducted using the hollow filter 11 shown in FIG. 3 as an example and a conventional filter having a through-hole having no core portion 11a and sheath portion 11b as a comparative example.
- the pressurization test was performed on a total of three samples 1 to 3 for the hollow filter 11 of the example, and a total of three samples 4 to 6 for the filter of the comparative example.
- the single fineness of the core portion was 4.0 denier
- the total fineness was 40000 denier
- the plasticizer addition rate was 17%.
- the single fineness of the sheath part was 8.0 denier
- the total fineness was 15000 denier
- the plasticizer addition rate was 6%.
- Comparative Samples 4 to 6 only fibers having a single fineness of 5.0, a total fineness of 47,000 denier, and a plasticizer addition rate of 19% are used.
- the cellulose acetate fiber was used for the core part of an Example, the sheath part of an Example, and a comparative example.
- the hardness of the core portion and the sheath portion of Sample 1 to Sample 3 and the hardness of Sample 4 to Sample 6 are as shown in FIG.
- a winding paper having an air permeability of 10,000 CORESTA and a weight of 24.0 g / m 2 was wound around the sheath portion of Sample 1 to Sample 6.
- the hardness defined by the following method is meant. First, a 112 mm long cylindrical filter having the same diameter over the entire length is prepared as the measurement filter M.
- the measurement filter M is placed on a table 56 as shown in FIG. 13, and a pressing portion 53 having a diameter of 15 mm is brought into contact with the measurement filter M from above to apply a weight of 300 g and pressurize for 10 seconds (FIG. 13). 13 arrow L direction).
- the distance between the upper surface of the base 56 and the pressing surface of the pressing portion 53 when the pressing portion 53 is brought into contact with the measuring filter without applying a weight of 300 g is defined as h1 (mm).
- the hardness of the sheath part is measured using a measurement filter M (winding paper, core part and sheath and filter having a core part, a sheath part and a winding paper).
- the boundary line between the core portions is not shown), and the hardness of the core portion is measured with a filter for the core portion as the measurement filter M.
- the test method is a hollow filter 11 of sample 1 to sample 3 having a diameter of about 7.6 mm, a core diameter of about 5.0 mm, and a length of about 84 mm (the web 30 is omitted in the figure).
- the hollow filter 11 was pressurized until the distance between the two metal plates 52 became 6.0 mm.
- the shape of the through hole before, during and after pressurization (immediately after pressurization) was photographed and the distortion factor of the pore diameter was measured. Specifically, of the horizontal and vertical diameters in the cross-section of the through-hole, the longer major axis is A, and the shorter minor axis is B, and the distortion rate (A / B) is calculated. These average values were also calculated for each sample. When the distortion rate is smaller, the shape of the through hole is held against the external pressure. Note that the pressure test was performed in the same manner on Samples 4 to 6 as filters of the comparative example.
- the average values of the samples of the example and the comparative example were the same at a distortion rate of 1.02 before pressurization.
- the average value of the example was 1.22
- the average value of the comparative example was 2.07
- the through hole shape was maintained in the example.
- the average value of the example was 1.03
- the average value of the comparative example was 1.29
- the through hole shape was maintained in the example.
- FIG. 16 is a graph showing this, and it can be seen that the strain rate is lower in the example both during and after pressurization.
Landscapes
- Cigarettes, Filters, And Manufacturing Of Filters (AREA)
Abstract
A method for producing a filter cigarette comprises: a core fiber processing step of adding a plasticizer to a core fiber (4) having a total fineness of 23000 to 70000 deniers so that the addition rate becomes 13 to 40%; a sheath fiber processing step of adding a plasticizer to a sheath fiber (5) having a total fineness of 10000 to 47000 deniers so that the addition rate becomes 15% or less, or adding no plasticizer to the sheath fiber (5) so that the addition rate becomes 0%; subsequent to the core fiber processing step and the sheath fiber processing step, a hollow filter formation step of hardening the core fiber (4) to form a core part (11a) having, formed therein, a pore part (10) that extends from one end surface of the core fiber (4) toward the other end surface of the core fiber (4), and then covering the outside of the core part (11a) with the sheath fiber (5) to form a hollow filter (11) as a sheath part (11b); subsequent to the hollow filter formation step, a post-treatment step of conveying the hollow filter (11) while allowing the hollow filter (11) to pass through a narrow part that is narrower than the diameter of the hollow filter (11) and is larger than the diameter of the core part (11a).
Description
本発明は、フィルタシガレット製造方法並びにフィルタ及びフィルタシガレットに関する。
The present invention relates to a filter cigarette manufacturing method, a filter, and a filter cigarette.
軸線方向に貫通孔が形成された中空フィルタを製造するフィルタ製造機が知られている(例えば特許文献1参照)。このような貫通孔が形成されたフィルタは、通常のフィルタと比較してセルロースアセテートトウの重量が重く、さらにセルロースアセテートトウに添加する可塑剤の割合が高い。これにより、フィルタに十分な硬さを与え、貫通孔の形状を保持している。
2. Description of the Related Art A filter manufacturing machine that manufactures a hollow filter having a through hole formed in the axial direction is known (see, for example, Patent Document 1). A filter in which such through-holes are formed has a heavier weight of cellulose acetate tow than a normal filter, and further has a high proportion of plasticizer added to cellulose acetate tow. Thereby, sufficient hardness is given to the filter and the shape of the through hole is maintained.
しかしながら、製造された中空フィルタは後工程、例えばシガレットと接続するためにチップペーパを巻き付ける工程などにおいて、製造の都合上、フィルタ直径よりも狭い通路を押し潰されながら搬送される必要がある。そして、このとき、フィルタ端部の貫通孔形状が変化することがある。特にチップペーパを巻き付けるためのフィルタ装着装置では、通路に確実にフィルタを送ることを目的として回転のきっかけを与えるため、通路に向けて突出する凸部が備わっている。装置の製造能力が向上してフィルタの搬送速度が速くなると、フィルタが凸部部分を通過する際に上記貫通孔形状の変化の問題が顕著になる。
However, the manufactured hollow filter needs to be conveyed while being crushed in a passage narrower than the diameter of the filter in the subsequent process, for example, the process of winding the chip paper to connect with the cigarette. At this time, the shape of the through hole at the end of the filter may change. In particular, the filter mounting device for winding the chip paper is provided with a convex portion protruding toward the passage in order to give a trigger of rotation for the purpose of reliably sending the filter to the passage. When the manufacturing capability of the apparatus is improved and the conveying speed of the filter is increased, the problem of the change in the shape of the through hole becomes significant when the filter passes through the convex portion.
本発明は、上記課題を考慮してなされたものであり、中空フィルタを用いてフィルタシガレットを製造する後工程で中空フィルタが潰されても貫通孔形状変化を低減させることができるフィルタシガレット製造方法並びにフィルタ及びフィルタシガレットを提供することを目的とする。
The present invention has been made in consideration of the above-mentioned problems, and a filter cigarette manufacturing method capable of reducing a through-hole shape change even when the hollow filter is crushed in a subsequent process of manufacturing a filter cigarette using a hollow filter. An object of the present invention is to provide a filter and a filter cigarette.
前記目的を達成するため、本発明では、総繊度23000デニール~70000デニールのコア繊維に可塑剤を添加して添加率13%~40%とするコア繊維加工工程と、総繊度10000デニール~47000デニールのシース繊維に可塑剤を添加して添加率を15%以下とする、もしくは可塑剤を添加しないで添加率を0%とするシース繊維加工工程と、前記コア繊維加工工程と前記シース繊維加工工程との後に、前記コア繊維を硬化させて一方の端面から他方の端面に向かって延びる孔部が形成されたコア部とし、該コア部の外側を前記シース繊維で覆ってシース部として中空フィルタを形成する中空フィルタ形成工程と、前記中空フィルタ形成工程の後に、前記中空フィルタを前記中空フィルタの直径よりも狭く、前記コア部の直径よりも大きい狭小部を通過させて搬送する、後工程を含むフィルタシガレット製造方法を提供する。
In order to achieve the above object, in the present invention, a core fiber processing step in which a plasticizer is added to a core fiber having a total fineness of 23,000 denier to 70000 denier to an addition rate of 13% to 40%, and a total fineness of 10,000 denier to 47,000 denier. A sheath fiber processing step in which a plasticizer is added to the sheath fiber to reduce the addition rate to 15% or less, or the addition rate is 0% without adding a plasticizer, the core fiber processing step, and the sheath fiber processing step After that, the core fiber is cured to form a core portion having a hole extending from one end surface toward the other end surface, and the outer portion of the core portion is covered with the sheath fiber to form a hollow filter as a sheath portion. After the hollow filter forming step to be formed and the hollow filter forming step, the hollow filter is narrower than the diameter of the hollow filter and is equal to the diameter of the core part. Conveyed by passing also large narrow portion, to provide a filter cigarette manufacturing method comprising the subsequent step.
なお、本明細書における可塑剤の添加率(%)は、(可塑剤重量/トウ(繊維)重量)×100、の計算式で規定される。
また、デニール(g/9000m)×0.1111=テクス(g/1000m)となる。 In the present specification, the plasticizer addition rate (%) is defined by a calculation formula of (plasticizer weight / tow (fiber) weight) × 100.
Denier (g / 9000 m) × 0.1111 = tex (g / 1000 m).
また、デニール(g/9000m)×0.1111=テクス(g/1000m)となる。 In the present specification, the plasticizer addition rate (%) is defined by a calculation formula of (plasticizer weight / tow (fiber) weight) × 100.
Denier (g / 9000 m) × 0.1111 = tex (g / 1000 m).
好ましくは、前記コア繊維に対する前記可塑剤の添加率は13%~35%であり、前記シース繊維に対する前記可塑剤の添加率は略3%~12%である。
Preferably, the addition rate of the plasticizer to the core fiber is 13% to 35%, and the addition rate of the plasticizer to the sheath fiber is about 3% to 12%.
好ましくは、前記後工程は、前記中空フィルタ及びシガレットが転動する転動通路に導入される際に前記中空フィルタ及び前記シガレットを転動させるきっかけを与えるために前記転動通路の内側に向けて突出する凸部が形成された狭小部を通過させ、前記転動通路にて前記中空フィルタ及び前記シガレットにチップペーパを巻き付けて前記中空フィルタと前記シガレットとを接続するフィルタ装着工程である。
Preferably, the post-process is directed toward the inside of the rolling passage in order to provide an opportunity to roll the hollow filter and the cigarette when the hollow filter and the cigarette are introduced into the rolling passage. A filter mounting step of connecting the hollow filter and the cigarette by passing a narrow portion formed with a projecting convex portion, winding a tip paper around the hollow filter and the cigarette in the rolling passage.
また、本発明では、一方の端面から他方の端面に向かって延びる孔部が形成された筒形状の中空フィルタと、該中空フィルタに対して長手方向に連続して接続された吸着フィルタとを備え、前記中空フィルタは、一方の端面から他方の端面に向かって延びる孔部が形成されたコア部と該コア部の外側を覆うシース部とを有し、該コア部と該シース部との間には境界線が存在し、前記コア部は、総繊度が23000デニール~70000デニールであり、可塑剤添加率が13%~40%であり、前記シース部は、総繊度が10000デニール~47000であり、可塑剤添加率が0%~15%であるフィルタを提供する。
The present invention also includes a cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed, and an adsorption filter continuously connected to the hollow filter in the longitudinal direction. The hollow filter has a core portion in which a hole extending from one end face toward the other end face is formed, and a sheath portion covering the outside of the core portion, and between the core portion and the sheath portion. The core portion has a total fineness of 23,000 denier to 70000 denier, a plasticizer addition rate of 13% to 40%, and the sheath portion has a total fineness of 10,000 denier to 47,000. There is provided a filter having a plasticizer addition rate of 0% to 15%.
さらに、本発明では、一方の端面から他方の端面に向かって延びる孔部が形成された筒形状の中空フィルタと、該中空フィルタに対して長手方向に連続して接続された吸着フィルタとを備え、前記中空フィルタは、一方の端面から他方の端面に向かって延びる孔部が形成されたコア部と該コア部の外側を覆うシース部とを有し、該コア部と該シース部との間には境界線が存在し、前記コア部は0mm/10以上5mm/10未満の硬度を有し、前記シース部は5mm/10以上10mm/10以下の硬度を有していることを特徴とするフィルタを提供する。
Furthermore, the present invention includes a cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed, and an adsorption filter continuously connected to the hollow filter in the longitudinal direction. The hollow filter has a core portion in which a hole extending from one end face toward the other end face is formed, and a sheath portion covering the outside of the core portion, and between the core portion and the sheath portion. There is a boundary line, the core portion has a hardness of 0 mm / 10 or more and less than 5 mm / 10, and the sheath portion has a hardness of 5 mm / 10 or more and 10 mm / 10 or less. Provide a filter.
好ましくは、前記コア部は、総繊度が23000デニール~70000デニールであり、可塑剤添加率が13%~40%であり、前記シース部は、総繊度が10000デニール~47000デニールであり、可塑剤添加率が0%~15%である。
Preferably, the core portion has a total fineness of 23000 denier to 70000 denier and a plasticizer addition rate of 13% to 40%, and the sheath portion has a total fineness of 10,000 denier to 47000 denier. The addition rate is 0% to 15%.
また、本発明では、前記フィルタと、刻みたばこを巻紙で包み込んだシガレットと、前記フィルタ及び前記シガレットを包み込んで長手方向に接続するチップペーパとを備えたフィルタシガレットを提供する。
Also, the present invention provides a filter cigarette comprising the filter, a cigarette in which chopped cigarettes are wrapped with a wrapping paper, and chip paper that wraps the filter and the cigarettes and connects them in the longitudinal direction.
本発明では、中空フィルタを用いてフィルタシガレットを製造する後工程で中空フィルタが潰されても貫通孔形状変化を低減させることができる。
In the present invention, even if the hollow filter is crushed in a subsequent process of manufacturing a filter cigarette using the hollow filter, the shape change of the through-hole can be reduced.
まずはフィルタ製造に用いるフィルタシガレット製造機1について説明する。図1に示すように、フィルタシガレット製造機1は、コア繊維4及びシース繊維5が図の矢印方向に連続的に繰り出されて走行する第1及び第2の繰り出し経路2、3を有している。図1で繰り出し経路2、3に沿って示す矢印は、コア繊維4及びシース繊維5の走行方向を表している。各繰り出し経路2、3の始端には、例えばセルロースアセテート繊維からなるコア繊維4、シース繊維5がそれぞれ束となってトウベール28として配設されている。各繰り出し経路2、3は、ガイド36やガイドローラ6によって案内されている。第1の繰り出し経路2には第1の開繊及び可塑剤添加装置7が設けられている。この第1の開繊及び可塑剤添加装置7では、公知のバンディングジェット、一対のプレテンションローラ、一対のブルーミングローラ等を用いて第1の繰り出し経路2を走行するコア繊維4を開繊する。そして開繊されたコア繊維4に対して公知の噴射スプレー等を用いて可塑剤を添加する。シース繊維5が走行する第2の繰り出し経路3にも第1の開繊及び可塑剤添加装置7と同様の機能を有する第2の開繊及び可塑剤添加装置8が設けられている。
First, the filter cigarette manufacturing machine 1 used for filter manufacturing will be described. As shown in FIG. 1, the filter cigarette making machine 1 has first and second feeding paths 2 and 3 in which the core fiber 4 and the sheath fiber 5 are continuously drawn out in the direction of the arrow in the figure and travel. Yes. The arrows shown along the feeding paths 2 and 3 in FIG. 1 indicate the traveling directions of the core fiber 4 and the sheath fiber 5. For example, a core fiber 4 and a sheath fiber 5 made of cellulose acetate fiber are bundled at the start ends of the feeding paths 2 and 3, respectively, as a tow bail 28. Each feeding path 2, 3 is guided by a guide 36 or a guide roller 6. The first unwinding path 2 is provided with a first fiber opening and plasticizer addition device 7. In the first fiber opening and plasticizer addition device 7, the core fiber 4 traveling on the first feeding path 2 is opened using a known banding jet, a pair of pretension rollers, a pair of blooming rollers, and the like. Then, a plasticizer is added to the opened core fiber 4 using a known spray spray or the like. A second opening and plasticizer addition device 8 having the same function as the first opening and plasticizer addition device 7 is also provided in the second feeding path 3 along which the sheath fiber 5 travels.
第1及び第2の繰り出し経路2、3は、孔成形装置9に接続されている。孔成形装置9(図2参照)については後述する。孔成形装置9では、長手方向に貫通孔10が形成された中空フィルタ中間体54が製造される。中空フィルタ中間体54は搬送経路12を通って紙巻装置13に送られる。なお、実際には中空フィルタ中間体54は紙巻装置13の入口側に備わるトランペットガイド18を通過して製造されるが、本明細書では便宜上このトランペットガイド18を孔成形装置9の一部として取り扱う。紙巻装置13で中空フィルタ中間体54は巻取紙30(図4参照)で包み込まれ、中空フィルタ11となる(図3参照)。さらに紙巻装置13で中空フィルタ11は切断された後に、煙中の成分を吸着する吸着フィルタ31と長手方向に並んだ状態で、外周全域を成形紙32(図4参照)で包み込まれる。そして成形紙32で包み込まれた中空フィルタ11及び吸着フィルタ31はフィルタ22(図4参照)となり、フィルタ装着装置14に送られ、チップペーパ15を介してシガレット16と接続される。尚、中空フィルタ11は煙中の成分を吸着してもよいし、実質的に煙中の成分を吸着できなくてもよい。
The first and second feeding paths 2 and 3 are connected to the hole forming device 9. The hole forming device 9 (see FIG. 2) will be described later. In the hole forming device 9, the hollow filter intermediate 54 in which the through holes 10 are formed in the longitudinal direction is manufactured. The hollow filter intermediate 54 is sent to the paper winding device 13 through the conveyance path 12. In practice, the hollow filter intermediate body 54 is manufactured by passing through the trumpet guide 18 provided on the inlet side of the paper winding device 13. In this specification, the trumpet guide 18 is handled as a part of the hole forming device 9 for convenience. . In the paper winding device 13, the hollow filter intermediate 54 is wrapped with the web 30 (see FIG. 4) to become the hollow filter 11 (see FIG. 3). Further, after the hollow filter 11 is cut by the paper winding device 13, the entire outer periphery is wrapped with the forming paper 32 (see FIG. 4) in a state of being arranged in the longitudinal direction with the adsorption filter 31 that adsorbs the components in the smoke. Then, the hollow filter 11 and the adsorption filter 31 wrapped with the molding paper 32 become the filter 22 (see FIG. 4), and are sent to the filter mounting device 14 and connected to the cigarette 16 via the chip paper 15. In addition, the hollow filter 11 may adsorb | suck the component in smoke, and does not need to be able to adsorb | suck the component in smoke substantially.
上述したように、中空フィルタ中間体54は孔成形装置9で製造される。図2に示すように、孔成形装置9は、成形管17と、トランペットガイド18と、マンドレル19とを備えている。マンドレル19は、支持台20に一方の端部を支持され、コア繊維4の入口側から成形管17内に延びている。成形管17は中空の筒形状、トランペットガイド18は入口側が拡径した中空の筒形状であり、シース繊維5を絞り込みながらコア繊維4と共に通過させる。
As described above, the hollow filter intermediate 54 is manufactured by the hole forming apparatus 9. As shown in FIG. 2, the hole forming device 9 includes a forming tube 17, a trumpet guide 18, and a mandrel 19. One end of the mandrel 19 is supported by the support base 20 and extends into the forming tube 17 from the inlet side of the core fiber 4. The forming tube 17 has a hollow cylindrical shape, and the trumpet guide 18 has a hollow cylindrical shape with an enlarged diameter on the inlet side, and allows the sheath fiber 5 to pass along with the core fiber 4 while narrowing down.
成形管17には、第1の開繊及び可塑剤添加装置7を通過したコア繊維4が入り込む。コア繊維4は、成形管17とマンドレル19とで協働して形成された通路を通過し、成形管17内にて、熱処理されて長手方向にマンドレル19の外形に沿った貫通孔10を有する中空筒形状のコア部11aとなる。
The core fiber 4 that has passed through the first fiber opening and plasticizer addition device 7 enters the forming tube 17. The core fiber 4 passes through a passage formed by the molding tube 17 and the mandrel 19 in cooperation with each other. The core fiber 4 is heat-treated in the molding tube 17 and has a through hole 10 along the outer shape of the mandrel 19 in the longitudinal direction. It becomes the hollow cylindrical core part 11a.
この熱処理は加熱処理部50にて行われる。加熱処理部50は、成形管17の周壁を貫通する孔51として設けられていて、この孔51を通して蒸気が成形管17内に吹き込まれる。この加熱処理部50により、コア繊維4は成形管17内を通ずる過程にて可塑化が促進されて固められる。なお、蒸気の他、マイクロ波や高温空気、あるいは電熱線等の新たな熱源を利用してもよい。
This heat treatment is performed in the heat treatment unit 50. The heat treatment unit 50 is provided as a hole 51 that penetrates the peripheral wall of the molded tube 17, and steam is blown into the molded tube 17 through the hole 51. By the heat treatment unit 50, the core fiber 4 is plasticized and hardened in the process of passing through the molding tube 17. In addition to steam, a new heat source such as microwave, high-temperature air, or heating wire may be used.
なお、コア繊維4を安定して流入しやすくするために、第1の成形管17の入口側の径は徐々に拡大されている。図2の例では、第1の成形管17の入口側は湾曲している。
In addition, in order to make it easy to flow in the core fiber 4 stably, the diameter of the inlet side of the 1st shaping | molding pipe | tube 17 is expanded gradually. In the example of FIG. 2, the inlet side of the first molded tube 17 is curved.
また、コア繊維4が成形管17に入る手前にて内側から可塑剤を添加してもよい。例えば、支持台20の一部をスプレーノズル化し、このノズルから可塑剤を添加することができる(図2の矢印S)。このような位置から可塑剤を添加することで、可塑剤は貫通孔10の表面となるべき部分に向けて供給されるので、貫通孔10の表面を適切に硬化できる。また、この支持台20からの可塑剤の添加は局所的に行われるので、少量の可塑剤で十分にコア繊維4を硬化することができる。このように貫通孔10の表面を硬化させれば、例えば中空フィルタ11を切断したときに、その切断面で貫通孔10が潰れることを防止できる。
Further, a plasticizer may be added from the inside before the core fiber 4 enters the forming tube 17. For example, a part of the support 20 can be made into a spray nozzle, and a plasticizer can be added from this nozzle (arrow S in FIG. 2). By adding the plasticizer from such a position, the plasticizer is supplied toward the portion to be the surface of the through-hole 10, so that the surface of the through-hole 10 can be appropriately cured. In addition, since the plasticizer is locally added from the support base 20, the core fiber 4 can be sufficiently cured with a small amount of plasticizer. If the surface of the through hole 10 is cured in this way, for example, when the hollow filter 11 is cut, the through hole 10 can be prevented from being crushed by the cut surface.
成形管17の出口側には、成形管17と同一軸線を有するトランペットガイド18が配設されている。成形管17によって形成されたコア部11aはそのまま繰り出されてトランペットガイド18内に流入する。トランペットガイド18には、第2の開繊及び可塑剤添加装置8を通過したシース繊維5が入り込む。シース繊維5は、トランペットガイド18とコア部11aとで協働して形成された通路を通過するため、コア部11aの外側を覆うシース部11bとなる。その後、中空フィルタ中間体54はガニーチャベルト55上で巻取紙30で包み込まれ、中空フィルタ11となる。
なお、コア部11aの外側を覆うシース部11bの状態を見やすくするため図2においてガニーチャベルト55上の巻取紙30は不図示としている。 Atrumpet guide 18 having the same axis as the forming tube 17 is disposed on the outlet side of the forming tube 17. The core portion 11 a formed by the forming tube 17 is drawn out as it is and flows into the trumpet guide 18. The sheath fiber 5 that has passed through the second opening and plasticizer addition device 8 enters the trumpet guide 18. Since the sheath fiber 5 passes through a passage formed by the trumpet guide 18 and the core portion 11a in cooperation, the sheath fiber 5 becomes a sheath portion 11b that covers the outside of the core portion 11a. After that, the hollow filter intermediate 54 is wrapped with the web 30 on the ganiche belt 55 to become the hollow filter 11.
In addition, in order to make it easy to see the state of thesheath portion 11b covering the outside of the core portion 11a, the web 30 on the ganiche belt 55 is not shown in FIG.
なお、コア部11aの外側を覆うシース部11bの状態を見やすくするため図2においてガニーチャベルト55上の巻取紙30は不図示としている。 A
In addition, in order to make it easy to see the state of the
このようにして形成された中空フィルタ11は、図3に示すように、内筒としてコア部11aを、外筒としてシース部11bを有する2層構造となる。このコア部11aとシース部11bとは、中空フィルタ11の横断面にて境界線21を介して明確に分け隔てられている。なお、通常サイズの中空フィルタ11であれば、その直径は7.4mm~8.0mm、コア部11aの直径は4.6mm~5.2mmとすることが出来る。細いタイプのシガレットに用いられる中空フィルタ11であれば、その直径は5.0mm~7.3mm、コア部11aの直径は2.4mm~4.7mmとすることも出来る。また、直径7.4mm~8.0mmの中空フィルタ11のコア部11aの直径を2.4mm~4.7mmとすることも出来る。このような中空フィルタ11は、以下のような製造方法を経て製造される(図5参照)。
As shown in FIG. 3, the hollow filter 11 thus formed has a two-layer structure having a core portion 11a as an inner cylinder and a sheath portion 11b as an outer cylinder. The core portion 11 a and the sheath portion 11 b are clearly separated by a boundary line 21 in the cross section of the hollow filter 11. If the hollow filter 11 has a normal size, the diameter can be 7.4 mm to 8.0 mm, and the diameter of the core portion 11a can be 4.6 mm to 5.2 mm. In the case of the hollow filter 11 used in a thin type cigarette, the diameter may be 5.0 mm to 7.3 mm, and the diameter of the core portion 11a may be 2.4 mm to 4.7 mm. Further, the diameter of the core portion 11a of the hollow filter 11 having a diameter of 7.4 mm to 8.0 mm can be set to 2.4 mm to 4.7 mm. Such a hollow filter 11 is manufactured through the following manufacturing method (see FIG. 5).
まずはコア繊維加工工程が行われる(ステップS1)。コア繊維加工工程は、第1の開繊及び可塑剤添加装置7を用いて行われる。コア繊維4の総繊度を23000デニール~70000デニール(2555.3テクス~7777テクス)とする。繊維はセルロースアセテート繊維などを用いることができる。ここから第1の繰り出し経路2に繰り出されるコア繊維4を開繊し、添加率13%~40%(好ましくは15~35%、最も好ましくは17~30%)として可塑剤を添加する。なお、この可塑剤の添加率は第1の開繊及び可塑剤添加装置による添加と、支持台20からの局所添加の合計によって定まる値である。一方で、シース繊維加工工程が行われる(ステップS2)。シース繊維加工工程は、第2の開繊及び可塑剤添加装置8を用いて行われる。シース繊維5の総繊度を10000デニール~47000デニール(1888.7テクス~2999.7テクス)とする。繊維はセルロースアセテート繊維などを用いることができる。ここから第2の繰り出し経路3に繰り出されるシース繊維5を開繊し、添加率15%以下(好ましくは3~12%、最も好ましくは6~9%)として可塑剤を添加する。または、可塑剤を添加しなくても良い。
First, a core fiber processing step is performed (step S1). The core fiber processing step is performed using the first fiber opening and plasticizer addition device 7. The total fineness of the core fiber 4 is set to 23000 denier to 70000 denier (2555.3 tex to 7777 tex). A cellulose acetate fiber etc. can be used for a fiber. From here, the core fiber 4 fed to the first feeding path 2 is opened, and a plasticizer is added at an addition rate of 13% to 40% (preferably 15 to 35%, most preferably 17 to 30%). The addition rate of the plasticizer is a value determined by the sum of the first fiber opening and the addition by the plasticizer addition device and the local addition from the support base 20. On the other hand, a sheath fiber processing step is performed (step S2). The sheath fiber processing step is performed using the second fiber opening and plasticizer addition device 8. The total fineness of the sheath fiber 5 is set to 10,000 denier to 47,000 denier (1888.7 tex to 2999.7 tex). A cellulose acetate fiber etc. can be used for a fiber. From here, the sheath fiber 5 fed to the second feeding path 3 is opened, and a plasticizer is added at an addition rate of 15% or less (preferably 3 to 12%, most preferably 6 to 9%). Alternatively, a plasticizer may not be added.
そして、中空フィルタ形成工程を行う(ステップS3)。この中空フィルタ形成工程は、孔成形装置9を用いて行われる。孔成形装置9では、上述したように、コア繊維4を長手方向に貫通孔10が形成された筒形状のコア部11aとし、コア部11aの外側をシース繊維5で覆ってシース部11bとし、巻取紙30で包み込むことで中空フィルタ11を形成する。
And a hollow filter formation process is performed (step S3). This hollow filter forming step is performed using the hole forming apparatus 9. In the hole forming device 9, as described above, the core fiber 4 is a cylindrical core portion 11a in which the through hole 10 is formed in the longitudinal direction, and the outside of the core portion 11a is covered with the sheath fiber 5 to form a sheath portion 11b. The hollow filter 11 is formed by wrapping with a web 30.
このような中空フィルタ11には、後工程の一例としてのフィルタ装着工程(ステップS4)が行われるが、まずはこの工程で用いられるフィルタ装着装置14について説明する。すなわち、中空フィルタ11を用いてフィルタシガレット27を製造するには、図6に示すようなフィルタ装着装置14が用いられる。このフィルタ装着装置14では、まず2本のシガレット16間にフィルタプラグ37を配する。このフィルタプラグ37は、両側に吸着フィルタ31が位置づけられている状態でフィルタ22が2本分の長さで形成されている。これによりダブルフィルタシガレット49の中間品25が形成される。この後、片面に接着剤が塗布されたチップペーパ15を中間品25に巻き付けてダブルフィルタシガレット49を形成する。ここで、フィルタ装着装置14は、第1の搬送ドラム38と第2の搬送ドラム23とで形成される搬送経路39を備えている。すなわち、第1の搬送ドラム38が矢印R1方向に、第2の搬送ドラム23が矢印R2方向に回転することで中間品25の搬送経路39が形成される。搬送経路39は、中間品25が搬送される経路である。第1の搬送ドラム38はこの搬送経路39の上流部分を形成し、第2の搬送ドラム23は下流部分を形成している。
Such a hollow filter 11 is subjected to a filter mounting step (step S4) as an example of a post-process. First, the filter mounting device 14 used in this step will be described. That is, in order to manufacture the filter cigarette 27 using the hollow filter 11, a filter mounting device 14 as shown in FIG. 6 is used. In this filter mounting device 14, a filter plug 37 is first disposed between two cigarettes 16. This filter plug 37 is formed with a length of two filters 22 with the adsorption filter 31 positioned on both sides. Thereby, the intermediate product 25 of the double filter cigarette 49 is formed. Thereafter, the chip paper 15 having an adhesive applied on one side is wound around the intermediate product 25 to form a double filter cigarette 49. Here, the filter mounting device 14 includes a transport path 39 formed by the first transport drum 38 and the second transport drum 23. That is, the transport path 39 for the intermediate product 25 is formed by the first transport drum 38 rotating in the direction of arrow R1 and the second transport drum 23 rotating in the direction of arrow R2. The conveyance path 39 is a path along which the intermediate product 25 is conveyed. The first transport drum 38 forms an upstream portion of the transport path 39, and the second transport drum 23 forms a downstream portion.
第1の搬送ドラム38はスワッシュプレートドラムとも称されている。また、第2の搬送ドラム23はローリングドラムとも称されている。第1の搬送ドラム38も第2の搬送ドラム23も、外周に中間品25の一部を収容しながら吸着する吸着溝(不図示)を周方向に複数有している。中間品25は、この吸着溝に一つずつ収容されて第1の搬送ドラム38及び第2の搬送ドラム23の周方向に搬送される。
The first transport drum 38 is also called a swash plate drum. The second transport drum 23 is also called a rolling drum. Both the first conveyance drum 38 and the second conveyance drum 23 have a plurality of adsorption grooves (not shown) that adsorb while accommodating a part of the intermediate product 25 on the outer periphery. The intermediate products 25 are accommodated one by one in the suction grooves and conveyed in the circumferential direction of the first conveyance drum 38 and the second conveyance drum 23.
一方で、第1の搬送ドラム38と隣接して矢印R3方向に回転する供給ドラム40が配設されている。この供給ドラム40からはチップペーパ15が巻き出され、このチップペーパ15の一側縁は第1の搬送ドラム38に沿って搬送されている中間品25に貼り付けられる。第2の搬送ドラム23には、その周方向に沿ってガイド部材24が隣接して配設されている。ガイド部材24は、第2の搬送ドラム23と協働して中間品25を転動させ、チップペーパ15を中間品25に巻き付ける。
On the other hand, a supply drum 40 that rotates in the direction of arrow R3 is disposed adjacent to the first transport drum 38. The chip paper 15 is unwound from the supply drum 40, and one side edge of the chip paper 15 is affixed to the intermediate product 25 that is transported along the first transport drum 38. A guide member 24 is disposed adjacent to the second transport drum 23 along the circumferential direction thereof. The guide member 24 rolls the intermediate product 25 in cooperation with the second transport drum 23 and winds the chip paper 15 around the intermediate product 25.
以上のような構造を有するフィルタ装着装置14を用いて実際に中間品25にチップペーパ15を巻き付ける後工程の一例としてのフィルタ装着工程(ステップS4)を順番に説明する。公知の手段で製造されたシガレット2本分の長さを有するダブルシガレットDSは、これを搬送する過程にて2本のシガレット16に切断される(図6の矢印F1)。この後、これら2本のシガレット16が軸方向に離間されてシガレット列が形成される(図6の矢印F2)。そして、シガレット列は第1の搬送ドラム38に供給される(図6の矢印F3)。
The filter mounting process (step S4) as an example of a post-process for actually winding the chip paper 15 around the intermediate product 25 using the filter mounting apparatus 14 having the above structure will be described in order. The double cigarette DS having a length corresponding to two cigarettes manufactured by a known means is cut into two cigarettes 16 in the process of transporting the cigarette DS (arrow F1 in FIG. 6). Thereafter, these two cigarettes 16 are separated in the axial direction to form a cigarette row (arrow F2 in FIG. 6). Then, the cigarette row is supplied to the first transport drum 38 (arrow F3 in FIG. 6).
一方、上述したフィルタプラグ37は搬送方向にグレーディング処理を経て1列に整列され、この後、矢印R4方向に回転する加速ドラム41を通じて第1の搬送ドラム(スワッシュプレートドラム)38に供給される。
On the other hand, the above-described filter plugs 37 are aligned in a row through a grading process in the transport direction, and then supplied to a first transport drum (swash plate drum) 38 through an acceleration drum 41 that rotates in the direction of arrow R4.
上述したシガレット列は、各シガレット16の間にフィルタプラグ37を受け入れ可能な間隔を存しており、この間隔を保持したまま第1の搬送ドラム38に供給される。そしてシガレット列が第1の搬送ドラム38に供給されると、フィルタプラグ37と同一の軸線上に並ぶ。第1の搬送ドラム38は両側に一対のフローティングディスク(不図示)を備えていて、第1の搬送ドラム38の回転に伴い、各シガレット16は両側のフローティングディスクに挟み込まれ、軸方向にその間隔を詰められる。これにより、2本のシガレット16の間にフィルタプラグ37を位置付けたダブルフィルタシガレットの中間品25が形成される。
The above-described cigarette row has an interval in which the filter plug 37 can be received between the cigarettes 16 and is supplied to the first transport drum 38 while maintaining this interval. When the cigarette row is supplied to the first transport drum 38, it is aligned on the same axis as the filter plug 37. The first transport drum 38 is provided with a pair of floating disks (not shown) on both sides. As the first transport drum 38 rotates, each cigarette 16 is sandwiched between the floating disks on both sides, and the distance between them in the axial direction. Packed. Thereby, the intermediate product 25 of the double filter cigarette in which the filter plug 37 is positioned between the two cigarettes 16 is formed.
一方で、図示しないチップペーパのロールからはチップペーパのウエブWが繰り出されている(図6の矢印E方向)。このウエブWは供給ドラム(コークドラム)40まで導かれる。ウエブWは供給ドラム40の手前でその片面に接着剤(糊)を塗布される。具体的には、供給ドラム40の手前の位置に接着剤ローラ42が配されていて、この接着剤ローラ42は下半分を接着剤液43に浸された状態で回転する。接着剤ローラ42の上方にはトランスミッションローラ44が隣接して配置されていて、接着剤ローラ42の外周面に付着した接着剤はトランスミッションローラ44の外周面に所定の層厚で移し替えられる。トランスミッションローラ44はウエブWの通過に伴いその片面に転接し、所定の塗布パターンにしたがって接着剤を塗布する。
On the other hand, a tip paper web W is fed out from a tip paper roll (not shown) (in the direction of arrow E in FIG. 6). The web W is guided to a supply drum (coke drum) 40. An adhesive (glue) is applied to one side of the web W before the supply drum 40. Specifically, an adhesive roller 42 is disposed at a position in front of the supply drum 40, and the adhesive roller 42 rotates with its lower half immersed in the adhesive liquid 43. A transmission roller 44 is disposed adjacently above the adhesive roller 42, and the adhesive adhering to the outer peripheral surface of the adhesive roller 42 is transferred to the outer peripheral surface of the transmission roller 44 with a predetermined layer thickness. As the web W passes, the transmission roller 44 rolls on one side and applies an adhesive according to a predetermined application pattern.
供給ドラム40はその外周に吸引面を有していて、この吸引面にウエブWを保持して回転する。供給ドラム40に近接して刃付きドラム45が配されている。この刃付きドラム45は外周に多数のコークナイフ(不図示)を有している。これらコークナイフは一定の間隔を存して配置され、刃付きドラム45の回転に伴い供給ドラム40に同期して回転する。これら回転するコークナイフにより、供給ドラム40の吸引面上にてウエブWはチップペーパ15に切断される。
The supply drum 40 has a suction surface on its outer periphery, and rotates while holding the web W on this suction surface. A bladed drum 45 is disposed adjacent to the supply drum 40. The bladed drum 45 has a number of coke knives (not shown) on its outer periphery. These coke knives are arranged at regular intervals, and rotate in synchronization with the supply drum 40 as the bladed drum 45 rotates. The web W is cut into chip paper 15 on the suction surface of the supply drum 40 by these rotating coke knives.
チップペーパ15はそのまま供給ドラム40に吸引保持されながら回転し、第1の搬送ドラム38上の中間品25に供給される。なお供給ドラム40と第1の搬送ドラム38との間は貼り付け通路46として形成されている。チップペーパ15はその先頭部分から中間品25の外面に貼り付き、中間品25とともに第1の搬送ドラム38上を搬送される。チップペーパ15が貼り付けられた状態で、中間品25は第1の搬送ドラム38から第2の搬送ドラム(ローリングドラム)23に受け渡される。なお、第1の搬送ドラム38と第2の搬送ドラム23との間は受け渡し通路47として形成されている。中間品25は第2の搬送ドラム23の回転に伴いガイド部材24との間に搬送される。
The chip paper 15 rotates while being sucked and held by the supply drum 40 and is supplied to the intermediate product 25 on the first transport drum 38. A gap between the supply drum 40 and the first transport drum 38 is formed as a pasting passage 46. The chip paper 15 is attached to the outer surface of the intermediate product 25 from the leading portion thereof, and is conveyed on the first conveyance drum 38 together with the intermediate product 25. The intermediate product 25 is transferred from the first transport drum 38 to the second transport drum (rolling drum) 23 with the chip paper 15 attached. A transfer passage 47 is formed between the first transfer drum 38 and the second transfer drum 23. The intermediate product 25 is transported between the guide member 24 as the second transport drum 23 rotates.
ガイド部材24は第2の搬送ドラム23の回転方向に沿って延びている。なお第2の搬送ドラム23の外周とガイド部材24との間に中間品25の転動通路26が形成されていて、転動通路26は第2の搬送ドラム23の外周に沿って湾曲している。この転動通路26を通過することで、中間品25にはチップペーパ15が巻き付けられ、ダブルフィルタシガレット49が製造される。そして、ダブルフィルタシガレット49を中空フィルタ11の箇所で切断することで口端部側の端面に中空フィルタ11が位置づけられたフィルタシガレット27が製造される。
The guide member 24 extends along the rotation direction of the second transport drum 23. A rolling passage 26 of the intermediate product 25 is formed between the outer periphery of the second transport drum 23 and the guide member 24, and the rolling passage 26 is curved along the outer periphery of the second transport drum 23. Yes. By passing through the rolling passage 26, the chip paper 15 is wound around the intermediate product 25, and the double filter cigarette 49 is manufactured. Then, the filter cigarette 27 in which the hollow filter 11 is positioned on the end surface on the mouth end side is manufactured by cutting the double filter cigarette 49 at the location of the hollow filter 11.
ここで、搬送経路39には、中間品25の一部として搬送されるフィルタプラグ37、すなわち中空フィルタ11の直径よりも狭く、コア部11aの直径よりも大きい幅の狭小部48(例えば貼り付け通路46、受け渡し通路47、転動通路26)が存在する。例えば貼り付け通路46ではチップペーパー15を多少中間品25を径方向に圧縮して貼り付ける必要があるし、ドラム38、23はエア吸引で中間品25を吸着しているので受け渡し通路47ではある程度中間品25を径方向に圧縮してエア漏れを起こさずに中間品25の受け渡しを確実にする必要がある。また、転動通路26ではある程度中間品25を径方向に圧縮しながら転動させてチップペーパ15を確実に巻き付ける必要がある。このように何かしらの目的によって搬送経路39には狭小部48が必要となる。
Here, a narrow portion 48 (for example, affixed to the conveyance path 39) is narrower than the diameter of the filter plug 37, that is, the hollow filter 11, which is conveyed as a part of the intermediate product 25, and larger than the diameter of the core portion 11a. There are passages 46, delivery passages 47, rolling passages 26). For example, in the affixing passage 46, the chip paper 15 needs to be a little compressed in the radial direction and affixed, and the drums 38 and 23 adsorb the intermediate product 25 by air suction. It is necessary to ensure the delivery of the intermediate product 25 without causing air leakage by compressing the intermediate product 25 in the radial direction. Further, in the rolling passage 26, it is necessary to roll the tip paper 15 securely by rolling the intermediate product 25 while compressing the intermediate product 25 in a radial direction to some extent. As described above, the narrow portion 48 is required in the transport path 39 for some purpose.
また、ガイド部材24の搬送方向入口側には、中間品25に転動のきっかけを与えるための凸部29が転動通路26側に突出して設けられている。転動通路26を通過することで中間品25のチップペーパ15は巻き付けられ、中空フィルタ11を用いたダブルフィルタシガレット49が製造される。
Also, on the entrance side of the guide member 24 in the conveyance direction, a convex portion 29 is provided so as to project the rolling of the intermediate product 25 to the rolling passage 26 side. By passing through the rolling passage 26, the chip paper 15 of the intermediate product 25 is wound, and a double filter cigarette 49 using the hollow filter 11 is manufactured.
中空フィルタ11を用いたフィルタシガレット27は、図4に示すように、フィルタ22を有し、フィルタ22の吸い口端部側に中空フィルタ11を用いている。中空フィルタ11の長手方向には連続して吸着フィルタ31が接続されている。これら中空フィルタ11、吸着フィルタ31はそれぞれ巻取紙30で包み込まれている。そして中空フィルタ11と吸着フィルタ31とは、ともに成形紙32で包み込まれて一体とされている。シガレット16は刻みたばこ33を巻紙34で包み込んで形成されている。そして上述したように、フィルタ22とシガレット16とはチップペーパ15を介して接続され、一体とされている。
As shown in FIG. 4, the filter cigarette 27 using the hollow filter 11 has a filter 22, and the hollow filter 11 is used on the mouth end side of the filter 22. An adsorption filter 31 is continuously connected in the longitudinal direction of the hollow filter 11. The hollow filter 11 and the adsorption filter 31 are each wrapped in a web 30. The hollow filter 11 and the adsorption filter 31 are both integrated with a molding paper 32. The cigarette 16 is formed by wrapping a cigarette 33 with a wrapping paper 34. As described above, the filter 22 and the cigarette 16 are connected via the chip paper 15 and integrated.
フィルタシガレット27は、コア部11aが0mm/10~5mm/10、シース部11bが5mm/10~10mm/10の硬度を有している。すなわち、コア部11aは硬度が高く、シース部11bは硬度が低い。そして、コア部11aの直径は、狭小部の幅より小さい。具体的な一例として、後工程はフィルタ装着装置14を用いたフィルタ装着工程である。特に上述した転動通路26の導入部にある凸部29が設けられた部分は通路幅が狭いが、コア部11aの直径はこの凸部29が設けられた部分の搬送通路の幅よりも小さい。
In the filter cigarette 27, the core portion 11a has a hardness of 0 mm / 10 to 5 mm / 10, and the sheath portion 11b has a hardness of 5 mm / 10 to 10 mm / 10. That is, the core portion 11a has a high hardness, and the sheath portion 11b has a low hardness. And the diameter of the core part 11a is smaller than the width | variety of a narrow part. As a specific example, the post-process is a filter mounting process using the filter mounting device 14. In particular, the portion provided with the convex portion 29 in the introduction portion of the rolling passage 26 described above has a narrow passage width, but the diameter of the core portion 11a is smaller than the width of the conveyance passage in the portion where the convex portion 29 is provided. .
このように、コア部11aとシース部11bとは総繊度と可塑剤の添加率を異ならせてコア部11aを固く、シース部11bを柔らかく設定しているので、上述したような狭小部48を通過時にシース部11bが押し潰されてもシース部11bが外圧を吸収し、コア部11aにかかる圧力が低減される。したがって貫通孔10の形状変化を低減させることができる。また、少なくともコア部11aの直径が狭小部48の幅より小さいため、直接的に貫通孔10が押し潰されることはない。例えば、図7に示すように、中間品25すなわち中空フィルタ11の径よりも幅が狭い転動通路26(狭小部48)を中空フィルタ11が通過する際、シース部11bは直接押し潰されているがコア部11aは直接押し潰されない。
As described above, the core portion 11a and the sheath portion 11b are set so that the core portion 11a is hardened and the sheath portion 11b is softened by changing the total fineness and the addition rate of the plasticizer. Even if the sheath portion 11b is crushed during passage, the sheath portion 11b absorbs external pressure, and the pressure applied to the core portion 11a is reduced. Therefore, the shape change of the through hole 10 can be reduced. Further, since at least the diameter of the core portion 11a is smaller than the width of the narrow portion 48, the through hole 10 is not directly crushed. For example, as shown in FIG. 7, when the hollow filter 11 passes through the intermediate product 25, that is, the rolling passage 26 (narrow portion 48) whose width is narrower than the diameter of the hollow filter 11, the sheath portion 11 b is directly crushed. However, the core portion 11a is not directly crushed.
この効果は、特にフィルタ装着装置14の転動通路26の導入部に設けられた凸部29を通過する際に有用である。この部分は中空フィルタ11の直径よりも狭い狭小部48の中でも特に幅が狭い部分だからである。また、コア部11aとシース部11bとは中空フィルタ11の断面視で明確に境界線21を介して分かれている。従って、コア繊維4とシース繊維5とが混在し、コア繊維4とシース繊維5との比率が中空フィルタ11の径方向によって段階的に変化するようないわゆるグラデーション層があることに比べ、境界線21で外部からの圧力を遮断し効果的にコア部11aを外圧から保護可能であり、同一品質のフィルタを製造しやすくなる。
This effect is particularly useful when passing through the convex portion 29 provided in the introduction portion of the rolling passage 26 of the filter mounting device 14. This is because this portion is particularly narrow in the narrow portion 48 narrower than the diameter of the hollow filter 11. Further, the core portion 11 a and the sheath portion 11 b are clearly separated via a boundary line 21 in a cross-sectional view of the hollow filter 11. Therefore, compared with the so-called gradation layer in which the core fiber 4 and the sheath fiber 5 are mixed and the ratio of the core fiber 4 and the sheath fiber 5 changes stepwise depending on the radial direction of the hollow filter 11, The pressure from the outside can be cut off at 21 to effectively protect the core portion 11a from the external pressure, and it becomes easy to manufacture a filter of the same quality.
コア部11aに添加する可塑剤が多すぎると可塑剤の臭いが強くなる。また、可塑剤が少なすぎるとしっかりと成形されにくくなり、貫通孔の表面が毛羽立ちやすくなり、貫通孔の形状が維持しにくくなる。また、総繊度が少なすぎるとコア部11aとしたときに孔等の欠陥要因が発生しやすくなる。また、総繊度が多すぎると第1の成形管17に挿入しにくくなり、可塑剤を均一に添加し難くなる。なお、可塑剤添加率や総繊度の値が大きくなるとコア部11aは硬くなり、可塑剤添加率や総繊度の値が少なくなるとコア部11aは柔らかくなる。そして、コア部11aは、柔らかすぎると毛羽立ちが起こってしまい、貫通孔の形状が維持しにくくなる。これらの事柄を考慮すると、コア部11aを形成するためのコア繊維4は総繊度23000デニール~70000デニールとするのが好ましく、26000デニール~60000デニールとするのがさらに好ましく、30000デニール~50000デニールとするのが最も好ましい。また、コア繊維4の可塑剤添加率は13%~40%とするのが好ましく、15%~35%とするのがさらに好ましく、17%~30%とするのが最も好ましい。そして、この様な総繊度と可塑剤添加率によってコア部11aの硬度を0mm/10以上5mm/10未満とするのが好ましい。
If there is too much plasticizer added to the core part 11a, the odor of the plasticizer becomes strong. Moreover, when there are too few plasticizers, it will become difficult to shape | mold firmly, the surface of a through-hole will become fuzzy easily, and it will become difficult to maintain the shape of a through-hole. If the total fineness is too small, a defect factor such as a hole is likely to occur when the core portion 11a is formed. Moreover, when there is too much total fineness, it will become difficult to insert in the 1st shaping | molding pipe | tube 17, and it will become difficult to add a plasticizer uniformly. The core portion 11a becomes hard when the plasticizer addition rate and the total fineness value are increased, and the core portion 11a is soft when the plasticizer addition rate and the total fineness value are decreased. And if the core part 11a is too soft, fluff will occur and it will become difficult to maintain the shape of a through-hole. Considering these matters, the core fiber 4 for forming the core portion 11a preferably has a total fineness of 23,000 denier to 70000 denier, more preferably 26000 denier to 60000 denier, and 30000 denier to 50000 denier. Most preferably. The plasticizer addition rate of the core fiber 4 is preferably 13% to 40%, more preferably 15% to 35%, and most preferably 17% to 30%. And it is preferable that the hardness of the core part 11a shall be 0 mm / 10 or more and less than 5 mm / 10 by such a total fineness and a plasticizer addition rate.
一方で、シース繊維11bは、可塑剤が多すぎると可塑剤の臭いが強くなる。また、総繊度が少なすぎるとシース繊維11bとしたときに中空フィルタ11の円周が所望の値よりも細くなりやすく。また、総繊度が多すぎると中空フィルタ11の円周が所望の値よりも太くなりやすい。なお、可塑剤添加率や総繊度の値が大きくなるとコア部11aは硬くなり、可塑剤添加率や総繊度の値が少なくなるとコア部11aは柔らかくなる。そして、シース繊維11bは、柔らかすぎるとコア部の位置を所望の位置に維持することが難しくなり、カット面が毛羽立ちやすくなる。また、硬すぎると幅の狭い搬送通路を通過時に外圧を吸収しきれなくなり、また、フィルタ22としたときに表面が硬すぎてくわえ心地が悪くなる要因となる。これらの事柄を考慮すると、シース繊維11bを形成するためのコア繊維4は総繊度10000デニール~47000デニールとするのが好ましく、10000デニール~40000デニールとするのがさらに好ましく、12000デニール~30000デニールとするのが最も好ましい。また、シース繊維11bの可塑剤添加率は0%~15%とするのが好ましく、3%~12%とするのがさらに好ましく、6%~9%とするのが最も好ましい。そして、この様な総繊度と可塑剤添加率によってシース繊維11bの硬度を5mm/10以上10mm/10以下とするのが好ましい。
On the other hand, if the sheath fiber 11b has too much plasticizer, the smell of the plasticizer becomes strong. If the total fineness is too small, the circumference of the hollow filter 11 tends to be thinner than a desired value when the sheath fiber 11b is used. If the total fineness is too large, the circumference of the hollow filter 11 tends to be thicker than a desired value. The core portion 11a becomes hard when the plasticizer addition rate and the total fineness value are increased, and the core portion 11a is soft when the plasticizer addition rate and the total fineness value are decreased. And if the sheath fiber 11b is too soft, it becomes difficult to maintain the position of the core part at a desired position, and the cut surface is likely to fluff. On the other hand, if it is too hard, it will not be possible to absorb the external pressure when passing through a narrow conveyance path, and when the filter 22 is used, the surface will be too hard and the comfort will be worsened. Considering these matters, the core fiber 4 for forming the sheath fiber 11b preferably has a total fineness of 10,000 denier to 47,000 denier, more preferably 10,000 denier to 40000 denier, and 12000 denier to 30000 denier. Most preferably. The plasticizer addition rate of the sheath fiber 11b is preferably 0% to 15%, more preferably 3% to 12%, and most preferably 6% to 9%. And it is preferable that the hardness of the sheath fiber 11b shall be 5 mm / 10 or more and 10 mm / 10 or less by such a total fineness and a plasticizer addition rate.
貫通孔10及びコア部11aの断面形状は、図8に示すように、両方ともに円形で中空フィルタ11の軸線に対し同心円である。他の例としては、図9に示すように、貫通孔10の中心が中空フィルタ11の軸線になくてもよい。または、貫通孔10の断面形状が図10に示すように星形であってもよい。また、図示はしないが十字型、ハート型等、種々の形状としてもよい。または、図11に示すように、コア部11aの断面形状が矩形であってもよい。また、図示はしないが三角形等の多角形でもよい。一方で、図3の例ではコア部11aに設ける孔部として貫通孔10を設けた例について説明したが、コア部11aに設ける孔部は貫通している必要はなく、一方の端面から他方の端面に向かって延びていればよい。例えば、図12に示すように、中空フィルタ11をカット線Cで切断した場合に、中空フィルタ11の一方の端面から他方の端面に向かって途中まで延びる孔部35を形成してもよい。このような孔部35が設けられている中空フィルタ11においても、孔部35の潰れや変形等を防止できる。なお、このような孔部35は孔成形装置9でマンドレル19を挿抜しながらコア繊維4を第1の成形管内に導入すれば形成できる。
The cross-sectional shapes of the through hole 10 and the core portion 11a are both circular and concentric with the axis of the hollow filter 11 as shown in FIG. As another example, as shown in FIG. 9, the center of the through hole 10 may not be on the axis of the hollow filter 11. Alternatively, the cross-sectional shape of the through hole 10 may be a star shape as shown in FIG. Although not shown, various shapes such as a cross shape and a heart shape may be used. Or as shown in FIG. 11, the cross-sectional shape of the core part 11a may be a rectangle. Further, although not shown, a polygon such as a triangle may be used. On the other hand, in the example of FIG. 3, the example in which the through hole 10 is provided as the hole provided in the core part 11 a has been described. However, the hole provided in the core part 11 a does not need to pass through, and from one end surface to the other What is necessary is just to extend toward an end surface. For example, as shown in FIG. 12, when the hollow filter 11 is cut along the cut line C, a hole 35 extending partway from one end surface of the hollow filter 11 toward the other end surface may be formed. Also in the hollow filter 11 provided with such a hole 35, the hole 35 can be prevented from being crushed or deformed. Such a hole 35 can be formed by introducing the core fiber 4 into the first forming tube while inserting and removing the mandrel 19 by the hole forming device 9.
図3に示す中空フィルタ11を実施例とし、従来のようなコア部11a及びシース部11bを有さない貫通孔を設けたフィルタを比較例として加圧試験を行った。実施例の中空フィルタ11はサンプル1~サンプル3の合計3本、比較例のフィルタはサンプル4~サンプル6の合計3本について加圧試験を行った。実施例のサンプル1~3では、コア部の単繊度は4.0デニールとし、総繊度は40000デニールとし、可塑剤の添加率は17%とした。また、シース部の単繊度は8.0デニールとし、総繊度は15000デニールとし、可塑剤の添加率は6%とした。また、比較例のサンプル4~6では、単繊度5.0、総繊度47000デニール、可塑剤添加率19%の繊維のみを用いている。なお、実施例のコア部、実施例のシース部、比較例、にはセルロースアセテート繊維を用いた。サンプル1~サンプル3のコア部、シース部の硬さ、サンプル4~サンプル6の硬さは図15に示す通りである。また、サンプル1~サンプル6のシース部の周りには通気度10000CORESTA、秤量24.0g/m2の巻取紙を巻いた。
The pressurization test was conducted using the hollow filter 11 shown in FIG. 3 as an example and a conventional filter having a through-hole having no core portion 11a and sheath portion 11b as a comparative example. The pressurization test was performed on a total of three samples 1 to 3 for the hollow filter 11 of the example, and a total of three samples 4 to 6 for the filter of the comparative example. In Samples 1 to 3 of the example, the single fineness of the core portion was 4.0 denier, the total fineness was 40000 denier, and the plasticizer addition rate was 17%. The single fineness of the sheath part was 8.0 denier, the total fineness was 15000 denier, and the plasticizer addition rate was 6%. In Comparative Samples 4 to 6, only fibers having a single fineness of 5.0, a total fineness of 47,000 denier, and a plasticizer addition rate of 19% are used. In addition, the cellulose acetate fiber was used for the core part of an Example, the sheath part of an Example, and a comparative example. The hardness of the core portion and the sheath portion of Sample 1 to Sample 3 and the hardness of Sample 4 to Sample 6 are as shown in FIG. Further, a winding paper having an air permeability of 10,000 CORESTA and a weight of 24.0 g / m 2 was wound around the sheath portion of Sample 1 to Sample 6.
また、硬さについては以下の方法によって定義された硬さを意味する。
まず、長さの全域に渡って同程度の直径を有する長さ112mmの円柱形状のフィルタを測定用フィルタMとして用意する。 Moreover, about hardness, the hardness defined by the following method is meant.
First, a 112 mm long cylindrical filter having the same diameter over the entire length is prepared as the measurement filter M.
まず、長さの全域に渡って同程度の直径を有する長さ112mmの円柱形状のフィルタを測定用フィルタMとして用意する。 Moreover, about hardness, the hardness defined by the following method is meant.
First, a 112 mm long cylindrical filter having the same diameter over the entire length is prepared as the measurement filter M.
次に測定用フィルタMを図13に示すように台56に置き、測定用フィルタMに対して上から直径15mmの押圧部53を接触させて300gの重さをかけて10秒間加圧する(図13の矢印L方向)。
Next, the measurement filter M is placed on a table 56 as shown in FIG. 13, and a pressing portion 53 having a diameter of 15 mm is brought into contact with the measurement filter M from above to apply a weight of 300 g and pressurize for 10 seconds (FIG. 13). 13 arrow L direction).
そして、300gの重さをかけずに測定用フィルタに対して上から押圧部53を接触させた際の台56上面と押圧部53の押圧面との距離をh1(mm)とし、測定用フィルタを10秒間加圧した際の台56上面と押圧部53の押圧面との距離をh2(mm)とした場合に、硬さ(mm/10)は以下の式で定義される。
硬さ(mm/10)=(h1-h2)×10 The distance between the upper surface of thebase 56 and the pressing surface of the pressing portion 53 when the pressing portion 53 is brought into contact with the measuring filter without applying a weight of 300 g is defined as h1 (mm). The hardness (mm / 10) is defined by the following equation, where h2 (mm) is the distance between the upper surface of the table 56 and the pressing surface of the pressing portion 53 when the pressure is applied for 10 seconds.
Hardness (mm / 10) = (h1-h2) × 10
硬さ(mm/10)=(h1-h2)×10 The distance between the upper surface of the
Hardness (mm / 10) = (h1-h2) × 10
なお、シース部とコア部とを有する中空フィルタの硬さ測定において、シース部の硬さ測定は、コア部とシース部と巻取紙とを有するフィルタを測定用フィルタM(巻取紙と、コア部とシース部との間の境界線、は図示略)とし、コア部の硬さ測定は、コア部のみのフィルタを測定用フィルタMとする。
In the measurement of the hardness of a hollow filter having a sheath part and a core part, the hardness of the sheath part is measured using a measurement filter M (winding paper, core part and sheath and filter having a core part, a sheath part and a winding paper). The boundary line between the core portions is not shown), and the hardness of the core portion is measured with a filter for the core portion as the measurement filter M.
試験方法は、図14に示すように、直径約7.6mm、コア直径約5.0mm、長さ約84mmのサンプル1~サンプル3の中空フィルタ11(図では巻取紙30は省略している。)を2つの金属の板52に挟み、2つの金属の板52の間の距離が6.0mmになるまで中空フィルタ11を加圧した。そのときの加圧前、加圧中、加圧後(加圧直後)の貫通孔の形状を撮影し、孔径の歪率を測定した。具体的には、貫通孔の断面における水平方向及び垂直方向の径のうち、長い方である長径をA、短い方である短径をBとし、歪率(A/B)を算出した。各サンプルにおいてこれらの平均値も算出した。歪率が少ない方が外圧に対して貫通孔形状が保持されていることになる。なお、比較例のフィルタであるサンプル4~サンプル6も同様にして加圧試験を行った。
As shown in FIG. 14, the test method is a hollow filter 11 of sample 1 to sample 3 having a diameter of about 7.6 mm, a core diameter of about 5.0 mm, and a length of about 84 mm (the web 30 is omitted in the figure). The hollow filter 11 was pressurized until the distance between the two metal plates 52 became 6.0 mm. The shape of the through hole before, during and after pressurization (immediately after pressurization) was photographed and the distortion factor of the pore diameter was measured. Specifically, of the horizontal and vertical diameters in the cross-section of the through-hole, the longer major axis is A, and the shorter minor axis is B, and the distortion rate (A / B) is calculated. These average values were also calculated for each sample. When the distortion rate is smaller, the shape of the through hole is held against the external pressure. Note that the pressure test was performed in the same manner on Samples 4 to 6 as filters of the comparative example.
その結果は、図15に示すように、加圧前は実施例及び比較例の各サンプルの平均値はともに歪率1.02で同じであった。加圧中の歪率は実施例の平均値が1.22であり、比較例の平均値が2.07であり、実施例のほうが貫通孔形状が保持されていた。加圧直後の歪率は実施例の平均値が1.03であり、比較例の平均値が1.29であり、やはり実施例のほうが貫通孔形状が保持されていた。これをグラフにしたものが図16であり、歪率は、加圧中及び加圧後においていずれも実施例のほうが低い値を取っていることがわかる。
As a result, as shown in FIG. 15, the average values of the samples of the example and the comparative example were the same at a distortion rate of 1.02 before pressurization. As for the distortion during pressurization, the average value of the example was 1.22, the average value of the comparative example was 2.07, and the through hole shape was maintained in the example. As for the distortion immediately after pressurization, the average value of the example was 1.03, the average value of the comparative example was 1.29, and the through hole shape was maintained in the example. FIG. 16 is a graph showing this, and it can be seen that the strain rate is lower in the example both during and after pressurization.
1:フィルタシガレット製造機、2:第1の繰り出し経路、3:第2の繰り出し経路、4:コア繊維、5:シース繊維、6:ガイドローラ、7:第1の開繊及び可塑剤添加装置、8:第2の開繊及び可塑剤添加装置、9:孔成形装置、10:貫通孔、11:中空フィルタ、11a:コア部、11b:シース部、12:搬送経路、13:紙巻装置、14:フィルタ装着装置、15:チップペーパ、16:シガレット、17:成形管、18:トランペットガイド、19:マンドレル、20:支持台、21:境界線、22:フィルタ、23:第2の搬送ドラム、24:ガイド部材、25:中間品、26:転動通路、27:フィルタシガレット、28:トウベール、29:凸部、30:巻取紙、31:吸着フィルタ、32:成形紙、33:刻みたばこ、34:巻紙、35:孔部、36:ガイド、37:フィルタプラグ、38:第1の搬送ドラム、39:搬送経路、40:供給ドラム、41:加速ドラム、42:接着剤ローラ、43:接着剤液、44:トランスミッションローラ、45:刃付きドラム、46:貼り付け通路、47:受け渡し通路、48:狭小部、49:ダブルフィルタシガレット、50:加熱処理部、51:孔、52:板、53:押圧部、54:中空フィルタ中間体、55:ガニーチャベルト、56:台
1: filter cigarette manufacturing machine, 2: first feeding path, 3: second feeding path, 4: core fiber, 5: sheath fiber, 6: guide roller, 7: first opening and plasticizer addition device 8: second fiber opening and plasticizer addition device, 9: hole forming device, 10: through-hole, 11: hollow filter, 11a: core portion, 11b: sheath portion, 12: transport path, 13: paper winding device, 14: Filter mounting device, 15: Tip paper, 16: Cigarette, 17: Molding tube, 18: Trumpet guide, 19: Mandrel, 20: Support base, 21: Boundary line, 22: Filter, 23: Second transport drum , 24: guide member, 25: intermediate product, 26: rolling passage, 27: filter cigarette, 28: tow veil, 29: convex portion, 30: winding paper, 31: suction filter, 32: molding paper, 33: chopped tobacco 34: wrapping paper, 35: hole, 36: guide, 37: filter plug, 38: first transport drum, 39: transport path, 40: supply drum, 41: acceleration drum, 42: adhesive roller, 43: adhesion Chemical solution, 44: Transmission roller, 45: Drum with blade, 46: Pasting passage, 47: Delivery passage, 48: Narrow portion, 49: Double filter cigarette, 50: Heat treatment portion, 51: Hole, 52: Plate, 53: Pressing part, 54: Hollow filter intermediate body, 55: Gannicha belt, 56: Stand
Claims (7)
- 総繊度23000デニール~70000デニールのコア繊維に可塑剤を添加して添加率13%~40%とするコア繊維加工工程と、
総繊度10000デニール~47000デニールのシース繊維に可塑剤を添加して添加率を15%以下とする、もしくは可塑剤を添加しないで添加率を0%とするシース繊維加工工程と、
前記コア繊維加工工程と前記シース繊維加工工程との後に、前記コア繊維を硬化させて一方の端面から他方の端面に向かって延びる孔部が形成されたコア部とし、該コア部の外側を前記シース繊維で覆ってシース部として中空フィルタを形成する中空フィルタ形成工程と、
前記中空フィルタ形成工程の後に、前記中空フィルタを前記中空フィルタの直径よりも狭く、前記コア部の直径よりも大きい狭小部を通過させて搬送する、後工程を含むフィルタシガレット製造方法。 A core fiber processing step in which a plasticizer is added to a core fiber having a total fineness of 23,000 denier to 70000 denier to obtain an addition rate of 13% to 40%;
A sheath fiber processing step in which a plasticizer is added to a sheath fiber having a total fineness of 10,000 denier to 47,000 denier so that the addition rate is 15% or less, or the addition rate is 0% without adding a plasticizer;
After the core fiber processing step and the sheath fiber processing step, the core fiber is cured to form a core portion formed with a hole extending from one end surface toward the other end surface, and the outside of the core portion is defined as the core portion. A hollow filter forming step of forming a hollow filter as a sheath part by covering with a sheath fiber,
A filter cigarette manufacturing method including a post-process, wherein after the hollow filter forming step, the hollow filter is transported through a narrow portion that is narrower than the diameter of the hollow filter and larger than the diameter of the core portion. - 前記コア繊維に対する前記可塑剤の添加率は13%~35%であり、前記シース繊維に対する前記可塑剤の添加率は3%~12%であることを特徴とする請求項1に記載のフィルタシガレット製造方法。 The filter cigarette according to claim 1, wherein an addition rate of the plasticizer to the core fiber is 13% to 35%, and an addition rate of the plasticizer to the sheath fiber is 3% to 12%. Production method.
- 前記後工程は、前記中空フィルタ及びシガレットが転動する転動通路に導入される際に前記中空フィルタ及び前記シガレットを転動させるきっかけを与えるために前記転動通路の内側に向けて突出する凸部が形成された狭小部を通過させ、前記転動通路にて前記中空フィルタ及び前記シガレットにチップペーパを巻き付けて前記中空フィルタと前記シガレットとを接続するフィルタ装着工程である請求項1に記載のフィルタシガレット製造方法。 The post-process is a convex projecting toward the inside of the rolling passage in order to give an opportunity to roll the hollow filter and the cigarette when introduced into the rolling passage where the hollow filter and cigarette roll. 2. The filter mounting step of passing a narrow portion formed with a portion, winding a tip paper around the hollow filter and the cigarette in the rolling passage, and connecting the hollow filter and the cigarette. Filter cigarette manufacturing method.
- 一方の端面から他方の端面に向かって延びる孔部が形成された筒形状の中空フィルタと、
該中空フィルタに対して長手方向に連続して接続された吸着フィルタと
を備え、
前記中空フィルタは、一方の端面から他方の端面に向かって延びる孔部が形成されたコア部と該コア部の外側を覆うシース部とを有し、
該コア部と該シース部との間には境界線が存在し、
前記コア部は、総繊度が23000デニール~70000デニールであり、可塑剤添加率が13%~40%であり、
前記シース部は、総繊度が10000デニール~47000であり、可塑剤添加率が0%~15%であるフィルタ。 A cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed;
An adsorption filter continuously connected in the longitudinal direction to the hollow filter,
The hollow filter has a core portion in which a hole extending from one end surface toward the other end surface is formed and a sheath portion covering the outside of the core portion,
A boundary line exists between the core portion and the sheath portion,
The core portion has a total fineness of 23000 denier to 70000 denier and a plasticizer addition rate of 13% to 40%.
The sheath portion has a total fineness of 10,000 denier to 47000 and a plasticizer addition rate of 0% to 15%. - 一方の端面から他方の端面に向かって延びる孔部が形成された筒形状の中空フィルタと、
該中空フィルタに対して長手方向に連続して接続された吸着フィルタと
を備え、
前記中空フィルタは、一方の端面から他方の端面に向かって延びる孔部が形成されたコア部と該コア部の外側を覆うシース部とを有し、
該コア部と該シース部との間には境界線が存在し、
前記コア部は0mm/10以上5mm/10未満の硬度を有し、
前記シース部は5mm/10以上10mm/10以下の硬度を有していることを特徴とするフィルタ。 A cylindrical hollow filter in which a hole extending from one end surface toward the other end surface is formed;
An adsorption filter continuously connected in the longitudinal direction to the hollow filter,
The hollow filter has a core portion in which a hole extending from one end surface toward the other end surface is formed and a sheath portion covering the outside of the core portion,
A boundary line exists between the core portion and the sheath portion,
The core portion has a hardness of 0 mm / 10 or more and less than 5 mm / 10,
The said sheath part has the hardness of 5 mm / 10 or more and 10 mm / 10 or less, The filter characterized by the above-mentioned. - 前記コア部は、総繊度が23000デニール~70000デニールであり、可塑剤添加率が13%~40%であり、
前記シース部は、総繊度が10000デニール~47000デニールであり、可塑剤添加率が0%~15%である請求項5に記載のフィルタ。 The core portion has a total fineness of 23000 denier to 70000 denier and a plasticizer addition rate of 13% to 40%.
The filter according to claim 5, wherein the sheath portion has a total fineness of 10,000 denier to 47,000 denier and a plasticizer addition rate of 0% to 15%. - 請求項5に記載のフィルタと、
刻みたばこを巻紙で包み込んだシガレットと、
前記フィルタ及び前記シガレットを包み込んで長手方向に接続するチップペーパと
を備えたフィルタシガレット。 A filter according to claim 5;
A cigarette wrapped with wrapping cigarettes,
A filter cigarette comprising the filter and chip paper that wraps around the cigarette and connects in the longitudinal direction.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2014548410A JP5877570B2 (en) | 2012-11-26 | 2012-11-26 | Filter cigarette manufacturing method, filter and filter cigarette |
EP12888733.8A EP2893820B1 (en) | 2012-11-26 | 2012-11-26 | Method for producing filter cigarette, filter, and filter cigarette |
PCT/JP2012/080465 WO2014080516A1 (en) | 2012-11-26 | 2012-11-26 | Method for producing filter cigarette, filter, and filter cigarette |
EP17172762.1A EP3254570B1 (en) | 2012-11-26 | 2012-11-26 | Filter cigarette producing method, filter and filter cigarette |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2012/080465 WO2014080516A1 (en) | 2012-11-26 | 2012-11-26 | Method for producing filter cigarette, filter, and filter cigarette |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2014080516A1 true WO2014080516A1 (en) | 2014-05-30 |
Family
ID=50775720
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2012/080465 WO2014080516A1 (en) | 2012-11-26 | 2012-11-26 | Method for producing filter cigarette, filter, and filter cigarette |
Country Status (3)
Country | Link |
---|---|
EP (2) | EP2893820B1 (en) |
JP (1) | JP5877570B2 (en) |
WO (1) | WO2014080516A1 (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016120583A1 (en) * | 2015-01-30 | 2016-08-04 | British American Tobacco (Investments) Limited | Apparatus and method for filter manufacture |
WO2017068664A1 (en) * | 2015-10-21 | 2017-04-27 | 日本たばこ産業株式会社 | Filter for tobacco products |
WO2018163253A1 (en) * | 2017-03-06 | 2018-09-13 | 日本たばこ産業株式会社 | Smoking article provided with filter |
EP3269266A4 (en) * | 2015-03-13 | 2018-11-21 | Japan Tobacco, Inc. | Filter for tobacco product, and tobacco product |
CN111542235A (en) * | 2017-12-22 | 2020-08-14 | 益升华过滤产品开发私人有限公司 | Smoking article holder |
JP2021517809A (en) * | 2018-03-26 | 2021-07-29 | フィリップ・モーリス・プロダクツ・ソシエテ・アノニム | Inhaler with composite porous support element |
CN113712253A (en) * | 2021-08-31 | 2021-11-30 | 南通烟滤嘴有限责任公司 | Filter rod with suspended inner core and preparation device and method thereof |
JP2022506151A (en) * | 2018-10-29 | 2022-01-17 | ネルディア リミテッド | Smoking substitute consumables |
JP2022524794A (en) * | 2019-03-11 | 2022-05-10 | ニコベンチャーズ トレーディング リミテッド | Goods for use in non-combustible aerosol supply systems |
JP2022525079A (en) * | 2019-03-11 | 2022-05-11 | ニコベンチャーズ トレーディング リミテッド | Goods for use in non-combustible aerosol supply systems |
CN115125674A (en) * | 2022-07-22 | 2022-09-30 | 广东鑫球新材料科技有限公司 | Internal inserting type hollow cotton die and forming method |
JP2023506995A (en) * | 2019-12-20 | 2023-02-20 | ニコベンチャーズ トレーディング リミテッド | Components used in aerosol delivery systems |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104824841B (en) * | 2015-03-21 | 2018-05-15 | 南通烟滤嘴有限责任公司 | The former of hollow filter stick |
BR112018010154B1 (en) | 2015-12-30 | 2022-03-03 | Philip Morris Products S.A. | filter making apparatus |
GB201608931D0 (en) * | 2016-05-20 | 2016-07-06 | British American Tobacco Co | Article for use in apparatus for heating smokeable material |
GB201608928D0 (en) * | 2016-05-20 | 2016-07-06 | British American Tobacco Co | Article for use in apparatus for heating smokable material |
IT201600075162A1 (en) * | 2016-07-18 | 2018-01-18 | Montrade S P A | FILTER WAND FOR SMOKE ITEMS, METHOD FOR ITS MANUFACTURE AND FILTER OBTAINED FROM THE FILTER WAND |
KR102022302B1 (en) * | 2016-10-25 | 2019-11-04 | 태영산업 주식회사 | apparatus for manufacturing cigarette filter |
WO2018229087A1 (en) * | 2017-06-15 | 2018-12-20 | Philip Morris Products S.A. | Method and apparatus for manufacturing inductively heatable aerosol-forming rods |
CN111328262B (en) * | 2017-11-28 | 2022-10-18 | 菲利普莫里斯生产公司 | Aerosol-generating article with improved mouth end cavity |
KR101978974B1 (en) * | 2018-08-23 | 2019-08-28 | 태영산업 주식회사 | cigarette base paper and method for manufacturing the same |
GB201817582D0 (en) * | 2018-10-29 | 2018-12-12 | Nerudia Ltd | Smoking and consumable |
CN114983017B (en) * | 2022-05-24 | 2023-08-22 | 云南中烟工业有限责任公司 | Inner core filled outer hollow filter stick and processing method thereof |
GB202300835D0 (en) * | 2023-01-19 | 2023-03-08 | Nicoventures Trading Ltd | Methods and assemblies for the processing of a continuous sheet of material |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3095343A (en) * | 1960-09-15 | 1963-06-25 | United States Filter Corp | Method for treating continuous filamentary tows |
JPS571226B2 (en) * | 1976-11-08 | 1982-01-09 | ||
JP3002173B2 (en) * | 1998-05-08 | 2000-01-24 | 日本たばこ産業株式会社 | Manufacturing method and device for tobacco filter |
JP3022624B2 (en) * | 1991-05-28 | 2000-03-21 | 日本フィルター工業株式会社 | Fiber rod for tobacco filter and apparatus for producing the same |
WO2011114440A1 (en) | 2010-03-16 | 2011-09-22 | 日本たばこ産業株式会社 | Filter manufacturing machine |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IE39466B1 (en) * | 1973-07-09 | 1978-10-11 | Reynolds Tobacco Co R | Filter element |
US4179323A (en) * | 1973-08-27 | 1979-12-18 | Liggett Group Inc. | Method for making a hollow filter rod |
JP3648072B2 (en) * | 1998-09-22 | 2005-05-18 | 三菱レイヨン株式会社 | Cigarette filter |
GB0800216D0 (en) * | 2008-01-07 | 2008-02-13 | British American Tobacco Co | Smoking article |
-
2012
- 2012-11-26 WO PCT/JP2012/080465 patent/WO2014080516A1/en active Application Filing
- 2012-11-26 EP EP12888733.8A patent/EP2893820B1/en active Active
- 2012-11-26 JP JP2014548410A patent/JP5877570B2/en active Active
- 2012-11-26 EP EP17172762.1A patent/EP3254570B1/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3095343A (en) * | 1960-09-15 | 1963-06-25 | United States Filter Corp | Method for treating continuous filamentary tows |
JPS571226B2 (en) * | 1976-11-08 | 1982-01-09 | ||
JP3022624B2 (en) * | 1991-05-28 | 2000-03-21 | 日本フィルター工業株式会社 | Fiber rod for tobacco filter and apparatus for producing the same |
JP3002173B2 (en) * | 1998-05-08 | 2000-01-24 | 日本たばこ産業株式会社 | Manufacturing method and device for tobacco filter |
WO2011114440A1 (en) | 2010-03-16 | 2011-09-22 | 日本たばこ産業株式会社 | Filter manufacturing machine |
Non-Patent Citations (1)
Title |
---|
See also references of EP2893820A4 |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2016120583A1 (en) * | 2015-01-30 | 2016-08-04 | British American Tobacco (Investments) Limited | Apparatus and method for filter manufacture |
EP3269266A4 (en) * | 2015-03-13 | 2018-11-21 | Japan Tobacco, Inc. | Filter for tobacco product, and tobacco product |
KR102124446B1 (en) * | 2015-10-21 | 2020-06-18 | 니뽄 다바코 산교 가부시키가이샤 | Filter for tobacco products |
WO2017068664A1 (en) * | 2015-10-21 | 2017-04-27 | 日本たばこ産業株式会社 | Filter for tobacco products |
JPWO2017068664A1 (en) * | 2015-10-21 | 2018-05-17 | 日本たばこ産業株式会社 | Tobacco article filter |
KR20180064457A (en) * | 2015-10-21 | 2018-06-14 | 니뽄 다바코 산교 가부시키가이샤 | Filter for tobacco products |
EP3586652B1 (en) | 2017-03-06 | 2021-12-29 | Japan Tobacco, Inc. | Smoking article provided with filter |
WO2018163253A1 (en) * | 2017-03-06 | 2018-09-13 | 日本たばこ産業株式会社 | Smoking article provided with filter |
CN111542235A (en) * | 2017-12-22 | 2020-08-14 | 益升华过滤产品开发私人有限公司 | Smoking article holder |
JP2021517809A (en) * | 2018-03-26 | 2021-07-29 | フィリップ・モーリス・プロダクツ・ソシエテ・アノニム | Inhaler with composite porous support element |
JP7458985B2 (en) | 2018-03-26 | 2024-04-01 | フィリップ・モーリス・プロダクツ・ソシエテ・アノニム | Inhaler with composite porous support element |
US11744962B2 (en) | 2018-03-26 | 2023-09-05 | Philip Morris Products S.A. | Inhaler with composite porous support element |
JP2022506151A (en) * | 2018-10-29 | 2022-01-17 | ネルディア リミテッド | Smoking substitute consumables |
JP2022525079A (en) * | 2019-03-11 | 2022-05-11 | ニコベンチャーズ トレーディング リミテッド | Goods for use in non-combustible aerosol supply systems |
JP2022524794A (en) * | 2019-03-11 | 2022-05-10 | ニコベンチャーズ トレーディング リミテッド | Goods for use in non-combustible aerosol supply systems |
JP2023506995A (en) * | 2019-12-20 | 2023-02-20 | ニコベンチャーズ トレーディング リミテッド | Components used in aerosol delivery systems |
JP7534411B2 (en) | 2019-12-20 | 2024-08-14 | ニコベンチャーズ トレーディング リミテッド | Components for use in aerosol delivery systems and methods for making the components - Patents.com |
CN113712253A (en) * | 2021-08-31 | 2021-11-30 | 南通烟滤嘴有限责任公司 | Filter rod with suspended inner core and preparation device and method thereof |
CN115125674A (en) * | 2022-07-22 | 2022-09-30 | 广东鑫球新材料科技有限公司 | Internal inserting type hollow cotton die and forming method |
CN115125674B (en) * | 2022-07-22 | 2023-08-29 | 广东鑫球新材料科技有限公司 | Internal inserting hollow cotton mold and molding method |
Also Published As
Publication number | Publication date |
---|---|
EP3254570B1 (en) | 2023-06-21 |
JP5877570B2 (en) | 2016-03-08 |
EP3254570A1 (en) | 2017-12-13 |
EP2893820A4 (en) | 2016-06-01 |
EP2893820B1 (en) | 2022-07-20 |
JPWO2014080516A1 (en) | 2017-01-05 |
EP2893820A1 (en) | 2015-07-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5877570B2 (en) | Filter cigarette manufacturing method, filter and filter cigarette | |
JP4584371B2 (en) | Method and apparatus for processing filter tow strips | |
JP5487357B2 (en) | Cigarette filter manufacturing apparatus and cigarette filter manufacturing method | |
JP2012523223A (en) | Equipment for introducing objects into filter rod material | |
JPWO2012132972A1 (en) | Filter manufacturing machine, filter manufacturing method using the same, and hollow filter | |
ITBO20110419A1 (en) | DEVICE AND METHOD OF ROLLING OF CIGARETTES WITH FILTER. | |
JP6586423B2 (en) | Smoking article with filter element and smoking article | |
JP2012239437A (en) | Tow transport jet | |
JP5640090B2 (en) | Filter manufacturing apparatus, filter manufacturing method, and filter | |
KR102022302B1 (en) | apparatus for manufacturing cigarette filter | |
WO2009083240A1 (en) | Filter tube making | |
JPWO2017021994A1 (en) | Tow band manufacturing method, tow band manufacturing apparatus and cigarette filter manufacturing method | |
CN104585878A (en) | Device for manufacturing a filter rod and machine for the tobacco processing industry | |
TWI468120B (en) | Method for manufacturing filter cigarette as well as filter and filter cigarette | |
KR101978974B1 (en) | cigarette base paper and method for manufacturing the same | |
JP2004521633A (en) | Method and apparatus for manufacturing filters and suitable filters | |
US11896048B2 (en) | Aerosol generating articles | |
JP4945071B2 (en) | Apparatus and method for producing at least two fiber continuums | |
KR20120071390A (en) | Tow cutter | |
KR102057992B1 (en) | cigarette filter | |
JP7446379B1 (en) | Paper cigarette filter and its manufacturing method and manufacturing device | |
JP2824204B2 (en) | Method and apparatus for supplying cigarettes and chopped tobacco | |
JP5243142B2 (en) | Apparatus for processing at least one strip filter material in the tobacco industry | |
CN109936985A (en) | Method and apparatus of the production for the filtering rod of smoking product | |
TW202430064A (en) | Methods and assemblies for the processing of a continuous sheet of material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 12888733 Country of ref document: EP Kind code of ref document: A1 |
|
ENP | Entry into the national phase |
Ref document number: 2014548410 Country of ref document: JP Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2012888733 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |