US3093142A - Cigarette filter - Google Patents

Cigarette filter Download PDF

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US3093142A
US3093142A US833230A US83323059A US3093142A US 3093142 A US3093142 A US 3093142A US 833230 A US833230 A US 833230A US 83323059 A US83323059 A US 83323059A US 3093142 A US3093142 A US 3093142A
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filaments
crimps
tow
crimping
filter
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US833230A
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Swerdloff Jack
Ezra B Larsen
Adriaan J Troeleman
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Celanese Corp
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Celanese Corp
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/253Formation of filaments, threads, or the like with a non-circular cross section; Spinnerette packs therefor
    • AHUMAN NECESSITIES
    • A24TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24DCIGARS; CIGARETTES; TOBACCO SMOKE FILTERS; MOUTHPIECES FOR CIGARS OR CIGARETTES; MANUFACTURE OF TOBACCO SMOKE FILTERS OR MOUTHPIECES
    • A24D3/00Tobacco smoke filters, e.g. filter-tips, filtering inserts; Filters specially adapted for simulated smoking devices; Mouthpieces for cigars or cigarettes
    • A24D3/04Tobacco smoke filters characterised by their shape or structure

Definitions

  • the present invention relates to high bulk filamentary material. More particularly, it relates to filamentary material, i.e. continuous filaments or staple fibers, of organic acid esters of cellulose, which is especially suited as a filtering, filling or stufiing material. The present invention also relates to the process or method used for manuiacturing the high bulk filamentary material, and to the application of this material in the trade.
  • Synthetic filamentary materials such as cellulose esters are formed by extrusion of solutions through orifices in a member known as a jet.
  • the orifices are small and usually circular so that the resulting filamentary ma terials are bulbous or generally circular in cross-section, although the surface of the said materials is normally crenulated and irregular. Consequently, the specific volume or volume per unit mass of such material is comparatively low, so that a predetermined weight will occupy less volume than that desired for certain applications, or if placed in an enclosure of a predetermined volume they will pack less tightly than is desired.
  • Another object of the invention is to provide improved filter materials and articles containing said filter materials.
  • filament-forming materials such as cellulose esters are spun, i.e. extruded, through orifices in jets and the filamentary material is then subjected to at least two crimping operations to impart thereto a non-rectilinear configuration.
  • the first crimping operation increases the bulk or specific volume because adjacent filaments cannot pack as closely.
  • the second crimping operation introduces additional crimps and these deformations will lie in a plurality of planes directed at an angle to that generally defined by the first crimping.
  • the filamentary material is three di' mensional and has a still higher specific volume.
  • the filamentary material Before each crimping, which is preferably effected by use of a stufiing box so as to avoid tearing of the filamentary material such as results when using a gear toothed crimper which pulls the filaments into their new shapes, the filamentary material is moistened with water or an aqueous solution of a softening agent.
  • the use of a plurality of stuffing box crimpers in succession ensures that the crimps will be randomly distributed along the filaments and in a multiplicity of planes so that the specific volume will not be diminished due to packing of adjacent filaments.
  • the filamentary material is spun through spinning jets having non-circular apertures so that the filamentary material after crimping will have high resilience and a specific 3,093,142 Patented June 11, 1963 "ice.
  • the preferred filamentary crosssection is Y-shaped, such as is produced by spinning through triangular orifices. However, mixtures of filaments spun through diiferently shaped non-circular orifices may be used. Minor amounts of filaments spun through circular orifices can be included. Accordingly, if filaments spun through circular orifices are included, they should be used only in such an amount as will still leave the total specific volume after crimping asleast 20% greater than that of a mass spun wholly through circular orifices.
  • a tow or large bundle of the bulky filamentary material is formed into cigarette filters by more or less conventional steps such as opening the tow, applying about 2 to 30% by weight of a plasticizer whose composition depends upon the composition of the tow, e.g. glycerol triinto plugs of predetermined length, and curing to efiect bonding of filaments to one another by the plasticizer so as to increase the firmness of the plug, i.e. the resistance to transverse compression.
  • the time and temperature of curing will vary inversely, and will vary withthe plasticizer, e.g. several hours at room temperature will cure a cellulose acetate filter plasticized with glycerol triacetate.
  • cigarettes including the novel filters are more firm than filters from conventional plugs.
  • the amount of plasticizer can be decreased or a lesser weight of filaments can be employed, with obvious advantage.
  • the filters in the finished cigarettes generally range from about 10 to 17 mm. in length.
  • FIG. 1 is a schematic illustration of the process
  • FIGS. 2 to 6 are cross-sectional views of different shapes of filaments which can be spun and processed in accordance with the invention.
  • FIG. 7 is a schematic perspective view of a portion of a filament having the shape shown in FIG. 2 and subjected to one crimping operation;
  • FIG. 8 is a perspective vector diagram for defining the spatial disposition of the filament of FIG. 7;
  • FIG. 9 is a schematic perspective view of a portion of the filament of FIG. 7 after being subjected to a second crimping operation;
  • FIG. 10 is a perspective view of a pillow, a portion being shown broken away to expose the stuffing;
  • FIG. 11 is a perspective view of a cigarette including a filter produced from a tow processed in accordance vwith the present invention.
  • FIG. 12 is a sketch diagrammatically defining theamplitude and number of crimps per unit length as employed herein.
  • a lubricated tow 1.1 of filaments of cellulose acetate is passed over a roller 12 dipping into a trough 13 containing water or a water emulsion of lubricants and softening agents.
  • Another roller 14 flattens out the tow L11 somewhat to ensure wetting of all filaments.
  • the tow passes through a first stuffing box crimper 15 which crimps the tow, imparting to each filament an appearance somewhat as is shown in FIG. 7.
  • the tow then passes over a further roller 16 dipping into a trough 3 1 7 which contains warm water or other lubricant.
  • An upper roller 18 ensures wetting of all filaments of the tow 1-1.
  • Other equivalent structures such as sprays or wet felt .pads may be employed to lubricate the tow.
  • the tow next passes into a second stufiing box crimper 19 which may be of identical construction or which may be designed to produce crimps of a slightly lower amplitude, for example.
  • the tow leaving the crimper 19 is dried and cut by cutter '20 into staple lengths 21.
  • the filaments 22 of the tow which leaves the crimper 19 have the approximate appearance shown in FIG. 8.
  • the staple lengths 2 -1 of multi-crimped cellulose acetate can be used to stuff a ticking 23 to form a pillow 24 as shown in FIG. 10.
  • the fibers are also useful as fillings for other articles such as mattresses, comforters, jacket interlinings and the like.
  • the tow leaving second crimper 19 can be baled and then used, or directly used, in making cigarette filters employing conventional apparatus (not shown).
  • the filter plugs produced from the tow by opening, plasticizing, wrapping, cutting and curing comprise generally longitudinally extending filaments 34 held inside a paper wrapper 35 which is wrapped, together with a rod of tobacco 36 inside an outer paper 37, as shown in FIG. 11.
  • the filaments can be Y-shaped in cross-section as shown at 22 in FIG. 2, this configuration resulting upon drying and shrinking of filaments spun through a jet having triangular orifices.
  • the non-circular contour produces a high bulk or specific volume which is increased by the successive crimpings.
  • 'Ihe cross-sectional shape of the filaments resists bending and deformation which is particularly desirable for stufiings and battings. This resistance gives the stuffed article a resilient quality in addition to its light weight resulting from the low specific volume of the filling.
  • the individual filaments can be substantially circular in cross-section as shown at 25 in FIG. 3 but such filaments will have a lower specific volume than either filament 22 or filaments 26, 27 or 28 (FIGS. 4 to 6), respectively produced by spinning through slotted, square or star-shaped orifices.
  • the denier of the individual filaments can range from 3 or even lower to as much as 25 or even higher. Preferably, however, it lies between and 10.
  • the number of filaments per yam end will depend upon the number of holes per jet and the number of yarns which may be gathered into a tow will depend upon the capacity of the crimping devices and the intended end uses.
  • the total number of filaments may be as much as 3000 to 40,000 or more and the total denier may range from about 50,000 to 250,000 or more.
  • the filaments preferably are treated with a lubricant or finish ranging from about 0.3 to 2.0% by weight of the filamentary material.
  • a lubricant or finish ranging from about 0.3 to 2.0% by weight of the filamentary material.
  • An especially soft luxurious hand will result from use of a finishing composition comprising one of the cationic group of softeners such as quaternary ammonium compound, or other chemical softener imparting a similar hand.
  • An even bulkier yarn will result by substituting as the lubricant an alkyl phosphate in mineral oil, especially compositions such as that described in Example III of Fortess et al. U.S. Patent No. 2,676,924 of April 27, 1954.
  • the cutter 20 can constitute any device known in the art, such as a reciprocating blade or a rotary cutter.
  • the cutter can be operated to form staple fibers ranging in length from /2 to 8 inches, although they preferably range in length from 1 to 4 inches.
  • the crimpers and 19 can constitute an apparatus such as that described in Upton et al. U.S. Patent No. 2,693,008 of November 2, 1954, or any other equivalent device.
  • the function of the second crimper can be appreciated by a comparison of FIGS. 7 and 9 which respectively show the spatial configuration of one filament 22 before and after it leaves cn'mper 19.
  • the filament 22 has a predominantly two-dimensional sinusoidal or saw-tooth configuration, comprising crimps 29, 30, 31, 32 and 33 generally in the XY plane of FIG. 8.
  • FIG. 9 it can be seen that after the second crimping the filament 22 is crimped more randomly and without large lengths wholly devoid of crimp.
  • the crimp 30, for example, has had impressed therein a sub-crimp 30a which has been deflected out of the XY plane toward the XZ plane.
  • Sub-crimp 31a has been formed out of a comparatively straight section of crimp 31 and is generally directed in still another plane. Portions of the other crimps are similarly afiected so that a filament of higher crimp and bulk is achieved.
  • Each crimper 15, 19 can generally impart from about 3 to 15 crimps per inch of an amplitude ranging from about 0.5 to 4.0 mm. and the two crimpers are conveniently synchronized in speed so that the second operates a little more slowly than the first but sufiicient to receive the filaments at the same rate they are discharged from the first crimper.
  • the tow may be fed to the first crirnper at the rate of 400 meters per minute and, to compensate for shrinkage due to crimping, it may be fed to the second erimper at the rate of 250300 meters per minute.
  • a reserve of filaments can be provided before the second crimper to compensate for any minor variations in feed rate.
  • the second crimpe-r can produce deviations in the XY plane itself, thereby modifying the generally sinusoidal pattern within that plane.
  • the successive crimpings need not be performed in tandem but instead the tow can be collected after the first crimping and can then be lubricated and again crimped at a differ. ent rate, further to modify the crimp pattern.
  • the multi-crimping in accordance with the present inv-ention will serve to increase the total crimp of the filaments to about 5 to 17 crimps per inch, for example, without undue mechanical strain, it will ensure a more permanent set of the crimps and it will ensure more uniform crimp frequency, i.e. fewer sections of the filaments will have no or only low crimp.
  • FIG. 12 illustrates the definition of the crimps as employed herein.
  • a length of filament 38 shown as a dot and dash line before crimping, and assumed to be one inch, after crimping will be shortened.
  • the number of peaks in the crimped fiber will represent the crimps per inch, i.e. two, and the amplitude 11 will be equal to the distance between peaks and valleys.
  • the peaks are first counted, the fiber is tensioneal so as to be straight, and the straight length of the fiber is determined.
  • the number of peaks divided by the straightened length in inches is the number of crimps per inch.
  • the sequence of treatments indicated can be varied in that the tow can first be cut into staple fibers, formed into a sliver and then double-ciimped or the cutting can take place after the first crimping operation but before the second crimping operation.
  • the lubrication in these modifications can be applied either to the tow or the sliver.
  • the invention is generally applicable to filamentary materials of various kinds including synthetic polyamides such as polyhexamethylene adipamide and poly-amino caproic acid, polyesters such as polyethylene terephthalate, polyurethanes, polyaminotriazoles, and polymers and copolymers of vinyl chloride such as vinyl chloride-vinyl acetate copolymers. It is eminently suited for the treatment of organic derivatives of cellulose, including, for example, cellulose acetate, cellulose propionate, cellulose butyrate, cellulose acetate formate, cellulose acetate propionate, cellulose acetate butyrate, cellulose benzoate, and ethyl cellulose.
  • synthetic polyamides such as polyhexamethylene adipamide and poly-amino caproic acid
  • polyesters such as polyethylene terephthalate
  • polyurethanes polyaminotriazoles
  • vinyl chloride such as vinyl chloride-vinyl acetate copolymers.
  • the hydroxyl groups of the anhydroglucose units of the cellulose molecules can be substantially completely replaced as in cellulose triacetate or they can be partially replaced as in ripened cellulose acetate wherein about 0.6 free hydroxyl group per anhydrogluco-se unit is present.
  • the tow is then cut into staple fibers about 1 /2 inches in length.
  • the specific volume of the staple fibers when placed in a vessel and put under a pressure of 2.5 pounds per square inch is about 0.75 cubic inch per gram whereas if the second crimping operation is omitted the specific volume is about 0.70 cubic inch per gram.
  • Example II The procedure of Example I is repeated, substituting for the lubricant there described a quaternary ammonium lubricant sold under the trade name of Ahcovel.
  • the staple fibers which are almost of equal specific volume are bright and have a very soft, luxurious hand.
  • a tow was formed of cellulose acetate filaments spun through a 70-hole jet having pentagonal orifices and another 7 O-hole jet having triangular orifices, each filament being 8 denier.
  • the tow was processed as in Example I to produce double-crimped staple fibers having a specific volume of 0.6 cubic inch per gram as opposed to a specific volume of 0.5 cubic inch per gram 'for regular staple.
  • EXAMPLE V A tow comprising 5000 cellulose acetate 16 denier filaments, having an acetyl value of 55%, is finished and crimped as in Example I and the tow is collected in la bale. The baled tow is then processed into cigarette filter plugs as shown in FIG. 11. As compared with a tow singly crimped, the double crimped tow is much more uniform and opens more uniformly. The novel filters are firm, uniform and free of random soft spots.
  • Example VI The process of Example V is repeated with the sole diflerence that the tow is made up of 8750 filaments of 8 denier each.
  • the resulting filters are uniform and very firm. If the flapper pressure of the stuffing box crimpers is reduced to insert only 6 crimps per inch into the tow, the resulting filters are of excellent uniformity and their firmness compares favorably with that of filters from a tow cri-mped to a higher level in a single stage.
  • a filter comprising a plurality of longitudinally extending filaments having a multiplicity of sets of crimps imparted by mechanical crimping, each of said sets of crimps comprising individual crimps which are angularly offset with respect to the general plane of other sets of crimps, wherein at least some of said filaments are of noncircular shape in cross section.
  • a filter comprising a plurality of longitudinally extending filaments crimped in a first direction having a first set of random amplitude mechanically imparted crimps to the extent of from about 3 to 15 crimps per inch and having superimposed thereon a second set of random amplitude crimps to give a total of from about 5 to 17 crimps per inch, the second set of crimps comprising individual crimps which are angularly offset with respect to the general plane of the first set of crimps.
  • a filter comprising about 3,000 to 40,000 longitudinally extending cellulose acetate filaments of about 50,000 to 250,000 total denier, said filaments having a first set of random amplitude mechanically imparted crimps to the extent of from about 3 to 15 crimps per inch and having superimposed thereon a second set of random amplitude crimps to give a total of from about 5 to 17 crimps per inch, the second set of crimps comprising individual crimps which are angularly offset with respect to the general plane of the first setof crimps.
  • a cigarette having incorporated therein a filter comprising a plurality of longitudinally extending filaments having multiple sets of crimps therein, each of said sets of crimps comprising individual random amplitude crimps which are angularly oilset with respect to the general plane of another of said sets of crimps, wherein at least some of said filaments are of non-circular shape in cross section formed by extrusion through non-circular orifices.

Description

June 1963 -J. SWERDLOF'F ET AL 3,093,142
CIGARETTE FILTER Filed Aug. 12, 1959 United States Patent 3,093,142 CIGARETTE FILTER Jack Swerdloif, Miami, Fla., Ezra B. Larsen, Boulder,
Colo., and Adriaan J. Troeleman, Narrows, Va., amigoors to Celanese Corporation of America, New York, N.Y., a corporation of Delaware Filed Aug. 12, 1959, Ser. No. 833,230 7 Claims. (Cl. 131-10) The present invention relates to high bulk filamentary material. More particularly, it relates to filamentary material, i.e. continuous filaments or staple fibers, of organic acid esters of cellulose, which is especially suited as a filtering, filling or stufiing material. The present invention also relates to the process or method used for manuiacturing the high bulk filamentary material, and to the application of this material in the trade.
Synthetic filamentary materials such as cellulose esters are formed by extrusion of solutions through orifices in a member known as a jet. The orifices are small and usually circular so that the resulting filamentary ma terials are bulbous or generally circular in cross-section, although the surface of the said materials is normally crenulated and irregular. Consequently, the specific volume or volume per unit mass of such material is comparatively low, so that a predetermined weight will occupy less volume than that desired for certain applications, or if placed in an enclosure of a predetermined volume they will pack less tightly than is desired.
It is an object of the present invention to provide filamentary materials of comparatively high specific volume, i.e. of high bulk, and to provide a process for manufacturing these filamentary materials.
It is another object of the present invention to provide articles such as pillows and mattresses filled or stufied with high-bulk materials, which articles will be light in weight and comfortable but nonetheless moderately firm and resilient.
Another object of the invention is to provide improved filter materials and articles containing said filter materials.
Other objects and advantages of the invention will become apparent from the detailed description and claims which follow.
In accordance with the invention, filament-forming materials such as cellulose esters are spun, i.e. extruded, through orifices in jets and the filamentary material is then subjected to at least two crimping operations to impart thereto a non-rectilinear configuration. The first crimping operation increases the bulk or specific volume because adjacent filaments cannot pack as closely. The second crimping operation introduces additional crimps and these deformations will lie in a plurality of planes directed at an angle to that generally defined by the first crimping. Thus the filamentary material is three di' mensional and has a still higher specific volume.
Before each crimping, which is preferably effected by use of a stufiing box so as to avoid tearing of the filamentary material such as results when using a gear toothed crimper which pulls the filaments into their new shapes, the filamentary material is moistened with water or an aqueous solution of a softening agent. In addition to avoiding weakening of the filaments, the use of a plurality of stuffing box crimpers in succession ensures that the crimps will be randomly distributed along the filaments and in a multiplicity of planes so that the specific volume will not be diminished due to packing of adjacent filaments.
In accordance with one aspect of the invention, the filamentary material is spun through spinning jets having non-circular apertures so that the filamentary material after crimping will have high resilience and a specific 3,093,142 Patented June 11, 1963 "ice.
volume at least 20% greater than that of a mass of crimped circular filaments of equal denier, i.e. of equal cross-sectional area. The preferred filamentary crosssection is Y-shaped, such as is produced by spinning through triangular orifices. However, mixtures of filaments spun through diiferently shaped non-circular orifices may be used. Minor amounts of filaments spun through circular orifices can be included. Accordingly, if filaments spun through circular orifices are included, they should be used only in such an amount as will still leave the total specific volume after crimping asleast 20% greater than that of a mass spun wholly through circular orifices.
In accordance with another aspect of the invention a tow or large bundle of the bulky filamentary material is formed into cigarette filters by more or less conventional steps such as opening the tow, applying about 2 to 30% by weight of a plasticizer whose composition depends upon the composition of the tow, e.g. glycerol triinto plugs of predetermined length, and curing to efiect bonding of filaments to one another by the plasticizer so as to increase the firmness of the plug, i.e. the resistance to transverse compression. The time and temperature of curing will vary inversely, and will vary withthe plasticizer, e.g. several hours at room temperature will cure a cellulose acetate filter plasticized with glycerol triacetate. Because of the high bulk and resilience of the novel filaments and tows thereof cigarettes including the novel filters are more firm than filters from conventional plugs. Alternately, to produce a plug of given length and predetermined firmness either the amount of plasticizer can be decreased or a lesser weight of filaments can be employed, with obvious advantage. The filters in the finished cigarettes generally range from about 10 to 17 mm. in length.
The invention will now be described with reference to the accompanying drawing wherein:
FIG. 1 is a schematic illustration of the process;
FIGS. 2 to 6 are cross-sectional views of different shapes of filaments which can be spun and processed in accordance with the invention;
FIG. 7 is a schematic perspective view of a portion of a filament having the shape shown in FIG. 2 and subjected to one crimping operation;
FIG. 8 is a perspective vector diagram for defining the spatial disposition of the filament of FIG. 7;
FIG. 9 is a schematic perspective view of a portion of the filament of FIG. 7 after being subjected to a second crimping operation;
FIG. 10 is a perspective view of a pillow, a portion being shown broken away to expose the stuffing;
FIG. 11 is a perspective view of a cigarette including a filter produced from a tow processed in accordance vwith the present invention; and
FIG. 12 is a sketch diagrammatically defining theamplitude and number of crimps per unit length as employed herein.
Referring now more particularly to the drawing, a lubricated tow 1.1 of filaments of cellulose acetate is passed over a roller 12 dipping into a trough 13 containing water or a water emulsion of lubricants and softening agents. Another roller 14 flattens out the tow L11 somewhat to ensure wetting of all filaments.
The tow passes through a first stuffing box crimper 15 which crimps the tow, imparting to each filament an appearance somewhat as is shown in FIG. 7. The tow then passes over a further roller 16 dipping into a trough 3 1 7 which contains warm water or other lubricant. An upper roller 18 ensures wetting of all filaments of the tow 1-1. Other equivalent structures such as sprays or wet felt .pads may be employed to lubricate the tow. The tow next passes into a second stufiing box crimper 19 which may be of identical construction or which may be designed to produce crimps of a slightly lower amplitude, for example. The tow leaving the crimper 19 is dried and cut by cutter '20 into staple lengths 21. The filaments 22 of the tow which leaves the crimper 19 have the approximate appearance shown in FIG. 8.
The staple lengths 2 -1 of multi-crimped cellulose acetate can be used to stuff a ticking 23 to form a pillow 24 as shown in FIG. 10. The fibers are also useful as fillings for other articles such as mattresses, comforters, jacket interlinings and the like.
In place of being cut into staple fibers, the tow leaving second crimper 19 can be baled and then used, or directly used, in making cigarette filters employing conventional apparatus (not shown). The filter plugs produced from the tow by opening, plasticizing, wrapping, cutting and curing comprise generally longitudinally extending filaments 34 held inside a paper wrapper 35 which is wrapped, together with a rod of tobacco 36 inside an outer paper 37, as shown in FIG. 11.
The filaments can be Y-shaped in cross-section as shown at 22 in FIG. 2, this configuration resulting upon drying and shrinking of filaments spun through a jet having triangular orifices. The non-circular contour produces a high bulk or specific volume which is increased by the successive crimpings. 'Ihe cross-sectional shape of the filaments resists bending and deformation which is particularly desirable for stufiings and battings. This resistance gives the stuffed article a resilient quality in addition to its light weight resulting from the low specific volume of the filling.
The individual filaments can be substantially circular in cross-section as shown at 25 in FIG. 3 but such filaments will have a lower specific volume than either filament 22 or filaments 26, 27 or 28 (FIGS. 4 to 6), respectively produced by spinning through slotted, square or star-shaped orifices.
The denier of the individual filaments can range from 3 or even lower to as much as 25 or even higher. Preferably, however, it lies between and 10. The number of filaments per yam end will depend upon the number of holes per jet and the number of yarns which may be gathered into a tow will depend upon the capacity of the crimping devices and the intended end uses. For cigarette filters, the total number of filaments may be as much as 3000 to 40,000 or more and the total denier may range from about 50,000 to 250,000 or more.
The filaments preferably are treated with a lubricant or finish ranging from about 0.3 to 2.0% by weight of the filamentary material. An especially soft luxurious hand will result from use of a finishing composition comprising one of the cationic group of softeners such as quaternary ammonium compound, or other chemical softener imparting a similar hand. An even bulkier yarn will result by substituting as the lubricant an alkyl phosphate in mineral oil, especially compositions such as that described in Example III of Fortess et al. U.S. Patent No. 2,676,924 of April 27, 1954.
The cutter 20 can constitute any device known in the art, such as a reciprocating blade or a rotary cutter. The cutter can be operated to form staple fibers ranging in length from /2 to 8 inches, although they preferably range in length from 1 to 4 inches.
The crimpers and 19 can constitute an apparatus such as that described in Upton et al. U.S. Patent No. 2,693,008 of November 2, 1954, or any other equivalent device. The function of the second crimper can be appreciated by a comparison of FIGS. 7 and 9 which respectively show the spatial configuration of one filament 22 before and after it leaves cn'mper 19. In FIG. 7 the filament 22 has a predominantly two-dimensional sinusoidal or saw-tooth configuration, comprising crimps 29, 30, 31, 32 and 33 generally in the XY plane of FIG. 8. In FIG. 9 it can be seen that after the second crimping the filament 22 is crimped more randomly and without large lengths wholly devoid of crimp. The crimp 30, for example, has had impressed therein a sub-crimp 30a which has been deflected out of the XY plane toward the XZ plane. Sub-crimp 31a has been formed out of a comparatively straight section of crimp 31 and is generally directed in still another plane. Portions of the other crimps are similarly afiected so that a filament of higher crimp and bulk is achieved.
Each crimper 15, 19 can generally impart from about 3 to 15 crimps per inch of an amplitude ranging from about 0.5 to 4.0 mm. and the two crimpers are conveniently synchronized in speed so that the second operates a little more slowly than the first but sufiicient to receive the filaments at the same rate they are discharged from the first crimper. For example, the tow may be fed to the first crirnper at the rate of 400 meters per minute and, to compensate for shrinkage due to crimping, it may be fed to the second erimper at the rate of 250300 meters per minute. A reserve of filaments can be provided before the second crimper to compensate for any minor variations in feed rate. Because of the irregular crimping action of each crimper, the second crimpe-r can produce deviations in the XY plane itself, thereby modifying the generally sinusoidal pattern within that plane. The successive crimpings need not be performed in tandem but instead the tow can be collected after the first crimping and can then be lubricated and again crimped at a differ. ent rate, further to modify the crimp pattern.
The multi-crimping in accordance with the present inv-ention will serve to increase the total crimp of the filaments to about 5 to 17 crimps per inch, for example, without undue mechanical strain, it will ensure a more permanent set of the crimps and it will ensure more uniform crimp frequency, i.e. fewer sections of the filaments will have no or only low crimp.
FIG. 12 illustrates the definition of the crimps as employed herein. A length of filament 38, shown as a dot and dash line before crimping, and assumed to be one inch, after crimping will be shortened. The number of peaks in the crimped fiber will represent the crimps per inch, i.e. two, and the amplitude 11 will be equal to the distance between peaks and valleys. In determining the crimps per inch of an already crimped fiber, the peaks are first counted, the fiber is tensioneal so as to be straight, and the straight length of the fiber is determined. The number of peaks divided by the straightened length in inches is the number of crimps per inch.
The sequence of treatments indicated can be varied in that the tow can first be cut into staple fibers, formed into a sliver and then double-ciimped or the cutting can take place after the first crimping operation but before the second crimping operation. The lubrication in these modifications can be applied either to the tow or the sliver.
The invention is generally applicable to filamentary materials of various kinds including synthetic polyamides such as polyhexamethylene adipamide and poly-amino caproic acid, polyesters such as polyethylene terephthalate, polyurethanes, polyaminotriazoles, and polymers and copolymers of vinyl chloride such as vinyl chloride-vinyl acetate copolymers. It is eminently suited for the treatment of organic derivatives of cellulose, including, for example, cellulose acetate, cellulose propionate, cellulose butyrate, cellulose acetate formate, cellulose acetate propionate, cellulose acetate butyrate, cellulose benzoate, and ethyl cellulose. In the cellulose derivatives the hydroxyl groups of the anhydroglucose units of the cellulose molecules can be substantially completely replaced as in cellulose triacetate or they can be partially replaced as in ripened cellulose acetate wherein about 0.6 free hydroxyl group per anhydrogluco-se unit is present.
The following examples are given to illustrate the invention further.
EXAMPLE I A tow comprising 30,000 filaments of cellulose acetate having an acetyl value of 55% by weight calculated as acetic acid, each filament of which is 5.5 denier and Y- shaped in cross section, finished with about 1.5% by weight of the composition of Example III of 'Fontess et al. Patent No. 2,676,924, is passed first through a stuffing box crimper operating to impart thereto about 7 crimps per inch of an amplitude varying between 0.5-4.0 mm. The crimped tow when is wet with water and passed through a second stuffing box crimper which increases the crimp to about 9 crimps per inch of an amplitude varying between 0.5-4.0 mm. The tow is then cut into staple fibers about 1 /2 inches in length. The specific volume of the staple fibers when placed in a vessel and put under a pressure of 2.5 pounds per square inch is about 0.75 cubic inch per gram whereas if the second crimping operation is omitted the specific volume is about 0.70 cubic inch per gram.
EXAMPLE II The procedure of Example I is repeated, substituting for the lubricant there described a quaternary ammonium lubricant sold under the trade name of Ahcovel. The staple fibers which are almost of equal specific volume are bright and have a very soft, luxurious hand.
EXAMPLE III By the process of Example I, cellulose acetate filament yarns spun through orifices of different shape and each 4 denier per filament were double crimped and cut into staple fiber. The relative specific volumes are indicated in the following table:
A tow was formed of cellulose acetate filaments spun through a 70-hole jet having pentagonal orifices and another 7 O-hole jet having triangular orifices, each filament being 8 denier. The tow was processed as in Example I to produce double-crimped staple fibers having a specific volume of 0.6 cubic inch per gram as opposed to a specific volume of 0.5 cubic inch per gram 'for regular staple.
EXAMPLE V A tow comprising 5000 cellulose acetate 16 denier filaments, having an acetyl value of 55%, is finished and crimped as in Example I and the tow is collected in la bale. The baled tow is then processed into cigarette filter plugs as shown in FIG. 11. As compared with a tow singly crimped, the double crimped tow is much more uniform and opens more uniformly. The novel filters are firm, uniform and free of random soft spots.
EXAMPLE VI The process of Example V is repeated with the sole diflerence that the tow is made up of 8750 filaments of 8 denier each. The resulting filters are uniform and very firm. If the flapper pressure of the stuffing box crimpers is reduced to insert only 6 crimps per inch into the tow, the resulting filters are of excellent uniformity and their firmness compares favorably with that of filters from a tow cri-mped to a higher level in a single stage.
This application is a continuationdn-part of application Serial No. 675,120 filed July 30, 1957, now US. Patent No. 2,968,857 issued January 24, 1961.
It is to be understood that the foregoing detailed description is merely given by way of illustration and that many variations may be made therein without departing from the spirit of our invention.
Having described our invention, what we desire to secure by Letters Patent is:
1. A filter comprising a plurality of longitudinally extending filaments having a multiplicity of sets of crimps imparted by mechanical crimping, each of said sets of crimps comprising individual crimps which are angularly offset with respect to the general plane of other sets of crimps, wherein at least some of said filaments are of noncircular shape in cross section.
2. A filter comprising a plurality of longitudinally extending filaments crimped in a first direction having a first set of random amplitude mechanically imparted crimps to the extent of from about 3 to 15 crimps per inch and having superimposed thereon a second set of random amplitude crimps to give a total of from about 5 to 17 crimps per inch, the second set of crimps comprising individual crimps which are angularly offset with respect to the general plane of the first set of crimps.
3. A filter comprising about 3,000 to 40,000 longitudinally extending cellulose acetate filaments of about 50,000 to 250,000 total denier, said filaments having a first set of random amplitude mechanically imparted crimps to the extent of from about 3 to 15 crimps per inch and having superimposed thereon a second set of random amplitude crimps to give a total of from about 5 to 17 crimps per inch, the second set of crimps comprising individual crimps which are angularly offset with respect to the general plane of the first setof crimps.
4. A filter according to claim 3, wherein at least some of said filaments are Y-shaped in cross-section.
5. A cigarette having incorporated therein a filter comprising a plurality of longitudinally extending filaments having multiple sets of crimps therein, each of said sets of crimps comprising individual random amplitude crimps which are angularly oilset with respect to the general plane of another of said sets of crimps, wherein at least some of said filaments are of non-circular shape in cross section formed by extrusion through non-circular orifices.
6. A cigarette having incorporated therein the filter of claim 2.
7. A cigarette having incorporated therein the filter of claim 3.
References Cited in the file of this patent UNITED STATES PATENTS 212,392 Millandon Feb. 18, 1879 606,537 Goldenfarb June 28, 1898 1,356,148 Hobert Oct. 19, 1920 1,389,715 Van Gelder Sept. 6, 1921 2,063,743 Kamrath Dec. 8, 1936 2,249,745 Charch et al July 22, 1941 2,326,174 Rutischauser Aug. 10, 1943 2,517,694 Merion et 13.1 Aug. 8, 1950 2,669,001 Keen Feb. 16, 1954 2,750,653 White June 19', 1956 2,780,228 Touey Feb. 5, 1957 2,789,563 Taylor et a1 Apr. 23, 1957 2,792,841 Larson May 21, 1957 2,794,480 Crawford et al. June 4, 1957 2,818,630 Le Boeuf Jan. 7, 1958 2,828,752 Jackson Apr. 1, 1958

Claims (1)

1. A FILTER COMPRISING A PLURALITY OF LONGITUDINALLY EXTENDING FILAMENTS HAVING A MULTIPLICITY OF SETS OF CRIMPS IMPARTED BY MECHANICAL CRIMPING, EACH OF SAID SETS OF CRIMPS COMPRISING INDIVIDUAL CRIMPS WHICH ARE ANGULARLY OFFSET WITH RESPECT TO THE GENERAL PLANE OF OTHER SETS OF CRIMPS, WHEREIN AT LEAST SOME OF SAID FILAMENTS ARE OF NONCIRCULAR SHAPE IN CROSS SECTION.
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3268084A (en) * 1958-12-04 1966-08-23 Celanese Corp Bulked non-wovens
US3752165A (en) * 1971-12-20 1973-08-14 G Harllee Smoke filter plug and process and cigarette made therefrom
US4164438A (en) * 1976-10-05 1979-08-14 Baumgartner Papiers S.A. Method of making transverse flow of cigarette filters
EP1274324A1 (en) * 2000-04-20 2003-01-15 Philip Morris Products Inc. Cigarette filters of shaped micro cavity fibers impregnated with flavorant materials
US20040131790A1 (en) * 2003-01-07 2004-07-08 Voegtli Leo Paul Method for using an ethoxylated alkyl phosphate ester additive as plugmaker processing aid
US20050202993A1 (en) * 2003-01-07 2005-09-15 Voegtli Leo P. Method for using an ethoxylated alkyl phosphate ester additive as a plugmaker processing aid
JP2015525079A (en) * 2012-07-25 2015-09-03 セラニーズ アセテート,エルエルシー Spinneret containing three arc holes and three arc filaments made therefrom
EP2877618A4 (en) * 2012-07-25 2016-04-06 Celanese Acetate Llc Spinneret comprising tri-arc holes and tri-arc filaments produced therefrom

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US212392A (en) * 1879-02-18 Improvement in cigarettes
US1356148A (en) * 1920-03-04 1920-10-19 Hobert Clayton Mattress
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US2789563A (en) * 1948-12-10 1957-04-23 British Celanese Filter elements
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US2818630A (en) * 1954-05-10 1958-01-07 Dow Chemical Co Process for crimping fibers
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3268084A (en) * 1958-12-04 1966-08-23 Celanese Corp Bulked non-wovens
US3752165A (en) * 1971-12-20 1973-08-14 G Harllee Smoke filter plug and process and cigarette made therefrom
US4164438A (en) * 1976-10-05 1979-08-14 Baumgartner Papiers S.A. Method of making transverse flow of cigarette filters
EP1274324A1 (en) * 2000-04-20 2003-01-15 Philip Morris Products Inc. Cigarette filters of shaped micro cavity fibers impregnated with flavorant materials
EP1274324A4 (en) * 2000-04-20 2007-06-13 Philip Morris Prod Cigarette filters of shaped micro cavity fibers impregnated with flavorant materials
US20040131790A1 (en) * 2003-01-07 2004-07-08 Voegtli Leo Paul Method for using an ethoxylated alkyl phosphate ester additive as plugmaker processing aid
US20050202993A1 (en) * 2003-01-07 2005-09-15 Voegtli Leo P. Method for using an ethoxylated alkyl phosphate ester additive as a plugmaker processing aid
US20050202179A1 (en) * 2003-01-07 2005-09-15 Voegtli Leo P. Method for using an ethoxylated alkyl phosphate ester additive as a plugmaker processing aid
JP2015525079A (en) * 2012-07-25 2015-09-03 セラニーズ アセテート,エルエルシー Spinneret containing three arc holes and three arc filaments made therefrom
EP2877618A4 (en) * 2012-07-25 2016-04-06 Celanese Acetate Llc Spinneret comprising tri-arc holes and tri-arc filaments produced therefrom

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