US3501361A - Method for producing cigarette filters - Google Patents
Method for producing cigarette filters Download PDFInfo
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- US3501361A US3501361A US688291A US3501361DA US3501361A US 3501361 A US3501361 A US 3501361A US 688291 A US688291 A US 688291A US 3501361D A US3501361D A US 3501361DA US 3501361 A US3501361 A US 3501361A
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- United States
- Prior art keywords
- filter
- tow
- filaments
- fibers
- polyolefin
- Prior art date
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- 235000019504 cigarettes Nutrition 0.000 title description 24
- 238000004519 manufacturing process Methods 0.000 title description 9
- 239000000835 fiber Substances 0.000 description 43
- 239000000779 smoke Substances 0.000 description 36
- 241000208125 Nicotiana Species 0.000 description 25
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 25
- 239000004014 plasticizer Substances 0.000 description 25
- 239000004793 Polystyrene Substances 0.000 description 24
- 229920002223 polystyrene Polymers 0.000 description 23
- 229920002301 cellulose acetate Polymers 0.000 description 21
- 229920000098 polyolefin Polymers 0.000 description 17
- 239000000463 material Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 12
- 239000002245 particle Substances 0.000 description 11
- 239000000155 melt Substances 0.000 description 8
- -1 polypropylene Polymers 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- 239000004743 Polypropylene Substances 0.000 description 6
- 239000000654 additive Substances 0.000 description 6
- 239000000853 adhesive Substances 0.000 description 6
- 230000001070 adhesive effect Effects 0.000 description 6
- 230000008901 benefit Effects 0.000 description 6
- 238000002788 crimping Methods 0.000 description 6
- FLKPEMZONWLCSK-UHFFFAOYSA-N diethyl phthalate Chemical compound CCOC(=O)C1=CC=CC=C1C(=O)OCC FLKPEMZONWLCSK-UHFFFAOYSA-N 0.000 description 6
- 229920001155 polypropylene Polymers 0.000 description 6
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 5
- 206010041662 Splinter Diseases 0.000 description 5
- 206010061592 cardiac fibrillation Diseases 0.000 description 5
- 230000002600 fibrillogenic effect Effects 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 229960002715 nicotine Drugs 0.000 description 5
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 5
- 230000000996 additive effect Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000000391 smoking effect Effects 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000035945 sensitivity Effects 0.000 description 2
- 238000009987 spinning Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- URAYPUMNDPQOKB-UHFFFAOYSA-N triacetin Chemical compound CC(=O)OCC(OC(C)=O)COC(C)=O URAYPUMNDPQOKB-UHFFFAOYSA-N 0.000 description 2
- OVOUKWFJRHALDD-UHFFFAOYSA-N 2-[2-(2-acetyloxyethoxy)ethoxy]ethyl acetate Chemical compound CC(=O)OCCOCCOCCOC(C)=O OVOUKWFJRHALDD-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 208000003028 Stuttering Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 235000013773 glyceryl triacetate Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012943 hotmelt Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 235000019505 tobacco product Nutrition 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229960002622 triacetin Drugs 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
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
- A24D3/0229—Filter rod forming processes
- A24D3/0237—Filter rod forming processes by extrusion
Definitions
- This invention relates to a tow material that is particularly useful for the manufacture of tobacco smoke filters. More particularly, this invention relates to a modified type of crimped polyolefin which, due to its plasticizer sensitivity and the structure of its filaments, is more suitable as an intermediate for the production of cigarette filters than are those heretofore known and used crimped tows made of melt spun filaments. Specifically, this invention relates to plasticizer bondable crimped filter tows the fibers of which are obtained by drafting and fibrillating a melt extruded film of polypropylene containing polystyrene as an additive, and to tobacco smoke filters made therefrom.
- cellulose acetate or other like spun fibers have enjoyed such popularity in the tobacco filter industry.
- cellulose acetate filter tow is its sensitivity to liquid, essentially nonvolatile, plasticizers.
- a nonvolatile, oily, liquid plasticizer such as glycerol triace'tate can be added to the towtoproduce a firm filter element.
- This firmness of the cellulose acetate filter element is produced by the plasticizer liquid gradually dissolving and bonding together adjacent fibers within the filter at random points of contact.
- Such a rigid filter structure can then be easily and cleanly cut into smaller segments the size of a filter tip.
- a cellulose acetate filter tow has numerous other features which are highly desirable, if not mandatory, for any tobacco smoke filter, especially those to be used on cigarettes. These additional features include being nontoxic, nonodorous, white, and stable to storage under varying conditions of humidity and temperature. However, even in view of these many attributes, filter tow made from cellulose acetate or other like spun filamentary materials surfaces. In addition to this they are relatively weak and,
- these crimps have been produced mechanically by means of intermeshing gear-like elements, by means of a stutter-box type crinkler, or by twisting the fibers, setting the twist, and then untwisting.
- this crimping operation is somewhat time consuming and adds to the over-all expense of the finished filtered product it nevertheless has I been reasonably successful and is widely accepted by the industry since it not only results in the breaking up of those channels which would otherwise exist in the intersticesbetween the fib'e'r s, but
- a tow made of melt spun polyolefin fibers can be crimped .to contain 30 to 4 crimps/inch and the resulting product has ample strength to permit its use in commercial filter forming equipment.
- a high degree of crimp is given to a cellulose acetate tow, i.e., 20 crimp/inch. or higher, it is rendered too weak to be processed into fibers on existing commercial equipment operating at practical speeds.
- an object of this invention is to produce a new and improved polyolefin type of crimped tow which can be used as a tobacco smoke filter intermediate.
- Another object of this invention is to disclose a plasticizer sensitive and structurely strong polyolefin type material that can be used to produce a filter tow having an extremely high crimp count.
- Yet another'object of this invention is to disclose a highly crimped polyolefin tow, the filaments of which contain tiny hairlike splinters or fibrils which are firmly attached to and form an integral part of the filaments.
- a further object of this invention is to disclose a polyolefin tow that can be highly crimped, fibrillated and treated with high boiling, oily plasticizers to give a firm cigarette filter.
- a still further object of this invention is to disclose an inexpensive cigarette filter that'is formed from a highly crimped, fibrillated and plasticizer treated polyolefin tow which is very effective for the removal of the tar and nicotine found in the effluent stream of tobacco smoke.
- FIGURE 1 is a diagrammatic illustration on an enlarged scale of a bundle of smooth surface filaments such as cellulose acetate;
- FIGURE 2 is a diagrammatic illustration on an enlarged scale of a bundle of'fibrillated and bonded polyolefin-polystyrene filaments made in accordance with this invention.
- FIGURE 3 illustrates a cigarette having attached to the tip thereof a tobacco smoke filter made from fibrillated and bonded polyolefin-polystyrene filaments.
- reference numeral 10 is used "to generally designate a bundle of crimped cellulose acetate fibers.
- the outer surface of each fiber 12 is substantially smooth and thus large channels or openings 14' exist between the varifous fibers through which the tobacco smoke may pass without encountering any filtering action.
- the fibers are shown bonded together at 16 by a suitablehigh boiling, oily plasticizer.
- FIGURE 2 illustrates a bundle 18 of fibers taken from 9.
- highly crimped filter tow formedin accordance with is that the polyolefin-polystyrene fibers 20 are flat and ribbon-like in appearance with a thickness of from 15 to 100 microns which permits them to be fibrillated to produce the desired results. Since the fibers 20 are fractured during their preparation, numerous fine hairlike fibrils 22 of varying thickness and length will be produced and will extend from their surface in all directions. As can be seen, these fine splinter fibrils 22, which have a thickness from about 0.5 micron to about 15 microns, extend into the spaces 24 that exist between the various fibers 20 and therefore allow less of the solid tobacco smoke constituents carried in the efiiuent stream of smoke to pass therethrough.
- the filaments 20 may be fibrillated to the point that the splinter or fibril filaments 22 represent from to 70 percent of the total make-up of the crimped filter tow 18. Below this value of fibrillation there are not enough of these fine fibrils in the tow to render it very effective as a filter material while above this value the main continuous trunk portion of the filaments 20 is so reduced in size as to substantially weaken the tow thereby making it too weak to be processed into filter rods on standard equipment.
- the preferred ratio of fibrillation of the tow has been found to be 20 to 50 percent splinter fibrils and 50 to 80 percent ribbon-like filaments.
- the total number of filaments in the filter tow which includes both the ribbon-like filaments 20 and fibrils 22, can vary over a wide range since their thickness can vary from 0.5 to about microns for the fibril type to over 100 microns for the heavier ribbon-like type. Therefore, in terms of total denier it can be said that the tow 18 may vary from about 20,000 total denier to 150,000 total denier.
- polyolefin fibers per se cannot be bonded together with a high boiling, oily plasticizer.
- the filaments were made plasticizer sensitive by placing at least 30 percent by weight of polystyrene in the polyolefin spinning dope.
- the tow 18 is rendered plasticizer sensitive and can be bonded together by a plasticizer as illustrated at 26 in FIGURE 2.
- this capability of the polyolefin-polystyrene filter material of 'this invention is of utmost importance.
- the percentage of polystyrene added is somewhat critical with the optimum amount of polystyrene additive having been found to' be between 35 and 50 percent by weight. Lower amounts of polystyrene give a filter tow that cannot be hardened by the application of a plasticizer while, conversely, too much polystyrene .(over 60 percent) makes the tow too weak to withstand the tensions applied to it during the vfilter rod making process.
- the type of polyolefin in the mixture of polyolefin and styrene from which the filaments of the tow are made can Concerning the polystyrene, it can have a molecular weight of from 5,000 to 500,000; the preferred range in molecular weight being from 10,000 to 100,000.
- the softening point of the polystyrene should fall between C. and 160 C., and preferably between C. and C. Both polymers may contain substituent grouping providing such groupings do not change the softening points beyond those stipulated.
- the fibrillated filaments from which this novel filter tow is made can be produced by any of the known techniques for fracturing elongated polymeric strands so that splinter type fibrils extend from them.
- the preferred technique is the one disclosed in pending application 446,059 filed Apr. 6, 1965, and assigned to the same assignee as this invention.
- This method of fibrillating ribbon-like filaments is simple, economical, and can be carried out in one continuous operation. For example, a blend of the polyolefin and the polystyrene is melt extruded into a film which is then continuously drafted and fibrillated into fractured, ribbon-like filaments. A number of these filaments are gathered together to produce the tow of this invention.
- the polyolefin-polystyrene filter tow should be crimped.
- the number of crimps placed in filter tow 18 should be sufiiciently high to raise the bulk factor of the tow to the point where it fills out the cigarette filter rod.
- This crimp value has been found to be between 15 and 50 crimps/inch with the preferred number of crimps being between 20 and 30.
- These crimps can be applied to the tow by any suitable method such as a conventional stuffer box crimping device known in the teX- tile art.
- EXAMPLE 1 Highly fibrillated filaments formed from a melt eX- truded film of 50 percent polypropylene (mol. wt. 32,000) and 50 percent polystyrene (mol. wt. 10,000) were prepared according to the procedures given in the aforementrunk portion of the continuous filaments and that these .fibrils had a thickness of from 1 to 10 microns. A 250-ft.
- tow length of tow of 60,000 total denier was produced from these filaments and was given 30 crimps/inch through the use of a stuifer box.
- the crimped tow was then processed into filter rods (25.4 in. circumference) on a machine similar to the one disclosed in the Crawford-Stevens US. Patents 2,794,239 and 2,794,480. During the passage of the tow through the machine it was opened or bloomed out at one point and sprayed with diethyl phthalate.
- the plasticizer treated and paper (cigarette paper) wrapped rods contained 10 percent diethyl phthalate; after 60 minutes they had sufficient rigidity so that they could be cleanly cut into 15 mm. filter segments.
- tar signifies the liquid-solid particles of cigarette smoke. Since it is known that the nicotine is an integral part of these particles a filter which removes particles by impingement removes the same percentage or amount of nicotine as tar.
- EXAMPLE 2 Highly fibrillated filaments formed from a melt extruded film of 65 percent polyethylene (mol. wt. 42,000) and 35 percent polystyrene (mol. wt. 12,500) were prepared according to the procedure disclosed in application Ser. No. 446,059. A 200-ft. crimped (25 crimps/inch) tow of 65,000 total denier was prepared from these filaments which consisted of about 35 percent of the fibril type and 65 percent of the heavier and parallel type. During the passage of the tow through the cigarette filter rod making machine it was bloomed out at one point and sprayed with dibutyl phthalate. The plasticizer treated and cigarette paper wrapped rods contained 8 percent plasticizer. About 45 minutes after the filter rods were made they were firm enough to be cleanly cut into 15 mm. filter tip segments.
- Highly fibrillated filaments formed from a melt extruded film of 45 percent polypropylene (mol. wt. 60,000) and 55 percent polystyrene (mol. wt. 15,000) were prepared according to the procedure disclosed in application Ser. No. 446,059.
- a ZOO-ft. crimped tow (30 crimps per inch) of 70,000 total denier was prepared from these filaments which consisted of about 50 percent the fibril type and 50 percent the heavier parallel type.
- the final paper wrapped filter rods were firm enough to be cleanly cut into small mm. filter segments about 1 hour after they were prepared.
- a tobacco smoke filter element which comprises mixing from 30 to 60 percent of a polystyrene with a melt of a polyolefin, extruding said melt to form ribbon-like filaments, fibrill-ating the melt extruded polyolefin-polystyrene filaments until fine splin- .ter fibrils are formed theron in the ratio of about 20 to 50 percent fibrils to about to 50 percent ribbon-like filaments, gathering thefibrillated filaments into a filter tow, subjecting the filter tow to a crimping operation until the filaments thereof have between about 15 and 50 crimps per inch, placing a liquid plasticize-r on the highly crimped filter tow, forming the plasticizer treated highly crimped filter tow into the shape of the desired tobacco smoke filter element, and severing the formed filter tow into suitable length filter elements after the tow has become firm.
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- Cigarettes, Filters, And Manufacturing Of Filters (AREA)
Description
March 17, 1970 TOUEY ETAL METHOD FOR PRODUCING CIGARETTE FILTERS ori inal Filed Sept. 22, 1965 SMOKE FLOW O C C A B o T FIG.2
TOBACCO CIGARETTE PAPER F I LT ER WRAPPER POLYO LE FlN- POLYSTRENE HIGHLY CRIMPED, FIBRILLATED, AND PLASTICIZER TREATED TOBACCO SMOKE FILTER GEORGE P TOUEY ROBERT C. MUMPOWER INVENTORS ATTORN YS United States Patent 3,501,361 METHOD FOR PRODUCING CIGARETTE FILTERS George P. Touey, Kingsport, Tenn., and Robert C. Mumpower, Bristol, Va., assignors to Eastman Kodak Company, Rochester, N .Y., a corporation of New Jersey Original application Sept. 22, 1965, Ser. No. 489,329, now Patent No. 3,393,120, dated July 16, 1969. Divided and this application Oct. 18, 1967, Ser. No. 688,291
Int. Cl. D04h 3/16 US. Cl. 156-167 1 Claim ABSTRACT OF THE DISCLOSURE Method for producing a tobacco smoke filter element in a continuous manner from a polyolefin-polystyrene tow material.
This application is a division of Touey and MumpoWer U.S. Ser. No. 489,329, filed Sept. 22,1965 now Patent No. 3,393,120, which is a continuation-impart of US. Ser. No. 65,941, filed Oct. 31, 1960', now abandoned.
This invention relates to a tow material that is particularly useful for the manufacture of tobacco smoke filters. More particularly, this invention relates to a modified type of crimped polyolefin which, due to its plasticizer sensitivity and the structure of its filaments, is more suitable as an intermediate for the production of cigarette filters than are those heretofore known and used crimped tows made of melt spun filaments. Specifically, this invention relates to plasticizer bondable crimped filter tows the fibers of which are obtained by drafting and fibrillating a melt extruded film of polypropylene containing polystyrene as an additive, and to tobacco smoke filters made therefrom.
There exists in the vapor phase of tobacco smoke certain small, but yet highly important, quantities of various gaseous and solid compounds which exhibit a specific toxic action on the human tissue with which they come into contact. Thus in an effort to reduce or, if possible, completely eliminate the presence of these deleterious tobacco smoke constituents the tobacco industryhas extensively investigated the use of various types of tobacco smoke filters. Of all these various types of tobacco smoke filters tested those made from crimped textile-like strands of cellulose acetate are by far the most widely accepted.
There are a number of reasons why cellulose acetate or other like spun fibers have enjoyed such popularity in the tobacco filter industry. For example, not only is cellulose acetate relatively inexpensive and readily available, but it can be continuously and rapidly processed into filter rods on existing commercial equipment. Another important attribute of cellulose acetate filter tow is its sensitivity to liquid, essentially nonvolatile, plasticizers. By this it is meant that during the continuous processing of the filter rods a nonvolatile, oily, liquid plasticizer such as glycerol triace'tate can be added to the towtoproduce a firm filter element. This firmness of the cellulose acetate filter element is produced by the plasticizer liquid gradually dissolving and bonding together adjacent fibers within the filter at random points of contact. Such a rigid filter structure can then be easily and cleanly cut into smaller segments the size of a filter tip.
The use of such a plasticizer hardening or bonding agent in producing tobacco smoke filter elements has many obvious advantages over the use of conventional adhesives 3,501,361 Patented Mar. 17, 1970 "ice of the type which make the tow tacky as soon as they are applied. For example, the used of a tacky adhesive is objectionable since they cause the rapidly moving tow to adhere to the various parts of the filter making machine. Also, the use of such conventional tacky adhesives requires the removal of water or an organic solvent from either the tow or the finished filter rod. 3
Of course a cellulose acetate filter tow has numerous other features which are highly desirable, if not mandatory, for any tobacco smoke filter, especially those to be used on cigarettes. These additional features include being nontoxic, nonodorous, white, and stable to storage under varying conditions of humidity and temperature. However, even in view of these many attributes, filter tow made from cellulose acetate or other like spun filamentary materials surfaces. In addition to this they are relatively weak and,
in the case of cellulose acetate, somewhat more expensive to produce than certain other types of synthetic materials.
It is now well known to the art of tobacco smoke filtration that a fiber which has a smooth outer surface and is'inherently straight cannot successfully be used Without physical modification in a filter since the fibers will lie in a more or less parallel arrangement and thus permit smoke particles to channel through its length and into the smokers mouth. The first efforts by the industry to alleviate this basic and undesirable characteristic of such straight, smooth filamentary materials was by subjecting them to a crimping operation. This crimping operation was accomplished through the use of various methods and apparatus designed for placing any desired crimp count (defined as one-half the number of fiber bends per linear inch) into a substantially straight filamentarymaterial. For instance, these crimps have been produced mechanically by means of intermeshing gear-like elements, by means of a stutter-box type crinkler, or by twisting the fibers, setting the twist, and then untwisting. Needless to say, although this crimping operation is somewhat time consuming and adds to the over-all expense of the finished filtered product it nevertheless has I been reasonably successful and is widely accepted by the industry since it not only results in the breaking up of those channels which would otherwise exist in the intersticesbetween the fib'e'r s, but
also increases the bulk factor of the fibers.
This crimping of fibrous tow materials is not, however,
without its own drawbacks. Besides the added time and of cellulose acetate and other like fibrous filters, it was proposed that certain solid and liquid additives be applied to thetow. Certain melted waxy combinations wereflthu's sprayed upon the spread out tow to produce a mass of discontinuous hairlike projections which extended from the otherwise smooth surface of the cellulose acetate fibers. The fact that these hairlike projections extended into the space between the fibers produced a more torturous path for the smoke particles and as a result many of the particles which wuold normally channel through the filter by passing between the parallel filaments were impinged on the hairlike protrusions. However, as might be imagined, the production of such fibrils on the tow is not an easy or simple task but involves the spraying of a hot melt of wax onto the moving tow. This spraying operation entails the use of an elaborate spray booth as well as a system for recovering the overspray. Furthermore, for best results this spraying operation had to be performed just prior to the processing of the tow into the filter elements. This meant that the manufacturer of the filter elements had to apply the additive to the tow which is not nearly as desirable a condition as when the manufacturer can purchase a tow which does not have tobe specially treated in order to yield an effective filter.
A second and later approach taken to improve the tar removal properties of cellulose acetate tow included the addition of certain crystallizable types of compounds to the spinning solution. These additives became a part of the spun fibers and as they gradually exuded to the surface they produced tiny protrusions which extended from the, otherwise smooth fiber surface into the interstices between the fibers. However, this migration of the incorporated solid compounds to the surface of the fibers required a considerable length of time. Therefore a somewhat indefinite length of storage time was required before the solid particles started to appear on the surface of the fibers. Also, during the passage of the tow through the many parts of the filter rod making machine there was a tendency for the extruded particles to fall off or be wiped off the fibers. Furthermore, these filter tows were still 1 inherently weak and could not be crimped to any appreciable extent without breaking.
In an effort to completely alleviate the undesirable low crimp count and bulk factor characteristics of heretofore known tow materials we disclosed in our copending application Ser. No. 65,941, of which this is a continuation-impart, a crimped tow of melt spun polyolefin fibers. These new fibers can be made into a tow that has certain very definite advantages over a cellulose acetate type tow as a filter intermediate. For example, in addition to being potentially less expensive than a tow of cellulose acetate fibers it is considerably stronger and can, therefore, be processed to have a much higher crimp count without beingrendered too weak tobe processed into filter rods on'existing commercial equipment. By way of example, a tow made of melt spun polyolefin fibers can be crimped .to contain 30 to 4 crimps/inch and the resulting product has ample strength to permit its use in commercial filter forming equipment. By comparison, when a high degree of crimp is given to a cellulose acetate tow, i.e., 20 crimp/inch. or higher, it is rendered too weak to be processed into fibers on existing commercial equipment operating at practical speeds.
'Another advantage of a tow of melt spun polyolefin the smoking of the tobacco product the filter shows no tendency whatsoever to become soggy or distorted because of the retention of water from the smoke or from the smokers mouth. Also, its low moisture pickup prevents the filter from drying the smoke and thereby making it tain' advantages over a tow of cellulose acetate fibers it too has some disadvantages. These disadvantages include the fibers 'is its hydrophobic nature. Because of this during fact that conventional, inexpensive high boiling plasticizers such as glycerol triacetate, triethylene glycol diacetate, diethyl phthalate, 'dibutyl phthalate, and the like will not fuse the fibers together atrandom points to produce a firm filter rod as they do in the case of cellulose of the easy-to-cut, thin paper wrappers commercially Lacet'ate tow filters. This means that a difiicult-to-cut, heavy paper wrap must beplaced around the rod instead 4 used for cigarette filter rods. Or, as an alternative to the heavy paper wrapper, it means that an expensive heating step might have to be applied to the filter rods to fuse some fibers together into a rigid structure. It could also require the use of a tacky adhesive with its accompanying problems to harden the filter rods. Furthermore, these spun fibers of polyolefin have smooth surfaces which let more smoke particles channel through than would occur if the fibers contained bumps, protrusions or other fibrils extending from their surfaces. According to this invention it has beenv found that a plasticizer sensitive and structurely strong tow material can be produced which forms an exceptionally good intermediate for the production of tobacco smoke filters. This new'and novel material is obtained by drafting and fibrillating a melt extruded film of polypropylene containing a polystyrene additive. The ribbon-like, fiat fibrous material thus produced is easily formed intoa filter element on standard equipment operated in a conventional manner to give a tobacco smoke filter having very high tar and nicotine removable capabilities.
Therefore, an object of this invention is to produce a new and improved polyolefin type of crimped tow which can be used as a tobacco smoke filter intermediate.
Another object of this invention is to disclose a plasticizer sensitive and structurely strong polyolefin type material that can be used to produce a filter tow having an extremely high crimp count.
Yet another'object of this invention is to disclose a highly crimped polyolefin tow, the filaments of which contain tiny hairlike splinters or fibrils which are firmly attached to and form an integral part of the filaments.
- A further object of this invention is to disclose a polyolefin tow that can be highly crimped, fibrillated and treated with high boiling, oily plasticizers to give a firm cigarette filter.
A still further object of this invention .is to disclose an inexpensive cigarette filter that'is formed from a highly crimped, fibrillated and plasticizer treated polyolefin tow which is very effective for the removal of the tar and nicotine found in the effluent stream of tobacco smoke.
These and other objects and advantages of this invention will be more apparent upon reference to the following description, appended claim, specific working examples, and drawings wherein:
' FIGURE 1 is a diagrammatic illustration on an enlarged scale of a bundle of smooth surface filaments such as cellulose acetate;
' FIGURE 2 is a diagrammatic illustration on an enlarged scale of a bundle of'fibrillated and bonded polyolefin-polystyrene filaments made in accordance with this invention; and
FIGURE 3 illustrates a cigarette having attached to the tip thereof a tobacco smoke filter made from fibrillated and bonded polyolefin-polystyrene filaments.
With continued reference to the accompanying figures and with initial attention directed to FIGURE 1, reference numeral 10 is used "to generally designate a bundle of crimped cellulose acetate fibers. As will be noted, the outer surface of each fiber 12 is substantially smooth and thus large channels or openings 14' exist between the varifous fibers through which the tobacco smoke may pass without encountering any filtering action. For purposes of illustration the fibers are shown bonded together at 16 by a suitablehigh boiling, oily plasticizer.
FIGURE 2 illustrates a bundle 18 of fibers taken from 9. highly crimped filter tow formedin accordance with is that the polyolefin-polystyrene fibers 20 are flat and ribbon-like in appearance with a thickness of from 15 to 100 microns which permits them to be fibrillated to produce the desired results. Since the fibers 20 are fractured during their preparation, numerous fine hairlike fibrils 22 of varying thickness and length will be produced and will extend from their surface in all directions. As can be seen, these fine splinter fibrils 22, which have a thickness from about 0.5 micron to about 15 microns, extend into the spaces 24 that exist between the various fibers 20 and therefore allow less of the solid tobacco smoke constituents carried in the efiiuent stream of smoke to pass therethrough. This coupled with the fact that these fine fibrils 22 are uniformly dispersed between the coarser trunk or continuous portion of the fibers 20' is believed to be the reason why filters formed from this novel tow can remove a higher percentage of the smoke particles (tar) found in cigarette smoke than other similar heretofore known filter materials without at the same time producing such a high pressure'drop (resistance to draw) that they would be impractical for use on cigarettes. Furthermore, since these hairlike protruding fibrils 22 are firmly attached by one end to the larger trunk portions of the filament and are, therefore, an integral part of the main ribbon-like filaments 20 they do not fall off nor can they be wiped oil? as the tow 18 passes through the many parts of the cigarette filter rod making machine.
The filaments 20 may be fibrillated to the point that the splinter or fibril filaments 22 represent from to 70 percent of the total make-up of the crimped filter tow 18. Below this value of fibrillation there are not enough of these fine fibrils in the tow to render it very effective as a filter material while above this value the main continuous trunk portion of the filaments 20 is so reduced in size as to substantially weaken the tow thereby making it too weak to be processed into filter rods on standard equipment. The preferred ratio of fibrillation of the tow has been found to be 20 to 50 percent splinter fibrils and 50 to 80 percent ribbon-like filaments. The total number of filaments in the filter tow, which includes both the ribbon-like filaments 20 and fibrils 22, can vary over a wide range since their thickness can vary from 0.5 to about microns for the fibril type to over 100 microns for the heavier ribbon-like type. Therefore, in terms of total denier it can be said that the tow 18 may vary from about 20,000 total denier to 150,000 total denier.
As is well known, polyolefin fibers per se cannot be bonded together with a high boiling, oily plasticizer. Thus, to avoid the use of tacky adhesives the filaments were made plasticizer sensitive by placing at least 30 percent by weight of polystyrene in the polyolefin spinning dope. Because of the presence of the plasticizer-soluble polymer in the melt spun polyolefin filaments 20, the tow 18 is rendered plasticizer sensitive and can be bonded together by a plasticizer as illustrated at 26 in FIGURE 2. As will be appreciated by those working in the filter art, this capability of the polyolefin-polystyrene filter material of 'this invention is of utmost importance. The percentage of polystyrene added is somewhat critical with the optimum amount of polystyrene additive having been found to' be between 35 and 50 percent by weight. Lower amounts of polystyrene give a filter tow that cannot be hardened by the application of a plasticizer while, conversely, too much polystyrene .(over 60 percent) makes the tow too weak to withstand the tensions applied to it during the vfilter rod making process.
The type of polyolefin in the mixture of polyolefin and styrene from which the filaments of the tow are made can Concerning the polystyrene, it can have a molecular weight of from 5,000 to 500,000; the preferred range in molecular weight being from 10,000 to 100,000. The softening point of the polystyrene should fall between C. and 160 C., and preferably between C. and C. Both polymers may contain substituent grouping providing such groupings do not change the softening points beyond those stipulated.
The fibrillated filaments from which this novel filter tow is made can be produced by any of the known techniques for fracturing elongated polymeric strands so that splinter type fibrils extend from them. However, the preferred technique is the one disclosed in pending application 446,059 filed Apr. 6, 1965, and assigned to the same assignee as this invention. This method of fibrillating ribbon-like filaments is simple, economical, and can be carried out in one continuous operation. For example, a blend of the polyolefin and the polystyrene is melt extruded into a film which is then continuously drafted and fibrillated into fractured, ribbon-like filaments. A number of these filaments are gathered together to produce the tow of this invention.
For best results the polyolefin-polystyrene filter tow should be crimped. The number of crimps placed in filter tow 18 should be sufiiciently high to raise the bulk factor of the tow to the point where it fills out the cigarette filter rod. This crimp value has been found to be between 15 and 50 crimps/inch with the preferred number of crimps being between 20 and 30. These crimps can be applied to the tow by any suitable method such as a conventional stuffer box crimping device known in the teX- tile art.
A further understanding of the invention will be had from a consideration of the following examples that may be used in actual commercial practice and are set forth to illustrate certain preferred embodiments.
EXAMPLE 1 Highly fibrillated filaments formed from a melt eX- truded film of 50 percent polypropylene (mol. wt. 32,000) and 50 percent polystyrene (mol. wt. 10,000) were prepared according to the procedures given in the aforementrunk portion of the continuous filaments and that these .fibrils had a thickness of from 1 to 10 microns. A 250-ft.
length of tow of 60,000 total denier was produced from these filaments and was given 30 crimps/inch through the use of a stuifer box. The crimped tow was then processed into filter rods (25.4 in. circumference) on a machine similar to the one disclosed in the Crawford-Stevens US. Patents 2,794,239 and 2,794,480. During the passage of the tow through the machine it was opened or bloomed out at one point and sprayed with diethyl phthalate. The plasticizer treated and paper (cigarette paper) wrapped rods contained 10 percent diethyl phthalate; after 60 minutes they had sufficient rigidity so that they could be cleanly cut into 15 mm. filter segments.
Several of these filters were attached to standard cigarettes which had been 85 mm. in length but which were shortened to 70 mm. to compensate for the length of the filters. These filter cigarettes, (now 85 mm.) were smoked to 35 mm. butt lengths on an automatic smoking machine. The weight percentage of smoke particles (tar) removed by the filters is shown in Table 1. This method of smoking filter cigarettes and determining the efficiency of -,their filters (percent smoke solids or tar removed) is described by WQV. McConnell, R. C. Mumpower, and
G. P. Touey in Tobacco Science, vol. 4, pp. 55-61 (1960). The pressure drops (resistance to draw) of the filters were also obtained and the average value was calculated (Table l); The method for determining pressure TABLE 1 Average pressure drop Percent of ten filters tar Filter (15 mm.) (inches H2O) removed Fibrillated filaments of polypropylene and polystyrene- 2. 1 44 Melt spun smooth surfaced filaments of polypropylene and polystyrene 2. 34
The term tar signifies the liquid-solid particles of cigarette smoke. Since it is known that the nicotine is an integral part of these particles a filter which removes particles by impingement removes the same percentage or amount of nicotine as tar.
EXAMPLE 2 Highly fibrillated filaments formed from a melt extruded film of 65 percent polyethylene (mol. wt. 42,000) and 35 percent polystyrene (mol. wt. 12,500) were prepared according to the procedure disclosed in application Ser. No. 446,059. A 200-ft. crimped (25 crimps/inch) tow of 65,000 total denier was prepared from these filaments which consisted of about 35 percent of the fibril type and 65 percent of the heavier and parallel type. During the passage of the tow through the cigarette filter rod making machine it was bloomed out at one point and sprayed with dibutyl phthalate. The plasticizer treated and cigarette paper wrapped rods contained 8 percent plasticizer. About 45 minutes after the filter rods were made they were firm enough to be cleanly cut into 15 mm. filter tip segments.
Several of these filter tips were tested for pressure drop and for their effectiveness in removing tar from cigarette smoke in the manner described in Example 1. The results obtained are listed in Table 2. Commercial 15 mm. filters made from a tow of cellulose acetate fibers den./fil.) were also tested for pressure drop and for their effectiveness in removing tar from cigarette smoke. For comparative purposes these results are also listed in Table 2.
Highly fibrillated filaments formed from a melt extruded film of 45 percent polypropylene (mol. wt. 60,000) and 55 percent polystyrene (mol. wt. 15,000) were prepared according to the procedure disclosed in application Ser. No. 446,059. A ZOO-ft. crimped tow (30 crimps per inch) of 70,000 total denier was prepared from these filaments which consisted of about 50 percent the fibril type and 50 percent the heavier parallel type. During the passage of the tow through the rod making machine it was bloomed out at one point. and treated with 10 percent di- (Z-ethylhexyl) phthalate by means of a wicking device which wiped the plasticizer on the filaments. The final paper wrapped filter rods were firm enough to be cleanly cut into small mm. filter segments about 1 hour after they were prepared.
Several of these filter tips were tested for pressure drop and for their efiec-tiveness in removing tar from cigarette smoke in the manner described in Example 1. A 15 mm. commercial filter of cellulose acetate (1.6 denier/filament fibers) was tested in a similar manner. The results shown in Table 3 indicate that a filter of the finest commercially 8 available cellulose acetate fibers is still not'qui-te as effective as one which can be prepared from the inexpensive and novel tows disclosed in this invention.
* See footnote to Table 1.
From the foregoing it is readily apparent that the highly-crimped, fibrillated, plasticizer sensitive polyolefin-polystyrene filter tow of this invention ofiers numerous advantagesover those tows heretofore known and used to produce tobacco smoke filter elements. For example,
the polyolefin-polysty-rene,
not only is the tow easily bonded by known and commercially acceptable plasticizer, thus alleviating the need .-for using heavy wrapper papers or tacky adhesives, but ribbon-like filaments are strong enough to permit high fibrillation and easy processing in existing commercial equipment. This high degree of fibrillation results in a more effective tar and nicotine filter than was heretofore though possible. Furthermore, not only are the filaments less expensive to produce than conventional cellulose acetate type fibers, but the high fibrillation and extremely high crimp count that can be placed in the new filaments greatly increases the bulk factor of a filter tow made from the fibers. The desirable ramifications of this high bulk factor, including the fact that with a higher crimp level less fibers of a given denier/ filament are required to fill out the filter element to its proper size, is readily apparent to those working in the filter tow art. The other advantages of the new polyolefinpolystyrene tow, such as its low moisture retention characteristic and ease of production to name only a few, will also be appreciated by those working in the field.
This invention may be embodied in other specific forms without departing from the spirit or essential characteristics thereof.
What is claimed and desired to be secured by the United States Letters Patent is:
1. The method of producing a tobacco smoke filter element which comprises mixing from 30 to 60 percent of a polystyrene with a melt of a polyolefin, extruding said melt to form ribbon-like filaments, fibrill-ating the melt extruded polyolefin-polystyrene filaments until fine splin- .ter fibrils are formed theron in the ratio of about 20 to 50 percent fibrils to about to 50 percent ribbon-like filaments, gathering thefibrillated filaments into a filter tow, subjecting the filter tow to a crimping operation until the filaments thereof have between about 15 and 50 crimps per inch, placing a liquid plasticize-r on the highly crimped filter tow, forming the plasticizer treated highly crimped filter tow into the shape of the desired tobacco smoke filter element, and severing the formed filter tow into suitable length filter elements after the tow has become firm.
References Cited UNITED STATES PATENTS 3,026,226 3/1962 Touey 156180 7 3,080,611 3/1963 Jarrett 156-167 3,220,904 11/1965 Touey 156167 3,336,174 8/1967 Dyer 156 -167
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US489329A US3393120A (en) | 1965-09-22 | 1965-09-22 | Polyolefin tow for cigarette filters |
US68829167A | 1967-10-18 | 1967-10-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3501361A true US3501361A (en) | 1970-03-17 |
Family
ID=27049679
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US688291A Expired - Lifetime US3501361A (en) | 1965-09-22 | 1967-10-18 | Method for producing cigarette filters |
Country Status (1)
Country | Link |
---|---|
US (1) | US3501361A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4752348A (en) * | 1985-03-29 | 1988-06-21 | Celanese Corporation | Localized liquid additive applicator system for continuous cylindrical product |
US20130137561A1 (en) * | 2010-05-12 | 2013-05-30 | British American Tobacco (Investments) Limited | Filter Additive |
US10524500B2 (en) * | 2016-06-10 | 2020-01-07 | R.J. Reynolds Tobacco Company | Staple fiber blend for use in the manufacture of cigarette filter elements |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3026226A (en) * | 1957-12-09 | 1962-03-20 | Eastman Kodak Co | Process of manufacturing filters |
US3080611A (en) * | 1960-11-08 | 1963-03-12 | Eastman Kodak Co | Method for the production of cigarette filters |
US3220904A (en) * | 1960-05-23 | 1965-11-30 | Eastman Kodak Co | Method of making a rigid filter for cigarettes |
US3336174A (en) * | 1965-04-06 | 1967-08-15 | Eastman Kodak Co | Method of making a fibrous filter product |
-
1967
- 1967-10-18 US US688291A patent/US3501361A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3026226A (en) * | 1957-12-09 | 1962-03-20 | Eastman Kodak Co | Process of manufacturing filters |
US3220904A (en) * | 1960-05-23 | 1965-11-30 | Eastman Kodak Co | Method of making a rigid filter for cigarettes |
US3080611A (en) * | 1960-11-08 | 1963-03-12 | Eastman Kodak Co | Method for the production of cigarette filters |
US3336174A (en) * | 1965-04-06 | 1967-08-15 | Eastman Kodak Co | Method of making a fibrous filter product |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4752348A (en) * | 1985-03-29 | 1988-06-21 | Celanese Corporation | Localized liquid additive applicator system for continuous cylindrical product |
US20130137561A1 (en) * | 2010-05-12 | 2013-05-30 | British American Tobacco (Investments) Limited | Filter Additive |
US10524500B2 (en) * | 2016-06-10 | 2020-01-07 | R.J. Reynolds Tobacco Company | Staple fiber blend for use in the manufacture of cigarette filter elements |
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