Note: Descriptions are shown in the official language in which they were submitted.
~Q5',~655
This invcntion relates to a filter rod suitable
for use in nlaking filters for cigarettes. In particu-
lar, the present invention involves a cigarette filter
composed of two concentric cylinders of fibrous filter
materials possessing different filtering characteristics
coupled with means for air dilution.
llerctofore, various types of filters have been
dcvised for use in cigarettes in order to screen out
various filterable materials in the smoke generated
during smoking. For example, filters made up of fib-
rous matcrials, such as a cellulose acetate, have been
known for filtering out particulate matter from the
smo~e generatcd during smoking. However, such a fil-
tering medium between a smoker's mouth and the tobacco
column of the cigarette generally required additional
drawing or inhaling forces on the part of the smoker
in order to draw the smoke through the filtering
material. As a result, a practical limit has been
imposed on the amount of particulate matter that can
be filtered out by a particular filtering material
due to,the need to have a pressure drop across a fil-
tcr that can ~e tolerated by a smoker without discom-
fort.
In more recent times, attempts have been made
to dilute the smoke stream from a cigarette with
ventilating air to reduce the quantity of particulate
matter drawn into a smoker's mouth for each puff
while allowing the taste to pass through as taught in
U.S. Patent 3,242,925. Some of these attempts have
use~ bypass arrangements by which a greater or lesser
proportlon of the cigarette smoke can be bypassed
--1--
105'~55
drOUn~ d ~ilt~r mediuln an~ drawn into a smoker's
mouth . I 1l some case~, tlle ~ilters have been provided
with passageways througll wnich a portion oE unfil-
tered smokc can be passcd directly to the smoker's
mouth. Such passageways hav~ usually been provided
dircctly in the filter material and the filter ma-
terial has been constructed so as to be collapsed
manually about the passageway to constrict the size
of the passageway and, thus, reduce the proportion of
unfiltered smoke passing through to a smoker, for
example, as described in U.S. Patent 3,270,750.
On~ of the reasons for utilizing filters with
smoke passag~s was to provide a passageway through
whicll a str~am of concentrated, unfiltered smoke could
pass. Thc impingement of this concentrated smoke
strcam on th~ smoker's tongue and taste buds was be-
lieved to impart a greater taste to the smoke, thereby
lowering the amount of smoke required to be delivered
to the smoker's mouth to achieve a given taste level.
Since a smaller proportion of smoke can be directed
- into the smoker's mouth a concomitant decrease in the
.
amount of particulate matter is drawn into the
smoker's mouth. ~ filter which makes good utiliza-
tion of this principle is described in U.S. Patent
3,860,011 to Norman, et. al. The Norman, et. al.,
filter makes use of a non-deformable rigid tube cen-
tered inside a cylindrical layer of filter material,
such as cellulose acetate, to deliver a high velocity
stream of undiluted and unfiltered smoke into a
smoker's mouth. Though the amount of smoke delivered
--2--
105;~655
is r~duced in quantity, the intensity of smoke has
the effect of enhancing the taste of the cigarette
to the smoker. Norman, et. al., use ventilation air
drawn-in from the surrounding environment to comple-
ment the ~raw resistance of the smoke passage. How-
~ver, it has now been found that the smoke stream,
issuing from the tube of the Norman, et. al., filter,
remains too cohercnt and concentrated, and impinges
; on only a small area of the tongue, and that the smoke
drawn into the smoker's mouth is too hot during the
last few puffs when the tube intake is fairly close to
the burning cone. In addition, the tube is hard to
ccnter in the filter which is undesirable from an
acsthctic viewpoint.
~ccordingly, it is an object of the present in-
vention to provide a filter having a centered smoke
passage of minimal filtering capability with~n a fil-
ter media to accurately direct a concentrated stream
of smoke into a smoker's mouth without any of the
. 20 disadvantages of the Norman, et. al., filter.
- It is another object of the present invention
to accurately regulate the amount of smoke delivered
to the smoker's mouth while simultaneously maximizing
the taste characteristics thereof.
A further object of the present invention is
to eliminate ~he need for additional extensive capi-
tal investment when a manufacturer decides to make
cigarettes from the same tobacco blend having diffe-
rent smoke delivery capabilities by eliminating the
need for additional equipment.
~05Z655
~ riefly, the invention provides a filter for a
cigarette which allows a portion of relatively unfil-
tered smoke to enter a smoker's mouth at a relatively
hi~h con~ntration while reducing the volumetric de-
liv~ry of smoke with drawn-in air from the surrounding
environment. The invention also provides a method
and ~pparatus for making a continuous filter rod for
m~king ci~3arctte filters.
: Th~ filter of the present invention is used in
combination with a cigarette tobacco section and is
joined to the tobacco section by a cylinder or outer
wrap of tipping paper. The filter is composed of two
concentric cylindrical layers of compacted filter
material and a cylinder of perforated or inherently
porous plugwrap paper. The inne~ cylinder defines a
smoke passage of constant cross-sectional area
throughout having a draw resistance for controlling
hc amount of smoke delivered to the smoker's mouth
for a givcn draw. The filter material which makes
up the inner cylinder should be of a structure that
, allows it to have a minimal effect on the filtration
; of the delivered smoke stream but yet creates a
~; sufficient turbulent smoke-flow pattern so as to
lower the temperature and coherency of the smoke
stream drawn into the smoker's mouth. An outer
; layer of filter ~aterial surrounds and is concentric
.. ~ .
to the inner cylinder of filter material. The plug-
wrap paper is porous, e.g., the paper is either in-
herently porous or has numerous perforations some
of which are aligned with perforations in the
105'~655
tipping paper. In either case, the number and size
of the perforations in the tipping paper define the
air flow ~ath through the tipping paper and the layers
of filter material to a smoker's mouth. The flow path
is of a draw resistance to complement the draw resis-
tance of the smoke passage whereby for a given draw a
desired amount of smoke and ventilation air are drawn
into the smoker's mouth.
~; ~ccordingly, the filter of the present inven-
tion delivers through a low resistance filter core to
the smoker's mouth a concentrated smoke stream which
,' is balanced off with additional air from the outside
to yield a smoke stream containing low smoke solids
and a high taste value in each puff de,livered to the
', smoker's mouth.
, The filter materials used to make the respec-
tive concentric cylindrical layers of the filter can
be made of any suitable filter material provided that
', the inner cylinder has a lower resistance to the
-~ 20 passage of smoke than the outer cylinder. Preferably,
the fiiter materials are of cellulosic origin and
most preferably both smoke filter cylinders are made
of cellulose acetate.
The method of the inventlon includes the steps
'~ of generating a first stream of fibrous filter ma-
, terial and a second stream of fibrous filter material,
' of placing these streams in juxtaposition during
travel at a first station while simultaneously en-
, veloping the first stream of fibrous filter material
,-, 30 circumferentially about the second stream of fibrous
~OSf~655
filt~r rnaterial, and of circurnferentially enveloping
a s~re~m of p~er about the juxtaposed streams of
fi~roucs filter material during thcir continued travel
to form a filter rod. ~uring movement of the various
continuous stxeams of materials, the first stream of
fibrous filter material is constricted about the
second stream to frictionally engage the second
stream so that the second stream is positively
gripped for continued travel with the fibrous material.
~n embodiment of this method involves subjecting the
second stream of fibrous filter material to a longi-
tudinal tension greater than the first stream of
fibrous filter material during the rod making process.
The apparatus of this invention includes means
for supplying a first and second continuous streams
of fibrous filter material, a means for maintaining
the second supplied stream of fibrous filter material
under a longitudinal tension greater than the first
supplied stream, a mandrel having a passageway for ~ -
recciving and passage of the second supplied stream
of fibrous filter material, a forming means for re-
,
ceiving the supplied streams of filter material anda stream of paper, said forming means circumferen-
tially envelopes said mandrel to direct the first
supplied stream of fibrous filter material and the
i paper circumferentially about the mandrel and the
second supplied stream of filter material to form a
filter rod. The mandrel is adjustable relative to
the forming means to accurately position the second
stream of filter matexial at the center of the first
stream.
-6-
~05Z655
S 'l'hese and other o~jects and advantages of the
invention will b~come more apparent from the follow-
ing detailed description and appended claims taken
in conjunction with the accompanying drawings in
which:
Figure 1 illustrates a schematic view of an
apparatus for making a filter rod according to this
invention;
Figures 2 through 6 illustrate enlarged
cross-sectional views of the apparatus at various
stages, vicws 2 through 6, of filter formation;
Pigure 7 illustrates a part cross-sectional
view of a cigarette having a filter made in accor-
dance with this invention;
`J, Figure 8 illustrates a cross~sectional view
of thc filter in Figure 7; and
Figure 9 illustrates an enlarged view of
the forming section of the apparatus of Figuxe 1.
I~o~erring to Figure 1, the apparatus 10 for
~0 making the filt~r rod 11 oE the present inv~ntion in-
cludes conventional means, not shown, for supplying
~ , .
two streams of fibrous filter material 12 and 13,
such as cellulose acetate tow. In addition, the
.- ~j .
apparatus 10 includes means 14 and 15 for adjusting
the tension applied on each of the streams 12 and 13
of filter material. A guide means 16, for example,
a funnel or trumpet shaped member, for positioning
in a predetermined path the first stream 12 of tow
for delivery to and in axial alignment ~elow a guide-
shaping means 17, to which has been delivered the
-7-
105Z655
sccond stream 13 of filter materiai, and a rod former
18 of conventional construction for wrapping the first
str~am 12 of filter material about the second stream
13 of filter material and wrapping the two formed con- I
centric cylinders into a filter rod 11.
Referring to Figures 1 and 9, the guide-shaping
means 17, whicll receives the inner stream 13 of fil-
ter material, is positioned downstream of gùide means
1~, which positions the first stream 12 of filter ma-
terial with r~spect to the guide-shaping means 17.
-~ ~uide-shaping means 17 includes a hollow mandrel 19
of elongated, tapered length which passes through
positioning means 20 and into the rod maker 18. The
entrance end 21 (Figure 2) of the guide-shaping means
17 is sized to receive the stream of filter material
'$i 13 with the material in a spread and decrimped manner.
,~j The diameter of the exit end 22 of mandrel 19 can vary
;, depending upon the amount of fibrous material supplied
and the desired bulk dcnsit~ of this material in the
.; 20 ~inAl rod 11, but i5 usually smaller than the en-
trance end 21.
: As illustrated in Figure 2, guide-shaping
~,
means 17 is positioned so that its base is parallel
and contiguous to the flattened U-shaped stream 12
of fibrous material supplied from guide means 16.
.~ Furthermore, the guide-shaping means 17 is adjustable
,~ r~lative to the forming means (not shown) of the rod
,' maker 18. For instance, the guide-shaping means 17
~: can be mounted in a cantilever manner (not shown) on
: 30 a support for adjusting the mandrel 19 vertically or
`
--8--
~05;~655
riz~n~;llly, as dcscribed at column 3, lines 17
through 23 i~clusivc of U.S. Patent 3,860,011, the
disclosure of which is incorporated herein by
ref~rence.
The rod former 18 is of conventional construc-
tion and contains a forming block 22 and a tongue 23
mounted on the topside of the block 22. The block 22
and tongue 23 form a passageway (not shown) into
which the mandrel 19 projects. This latter passage-
way is sized to receive the two streams 12 and 13 of
~ilter material and is tapered internally to form an
inwardly tapering surface for the passageway so that
the passageway gra~ually diminishes in cross-section.
In addition, the rod former 18 includes a conveyor 24
having a conveyor belt 25, such as a continuous fabric
belt, which is driven by a belt drive wheel 26 over
guide rolls 27 through the passageway formed by the
block 22 and tongue 23. The belt 25 is used to move
a stream of porous web 28, e.g., plugwrap paper,
from a suitable supply reel 29 into the passageway
via guide rollers 30 as well as to convey the two
streams 12 and 13 of filter material. The web 28
, has a uniform pattern of perforations 31 (Figure 7)
throughout, or is inherently porous for purposes ex-
plained below.
~s shown in Figure 1, the rod former 18 in-
cludes a pair of folding sections 32 as are known,
s a glue or adhesive applicator 33 and a sealer 34.
The folding sections 32 serve to fold the edges of
the delivered web 28 towards each other in enveloping
105;~655
relationship to the two concentric cylinders of fil- '~
ter material 35 and 36 (Figure 8) which are in a con-
tiguous relationship at this point. The adhesive ;~
applicator 33 serves to apply a line of adhesive on
the top surface of one edge so that the undersurface
of the opposite edge can be sealed thereto by the sub-
sequont folding section 32 and the sealer 34 to form
the filter rod 11. The web 28 may also be of the
typ~ wllich has a heat activated resin preapplied to
th~ surface, in which case, the applicator 33 may be
' eliminated.
,' A suitable cutting mechanism utilizing a knife
,~ 37 is disposed downstre,~m of the sealer 34, as is
known, for cutting the filter rod 11 into predeter-
~, mined lengths 38. Each length may thereafter be cut
'~! into a multiplicity of filters.
~efcrring to Figure 1, in operation, two
~', separate streams of filter material 12 and 13 are
5, fed from,~heir respective supply sources, spread out
... .
,~ 20 and decrlm~od in a conventional fashion as i9 known,
passed through a plasticizer chamber 39 and delivered
' into their respective guide means 16 and 17. The two
streams of filter material 12 and 13 are pulled by
'', conveyor belt 25 and a predetermined speed. As the
flrst stream of filter material 12 passes through
guide means 16, it is spread into a flattened
U-shape (Figure 2) and positioned so as to be in a
parallel and contiguous relationship with the guide-
shaping means 17 as it passes through guide means 20
into the rod maker 18. As filter stream 12 passes
~` .
:"
--10--
105'~6S5
int~ th~ r~d mclker 18 b~twecn t}le folding block 22
and the tongue 23, the fibrous material is gradually
reduc~d ~ircwnf~rentially due to a tapering of the
tonc~ue 23 r~lativ~ to the forming block 22., thereby
causing the filter material 12 to circumferentially
envelop m~ndrel 19 to which has been supplied the
second stream of filter material 13 which is in a
compressed state due to the tapering of mandrel 19.
'1 . ~
., .
~s the filter material 12, which is now in the shape
of a hollow cylinder, passes over the exit 21 of
mandrel 19, it is brought into frictional contact
with the filter material 13 which passes out of man-
drcl 19 within the rod former 18 whereby the first
stream of filter material 12 is juxtaposed in en-
veloping, contiguous, circumferential relationship
~ith the sccond stream of filter material 13. At
the same time., the web of paper 28 is guided into
the rod former 18 underneath the stream of filter
material 12 and i~ folded into a general U-shape.
. .,
~ 20 Continued travel of the streams 12 and 13 of filter
::' material causes filter stream 12 to be further con-
stricted circumferentially about filter stream 13
q~ to grasp or to frictionally engage filter stream 13
under a force sufficient to continuously pull the
remaining portion of filter stream 13 from its
'l supply source.
' The movement of the fibrous material streams
; 12 and 13 is facilitated by the conveyor belt 25 and
i. and the paper web 28 as is known. In addition, the
paper web 28 is subsequently folded about the con-
, .
~os~655 ~:
strictcd concentric, cylindrical layers 12 and 13
with the paper edges scaled together to form a filter
rod 11 of continuous length. The filter rod 11 is
t~len severed into predetermined lengths 38 by the
knife 37.
, Thc streams of filter material 12 and 13 may
I)e ~ed from their respective supply sources at a rate
pproximately equal to the rate of consumption, with
allowances being made for the blooming and decrimping
of the ilter material in accordance with conventional
s practices. The rate of consumption is governed by the
specd of drive wheel 26 which may be driven by any
conventional means.
Figures 3 through 6 illustrate the respective
positions of the two streams of filter material 12
and 13, thc plugwrap paper 28 and the conveyor drive
~, helt 25 just prior to entry into the rod maker 18 and
at various stages inside the rod maker 18. Figure S
illustrates the relationship between the positions of
the streams of filter material 12 and 13 just prior to
the passage of filter stream 13 from the inside of
mandrel 19. At this point, the stream of filter ma-
terial 12 has completely enveloped mandrel 19 and
due to the circumferentially constrictive force applied
.
by the inner surface of the rod maker 18, the stream
of filter material 12 will frictionally engage
stream of filter material 13 upon its exit from man-
drel 19.
!,
In one embodiment of the present invention
filter material stream 13 is placed under a linear
.. .
.
-12
105'~655
ten~ion ~reater than that of filter stream 12 during
th~ rod Eorming proccss. This can be accomplished
~y running the pair of frictional rollers 15 at a
linear surface s~eed helow that of conveyor drive
whecl 26. This results in a lower pressure drop and
higher flavor yield for the inner cylinder 35 (Figure
8) of filter material. At the same time, the filter
; material stream 12 is delivered to the rod maker 18
at a linear surface speed higher than that of the
conveyor drive wheel 26. This can be accomplished
by regulating the speed of the pair of friction rollers
14. This results in a packing of the filter material
in the outer concentric cylinder 36 (Figure 8),
thereb.y giving it a higher prcssure drop and a greater
filtering ability than the inner filter cylinder 35.
Subjecting the inner tow to a greater tension than
the outer làyer of tow 12 permits the attainment of
a greater bulk density of filter material inside the
inner cylinder of filter material 35, thereby giving
the smoke passageway 35 greater structural strength
; so that it remains substantially non-deformable during
.
smoking. The use of a cellulose acetate tow that
still retains some degree of registration for the
.
inner tow 35 of the filter has proven to be of par-
ticular effectiveness, as discussed below, when used
in this embodiment of the invention.
Referring to Figures 7 and 8, a filter 39
formed from the filter rod 11 includes an inner
cylindrical core of coarse fibrous filter material 35
surrounded hy an annular layer of compacted filter
,:~
-13-
-- r
~ 05'~655
material 36, a wrapping of perforated plugwrap paper
40 and an outer wrap of tipping paper 41. The filter
~9 is m~unted, as is known, by means of the outer wrap
of tippin~3 paper 41 on a tobacco column 42 to form a
cigarette. The outer wrap of tipping or mouthpiece
pap~r 41 is provided with a circumferential row of
perforations 43 which are located at about the mid-
section of the filter 39. The number of individual
perforations 43 or the number of rows thereof will
vary with the amount of ventilating air desired to be
drawn in with each puff of the cigarette.
' As shown in Figure 8, the inner cylindrical
core of filter material 35 i8 centered on the axis of
thc filter 39 and form~ a passageway through which
~;~ substantially all of the smoke will pass into the
~, smoker's mouth.
~ Referring to Figure 7, as the smoker takes a
,! puff of his normal puff volume, the flow of smoke
`; through the cigarette into and through the two annu-
lar concentric layers of filter material 35 and 36
and the air flow through the perforations 43 in the
~A~ tipping paper 41 will be proportional to the draw
resistances of the two annular layers of filter ma-
terial 35 and 36. Inasmuch as the draw resistance
of the outer annular layer of filter material 36 is
~ relatively high, there is virtually no delivery of
;' smoke between the tobacco column 42 and the smoker's
.
mouth through the outer annular layer 36.
The smoke generated in 'che burning cigarette
cone during the puffing process predominantly passes
-14-
105'~655
through the inner annular layer of filter material 35
due to its lower pressure drop. This smoke reaches
the smoker's mouth in a relatively concentrated state
and at a relatively high velocity. Even though the
quantity of this smoke i5 reduced when com~ared to
normal filter cigarettes, its relatively unfiltered
state, high concentration and high impingement velo-
city have the effect of enhancing the taste of the
cigarette to the smoker~
That portion of smoke generatcd in the ciga-
rette cone which passes into the outer annular laycr
of filter material 36 from the tobacco column 42
passes back into the inner layer of filtcr materis~l
35 before entering the smoker's mouth thereby achieving
complete radial flow across the fibers for the smoke
entering this outer annular layer. This is due to
the combined effect of the lower pressure drop of the
inner layer of filter material 35 and the laminar
flow of ventilation air drawn in from the surrounding
` 20 environment through perforations 43. This laminar
~, flow of ventilation air tends to compress and form an
annular ring around the smoke strcam within thc inncr
layer of filter material 35. Surprisingly, only a
small amount of actual mixing of the smoke strcam
with the ventilation air occurs before entering thc
smoker's mouth.
In addition to the smoke generated in the
cigarette cone, the smoker's puff will contain, as
indicated above, air drawn in from the surrounding
environmcnt via thc pcrforations 43 in thc tir~r~ing
-15--
1~)5;~655
paper, through the plugwrap paper 40 and the filter
materials 35 and 36 into the smo~er's mouth. Only a
relatively small proportion of the air mingles with
the smoke before it is delivered into the smoker's
mouth. This enhances the possibility of the smoker
getting an increased flavor impression from the de-
livered smoke stream, whereas in conventional ciga-
- rettes utilizing perforated tipping, diluting air
and smoke mix within the filter resulting in the de-
livered smoke stream being substantially prediluted
before impinging in the smoker's mouth. The air drawn
through the perforations 43 appears to form a laminar
~I sheath within the peripheral layer of filter material
and the outer extremities of the inner layer of filter
material and essentially confines or compresses the
smoke path to the central core element. Experimental
and mathematical models have confirmed this effect.
Initial smoke deposition occurs on the whole surface
of the tobacco end of the filter, but from the per-
forations on downstream, the deposition occurs sub-
-~ stantially only on the inner cylindrical coarse layer
of filter material.
The amount of air drawn in from the surrounding
environment can be varied by the number of individual
perforations in the tipping paper and the porosity of
the plugwrap paper. A suitable amount of air to be
drawn in from the outside, measured as percent dilu-
tion though substantially no dilution of the smoke
stream occurs, is from about 15 percent to about 60
percent, preferably from about 25 percent to about
:
- 16 -
,:~
105;~55
55 ~erc~nt, and most ~referably from about 35 percent
to about 45 percent, of the total volume of the puff
delivered to the smoker's mouth.
The amount and velocity of the smoke stream
and of the air stream can be regulated by varying
the respective draw resistances of the two annular
laycrs of filter material and the number of perfora-
ti~ns. The smoke yield of the cigarette can be varied
over a wide range by a choice of proper combinations
of these variables.
~ rhe filter matcrials suitable for use in the
manufactur~ of the filter of the present invention can
be any conventional filter material provided the inner
layer is of such a construction so as to have a lower
pressure drop than the outer annular layer. Preferably
both layers are made from cellulose acetate tows.
The cellulose acetate tow used in the manufacture of
the inner layer of filter material shouid be coarse
enough to offer only minimal draw resistance, have
relativcly little effective filtration efficiency and
should be able to diffuse the smoke stream issuing
from the ~ilter to only a moderate degree. This would
result in an increase in the impingement area on the
..
tongue so as to remove the objection of too concen-
trated a smoke stream, as in the filter of U.S.
Patent No. 3,860,011, but not increase the area of
impingement on the tongue to the eY.tent that you
would ~estroy the essential feature of the filter,
e.g. still yield a much more concentrated smoke
stream than issues from a normal cigarette filter.
.
~ -17-
: 1052655 `
-~ Illustrative of the cellulose ~cetate tows which are
suitable for the inner cylinder of filter material in
this invention are those having denier per filament
values (dpf) of 6 or higher with concomitant total
denier bundle values of from about 10,000 to about
50,000 total denier. Preferably the cellulose ace-
tate tow used in the inner layer of filter material
as a dpf valuo of from about 7 to about 9 with con-
comitant total denier values of less than about
25,000 being limited on the lower end of total denier
values by the capabilities of tow manufacturers.
~he cellulose acetate tow used for the outer annular
layer of filter material in this invention should
' offer more draw resistance than the tow selected
for the inner layer. Illustrative of cellulose ace-
tate tows which are'suitable for use in this outer
J layer of filter material are those of from about 1
~ dpf to about 5 dpf and 10,000 to 50,000 total denier
. , .
values. Preferably the outer tow is one having from
~bout i to about 4 dpf value with a concomitant total
,~ .
` denier value of from about 35,000 to about 45,000.
The inner tow should have a dpf value of from about
1. 5 to `5 times the dpf value for the outer tow,
preferably from about 2 to about 4 times as great
I as the outer tow's dpf value. These ratios should
hold truo for the majority of the tows provided
thcir total denier values fall in the range of from
about 10,000 to 50,000.
.,
A filter whose outer annular layer of filter
tow has bcen substantially deregistered as opposed
-18-
~05'~55
t~ inner l~yer of filter material has proven to
b~ ~.r par~icul~r utility in t}lO pre~ent invention.
Filters o~ this typ~ may b~ prepared by thc use of
a c~llulosc acetate tow that still retains some de-
gree of rcgistration, from about 5 percent to about
30 perc~nt, prcferably from about 10 to 25 percent,
registration for the inner layer of filter tow and
a substantially deregistered tow for the outer
annular layer. The degree of registration of the
respective tow layers may be regulated by varying
the cxtent of blooming and decrimping of the tows
and the amount of tension placed thereon during the
ro~ making process.
~eferring to Fi~ures 7 and 8, the inner layer
of filter material 35 may assume any geometric shape
f but preferably is substantially cylindrical in shape
and of substantially uniform cross-section throughout.
The diameter of the inner layex of filter material
35 preferably is no more than one half of the
A 20 diameter of the filter, e.g., the cross-sectional
arca is preferably less than about 25 percent of the
total cross-sectional area of the filter. A diameter
of from a~out one millimeter ~mm) to about 5 mrn,
prcfcrably from about 3 mm to 4 mm, for the inner
layer of filter material 35 is suitable in the
practice of the present invention.
; .
The apparatus and method have been used
successfully to make 126 mm long, 24.6 mm circum-
ference filter rods on production machinery at a
~ 30 production rate of about 500-600 cigarettes per
:: s
' ~ .
' .
--19--
- . - .. : : ,,
. - : . . -
, . ~ , . ~. , : . . .
- 105;~655
mil~utc u~in~ 2.8 dpf/38,000 total denier cellulose
acetate tow for the outer annular layer of filter ma-
terial and 8.0 dpf/20,000 total denier cellulose ace~
: tate tow for the inner layer of filter material.
The same production rate above was achieved
: using the following cellulose acetate tows for the
. outer annul~r layer of filter material while using
the 8.0 dpf/20,000 total denier tow for the inner
`. laycr.
10.SAMPLE INNER TOW OUTER TOW
4 A 8.0 dpf/20,000 1.8 dpf/38,000
total denier total denier
~ B 8.0 dpf/20,000 3.3 dpf/40,000
., - total denier total denier
,3, C 8.0 dpf/20,000 5.0 dpf/30,000 -
total denier total denier
- Vsing the above filter rods, four 85 mm (21 mm
filter section) sample cigarettes were fabricated and
, submitted to standard analytical smoking tests. The
data listed in Table I below are typical of results
;~ that can be obtainod with the filter of this inven-
' tlon. The yield reductions are calculated on the
basis of the same tobacco column smoked without a
filter.
~,
~:
:~ .
'
., .
-20-
105;~655
T~PsLF~ I
. _
n ~ ~ rt 3
O rJ~t-- O ~ ~-- C tt U~
rt ~ n. rt ~ ~ Q rt 1
,, ID C a~ ~ ~
rt ~ ~t ~
r,t r,t r,t ~- ~ --O
O ~ O :~
3 ~
: dP _
~n r~ o
~D O r
~ o ~ o ~ W
- ' o r,~
'
X
o
vl ~ rJ~ a~ . o ~--~ ~ ~J o
.. , ~n ~o ~ w ~ ~ O
' ~ . . ~ ri~D O . C~
~ W ~ ~D O C~
., - ~ ~ *
* *
* *
w
r.l a. o ~-- w ~ o w
:` W 1~ ~ ~ W :`
w o o
:
~ ul o lJ z ~
`:` ~ `~ ~ ~ ~ o o
:i ~ o ~ - l
o o
t
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*NFDS - Nicotine free dry solids.
, **Not determined.
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, ~*~Duplicate.
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lOS~S5
Using calculations based on the nicotine gen-
erated in the smoke stream of a non-filtered tobacco
column, a filtered tobacco column without perforations
and a filtered tobacco column with perforations it was
found that the perforations in the filter caused a
yield reduction in the amount of nicotine of 9.1%.
Thc cigarettes used in this experiment were the same
as those of sample 2 in Table I.
~xperiments have shown that the use of the
filter of the present invention on cigarettes allows
the use of cellulose acetate tows for the inner smoke
passage having effective filtration efficiencies
wh1ch closely approximates that of present commercial
high taste and high smoke solids (nicotine + NFDS)
cigarettes ~about 40~), and still deliver a high
taste low total solids smoke stream to the smoker.
~n inner smoke passage of minimal filtration effic-
iency and low draw resistance, without the concomi-
tant deficiencies of the Norman, et. al., filter dis-
~,~ Z0 cussed above, is desirable.
The cigarettes were prepared using a conven-
tional citrated web having a Griner porosity of 20
:, .
~3 seconds. The inner tow, 8.0 dpf/20,000 total denier,
. ~ . .
used in the manufacture of the above cigarette fil-
ters was only approximately 80% deregistered. In
the manufacture of the above cigarette filters, the
inner tow's 13 linear surface speed was 80~ that of
~ 2
~ the conveyor belt 25, the linear surface speed of
- which was only 80% that of outer tow 12, thereby
causing a degree of packing higher than normal of
, .,
-22-
:
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. . . .
~05'~655
the outer tow 12 and subjecting the inner tow to a
t~nsion along its longitudinal axis which is greater
than normal and greater than outer tow 12. In work-
ing with tows which are not substantially deregister-
cd a suitabl~ tenqion may bo created by running the
linear sur~ace speed of the tow, in this particular
apparatus the rollers 15, from about 75 to about 95
percent that of the rod making apparatus, which in
this particular case would be the linear surface
speed of conveyor belt 25. In order to achieve the
proper amount of packing of filter material 12 in
the outer annular layer of filter rod 11, the outer
tow may bc fcd at a sueed of from about 5 percent
to about 25 perccnt of the linear surface speed of
, . tllc rod making machine, conveyor belt 25.
.,
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-23-
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