Note: Descriptions are shown in the official language in which they were submitted.
~6~;35
Cellulose fiber is a raw material for many commercial
absorbent products. Because of the constant demand for improve-
ment in the absorbency of these products, there has been a con-
comitant demand for improvement in the absorbency of natural and
regenerated cellulose fiber. Because cellulose is a naturally `~
occurring polymer and is not synthesized by man, its structure
is not susceptible to alternation by copolymerization methods
used in the manufacture of synthetic polymers. However, absorb-
ency of cellulose fibers has been improved by modification of its
chemical structure. the known techniques being: (1) by substi-
tuting new chemical groups at the site of the original hydroxyl
groups of the cellulose fibers, (2) by crosslinking cellulose
chains into a network structure, (3) by introducing new groups `~
and crosslinking them together, or (4) by grafting polymer side
: ,
chains onto the cellulose backbone.
These chemical modifications are generally carried out
in liquid (preferably aqueous) slurries and the resulting modi-
fied fibers are then dried into pulpboard which is subsequently
ground into pulp fluff. While such prior methods have, in the
20 main, produced more absorbent cellulosic fibers, the fibers are ;;~
generally highly brittle and so easily lose their fibrous struc-
ture and reduce to extremely short fibers or powders upon mild
mechanical treatment, as for example, when the pulpboard is
ground into pulp fluff. Additionally, t has been discovered
that these prior products tend to have a high degree of bonding
between the fibers and so tend to form agglomerates of hard knot-
like material similar to solid resin when dried into pulpboard
from water slurries, a process known as hornification. Thes~
knots are not fibrous and so when the pulpboard is ground to
fluff the knots e~l~ther brea~down into powder or remain whole
and, in either form,are unuseable in absorbent dressings. Thus,
while modified cellulose fibers of the prior art have greater ak~
sorbency than unmodified cellulose fibers, they gain this
., - 1 -
. . . . . ,. . :
~ ~06~bi3~5
absorbency at the cost of decreased softness and 109s of other
desirable fibrous qualities.
By the present invention a cellulose fiber (natural or ~ ;
regenerated) of modified chemical structure is provided which
has significantly greater absorbency than an unmodified cellulose
fiber, while retaining the fibrous quality thereof and avoiding
the problems found in the modified cellulose fibers of the prior -
~art.
The invention relates to a cellulose graft copolymer in ~`
; 10 fibrous form and to the method for making the same. -
According to the present invention, there is provided
a cellulose graft copolymer having a backbone of natural or re~
; generated cellulose in fibrous form, which backbone has side
; chains of polymer moieties grafted thereto. This cellulose ;
graft copolymer is a highly water-absorbent, soft, non-flammable,
fibrous material useful for a variety of water or aqueous fluid
absorbent products, such as absorbent dressings in general and,
in particular, diapers, sanitary napkins, tampons, surgical
sponges, and the like. ;
The copolymer side chains on the cellulose backbone are
made up of ionic and non-ionic polymer moieties. On a weight :-
basis, these copolymer side chains may amount to from about 10% ~;
to about 90% of the cellulose graft copolymer, but preferably
from about 50% to about 85% of the cellulose graft copolymer.
These copolymer side chains are ideally made up of alternating ,
ionic and non-ionic polymer moieties, but they may be made up of
i~ alternating groups of ionic and non-ionic polymer moieties. A
particular side chain may even be made up completely of one type `
. ,~., .
of moiety or the other, so long as the overall proportions of -
ionic and non~ionic moieties (discussed below) are maintained. -`
., ,
More specifically, the invention relates to a cellulose ~;
graft copolymer in fibrous form, having a backbone of cellulose
' . :`
.
~0~i4635 ;
and side chains of polymer moieties grafted thereto, said polymer
moieties being selected from the class consisting of ionic and
non-ionic polymer moieties and constituting from about 10.5% to
about 90% by weight of the total weight of the cellulose graft
copolymer, some of said side chain polymer moieties being ionic
polymer moieties and comprising from about 10% to about 80% by
weight of the total weight of the cellulose graft copolymer, and
the other of said side chain polymer moieties being non-ionic
polymer moieties and comprising from about 0.5% to about 60% by
lO weight of the total weight of the cellulose graft copolymer. ;
The ionic polymer moieties may be any ionic polymer -~
moiety as, for example, poly(acrylic acid), sodium poly(acrylate), ;-
; poly(methacrylic acid), potassium poly(methacrylate), poly~vinyl
alcohol sulfate), poly(phosphoric acid), poly(vinyl amine), poly
(4-vinyl pyridine), hydrolyzed poly(acrylonitrile) and the like.
They comprise from about 10% to about 80% by weight of the cellu-
lose graft copolymer, but preferably from about 20% to about 70%
~, by weight of the cellulose graft copolymer.
The non-ionic polymer moieties may be any non-ionic
i 20 polymer moiety, as, for example, poly(methyl methacrylate),
poly(ethyl methacrylate), poly(ethyl acrylate), poly(butyl `
acrylate), poly(vinyl acetate), poly(styrene), poly(butadiene),
poly(isoprene), and the like. They comprise from about 0.5% to
about 60% by weight of the cellulose graft copolymer, but pre-
ferably from about 10% to about 60% by weight of the cellulose
~:, s~
graft copolymer.
The cellulosic fiber used in making the cellulose graft
copolymer fiber of the invention may be natural cellulose fiber
as, for example, wood pulp, hemp, bagasse, cotton, and the like,
30 or a regenerated cellulose fiber as, for example, rayon. ;
It is also contemplated that various modified cellulose
fibers such as, ethers and esters of cellulose may also be used
, , :
'
.. . .. . . . .
~64635
provided that such modifications are not inconsistent with the
teachings of this invention. .
The cellulose graft copolymer fiber is preferably pre~
pared according to the method of the invention by the copoly- .-
merization of (a) fibrous cellulose, (b) a copolymerizable
monomer which is also hydrolyzable after copolymerization to
form an ionic polymer moiety, and (c) a copolymerizable, non- .
.. ionic, at least particularly non-hydrolyzable monomer. The re- - -
sulting unhydrolyzed cellulose graft copolymer is reacted with
an excess of a solution of a strong base to effect hydrolysis .
10 of the hydrolyzable portion of the grafted polymer moieties and - .
convert them to ionic form such as the salts of the strong base, . ,.
while leaving the non-ionic, non-hydrolyzable portion of the .. `~
grafted polymer moieties unchanged.
The method for making a cellulose graft copolymer in ... ~ :~
fibrous form according to the invention comprises copolymerizing ;,
a cellulose selected from the class consisting of natural and
regenerated cellulose fibers, a monomer which is hydrolyzable
after copolymerization to provide ionic polymer moieties, and a . ~
.. non-ionic, at least partially non-hydrolyzable monomer to form , .` `;
, 20 a cellulose graft copolymer having a cellulose backbone with
copolymer side chains grafted thereto, said chains comprising
from 10 to 70% by weight of said graft copolymer, which copoly- ..
mer side chains are made up of hydrolyzable polymer moieties com- `~
prising from 10 to about 80% by weight of said graft copolymer
.~ and non-ionic, non-hydrolyzable polymer moieties comprising from .'~
0.5 to about 60% by weight of said graft copolymer, and subject-
ing said cellulose graft copolymer to hydrolysis, by refluxing `~
1 in a solution of from 1 to 50% by weight of a strong base, to :~
.~. hydrolyze the hydrolyzable polymer moieties on said cellulose
~ 30 graft copolymer to convert the same into ionic polymer moieties, L '~
~ thereby providing a cellulose graft copolymer having a cellulose
backbone with copolymer side chains grafted thereto, which copo-
.,. '`,~ ~ '
- 4 -
':,
i .... . .. .. . . . . . .. . .. . . . . . ...
~69~63~i :
lymer side chains are made up of ionic polymer moieties and non-
ionic polymer moieties.
It should be understood that it is within the scope of
the invention to graft either preformed copolymers of preformed
homopolymers to a fibrous cellulose backbone to prepare the
desired cellulose graft copolymer but the ln situ formation
described above is preferred. It is further within the scope
of the invention to polymerize a mixture of a cellulose and the
two monomers in a single reaction mixture (which is preferred)
10 or to carry out the polymerization in steps by adding first one ~;
monomer and then the other. ~`~
The cellulose graft copolym~r of the invention is pre-
ferably prepared by the copolymerization of (a) fibrous cellulose,
(b) a copolymerizable monomer which is hydrolyzable after co- -
polymerization to form an ionic polymer moiety, and (c) a co-
polymerizable, non-ionic, at least partially non-hydrolyzable
monomer. The reactants may be dispersed and the reaction
carried out in a vapor medium or a non-aqueous medium such as,
for example, acetone, alcohols (e.g., methanol, ethanol, iso-
20 propanol, etc.) benzene, liquid ammonia and the like. Prefer- ~ ~
ably, however, the reaction is carried out in an aqueous medium. ~ --
When in a liquid medium, to promote dispersion and
hence more uniform copolymerization of some monomers (e.g.,
butadiene), it is desirable to add a few drops of an emulsifier `-
¦ to the reaction mixture. Examples of such an emulsifier are
Triton X-100 (one of a class of acrylalkyl polyether alcohols,
sulfonates, and sulfates sold under that trade mark by Rohm and ;
Haas), sodium lauryl sulfate, lauryl trimethyl ammonium chlor- -~
ide, a cationic quaternary ammonium salt of the alkyl trimethyl-
30 ammonium chloride and dialkyl dimethylammonium chloride types -
wherein the average alkyl composition is 90% dodecyl, 9% tetra-
decyl, and 19% octadecyl and which is supplied as a solution
' ,. ..
5 _ ~
1~64635 ~ ~
of 33% active ingredient, 17% sodium chloride, and 50% water
under the trade mark Arquad 12 by Armour and Company, lauryl
pyridinium chloride, and the like~
The copolymerization reaction may be initiated with
an ionic initiator (e.g., alkali hydroxides) a cationic initia~
tor (e.g., a Lewis acid such as boron trifluoride), or even ~ -
radiation (ultraviolet, gamma, or X-radiation). It is pre-
ferred, however, that the polymerization be carried out by the `~
free-radical copolymerization mechanism using a free-radical -
10 initiator such as, for example, ceric ion, ferrous ion, cobaltic -~
ion, (N~I4)2S2O~ cuprous ion, and the like. The ceric ion ini-
tiator is preferred. ~` -
Because most free-radical reactions are inhibited by - -~
the presence of oxygen, it is desirable to flush out essential~
ly all the oxygen frorn the reaction mixture and reaction vessels ` ~;
by bubbling a non-oxidizing gas, such as nitrogen, helium, argon, ;
etc., through the system prior to the addition of the free-ra~
~ .
dical initiator.
The pH range used for the reaction depends on the ~ ;~
particular initiator used. One could use anywhere from a highly ~ ;
acidic pH (pH 0.8-2.3) to a highly basic pH (pH 12-14), depend- ~;
ing on the particular initiator. For the preferred ceric ion
initiator, the pH should be acidic, i.e., less than seven and
preferably about 0.8 to about 2.3.
The temperature of the copolymerization reaction may `~
be anywhere from room temperature (i.e., 20 to 30C.) to the `~
normal boiling point of the lowest boiling component of the mix- ~ ~
ture. If the reaction is carried out under greater than at- ~ -
mospheric pressure, the temperature could then be raised above
the boiling point of the lowest boiling component of the mixture.
The reaction mixture may also be cooled below room temperature, ;~
if desired.
- 6 -
, , . ~ :
~;463~ :
The hydrolyzable polymer moieties of the resulting `
cellulose graft copolymer fibers are hydrolyzed by reacting the ~ -
fibers, preferably under reflux, with an excess of a solution
of a strong base, e.g., sodium hydroxide, potassium hydroxide,
lithium hydroxide, and like bases~ The concentration of this
solution may be from about 1% to about 50% by weight and the
temperature of hydrolysis may be from room temperature to reflux.
One preferred procedure for forming the cellulose
graft copolymer fibers of this invention is as follows. A ceric
ammonium nitrate initiator solution is prepared by dissolving
ten millimoles of the ceric salt per 100 ml of lN nitric acid,
; as described by E. Schwab, et al, TAPPI, ~5, 390 (1962). Wood
pulp is then dispersed in water and dry nitrogen is bubbled `
through the dispersion with stirring. A small amount of the
initiator solution is then added to the stirred dispersion with ;~
continued bubbling of nitrogen gas, and then a mixture of hydro-
lyzable and non-hydrolyzable monomers as described above is
added. The total weight of monomer added is usually at least
four times the weight of wood pulp present. After the reaction
has been allowed to continue for the desired period of time
(generally from about one to about four hours), the resulting -;
; cellulose graft copolymer fibers are washed, hydrolyzed as
described above, washed again and dried.
The preferred ionic polymer moiety is sodium poly(a-
crylate), and the preferred non-ionic polymer moieties are poly- ` ~-~
(methyl methacrylate), poly(ethyl acrylate), and poly(butad1ene).
It was discovered in early experimentation that the use of acryl- '
ic acid as a starting hydrolyzable monomer for introduction of
the preferred ionic polymer moiety led to considerable homopoly-
merization of the hydrolyzable monomer rather than graft copo-
lymerization of both hydrolyzable and non-hydrolyzable monomers
to the cellulose backbone. Therefore, other hydrolyzable acrylic
~ ~ 7 ~
., , ,,,, ,,, ,, , ,,, ,,, , :,:
~ ' ," ',, " ~ " ' ' " : ~ ' ' ' : ,' : '
~C~69~63~
monomers were tested leading to the use of acrylonitrile as the
starting hydrolyzable monomer for the introduction of the pre-
ferred ionic polymer moiety. The non-hydrolyzable monomers used
are, of course, just the monomer forms of the desired non-ionic
polymer moieties' viz.: methyl methacrylate, ethyl acrylate,
and butadiene. After the oopolymerization reaction is complete,
hydrolysis of the poly(acrylonitrile) moieties as described above
yields ionic "alkali metal poly(acrylate)" moieties.
The cellulose graft copolymer fibers of the invention
have significantly greater absorbency (from about four to about
nine times greater) than unmodified wood pulp, while still re- ~-
taining a fibrous form. In addition, the cellulose graft co- ~
polymer fibers of the invention are not subject to the brittle- ~ `
ness and hornification as are prior art modified cellulose fibers.
A further unexpected useful quality of the hydrolyzed
cellulose graft copolymer fibers of the present invention is that
they are non-flammable, while unmodified cellulose fibers are
" highly flammable. The absorbent materials made from the fibers -~
of the present invention may thus advantageously be used where
stringent precautions must be taken against fire, e.g., in
hospitals, nursing homes, etc.
The cellulose graft copolymer fibers of the invention
may be used alone or mixed with unmodified cellulose fibers or
` other absorbent material in the manufacture of absorbent napkins, "
tampons, sponges, and the like. The fibers of the invention
may also be made into non-woven fabrics, which fabrics are use-
ful in the manufacture of absorbent napkins, tampons, sponges
and the like. --
The cellulose graft copolymer of the invention and its
method of preparation will be more fully understood from a con~
sideration of the following examples, which are given for the ~
purpose of illustration and are not to be construed as limiting
the invention in spirit or in scope except as set ~orth in the
., ,
8 -
.: .-,. -- . . ~ , . .. . .
,,. ~ , . .. . . . . ...
.. . ., .,, . ,. - . . ::, ,,,,,, : ~ ~ ,
635
appended claims.
Example I
Ceric ammonium nitrate initiator solution is prepared
by dissolving the ceric salt in lN nitric acid to a concentra-
tion of 10 millimoles/100 ml. Into a three-necked flask fitted
with a stirrer, a gas bubbling tuba, and a stopper funnel are
placed 500 ml. of water and 5 g of wood pulp. The wood pulp is
dispersed in the water by stirring and dry nitrogen is bubbled `
through the dispersion for fifteen minutes with continuous stir- -
ring. To the stirred dispersion is added 12.5 ml of the ceric
ammonium nitrate initiator solution with continued nitrogen '
; bubbling. A mixture of 5.5 g of methyl methacrylate and 15.0 g
of acrylonitrile is added to the stirred dispersion, and the
whole is allowed to react for one hour at room temperature. At
the end of one hour, the resulting unhydrolyzed cellulose graft
copolymer fibers are transferred to a Buchner funnel and are
washed thoroughly with water and acetone. The washed fibers are
then refluxed with an excess of 6% sodium hydroxide solution for
one-half hour to hydrolyze the hydrolyzable polymer moieties.
The resulting hydrolyzed cellulose graft copolymer fibers are
washed thoroughly with water, pressed to remove excess water and -
dried in an oven at 100C. to form a pulpboard. The composition
of the resulting product is given in Table I (sample No. 5). ;~
Example II
The procedure of Example I is repeated, except that
varying amounts of methyl methacrylate and acrylonitrile are - -
used. The amounts of methyl methacrylate and acrylonitrile used,
together with 'he compositions of the resulting products, are ;-~
shown in Table I. ;;
Example III
The process of Exam~le II is repeated, except that -`
ethyl acrylate is substituted for the methyl methacrylate used ~ ~
, "
_ g _
therein. The amounts of ethyl acrylate and acrylonitrile used -
and the compositions of the resulting products are given in Table
II.
Example IV
The pulpboard products of Examples I, II and III are
shredded into pulp fluff and then formed into absorbent pads
For comparative purposes, a pad consisting of unmodified wood
pulp is also prepared. The pads are tested for fluid retention
using a Porous Plate Testing Apparatus, as described in detail
10 in Textile Res. J., 37, pp. 356-366, 1967. Briefly, this test
involves placing the sample pad in what is essentially a Buchner
funnel having a porous bottom plate and holding the sampl~e in
place by applying thereon a standard weight to maintain a stand- -
ardized confining pressure. The porous plate is placed in con-
,
tact with a reservoir of fluid and the sample is allowed to
absorb fluid through the porous plate until saturated. By main-
taining the sample at essentially the level of the reservoir,
the fluid absorbed is subjected to essentially a zero hydraulic -
head with respect to the reservoir. To determine fluid reten-
tion, the saturated sample is elevated with respect to the fluid
reservoir, thereby imposing a hydraulic head upon the fluid
absorbed, the head being arbitrarily chosen as 36 inches of -~
fluid. The apparatus is provided with means for directly mea-
suring the volume of fluid retained under this hydraulic head.
Retention values are reported as the volume retained per unit
weight of absorbent fiber. The resulting values are reported -
` in Table III and IV under the heading, Uncompressed Retention
Values. The fluid used in these experiments is a 1% by weight
aqueous, sodium chloride solution
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~064~;35
which closely approximates the absorbent characteristics of
menstrual f luid .
Example V
The materials of Examples I, II and III are shredded ;~
into pulp fluff and combined with an equal quantity of unmodi-
:,
fied wood pulp fluff. The fluff mixture is formed into compress~
ed cylindrical tampons having a density of 0.4 gm/cc, a diameter
of about 0.57 inches and an axial length of about 1.68 inches.
The capacity of these tampons to absorb a 1% by weight aqueous
sodium chloride solution under simulated in-use conditions is
determined by allowing one end of the tampon to be submerged in
the solution for a period of 20 minutes while maintaining the
sides of the tampon under a confining pressure of 24 inches of
water maintained by enveloping the tampon in a hydraulically in- ~-
`: ; :
flated polyethylene sleeve. Excess fluid is drained from the ~ !~
tampon, the pressure is released and the weight of water absorbed
by the tampon is determined and reported in Tables III and IV as
the tampon capacity in units of volume of fluid absorbed per unit
weight of tampon.
Referring to Tables III and IV, it can be seen that
the grafted cellulose sample (1) containing only the non-ionic
polymer moiety methyl methacrylate (MMA in Table III and EA in
~` Table IV) exhibits an absorption capacity which differs only
moderately when compared to the wood pulp sample. It should be
noted in this connection that while MMA and EA grafted moieties l;-
are generally non-ionic and hence hydrophobic, they have been
subjected to a hydrolysis step and accordingly, the surface
characteristics of the grafted fibers have been affected, parti-
cularly that of the EA grafted fibers which explains the varia-
:. -; ~ .
tion in absorption properties with respect to wood pulp.
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At the other extreme, the samples which have been grafted with
only an ionic polymer (Na-Acry in Tables III & IV) are reported
as gelled, i.e., gell formation has occurred in the outside of `~
the absorbent sample tested and has precluded further absorption
of the fluid into the central portions of the sample. In marked
contrast to these extremes, it can be seen that samples having,
in accordance with this invention, a combination of ionic and
non-ionic polymer moieties grafted to the cellulose backbone,
exhibit a dramatic increase in their absorptive properties, both -
with respect to the retention of fluid in uncompressed absorbent
pads and the absorbent capacity of compressed fibrous bodies such
as tampons. It is also apparent that within the preferred ranges
of ionic and non-ionic polymer moiety compositions, absorption
" ~ .
properties are maximized.
Example VI
The products of Examples I, II and III are tested to
:
determine their ability to maintain their fibrous characteristics
after mechanical processing by grinding them into pulp fluff with
: :.
a T~eber hammer mill using a 1/4-inch screen. The knot content
of the resulting fluff is determined according to the constant -;
~' air-blowing technique wherein a 5 gram sample of the fluff is
placed in the bottom of a lO00 ml. burette and air is admitted
through the pet cock at the bottom at a controlled constant flow
rate of 3.5 cubic feet per minute to get a tumbling action of
the sample, thereby causing the individualized fiber of the sam-
ple to escape through the open top end of the burette while
-: , ,.
' leaving the heavier knots or clumps at the bottom. The knots
are then removed and weighed and the knot content (as a weight
percent of the sample) is determined and reported in Tables V and
VI. Additionally, samples of the fibrous fluff are examined and
the arithmetic average fiber length determined
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1~646;~
by microscopy. Fibers are introduced into a microscopic slide
and covered with a glass plate. A photo micrograph is taken of
this slide at a magnification of 53 times and the length of
each fiber photographed is measured. An arithmetic average of
these fiber lengths is calculated and these results are reported ~-
in Tables V and VI.
Referring now to Tables V and VI, it can be seen that ; ;~;
as long as the quantity of non-ionic polymer moiety is maintained
within the herein prescribed range, the grafted cellulose copoly- ;~-
mer exhibits the same physical properties with respect to fiber
length and knot content after mechanical treatment, as does wood ;~
pulp. However, as the quantity of non-ionic polymer moiety is `
decreased in a fiber containing ionic polymer moiety, knot con~
tent increases dramatically, making that weight portion of the ~ ~-
ground pulp fluff unsuitable for use in a dressing. With respect -
to fiber length, it can be seen that when the non-ionic polymer
moiety is decreased below the herein prescribed limits, the aver-
age fiber length has decreased to the point where, in effect, the
matérial may be considered a powder. In this condition, the
material cannot be used as a substitution for fibrous wood pulp. ~ ``;
Example VII ~ -
:i .~.. ~
A dispersion of 5 g of wood pulp in 500 ml of water is
- prepared in a three-necked flask fitted with a stirrer, a gas ~-
:: :"
bubbling tube, and a stopper-funnel. Dry nitrogen is bubbled ',~',;~.! "
through the dispersion for five minutes. Twelve and one half ~ -;
`j milliliters of ceric ammonium nitrate initiator solution as i~
, described in Example I is then added along with few drops of
,. . .
Triton X-lO0 emulsifier while the bubbling of nitrogen and the
stirring are continued. To this stirred, nitrogen-flushed dis- `
30 persion is added a mixture of 23 g of acrylonitrile and 2 g of -~
liquified butadiene. The system is then closed to the atmosphere
and the whole is allowed to react at room temperature for four ~-
:; '.'
:. , ;
i3S
hours. At the end of this time, the resulting cellulose graft
copolymer fibers are transferred to a Buchner funnel and are
washed thoroughly with water and acetone. The washed fibers are
refluxed with an excess of 1.5 N sodium h~droxide solution for
30 minutes, washed in water, and then dried in a hot air oven
at 60C. The resulting fibrous hydrolyzed cellulose graft co-
polymer has a maximum capacity of 13 cc per gram and a retention -
of 8.4 cc per gram in the uncompressed state. It has a tampon `
capacity of 5.2 cc per gram when used in a 50% by weight blend ~;
with untreated wood pulp in a tampon having a density of 0.4
grams per cc. The fluid used in all these tests is 1% sodium
chloride solution.
Example VIII ~ ;
A dispersion of 5 g of cotton (Johnson & Johnson Red ~ ~
Cross Brand) in 500 ml of water in a three-necked flask fitted - ;
with a stirrer, a gas bubbling tube, and a stopper funnel is
stirred as nitrogen is bubbled through the dispersion ~or 30
minutes. To this stirred, nitrogen-flushed dispersion is added ~ ;
12.5 ml of ceric ammonium nitrate initiator solution having a
20 concentration of 1 mole of ceric ammonium nitrate per liter-of `~
lN nitric acid. After further stirring and nitrogen bubbling for
; one minute, a mixture of 12.5 ml of acrylonitrile and 12.5 ml
of ethyl acrylate is added to the stirred dispersion, and the `
whole is allowed to react at room temperature for one hour.
The resulting fibers are washed and hydrolyzed as in Example I.
The resulting hydrolyzed cellulose graft copolymer fibers are ; -
~; ! ':`
pressed to remove excess water and dried in an oven at 100C to
form a sheet. The sheet is ground into a fluff form which ex-
- hibits excellent fibrous characteristic and absorbency.
Example IX `
Samples are prepared consisting of 2 gram pads of com-
pressed and uncompressed grafted cellulose copolymer fibers
" ~ :
- 20 -
106~35 ` ~
corresponding in composition to samples 2-8 of Table III and 2-7 ~
:.:
of Table IV. Additionally, further pads are prepared using
fibers made in accordance with the method of Examples I, II and ~
III and corresponding in all respect to the samples enumerated -~-
....
above with the exception that these further samples were not
hydrolyzed and so had the composition shown in Table II and IV
for samples 2-8 and 2-7, respectively, under the heading, Un-
hydrolyzed Product. Similarly, hydrolyzed and unhydrolyzed ;~
;~ samples of the cellulose acrylonitrile butadiene graft copolymers
.. . . .
; 10 of Example VII are made. The hydrolyzed and unhydrolyzed sample ~
pads are subjected to a flame test wherein each sample is gripped ~-;
: . :
in a pair of tongs and held in the hottest portion of the flame
from a Bunsen burner for ten seconds. The sample is then re-
?,
- moved. Samples which, after removal, exhibited a subsisting flame
or glow are characterized as flammable and the remaining samples
are characterized as non-flammable. The results of this test
. :
! shows in each instance, that the unhydrolyzed fibers are highly `
;~ . .
flammable whereas the hydrolyzed fibers are non-flammable.
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