Technical Field
[0001] This invention pertains to the art of applying polymeric finishes to textile fibers
and fabrics.
Backqround of the Invention
[0002] Unfinished polyester fiberfill fibers exhibit fiber scroop and a rough hand due to
high interfiber friction. It is known in the art that a silicone finish will lower
interfiber friction and thereby make polyester fiberfill fibers acceptable for commercial
uses where fiber scroop can be a problem. For example. DacronO Hollofil II. available
from E. I. du Pont de Nemours, is finished with a silicone which lowers the interfiber
friction associated with fiberfill fibers and thereby imparts a soft, down-like hand.
However, silicone finishes adversely affect the flammability and latex bondability
of polyester fiberfill fibers.
[0003] The unblended polyester fabrics produced for the garment industry are hydrophobic.
This leads to two problems in the use of a polyester fabric. Hydrophobic fabrics are
not easily treated in an aqueous medium unless a surfactant is added to aid in wetting
the fabric. Even more importantly. garments made from a polyester fabric do not readily
absorb perspiration from the skin of the wearer. This imparts a hot or clammy feel
to the polyester garment which leads to consumer discomfort and in turn to consumer
resistance of polyester fabrics. It would be advantageous to develop a durable hydrophilic
finish for a polyester fabric.
[0004] It is also known in the art of fabric finishing that a crosslinkable organic polymer,
when applied to a synthetic fabric, will provide various useful properties, e.g.,
reduction of the static electricity associated with such fabrics. For example. U.S.
Patent 3.213.053 to Kendrick discloses that an antistatic composition of a crosslinkable
terpolymer of: (1) 5% to 10% of glycidyl methacrylate: (2) 35% to 55% of an alkali
metal salt of a styrene sulfonate: and (3) 35% to 60% of methoxypoly(ethylene glycol)
methacrylate wherein the poly(ethylene glycol) chain has a molecular weight from 250
to 500, will reduce the static electricity of a synthetic fabric when applied as a
finish. French Patent No. 1.427.787 discloses that a copolymer of: (1) from 2% to
20% of an ethylenically unsaturated epoxide or a corresponding methylol compound:
with (2) from 98% to 80% of an ester of an ethylenically unsaturated carboxylic acid
and an alkylphenoxy polyethylene glycol, will reduce the static electricity or synthetic
fabrics when applied to said fabrics as a fabric finish. Swiss Patent No. 513,282
discloses that a copolymer composed of: (1) from 80% to 90% of an ester of an alkyl
polyethylene glycol having an alkyl residue with 1 to 3 carbon atoms and an average
molecular weight of from 300 to 1000 and an ethylenically unsaturated polmerizable
carboxylic acid: (2) 5% to 10% of a etherified N-methylolamide of an ethylenically
unsaturated polymerizable carboxylic acid: and (3) 5% to 10% of an ethylenically unsaturated
polymerizable compound containing at least one acid group capable of imparting solubility
in water, e.g. acrylic acid, will reduce the static electricity associated with a
synthetic fabric and enhance the soil release properties of such a fabric.
Summary of the Invention
[0005] In accordance with the present invention. it has been found that the process which
comprises (a) treating fibers and fabrics with a neat composition, solution or dispersion
containing:
(i) at least 0.001% by solution weight or neat composition weight of an acid catalyst,
and
(ii) from 0.1% to 15% by solution weight or neat composition weight of a graft copolymer
prepared by grafting to a poly(oxyalkylene) from 0.5% to 50% by graft copolymer weight
of an N-(oxymethyl)- acrylamide having the formula:

wherein R1, R , R . and R are hydrogen or monovalent hydrocarbon radicals containing from 1
to 6 carbon atoms each and may be the same or different, and a poly(oxyalkylene) of
the formula:

wherein R3 is a hydrocarbon radical having a valence of a and containing up to 21 carbon atoms,
a is an integer having values between 1 and 4, X is an oxygen, nitrogen or sulfur
atom, R6 is a hydrogen atom or hydrocarbon radical containing up to 6 carbon atoms and may
contain hydroxyl, amino or mercaptyl groups, n is an integer from 2 to 4, and z is
an integer having a value from 2 to 800, and
(b) drying and curing said treated fiber at between 100°C and 170°C, which imparts
to the fiber a durable finish which increases the lubricity of the fiber manifested
by a lowering of interfiber friction without adversely affecting the flammability
or the latex bondability of the fiber.
[0006] In a particular embodiment of the invention, the poly(oxyalkylene) preferably has
the formula:

wherein y is an integer from 2 to 5000, and the other designations are as above. The
graft copolymer produced from such poly(oxyalkylenes) imparts the property of hydrophilicity
to the fabric as manifested by a decrease in the time necessary to wet the fabric.
[0007] The graft copolymers useful in the present invention may be prepared as described
in copending U.S. application Serial No. 307,211 filed September 30, 1981.
Details of the Invention
[0008] Graft copolymers useful in the present invention having an N-(oxymethyl) acrylamide
grafted onto a poly(oxyalkylene) compound are prepared by a method which comprises
adding an N-(oxymethyl) derivative of acrylamide monomer as hereinafter more fully
described and a suitable catalyst to an agitated bath of the poly(oxyalkylene), whereby
all of said components are intimately admixed at a temperature at which reaction occurs,
and maintaining said temperature until said graft copolymer of acrylamide derivative
on poly(alkylene oxide) is obtained.
[0009] In general, the poly(oxyalkylene) compounds of this invention contain oxyethylene.
oxypropylene, oxybutylene groups or both oxyethylene groups and higher oxyalkylene
groups such as oxypropylene and oxybutylene groups. either in random or block distribution
in their molecules, and have molecular weights (number average) in the range of 100
to 35,000, and, preferably, in the range of 1,500 to 4,000. These poly(oxyalkylene)
compounds may be made by processes well known in the art by reacting an alkylene oxide
or mixtures of alkylene oxides with an aliphatic compound, which may be saturated
or contain some aliphatic unsaturation, having from one up to as many as four active
hydrogen atoms, such as water, monohydroxylic alcohols such as ethanol, propanol.
and allyl alcohol: dihydroxylic alcohols such as ethylene glycol and monoethylether
of glycerine: trihydroxylic alcohols such as glycerine and trimethylolpropane: and
tetrahydroxylic alcohols such as sorbitol. Especially preferred active hydrogen compounds
are allyl alcohol and glycerine. The poly(oxyalkylene) products of such reactions
will have linear or branched oxyalkylene or mixed oxyalkylene chains, and such chains
will terminate with hydroxyl groups. Although the poly(oxyalkylenes) may be hydroxyl
terminated, some or all of these hydroxyl groups may be etherified by reaction with
a dialkyl sulfate such as diethyl sulfate or an alkyl halide such as ethyl chloride.
These terminal hydroxyl groups may also be etherified with alkyl-halohydrins such
as 2-chloro ethanol. This will yield a poly(oxyalkylene) that has a terminal hydroxyl
group, which is preferred because of its ability to condense with the N-(oxymethyl)
functionality that is introduced into the poly(oxyalkylene) to facilitate crosslinking
of the poly(oxyalkylene) chains.
[0010] The grafting monomers employed in preparing the copolymers useful in the present
invention are substituted acrylamide monomers having the formula

wherein R
1, R
2, R
3 and R
4 may be the same or different and are hydrogen atoms or a monovalent hydrocarbon radicals
containing from 1 to 6 carbon atoms. These acrylamide derivative monomers are generally
homopolymerizable monomers with a reactive, cross-linkable pendent group or groups.
Illustrative suitable monomers are methoxymethyl acrylamide. ethyoxymethyl acrylamide,
N-butoxymethyl. acrylamide. allyloxymethyl acrylamide, N-butoxymethacrylamide and
preferably, N-methylolacrylamide and N-(iso-butoxymethyl)-acrylamide.
[0011] A grafting catalyst is employed which is a free-radical initiator. The choice of
such initiator is not narrowly critical, as any one of a wide variety of known inorganic
or organic initiators of free-radical polymerization may be used. The choice of initiator
will generally depend on the particular combination of reactants from which the graft
copolymer will be prepared. For example. if a given grafting monomer will self-condense
at the grafting reaction temperature necessary for a given catalyst, then the reaction
mixture will form an undesireable gel: i.e. the graft copolymer will cure before application
to the fiber. Therefore, a catalyst must be chosen such that the grafting reaction
temperature will not cause the grafting momomer self-condense. Exemplary of suitable
initiators are azobisisobutyronitrile: hydroperoxides such as t-butyl peroxypivalate,
di-t-butyl peroxide, and t-butyl perbenzoate: peroxycarbonates such as diethyl peroxydicarbonate
and diisopropyl peroxycarbonate; and persulfates such as potassium and sodium persulfates.
[0012] Homogeneous graft copolymers useful in the present invention which are substantially
free (contain less than 2 percent by weight) of insoluble homopolymerized acrylamide
derivative may be prepared by methods known in the art but preferably are prepared
by charging the reactants in two separate feed streams, advantageously in gradual
and/or incremental amounts, one of which consists of the grafting monomer and a second
consisting of the free-radical grafting initiator. Either of the reactants may be
mixed with a portion of the poly(oxyalkylene) compound prior to feeding them to the
reaction zone when doing so facilitates the gradual or incremental feeding thereof
to the reaction mixture. The amount of acrylamide derivative added to the polymerization
reactor zone is not critical and may be varied over a wide range. The preferred range
is from 6% to
[0013] 12% by weight of poly(oxyalkylene). In general, however, up to about 70 percent by
weight. and preferably from
0.5 percent by weight to 50 percent by weight based on the total weight of poly(alkylene
oxide) compound, is charged.
[0014] The temperatures at which the graft reaction may be carried out may vary over a wide
range and depend, in general, upon the combination of reactants to be used in the
reaction and the catalyst chosen to catalyze the graft reaction. For example, when
organic free-radical grafting initiators are employed, a temperature sufficient to
activate the initiator, to about 160°C, can be used in the grafting reacting, and
preferably, a temperature in the range from 70°C to 100°C. Where employing inorganic
free-radical initiators, a temperature from about above the freezing point of the
solvent to about 65°C may be employed. Reaction temperatures above 160°C lead to gelling
of the reaction mixture, and should be avoided.
[0015] Incremental and/or gradual addition of the two separate reactant feed streams coupled
with efficient agitation of the poly(oxyalkylene) compound in the reaction zone constitutes
the most important technique for producing the graft copolymers useful in the present
invention. This method is particularly important in large scale or commercial operations.
not only for preparing the desired homogenous graft compolymer. but also to facilitate
handling and storage of the monomer and the free radical initiator.
[0016] The grafting reaction is preferably carried out in bulk without the use of a solvent.
If desired, however, a solvent may be used which is inert to the reactants. Suitable
solvents include benzene, toluene, tertiary-butylbenzene, heptane. hexane. or octane,
and mixtures thereof, and water.
[0017] The preferred graft copolymers are made from a poly(oxyethylene-co-oxypropylene)
copolymer of molecular weight in the range of 350 g/mol to 4000 g/mol and which are
at least about 40% ethylene oxide monomer by weight of the polymer. The upper limit
is not critical as longer chain polymers have been found to impart better lubricity:
however, the high viscosity of very high molecular weight poly(oxyalkylenes) may make
the use of such polymers difficult.. The preferred poly(oxyalkylenes) have been treated
with a sufficient amount of N-methylol-acrylamide or N-(isobutoxymethyl)-acrylamide
in a grafting reaction such that at least an average of 1,5- N-(oxymethyl)-acrylamides
molecules are grafted onto each poly(oxyalkylene) molecule and most preferably an
average of from 3 to 6 N-(oxymethyl)-acrylamide molecules per poly(oxyalkylene) molecule.
[0018] An optional component of the treating solution is an antioxidant that will inhibit
the degradation of the poly(oxyalkylene) polymer thereby improving the durability
of the "fiber finish Such antioxidants are well known in the art of stabilizing poly(oxyalkylenes)
and may include any number of antioxidant compounds. Especially suitable are hindered
phenolic compounds such as Bisphenol A. BHA and BHT. The amount of such an antioxidant
is not critical and generally ranges from 1% to 3% by weight of the treating composition
or solution.
[0019] The graft copolymer is then mixed with an acid catalyst and applied to the fiber
or fabric to be treated.
[0020] Although the various examples given herein are directed to the practice of the instant
invention with fiberfill fibers, it is believed that the instant invention will impart
lubricity to any synthetic fiber, e.g., a textile fiber. It is to be understood that
the phrase "fiberfill fiber" is intended to mean any non-woven bating or fiber mat.
Although all the examples shown herein are directed to carded polyester fibers, it
is to be expected that non-carded, non-polyester fibers will exhibit similar properties
when treated by the process of the instant invention. In addition to the Hollofil-808
fibers available from E. I. du Pont de Nemours that are exemplified herein, other
fiberfill fibers, such as the round, solid fiber available from Hoechst. are useful
in the instant invention.
[0021] Similarly, the process of the instant invention is exemplified hereinafter by the
application of the graft copolymer to 100t polyester fabrics made from polyethylene
terephthalate. Examples of suitable polyester fabrics are Kodel. a registered trademark
of Eastman Kodak, and Dacron, a registered trademark of E.I. du Pont de Nemours. However,
it is to be understood that the process of the instant invention is not limited to
polyester fabrics. It is believed that substantial hydrophilicity would be imparted
to other textile fabrics, e.g. nylon, synthetic/natural fiber blends. etc.
[0022] The choice of acid catalyst suitable for use in the invention is not critical and
may depend on such considerations as economic or toxicological factors. Any acid that
will lower the pH sufficiently to make the solution weakly acidic will catalyze the
crosslinking of the graft copolymer on the fabric surface. Examples of acid catalysts
include inorganic acids such as hydrochloric. hydrobromic. sulfuric and nitric acids:
organic acids such as carboxylic acids, phenols, alkyl and aryl sulfonic acids, Lewis
acids. such as zinc fluoroborate, will also catalyze the graft copolymer cross-linking
on the surface of the fabric. An acid catalyst that is particularly suitable for use
in the instant invention is citric acid because of its commercial availability and
non-toxicity. In a most preferred embodiment, the acid catalyst chosen is water soluble
because an aqueous solution is a convenient medium with which to apply the graft copolymer
to the fiber.
[0023] The graft copolymer and acid catalyst may be applied as a neat composition or a solution.
Any solvent which will dissolve the graft copolymer may be used. Suitable solvents
include water, alcohols. ketones. esters or mixtures thereof that will dissolve the
graft copolymer and the acid catalyst. When water is used as the solvent, a functional
additive such as an anionic or nonionic surfactant may be added to facilitate the
initial wetting of the fiber. In a highly preferred embodiment, the graft copolymer
and acid catalyst are added to water to form a treatment solution that is from 1/2%
to 15% by solution weight of graft copolymer and 0.001% to 2% by solution weight of
an acid catalyst.
[0024] The solution may be applied in any manner that is effective to wet the fiber or fabric
with the solution. If the fiber or fabric is deposited in a bath containing the treatment
solution, the residence time in the bath need only be so long as to allow substantial
wetting by the solution. The addition of wetting agents such as surfactants will reduce
the necessary residence time. Other functional additives such as colorants, sizing
agents, may also be added to the treating bath along with a surfactant. The temperature
of the treatment solution is not critical so long as it is maintained below the temperature
that will cross-link the graft copolymer in solution with the acid catalyst. The treated
fiber or fabric is then heated at a temperature and for a period of time sufficient
to dry it and cure the graft copolymer on the fiber or fabric surface. Generally,
a few minutes in an oven at between 100°C and 170°C is sufficient to cure the graft
copolymer and remove any excess solvent taken up by the fabric in treatment, but the
actual time and temperature necessary will depend primarily upon the catalyst and
solvent chosen.
[0025] The dried, treated fiber or fabric is then ready for further processing with the
graft copolymer cross-linked on the surface of the fiber or fabric as a durable, lubricating
and hydrophilic fiber finish. Any residual acid catalyst may be removed by further
processing, which may include a simple rinsing procedure.
[0026] This invention is further described in the Examples which follow. These examples
are intended to be illustrative of specific embodiments of this invention and are
not intended in any way to limit the scope of the invention. All parts and percentages
are by weight unless otherwise specified.
Examples 1 & 2
Graft Copolymer Preparation
Example 1
[0027] A four-neck, round-bottom glass flask. fitted with a mechanical stirrer, thermometer,
water condenser, two 250 inch dropping funnels nitrogen source, and nitrogen outlet.
was charged with 184.3 g q of an allyl-started ethylene oxide/propylene oxide copolymer
(40/60 by weight) having a viscosity of 450 SUS (Seconds, Universal, Saybolt). One
dropping funnel was charged with 64.3 g of N-(isobutoxymethyl)-acrylamide (IBMA) and
the other was charged with 20.3 g of ethyl acetate and 1.3 g g of 2.2-azobis-(2-methylpropionitrile).
The flask contents were heated to 80°C with an electrical heating mantle and the flask
was purged with dry nitrogen. The IBMA and ethylacetate 2,2-azobis-(2-methylpropionitrile)
were added simultaneously and dropwise over a period of
1 hour at a rate which kept the reaction mixture between 80° and 83°C. After addition
of the IBMA and ethyl acetate/2,2-azobis (2-methylpropionitrile) was completed, the
flask and its contents were heated to 80°C for 3 additional hours and then allowed
to cool to room temperature. Any remaining unreacted IBMA was removed by vacuum stripping
along with the ethyl acetate used to introduce the acid catalyst. The graft copolymer
obtained thereby is a clear, pourable liquid that is added to water to make the fabric
treating solution or may be applied to the fabric as a neat composition with the acid
catalyst.
Example 2
[0028] A 250 ml three neck round bottom flask equipped with a stirrer was used in this example.
To this reactor was charged 120 q of distilled water. 0.5 g of sodium bicarbonate.
0.5 g of sodium sulfite and 0.5 g of sodium persulfate. After dissolution of the salts
was completed by stirring, 15.3 q (0.0059 mole) of the poly(oxyalkylene) polymer used
in Example 2 were added and the resulting solution was cooled to 0° to 5°C. A 48 percent
aqueous solution of N-methylolacrylamide containing 7.4 g (0.034 mole) (28.6 weight
percent of the total charge) with 5.0 g additional water was added dropwise to the
reaction mixture over a period of 15 minutes. After addition of all reactants was
completed, the reaction mixture was stirred for an additional 45 minutes while maintaining
the temperature at 0° to 5°C, and then the reaction mixture was allowed to warm to
room temperature.
[0029] This crude reaction mixture may then be diluted to form a treating solution upon
the addition of a solvent and a suitable acid catalyst.
Lubricity Testing
[0030] The samples tested in examples 3-7 were prepared by padding the aqueous finishing
composition onto carded Hollofil-808. a round. hollow, polyester fiberfill fiber available
from E.I. du Pont de Nemours. The amount of finish taken up was controlled such that
the Hollofil-808 takes up its own weight in aqueous finish. This 100% pick-up of finish
on the fiberfill translated into a percent by weight of finish on the fiberfill equal
to the percent by weight of finish in solution, i.e., a 1% graft copolymer finishing
solution yielded a finished Hollofil-808 sample that is 1% by weight of graft copolymer
finish.
[0031] The finished fibers were then dried at the temperature indicated and for the time
indicated in the following examples.
[0032] The treated samples were then allowed to condition for three days by maintaining
them in a constant environment of 50% relative humidity and 21°C (70°F). The samples
were then tested for lubricity according to a "Staple Pad Friction" technique. In
this technique, a weighted sled is pulled across a fiber sample by an Instron Model
1000 available from Instron Corp.. Canton. MA. The "Staple Pad Friction" is displayed
in grams by the Instron and the Staple Pad Friction (hereinafter referred to as SPF)
Index is computed by dividing the Staple Pad Friction in grams by the sled weight
in grams.
[0033] To test the durability of the graft copolymer finish, the samples as indicated were
washed for 10 min in a solution of 2.25 g of AATCC Detergent #124 held at 70°C. The
samples were then rinsed with deionized water at room temperature and were allowed
to recondition in a constant environment as hereinbefore described.
Example 3
[0034] This is a control for Examples 4-6 in which untreated Hollofil-808 exhibited an SPF
of o.40. The results of Examples 3-6 are tabulated in Table I.
Example 4
[0035] This is a comparative example in which a 1% solution of a ungrafted allyl-started
ethylene oxide/propylene oxide (40/60 by weight) with a viscosity of 2700 SUS (Seconds.
Universal. Saybolt) and an average molecular weight of 3700 g/mol was padded onto
a carded Hollofil-808 sample as hereinafter described and tested as herein before
described. The SPF for such an ungrafted sample was 0.36 before washing.
Example 5
[0036] This is a comparative example wherein no catalyst was used to cure the graft copolymer.
The procedure of Example 4 was followed with the exception that the graft copolymer
was composed of 26.6 g by weight of N-(isobutoxymethyl)-acrylamide grafted onto an
allyl-started ethylene oxide/propylene oxide (40/60 by weight) with a viscosity of
(450 SUS) and an average molecular weight of 1400 g/mol. No catalyst was, however,
added to the finishing solution. The treated Hollofil-808 fiber exhibited an SPF of
0.30 before washing and and SPF of 0.39 after washing.
Example 6
[0037] This is a preferred example wherein 7.5 gms of a graft copolymer composed of 12%
by weight of polymer of N-(isobutoxymethyl)-acrylamide grafted onto the poly(oxyalkylene)
of Example 4, 7.5 gms of citric acid and .15 g of Bisphenol A were dissolved in enough
deionized water to form 750 gms of finishing solution. Samples of Hollofil-808 were
treated and tested as hereinbefore described to yield an SPF Index of 0.27 after curing
for 10 min at 150°C but before washing, and an SPF of 0.29 after washing as hereinbefore
described.
Example 7
[0038] This is a preferred example wherein 7.4 g of a graft copolymer composed of 12% N-(isobutoxymethyl)-acrylamide
grafted onto a glycerol-started ethylene oxide/propylene oxide (14/86 by weight) with
a viscosity of (360 SUS) 78mm²/s and an average molecular weight of 4741 g/mol was
dispersed in 750 g of finishing to which was also added 0.75 g of ethoxylated nonyl-phenol,
Tergitol NP-40 available from Union Carbide Corporation (as a surfactant to disperse
the nearly insoluble graft copolymer). 7.5 g of citric acid and 0.15 g of Bisphenol
A. The procedure of application and testing of Example 5 then yield an SPF before
washing of 0.26 and an SPF after washing of 0.29.

[0039] Table I illustrates that a durable fiberfill finish is obtained by the practice of
the present invention which significantly lowers the interfiber friction associated
with polyester fiberfill fibers.
Hydrophilicity TestinQ
[0040] The 100% polyester fabric samples tested in the following examples, 8-19. were treated
by immersing them in a bath containing a solution of 5% graft copolymers by weight
along with 0.1% para- toulene sulfonic acid as a catalyst and 0.1% Tergitol TMN-6.
a non-ionic surfactant available from Union Carbide Corporation, to aid wetting in
treatment. The fabric was weighed before immersion, immersed. retrieved and then pressed
in a Mathis two-bowl Vertical Laboratory Padder. type VF, with a pad pressure of 1
bar and a roller speed of 6 rpm. The resulting weight of the wet, treated fabric indicated
a wet pickup of treating solution of 60% to 70% by weight of the fabric. These wet
samples were then placed upon a frame and dried in a Mathis Laboratory Drying and
Curing Apparatus, type LTF, for 2 minutes at 165°C. The curing of the graft copolymer
occurred during this drying cycle.
[0041] The samples were then conditioned and tested for wettability in accordance with AATCC
Test Method 39-1977 promulgated by the American Association of Textile Chemists and
Colorists for the evaluation of wettability of fabric. The , readings therefrom are
expressed in the average time in seconds needed visibly to wet the tested fabric with
a drop of water. The shorter the average wetting time, the more hydrophilic is the
fabric. The samples were then laundered in accordance with AATCC Test Method 130-1977
the number of times indicated in Table II.
[0042] The AATCC Standard Detergent 124 was used in an amount of about 140 grams in a #4
wash load with a washing temperture of about 120°F and a rinse temperature of about
(105°F). The laundered samples were then reconditioned in accordance with AATCC Test
Method 39-1977 for re-testing.
[0043] Table II sets forth the nature of the graft copolymer applied to the fabric, the
initial wettability of the samples and the wettability after five standard launderings.

[0044] The data show that significant durable hydrophilicity is obtained with N-methylol-
acrylamide graft copolymers and that superior durable hydrophilicity is obtained with
N-(isobutoxymethyl)-acrylamide graft polymers. The data also show that the structure
and functionality of the graft copolymer is not critical within the claimed ranges
of structure and functionality of the polyether precursor.
[0045] The data in Table III set forth the nature of the graft copolymers applied to the
100% polyester fabric tested in examples 20-24 along with the wettability results
after 5. 10. 15 and 20 standard launderings. The treatment process of examples 20-24
is otherwise identical to the treatment process described for examples 8-19.

[0046] The data in Table III show that extended durability of hydrophilicity is achieved
for the N-(isobutoxymethyl)-acrylamide graft copolymer of the present invention regardless
of the structure or functionality of the graft copolymer within those shown in Table
III.
[0047] The data in Table IV set forth the effect of a catalyst on the cross-linking of the
graft copolymer on the surface of the treated fabric. The graft copolymer is the same
as that described in Example 23 and the treatment process was identical with the exception
of the varied catalyst type and concentration.

[0048] The data in Table IV illustrate the need for a Lewis acid catalyst, but that the
choice of catalyst is not critical.
[0049] The data in Table V illustrate the effect of solution concentration of the graft
copolymer of Example 23 in the treatment bath. The other treatment process conditions
were identical to those of-examples 8-19.

[0050] The data show that although increasing hydrophilicity is imparted by increased solution
concentrations, as little as 1% graft copolymer in solution imparts substantial hydrophilicity
to the fabric tested.
1. A process to impart lubricity and hydrophilicity to fibers or fabric which comprises:
(a) treating said fibers or fabric with a neat composition, solution or dispersion
containing:
(i) at least 0.001% by solution or dispersion weight or neat composition weight of an acid catalyst,
(ii) from 0.1% to 15% by solution or dispersion weight or neat composition weight
of a graft copolymer prepared by grafting to a poly(oxyalkylene) from 0.5% to 50%
by polymer weight of an N-(oxymethyl) acrylamide of the formula:

wherein one or more R1, R2, R3. and R4 are hydrogen or monovalent hydrocarbon radicals containing from 1 to 6 carbon atoms
each and the poly(oxyalkylene) is of the formula:

wherein R is a hydrocarbon radical having a valence of a and containing up to 21 carbon
atoms, a is an integers having values between 1 and 4, X is an oxygen, nitrogen or
sulfur atom. R6 is a hydrogen atom or hydrocarbon radical containing up to 6 carbon atoms and may
contain hydroxyl, amino or mercaptyl groups, n is an integer from 2 to 4 and z is
an integer from 2 to 800, and
(b) drying and curing said treated fiber or fabric.
2. The process of claims 1 wherein the substituted N-methylol derivative of acrylamide
is N-(isobutoxymethyl) acrylamide.
3. The process of claims 1 or 2 wherein the poly(oxyalkylene) is made by reacting
an alkylene oxide, or mixtures thereof, with an aliphatic compound which is saturated
or contains aliphatic unsaturation and which contains from 1 to 4 active hydrogen
atoms.
4. The process of claims 1 to 3 wherein the poly(oxyalkylene) is poly(oxyethylene).
poly(oxypropylene) or mixtures or copolymers thereof or poly(oxyethylene-co-oxypropylene)
monoallyl ether, containing 40 percent oxyethylene/60 percent oxypropylene.
5. The process of claim 1 to 4 wherein the acid catalyst is citric acid or acetic
acid.
6. The process of claims 1 to 5 wherein the curing temperature is about 140°C and
preferably between 100 and 170°C.
7. The process of claims 1 to 6 wherein the hydrocarbon radical R5 is selected from the group of allyl, butyl, and glyceryl radicals.
8. The process of claims 1 to 7 wherein R6 is a hydrogen atom.
9. The process of claims 1 to 8 wherein z is between 40 and 135.
10. The process of claims 1 to 9 wherein bis-phenol is added to the treatment solution.
11. The process of claim 1 to 10 wherein the fiber treated is a fiberfill fiber.
12. The process of claim 1 to 11 wherein the substituents of the N-(oxymethyl) acrylamide
R
1, R , R and R are hydrogen or monovalent hydrocarbon radicals containing from 1 to
6 carbon atoms each and may be the same or different to the poly(oxyalkylene) of the
formula:

wherein R
6 is a hydrogen atom or hydrocarbon radical containing up to 6 carbon atoms and x is
an integer having a value from 2 to 5000, and y is and integer having a value from
zero to 5000.
13. The process of claim 12 wherein the fibers or fabric material is polyester.
14. The process of claim 12 or 13 wherein the acid catalyst is p-toluene sulfonic
acid or zinc fluoroborate.