[0001] This invention relates to a method for permanently sizing and, optionally, pigmenting
a polyester or polyester-blend yarn.
[0002] The sizing of textile yarns prior to weaving is conventional in the art. A principal
object of sizing is to protect the yarn from abrasion during the weaving operation
and material such as starches, polyvinyl alcohol, polyvinyl alcohol, polyacrylates,
polyacrylamides and polyesters are applied to the yarn and subsequently removed after
the weaving operation. Permanent sizes are also used to protect the yarn during weaving,
to stiffen the fabric and to bind a pigment or dye. The present invention teaches
a particularly suitable method for permanent size application employing a polymer
latex formulation which provides: a superior balance of polymer adhesion to polyester
fibers, fiber abrasion resistance under weaving conditions, wash and dry clean durability
of fabric produced from the fiber and, in many embodiments, low foaming tendency of
the formulation applied to the fiber.
[0003] Warp yarns, whether spun or filament, are composed of many fine fibers which are
soft and abrade easily. If left unprotected, they could not withstand the rough mechanical
action and abrasion they are subjected to on a loom, whether shuttle or shuttleless.
Therefore, a size is applied to these yarns to protect them during the weaving process,
thus making fabric production possible. After the fabric is woven, the size detracts
from the textile aesthetics (hand or feel), for most uses, and properties of the fabric
(dyeability) so the size is usually removed following weaving. However, there are
certain textiles such as drapery, upholstery fabric, and mattress ticking, in which
the presence of a size does not detract from the fabric but actually enhances the
desirable properties thereof.
[0004] The manufacture of such sized textiles may entail the permanent sizing of polyester
of polyester-blend yarn where the yarn is not only sized in a normal slashing operation
but permanently coloured simultaneously. This process protects the yarn for weaving
and eliminates the necessity of post-dyeing the yarn after it is woven into fabric.
This is especially useful when yarn dyed filling (weft) is used to give a solid or
multi-coloured fabric. Also energy can be saved when easily dyeable filling yarns
are used. The principal required properties for such a size are:
Warp Size Recuirements: (1) good bath stability, (2) no foaming, (3) no building up
on dry cans, (4) good leasin properties, (5) minimal binder or color migration during
dryin (6) no tack in the warp beam, and (7) no shredding during weavi
Pigment Dyeing Reauirements: (1) bindei must cure in available heat (ca. 130° C.),
(2) be durable to a peroxide bleach process, (3) be durable to home laundering and
dry cleani (4) withstand spot cleaning without a loss in color, and (5) produce maximum
color yield.
[0005] Employing the pigmented size of the instant inventic represents considerable savings
over prior art processes because a process step, the post-dyeing of the fabric or
yarn, is elimi With polyester yarns, the dye step normally requires both high temperature
and pressure each of which represents a considerable use of energy. Another energy
consuming step, the desizing of the fabric normally done in a hot bath, is also eliminated.
Partial savings are realized when a warp yarn is pre-dyed, by the process of this
invention, and used with an undyed fill yar which is more easily dyed, such as cotton
or rayon, and thus ma be dyed by a mild and less energy demanding.process. A particu
example would be a drapery which uses a polyester warp and a viscose fill.
[0006] This pigmented sizing produces materials with as good or better color fastness than
dyed yarn. Elimination of the desizing step means that the many advantages are carried
over into the final fabric. Altogether the process of this invention thus makes available
an inexpensive, color fast, convenient, high quality, pigment dyed yarn at a considerable
reduc-tion in the use of energy, labor, equipment and chemical raw materials. Pigments
are generally cheaper than dyes but heretc fore high quality color fastness via pigment
has been difficult The process of this invention achieves good fastness as well as
high color yield thus representing a further saving. Dyes, especially for polyester,
require auxiliaries such as defoamers leveling agents, solvents, and carriers in audition
to the dye itself as well as a size which then must be removed before the dyeing step.
Thus the process of the instant invention inherently entails the ecological improvements
of requiring 1) no solvent or carrier, 2) no disposal of the removed size, 3) less
dissipated heat, 4) less water usage and 5) less waste water disposal. The yarn produced
by the process of the instant invention yields, by art-known weaving processes, a
fabric which has a firm hand, is abrasion resistant, strong and peroxide bleach resistant
(particularly required if any direct dyes are present) as well as being laundry and
dry clean resistant. The yarn size of this irivention gives better adhesion to the,
chemically similar, acrylic back coatings widely used with drapery, mattress ticking
and upholstery fabrics. The improved strength, abrasion resistance and adhesion all
work together to increase the fabric life.
BRIEF DESCRIPTIOn OF INVENTION
[0007] In'accordance with the present invention there is provided a method for permanently
sizing and optionally pigmenting polyester filaments and yarns or blends of polyester
with other fibrous or filament materials which comprises applying to the yarn a sizing
composition comprising an aqueous polymer latex of an emulsion polymer comprising,
by weight, 45 to 65% of one or more of
C4 to
C8 alkyl acrylates, 28 to 52% of one or more of vinyl aromatic monomers or a mixture
thereof with up to an equal weight of methyl methacrylate, and 3 to 14% of acrylic
acid, methacrylic acid, itaconic acid or a mixture thereof, said latex also containing
a melamine aminoplast resin, suitable for crosslinking the latex polymer, and, optionally,
a pigment, and subsequently drying and curing the treated yarn.
[0008] The polymer latex of the instant invention preferably is made by a gradual addition
thermal emulsion polymerizatio: process to yield the product at about 35 to 50% solids.
Such processes are taught in books entitled "Emulsion Polymerization" by D. C. Blackley
(Wiley, 1975) and S. A. Bovey et al (Interscience Publishers, 1965). The polymer is
preferably a linear polymer free of crosslinks and branch points. The polymer is prepared
from monomers comprising, by weight, 45 to 65%, preferably 50 to 59% of a C
4 to C
8 alkyl acrylate or a mixture thereof, preferably n-butyl acrylate; 28 to 52%, preferably
31 to 46%, of a vinyl aromatic monomer such as styrene, alpha-methyl styrene, and
vinyl toluene, or a mixture thereof preferably styrene, with the further proviso that
up to half of the vinyl aromatic monomer may be replaced by methyl methacrylate;.
and 3-14%, preferably 4-12% acrylic acid, methacrylic acid and, less preferably, itaconic
acid or a mixture of these. Most preferabl the monomers consist essentially of 50
to 59% butyl acrylate, 31 to 46% styrene and 4 to 12% acrylic acid or methacrylic
acid. Desirably, the latex polymer has a weight average molecular weight of about
0.3 to about 2.5 million with 0.5 to about 2.0 million being preferred and 0.6 to
1.5 million being most prefer
[0009] The diameter of the latex particles is usually betwe 0.05 and 0.5 microns with the
range 0.1 to 0.2 microns being preferred.
[0010] The stiffness of the latex polymer is a particularly significant property. If the
polymer is too stiff the size willbe too hard and will flake off of the yarn as the
yarn is flexed during weaving. If the polymer is too soft it will be too stick causing
friction in the loom, sticking to the reeds, and easy removal from the yarn by abrasion,
and these processes may furt cause a build up of the polymer on parts of the machines
employed in processing the yarns and making fabric. Because of these property limitations
it is preferred that the latex polymer hav a T
300 between 0° C. and 40° C. with the range 10° C. to 30° C. being more preferred. T
300 is the temperature at which the ten second, torsional modulus of a film, made by
drying the polymer latex, is 300 kilograms per square centimeter as measured by the
American Society For Testing And Materials standard method of tes D 1043-72. As 300
kgs. per sq. cm. is roughly twenty fold below the glassy modulus of amorphous polymers,
such as those of intere herein, the T
300 is appreciably higher than the glass transition temperature (Tg); the difference
is usually about 15
0 C. which value may be used to obtain estimates of T
300 from tables of Tg data or calculations (see Fox, Bull. Am. Physics Soc. 1, 3 page
123 (1956) and "Polymer Handbook" 2nd ed, Brandrup and Immergut eds, (John Wiley,
N.Y. 1975) Section III, part 2 by Lee and Rutherford).
[0011] The melamine aminoplast condensates which are employ are either low molecular weight
oligomeric or monomeric reaction products of formaldehyde and melamine such as N,N-dimethylolmela
and alcohol-modified melamine formaldehyde thermosetting resin condensates, e.g. methyl
and ethyl alcohol modified, for example dimethoxymethyl monomethylolmelamine, etc.
Preferably, the exte of condensation of these resin-forming aminoplast condensates
is such that they are still soluble in water or self-dispersible therein to a colloidal
condition. The melamine aminoplast is present at 2 to. 40%, preferably 4 to 25% and
most preferably 8 t 15% by weight of the latex copolymer. The preferred aminoplast:
are hexamethoxymethyl melamine, such as Cymel
R 303, and partial methylated polymeric melamine having an equivalent weight about-225
to about 325, such as Cymel 373. Other useful melamine ami: plasts are sold under
the tradename Aerotex
R including Aerotex 3, Aerotex 900 and Aerotex 23SP.
[0012] The amount of copolymer applied to the yarn materia may vary from about 0.5 to about
20% by weight depending on the purpose for which the application is intended and on
whether or not auxiliary conditioning or sizing agents are included in the composition
when it is applied to the yarn. The aqueous bath formulation comprising the copolymer
latex may be applied by spraying, dipping, padding, by sizing rolls, transfer rolls
or the like, dipping being preferred. An entire warp may be passed through a conventional
slasher or a yarn may be individually treated in a single end sizer. The latex has
a concentration of 1-25% by weight solids in the application formulation and excess
is removed, such as by squeeze rolls or wipers, and the treated yarn is then dried.
Drying is effected by any suitable means such as by heated air or drying cans. Drying
may be effected at
a.
wide range of temperatures, such as from 70-120° C, or in conjunction with curing.
The formulation is applied at room temperature or at elevated temperatures such as
up to about 80
0 C. For warp sizing of spun yarns the preferred proportion of polymer applied to the
yarn is from 5-15% by weight of the initial weight of the yarn. For the sizing of
continuous filament yarns, the preferred proportion is from about 1% to about 10%
copolymer on the weight of the yarn. The higher amount of size is often needed for
fine (low) denier zero or low twist yarn. The preferred size add-on for 150 denier
zero twist polyester filament is 2.5 - 3.0% (copolymer on yarn).
[0013] The article obtained, after application of the sizing composition to the yarn and
drying, is essentially free from. the disadvantage of developing static charges and
loss of sizing material by transfer to guides or by shedding.
[0014] The permanent size of the instant application is applied to a yarn which is a polyester,
preferably polyethylene terephthalate, yarn or alternatively a polyester-blend yarn.
Filament yarn substrates are preferred although spun yarns are useful. Blend yarns
include blends of polyester with up to 50% of other, preferably organic, fibers including
natural fibers, such as cotton, and synthetic fibers, such as rayon; the cotton blend
being preferred.
[0015] The formulation for application of the polymer to the yarn preferably contains a
rheology modifier, such as a homopolymer or a copolymer of an ethylenically-unsaturated
acid, such as polyacrylic acid, polymethacrylic acid and hydrolyzed styrene/maleic
anhydride copolymer; other carboxyl polymers such as carboxymethyl cellulose; water-soluble
or water- dispersible non-ionic polymers, such as hydroxyethyl cellulose, polyoxyethylene
polymers (although the latter polymers are not as efficient as the ionic polymers),
and homo- and copolymers of acrylamide. Volatile bases, such as ammonia and amines,
are used for partial or complete neutralization of the rheology modifiers.
[0016] For immersion treatment of the yarn a desirable formulation has, on a solids basis,
3 to 15%, preferably 4 to 8% latex polymer; 0 to 12%, preferably 0 to 8%, most preferably
0 to 4% pigment; 0.05 to 6%, preferably 0.3 to 3% melamine aminoplast, 0.1 to 2.0%,
preferably 0.3 to 1.0%, rheology modifier or thickener, and up to 0.6%, preferably
up to 0.3% catalyst for the melamine resin; in many embodiments of this invention
no such catalyst is preferred. Optionally, surfactants, anti-foam agents, penetrants,
alkaline materials to control the pH (preferably volatile amines and most preferably
ammonia), penetrants and other additives known to those skilled. in the art are used
to achieve specific desirable properties in the formulation or the yarn.
[0017] Anionic surfactants which may be added _to the formulation include the following:
sulfosuccinates, such as sodium bis(2-ethylhexyl)sulfosuccinate; sulfates, such as
sodium lauryl sulfate; sulfonates, such as sodium isopropylnaphthalene sulfonate;
alkyl aryl polyester sulfates and sulfonates, phosphate ester types and the like.
[0018] Nonionic surfactants which may be added to the formulation include the following:
octylphenoxypoly(ethyleneoxy)ethanol, trimethylnonyloxypoly(ethyleneoxy)ethanol, nonylphenoxypoly
(ethyleneoxy)ethanol, glyceryl trioleate, ethyleneglycol ethyleneglycol monostearate,
sorbitan trioleate, sorbitan tristearate, and the like.
[0019] Nonionic and anionic penetrating agents and antifoaming agent commonly used by those
skilled in the art of sizing and coloring may also be employed. Suitable penetrating
agents which may be used include the following: diethanolamine, N-aminoethyl ethanolamine,
ethylene glycol monobutyl ether, diethylene glycol, diethyl ene glycol monobutyl ether,
dipropylene glycol monomethyl ether, ethylene glycol, dihexyl sodium sulfosuccinate,
and the like. Suitable antifoaming agents which may be used include the followir isobutanol,
n-butanol, iso-decanol, dibutyl phthalate, diethylene glycol laurate, 2-ethylhexanol,
n-octanol, polypropylene glycol, tributyl citrate, and the like.
[0020] The curing catalysts for the aminoplast which may be used include amine or ammonium
salts such as ammonium chloride, ammonia nitrate, ammonium sulfate, ammonium acid
phosphate, isopropanolam hydrochloride, and the like. Generally, any such catalyst
may be used with about equal results as may other latent acid catalysts including
Lewis acid catalysts.
[0021] Any pigments commonly used in textile pigmentation are usable. Suitable water-immiscible
colorants which may be used include the following wherein C. I. means Colour Index
(published by The Society of'Dyers and Colourists): C. I. Direct Blue 86, C. I. Pigment
Yellow 14, C. I. Pigment Blue 15, C. I. Pigment Black 7, C. I. Pigment Green 1, C.
I. Pigment Orange 5, C. I. Pigment Red 12, and the like. The preferred colorants are
C. I. Pigment Blue 15, and Yellow QR.
[0022] The application of the sizing, or colorant-binding, composition to the yarn is by
the methods described above, to deposit thereon about 1-10%, preferably 2-5%, by weight
solids from the aforedescribed latex polymer formulation. The preferred substrate
material is a polyester filament warp yarn.
[0023] The treated yarn is dried and cured by heating at 100°-350° F. (37-177°C) for a period
of about 5 seconds to 5 minutes, preferably at 250°-320° F. (121-160
0C) for a period of about 15 seconds to 2 minutes. Optionally the treated yarn may
be dried at a lower temperature, such as by standing at room temperature until dry,
and then cured at 225°-320°F. (107-160°C) for a period of about 10 seconds to 2 minutes,
preferably at 225°-300° F. (107-149°C) for a period of about 15 seconds to 1 minute.
[0024] The process of this invention produces an insoluble size colorant-binding coating
on the yarn substrate which is durable laundering and dry cleaning. The treated substrate
has satisfactory handle and is tack-free. The treated polyester wa yarn is characterized
by excellent weaving characteristics.
[0025] In the following examples, which are illustrative of t invention, the parts and percentages
are by weight and the temperatures are in degrees Celsius unless otherwise expressly
noted. The following abbreviations are used.

Example A - Preparation of Emulsion Polymer at 4% Acid
[0026] The preparation is a gradual addition thermal process producing a latex polymer 58.5%
BA, 37.5% St and 4% AA.

Process
[0027] Water and SLS are charged to a 5-liter kettle and heated to 82° C. The monomer preform,
a 100 g. portion of the monomer emulsion, is added, followed by the APS in water,
initiator solut Ten minutes later, gradual addition of the monomer emulsion, to which
had been added the co-feed solution, is begun at 82° C. and continued at a constant
rate for 2 hours, while the temperat is held at 82° - 86° C. A 15-minute hold at that
temperature follows the end of the gradual addition, then the reaction mixtu is cooled
to 55° C. Residual monomers are removed by free radic chasers. The batch is then cooled
to room temperature and filte through cheesecloth.

[0028] The pH may be elevated by the addition of aqueous ammonia to about 4.5, as was done
in the case of the material used in formulations I, V, and IX, Table I, or higher
such as 6, for convenience, long term stability, etc.
Example B - Preparation of Emulsion Polymer at 12% Acid
[0029] The preparation is a gradual addition thermal process producing a latex polymer,
57% BA, 31% St, and 12% MAA.
Ingredients
[0030]

Process
[0031] Water and SLS are charged to a 5-liter kettle and heated to 84
0C. The monomer preform, a 114 g. portion of the monomer emulsion, is added, followed
by the APS in water kettle charged initiator solution. Ten minutes later, gradual
addition of the monomer emulsion at 20 g./min. and of the cofeed catalyst at 1.7 g./min.
is begun and continued at a constant rate while the temperature is held at 83 to 85
0C. A 15 minute hold at the final temperature is maintained and then the reaction mixture
is cooled to.55°C. Residual monomers are removed by means of free radical chasers.
The batch is then cooled to room temperature and filtered through cheesecloth.

Example C - A Harder 4% Acid Emulsion Polymer
[0032] Employing the preparation method of Example A, a copolymer having the composition
50 BA/46 St/4 AA is prepared at 45% total solids and a pH of 4.5.
Example D - A Harder 12% Acid Emulsion Polymer
[0033] Employing the preparation method of Example B, a polymer emulsion is made having
the composition 50.5 BA/37 St/12 AA at a total solids of 39.5% and pH of 2.3.
Preparation of Formulations
[0034] A control formulation for the pigment sizing of polyester warp yarns is based on
a commercial water dispersible polyester used as a size (Eastman WD), a melamine formaldehyde
resin for crosslinking (Cymel 373), a latent acid catalyst, Acrysol G-110.as rheology
modifier and anti-migrant, and a pigment. The formulation follows:

Notes:
[0035]
1Cymel 373 - partially methylated polymeric melamine; equivalent wt. 225 to 325.
2Pigment - American Hoechst - Yellow QR
3Eastman WD - water dispersible polyester size
4Acrysol G-110- ammonium polyacrylate solution; viscosity 5% aqueous is 90 to 170 cps.
[0036] The above formulation is compared to tha following systems based on the Examples
A-
D copolymers (Table I). A water insoluble melamine formaldehyde resin, Cymel 303, is
employed at two levels, 0.3 and 1.0%, the second is equivalent to the Cymel 373 level.used
in these formulations and with Eastm WD. Following the first three formulations the
latent acid catalyst is removed from the formulation since the desired performance
is achieved without a catalyst.

Preparation of Yarn
[0037] Each formulation is applied to polyester filament-yarn (Avitex Fibers, Inc. Type
200-F polyester 150 denier, 50 filament 0 twist) on a laboratory single end slasher
run at 4M/min. The yarns are either dried thru a dry tube (a 1 meter heated glass
tube) for 15 seconds at 115° C. and post cured in a forced air oven for 45 seconds
at 132° C. (Example 1) or dried and cured in the dry tube set at 132° C. for 15 seconds
(Example 2). The amount of polymer applied to the yarn is believed to be 3 to 5%
0 the weight of the yarn.
[0038] All sized yarn is conditioned one day at 21° C. and 60% RH before testing.
Preparation of Films
[0039] Thin films are cast on a 2 mil Mylar® film with a #30 wire wound rod, dried for 3
minutes at 115° C. and cured for 45 seconds at 132° C. in a forced air oven.
[0040] Evaluation of Results - See Table 2
[0041] Adhesion: The sized yarns are evaluated for adhesion using a laboratory sand tumble
test (as follows):
Sand Tumble Test: Duplicate 3 yd. skeins of sized yarn are placed in an 8 oz. jar
containing 150 g.. of course sand, rotated for 30 minutes on an Atlas Launder-ometer®,
removed and rated for percent of the fiber bundle remaining intact; the sand rating
(STR).
[0042] In a second "adhesion to polyester" test the adhesion to Mylar (thin film) of each
formulation is determined by a crinkle test. The test is designed to measure film
adhesion to polyester sheet by crumbling the sheet by hand and flattening it noting
film separation or cracking. All the formulations including the control have. excellent
adhesion. No cracks or separation are noted. Tack is also rated and none of the films
are tacky.
Durability to a Peroxide Bleach Process
[0043] Each formulation is tested for'durability to a rather stringent process solution.
Thirty yard skeins of the sized yarns are subjected to bleaching in the bleach process
solution with mild agitation at the stated time and temperature conditions. The yarn
is then compared to unbleached yarn for changes in color, feel and filament to filament
adhesion and for the amount of color in the bleach solution.
Bleach Process Solution
[0044] 1% H
20
2 - 50% Active 0.1% Sodium Silicate 0.05% NaOH - 50% Active 0.05% Detergent Triton®
X-305 Rohm and Hass Co. Run for 1 hour at 93° C. Rinse in hot water. The results are
recorded as follows: Yarn Conditions - Excellent = no loss in color or feel Good =
slight loss in feel Fair = separation of yarn filaments Poor = major loss in color
and separation of yarn filaments Bleach Solution - Yellow, pale yellow, pale tinge,
clear in improving order. Solvent Resistance
[0045] Two solvent resistance tests are run - one relating to dry cleaning, the other to
spot cleaning. The dry cleaning test consists of soaking pieces of the thin film,
cast on Mylar, in perchloroethylene for 30 minutes and evaluating changes. In each
case, the wet films are "grabby" and show a slight reduction in adhesion, however,
when dried there are no differences between the soaked and control films. There is
no color bleeding into the perchloroethylene.
[0046] The resistance to spot cleaning is tested by mounting small skeins of yarn on white
cardboard and spraying them with 1,1,1 trichloroethane noting color loss or color
running. This test is done on yarn dried and cured simultaneously (Example 2) and
in all cases there is no loss in color or running of the pigment. Therefore, all are
considered to have excellent spot clean resistance and good durability to dry cleaning.
Formulation Stability
[0047] Each formulation is monitored for stability (settling or coagulation).

Example 3 - Polymer Substantivity to Polyester
[0048] Other emulsion polymers are tested for substantivity to a polyester substrate by
determining the tensile strength of a water wet non-woven polyester fabric employing
the polymer as its binder. High strength indicates good substantivity of the polymer
composition to the polyester or polyester-blend and thus is indicative of good performance,
when formulated, crosslinked and cured, as a permanent size.
[0049] Polymer emulsions (Example E through 0), prepared by the general procedure of Example
A, are formulated to 6% binder solid
[0050] A typical formulation is:

[0051] The pH of the mix may be adjusted with ammonia as desired without significantly effecting
web properties; in these examples it is between 2 and 9.
[0052] Carded polyester web (0.5 oz./yd., 17.2 g./m.
2) is prepare using Dacron® type 54W (Merge 113505) (DuPont) fiber of 1.5 denier and
1.5 in., 3.8 cm., staple length. The webs are supported between two layers of fiberglass
scrim and saturated by 6% polymer solids baths on a Birch Brothers Padder at 40 lbs.
18 kg nip roll pressure with a speed of 7.6 yds./min., 6.9 m./min. The padded webs
are dried for 7 minutes at 65° C. in a forced air oven. To insure that all samples
receive a similar heat treatment, all webs are cured for 1.5 minutes at 150° C. except
when otherwise noted. The finished fabrics weigh 0.7 oz./yd.
2, 24 g./m.
2, and contain 30% binder.
[0053] Fabrics are tested for wet tensile strength after soakinc for 30 minutes in room
temperature water and blotting lightly with a towel after removal from the water bath.
Specimens are cut to 1" x 6.5" (2.5 cm x 16.5 cm) in the machine direction and are
tested on an Instron® tester with a jaw separation of 5" (12.7 cm) and an extension
rate of 2" (5.1 cm)/minute in the machine direction.
[0054] All compositions contain 4% acrylic acid monomer as does Example A which is used
as an internal control for the series. Properties of polymers yielding fabrics with
a water-wet tensile strength similar to that of a fabric of Example A produ sized
yarns having the acceptable adhesion, durability to bleac solvent resistance and stability,characterized
by the polymer o Example A,when formulated and applied as a permanent size to a polyester
or a polyester-blend yarn.

[0055] Inspection of these data shows a number of interesting 'things. There is a marked
drop-off in substantivity when the polymer contains more than 75% butyl acrylate mer
units and, at the other end of the range, when the butyl acrylate mer unit: are as
low as 40% of the polymer. Substitution of methyl methacrylate for half of the styrene
in the copolymer produces a small decrease in the water-wet tensile strength of the
fabric. Replacement of a limited amount of butyl acrylate by ethyl acrylate has a
similar effect.
[0056] When binder A is'used to bond a rayon/polyester (1/1) non-woven fabric a water-wet
tensile strength of 1.6 kgs. is obtaixed, thus the polymer is effective on this substrate
as well. The rayon/polyester fabric is made from
DuPont Dacron® type 54 W (1.5 denier/4.0 cm.) polyester and
FMC viscose rayon (1.5 denier-4.0 cm.). The finished fabric weighs 23.7 g, per sq. meter
and contains 30% binder on fabric weight. Polyester-rayon yarns permanently sized
with Example A polymer, using the procedures and formulations of experiments 1 and
2,are acceptable sized yarns.