U.S. patent number 3,922,462 [Application Number 05/459,465] was granted by the patent office on 1975-11-25 for absorbent nonwoven fabrics.
This patent grant is currently assigned to National Starch and Chemical Corporation. Invention is credited to Stuart H. Ganslaw, Howard Katz.
United States Patent |
3,922,462 |
Katz , et al. |
November 25, 1975 |
Absorbent nonwoven fabrics
Abstract
A permanently absorbent nonwoven fabric comprises a web of
fibers, a crosslinkable latex binder, and a surfactant consisting
of at least one bis-alkyl sulfosuccinate having alkyl substituents
containing 13-14 carbon atoms. The preferred surfactant is
bis-tridecyl sodium sulfosuccinate, and the amount used is
generally 0.2-10.0 weight percent of the total fibers and binder.
The surfactant may be incorporated into the binder latex prior to,
during, or after polymerization.
Inventors: |
Katz; Howard (Hightstown,
NJ), Ganslaw; Stuart H. (Piscataway, NJ) |
Assignee: |
National Starch and Chemical
Corporation (Bridgewater, NJ)
|
Family
ID: |
23824898 |
Appl.
No.: |
05/459,465 |
Filed: |
April 10, 1974 |
Current U.S.
Class: |
442/149 |
Current CPC
Class: |
D04H
1/64 (20130101); D04H 1/587 (20130101); Y10T
442/2738 (20150401) |
Current International
Class: |
D04H
1/64 (20060101); D06N 007/06 () |
Field of
Search: |
;117/14A,14R,161UZ,1C
;19/144.5 ;428/290,411 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Kendall; Ralph S.
Assistant Examiner: Wolfe, Jr.; Charles R.
Claims
We claim:
1. An absorbent nonwoven fabric consisting essentially of
a. a web of fibers,
b. about 5.0 to about 100 weight percent, based on the fibers, of
crosslinkable binder, and
c. about 0.2 to about 10.0 weight percent, based on said fibers and
binder, of at least one surfactant consisting of at least one salt
of a bis-alkyl sulfosuccinate having alkyl substituents each alkyl
containing 13-14 carbon atoms.
2. The fabric of claim 1 wherein said surfactant consists of at
least one alkali metal salt of bis-tridecyl sulfosuccinate.
3. The fabric of claim 1 wherein at least one of said alkyl
constituents is branched.
4. The fabric of claim 1 wherein said surfactant consists of
bis-tridecyl sodium sulfosuccinate hving at least one branched
alkyl substituent.
5. The fabric of claim 3 wherein said binder consists essentially
of a copolymer of at least two .alpha.,.beta.-monoethylenically
unsaturated monomers, one of said monomers being effectively
monofunctional and another of said monomers being effectively
polyfunctional, said effectively monofunctional monomers comprising
from about 85 to about 99 weight percent and said effectively
polyfunctional monomers comprising from about 1 to about 15 weight
percent of said binder.
6. The fabric of claim 5 wherein said copolymer is a crosslinkable
emulsion copolymer.
7. The fabric of claim 5 wherein at least one of said
.alpha.,.beta.-monoethylenically unsaturated monofunctional
monomers is selected from the group consisting of alkyl acrylate,
vinyl acetate, ethylene, vinyl chloride, and mixtures thereof, said
alkyl acrylate having a C.sub.1 -C.sub.12 alkyl group.
8. The fabric of claim 5 wherein at least one of said
.alpha.,.beta.-monoethylenically unsaturated polyfunctional
monomers is selected from the group consisting of acrylamide,
isobutoxy methyl acrylamide, and N-methyol acrylamide.
9. The fabric of claim 3 containing about 0.3 to about 2.0 weight
percent, based on said fibers and binder, of said surfactant.
10. The fabric of claim 3 containing about 10 to about 70 weight
percent, based on said fibers, of said binder.
11. The fabric of claim 1 comprising on a weight basis:
a. a loosely assembled web of said fibers;
b. about 10 to about 70 weight percent, based on said fibers, of
said binder containing at least one
.alpha.,.beta.-monoethylenically unsaturated monofunctional monomer
selected from the group consisting of alkyl acrylate, vinyl
acetate, ethylene, vinyl chloride, and mixtures thereof, said alkyl
acrylate having a C.sub.1 -C.sub.12 alkyl group, and at least one
.alpha.,.beta.-monoethylenically unsaturated polyfunctional monomer
selected from the group consisting of acrylamide, N-methylol
acrylamide and isobutoxy methyl acrylamide, said monofunctional
monomers comprising from about 95 to about 98 weight percent and
said polyfunctional monomers comprising about 2 to about 5 weight
percent of said binder; and
c. about 0.3 to about 2.0 weight percent, based on said fibers and
binder, of bis-tridecyl sodium sulfosuccinate having at least one
branched alkyl substituent.
12. The fabric of claim 3 wherein said binder and said surfactant
comprise on a weight basis about 60-80 parts butyl acrylate, 40-20
parts vinyl acetate, 1.0-3.0 parts acrylamide, 1.0-4.0 parts
N-methylol acrylamide, and 1.5-3.5 parts bis-tridecyl sodium
sulfosuccinate.
Description
BACKGROUND OF THE INVENTION
This invention relates to so-called "nonwoven" fabrics of the type
composed of a loosely assembled web of fibers bound together by a
latex binder. Such bonded nonwoven fabrics have been formed by
impregnating, printing or otherwise depositing an adhesive bonding
material on a base web predominately comprising relatively long
fibers, including those of textile length from about 0.5 inch to
about 2.5 inches or more. The base web of the nonwoven fibers to
which the latex binder is applied can be produced inexpensively and
with low capital investment by carding, garnetting, interlaying,
paper-making procedures, or other known operations for which
automation is possible. The operation of bonding the fibers in
place is much less expensive than conventional spinning and
weaving. In comparison with woven fabric, the bonded nonwoven
fabrics can be made in a much greater range of thicknesses, with a
more homogeneous structure and no unravelling tendency, and with
greater water absorbency, porosity and resiliency, when
required.
To improve the absorbency of the bonded nonwoven fabrics, various
emulsifiers have been used during the emulsion polymerization to
produce the binder, and various wetting agents have been added to
the impregnated medium by which the binder is applied to the fiber
web. For example, bonded nonwoven fabrics for use as household
wipes -- wiping clothes to remove and pick up liquids, wash
furniture and cars, clean kitchens, etc. -- are typically absorbent
because of the presence of anionic surfactants such as dioctyl
sodium sulfosuccinate or sodium dodecyl benzene sulfonate. Such
bonded nonwoven fabrics have not proven to be entirely satisfactory
in use because the emulsifiers and wetting agents are generally
easily extractable by water rinsing, machine washing and/or steam
sterilization, thus rendering the fabric nonabsorbent. Such fabrics
are especially not satisfactory for the common industrial, hospital
and consumer wages where high absorbency after repeated usage is
required.
Accordingly, it is an object of the present invention to provide a
bonded nonwoven fabric incorporating a surfactant which resists
extraction by water rinsing and even steam sterilization.
It is another object to provide such a fabric which is formed by
bonding fibers with a crosslinkable binder latex incorporating a
specific surfactant which resists extraction.
It is a further object to provide such a fabric which comprises
fibers set with a commercially available binder to which a specific
surfactant has added to impart permanent absorbency characteristics
to the fabric.
SUMMARY OF THE INVENTION
It has now been found that the above and related objects of the
present invention are obtained in an absorbent nonwoven fabric
comprising a web of fibers, a crosslinkable binder, and at least
one surfactant consisting of at least one bis-alkyl sulfosuccinate
having alkyl substituents containing 13-14 carbon atoms. The
surfactant is preferably bis-tridecyl sodium sulfosuccinate having
branched alkyl substituents, and the crosslinkable binder is
preferably an emulsion copolymer of at least two
.alpha.,.beta.-monoethylenically unsaturated monomers, one an
effectively monofunctional monomer and the other an effectively
polyfunctional and hence cross-linkable comonomer. Generally the
fabric includes about 5 to about 100 weight percent of the binder
(based on the fiber weight), and about 0.2 to about 10.0 weight
percent of the surfactant (based on the weight of the fibers and
binder).
A preferred fabric comprises a loosely assembled web of fibers,
about 10 to about 70 weight percent (based on the fibers) of
crosslinkable binder, and about 0.3 to about 2.0 weight percent
(based on the weight of the fibers and binder) of bis-tridecyl
sodium sulfosuccinate having at least one branched alkyl
substituent. The binder is preferably comprised of at least one
.alpha.,.beta.-monoethylenically unsaturated monomer selected from
the group consisting of alkyl acrylate, vinyl acetate, ethylene,
vinyl chloride, and mixtures thereof, and at least one
.alpha.,.beta.-monoethylenically unsaturated polyfunctional
crosslinkable comonomer selected from the group consisting of a
crylamide, N-methylol acrylamide and isobutoxy methyl
acrylamide.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
The absorbent nonwoven fabric of the present invention is comprised
of a loosely assembled web of fibers, a crosslinkable polymeric
latex binder formed of at least one
.alpha.,.beta.-monoethylenically unsaturated monofunctional monomer
and at least one .alpha.,.beta.-monoethylenically unsaturated
polyfunctional crosslinking comonomer, and at least one surfactant
of the present invention. Various catalysts, emulsifying and
wetting agents, protective colloids, buffering agents,
plasticizers, thermosetting resins and the like known to those
skilled in the art may optionally be used during formation of the
binder or fabric.
THE FIBERS
The starting layer or mass can be formed by any one of the
conventional techniques for depositing or arranging fibers in a web
or layer. These techniques include carding, garnetting, air-laying,
and the like. Individual webs or thin layers formed by one or more
of the techniques can also be laminated to provide a thicker layer
for conversion into a fabric. In general, the fibers extend in a
plurality of diverse directions in general alignment with the major
plane of the fabric, overlapping, intersecting and supporting one
another to form an open, porous structure. When reference is made
to "cellulose" fibers, those fibers containing predominantly
C.sub.6 H.sub.10 O.sub.5 groupings are meant. Thus, examples of the
fibers to be used in the starting layer are the natural cellulose
fibers, such as cotton, silk and hemp, and the synthetic cellulose
fibers, such as rayon, and regenerated cellulose. Often the fibrous
starting layer contains at least 50% cellulose fibers, whether they
be natural or synthetic, or a combination thereof. Other fibers in
the starting layer may comprise natural fibers such as wool or
jute; artificial fibers such as cellulose acetate; synthetic fibers
such as polyamides (i.e., nylon), polyesters (i.e., "Dacron")
acrylics (i.e., "Dynel," "Acrilan," "Orlon") polyolefins (i.e.,
polyethylene, polyvinyl chloride, polyurethane, etc.), vinyl resin
fibers (i.e., the copolymers of vinyl chloride and vinyl acetate),
siliceous fibers (i.e., glass and mineral wools), alone or in
combination with one another.
The fibrous starting layer or web suitably weighs from about 100
grains to about 2,000 grains per square yard and preferably weighs
about 200 grains to about 800 grains per square yard. This fibrous
starting layer, regardless of its method of preparation, is then
subjected to at least one of the several types of bonding
operations to anchor the individual fibers together to form a
self-sustaining web. Some of the better-known methods of bonding
are overall impregnation or printing the web with intermittent or
continuous straight or wavy lines or areas of binder extending
generally transversely or diagonally across the web and
additionally, if desired, along the web.
THE MONOMERS
At least one .alpha.,.beta.-monoethylenically unsaturated
monofunctional monomer forms the major part of the binder,
generally from about 85 to about 99, preferably from about 95 to
about 98, weight percent of such monomers based on the total binder
monomers in the polymerization.
The monomers useful as this component include vinyl esters of the
formula: ##EQU1## wherein R is a C.sub.1 -C.sub.12 alkyl group, and
preferably a C.sub.1 -C.sub.3 alkyl group. Representative of such
vinyl esters are the preferred vinyl acetate compound, as well as
vinyl propionate, vinyl laurate, etc.
Other monomers useful as this component include the alkyl esters of
acrylic and methacrylic acid having the formula: ##EQU2## wherein R
is a C.sub.1 -C.sub.12 alkyl group, and R' is hydrogen or a methyl
group. Representative of such alkyl esters are methyl acrylate,
ethyl acrylate, butyl acrylate, methyl methacrylate, etc.
Still other monomers useful as this component include the C.sub.1
-C.sub.12 dialkyl esters of maleic, fumaric and itaconic acids
(e.g., dibutyl maleate, dioctyl fumarate, etc.), styrene, vinyl
chloride, vinylidene chloride, ethylene and acrylonitrile.
The monomers useful as this component are effectively
monofunctional at the processing parameters utilized (i.e., the
polymerization temperature, time, etc.) -- i.e., they enter into
chain growth but not crosslinking reactions.
The preferred monomers for this component are alkyl acrylates,
vinyl acetate, ethylene, vinyl chloride and mixtures thereof, If
desired, mixtures of the above monomers may be utilized as this
component. The preferred mixtures of monomers on a weight basis
include a 50-100/0-50 mixture of an alkyl acrylate (such as butyl
acrylate) and vinyl acetate, a 60-100/0-40 mixture of vinyl acetate
and ethylene, a 60-90/10-40 mixture of vinyl chloride and ethylene,
and a 0-100/0-100 mixture of various alkyl acrylates such as ethyl
acrylate and butyl acrylate.
THE CROSSLINKING COMONOMERS
At least one crosslinking .alpha.,.beta.-monoethylenically
unsaturated polyfunctional comonomer forms a minor part of the
binder to effect crosslinking of the binder, generally from about 1
to about 15, preferably from about 2 to about 5, weight percent of
such comonomers based on the total binder monomers (including
comonomers) used in the polymerization.
The comonomers useful as this component include
I. acrylamide and methacrylamide of the formula ##EQU3## wherein R
is hydrogen or a methyl group; II. N-alkylol and alkyl ether
derivatives of (I) having the formula ##EQU4## wherein R is
hydrogen or a methyl group,
R' is hydrogen or a C.sub.1 -C.sub.6 alkyl group, and
R" is (CH.sub.2).sub.1-4, preferably a CH.sub.2 group;
Iii. n-alkyl substituted derivatives of (I) having the formula
##EQU5## wherein R is a hydrogen or a methyl group, and
R' is a C.sub.1 -C.sub.12 alkyl group;
Iv. hydroxy alkyl esters of acrylic or methacrylic acid having the
formula ##EQU6## wherein R is hydrogen or a methyl group, and
R' is (CH.sub.2).sub.2-5, preferably a (CH.sub.2).sub.2 group;
V. glycidyl alkyl esters of acrylic and methacrylic acid (e.g.,
glycidyl acrylate) having the formula ##EQU7## wherein R is
hydrogen or a methyl group, and
R' is (CH.sub.2).sub.1-5, preferably a (CH.sub.2).sub.2 group;
Vi. .alpha.,.beta.-ethylenically unsaturated carboxylic acids (for
example, acrylic, methacrylic, itaconic, fumaric, and maleic acids)
including the mono-alkyl esters of dioic acids (for example, the
mono-alkyl maleate ester having a C.sub.1 -C.sub.12 alkyl group);
and
Viii. diacetone acrylamide, and hydroxy methyl diacetone
acrylamide.
The preferred comonomers are acrylamide, N-methylol acrylamide and
isobutoxy methyl acrylamide.
THE SURFACTANT
The surfactant useful in the practice of the present invention is a
bis-alkyl sulfosuccinate wherein the alkyl substituents each
contain 13-14 carbon atoms, preferably 13 carbon atoms. The
surfactant is preferably an alkali metal salt of the bis-alkyl
sulfosuccinic acid, and at least one of the alkyl group
substituents is preferably branched. The preferred surfactant is
bis-tridecyl sodium sulfosuccinate, especially where at least one
of the tridecyl groups is branched. Similar compounds having lower
alkyl groups substituents (e.g., 12 carbon atoms and less),
especially straight chain lower alkyl groups, are rapidly extracted
during rinsing, washing or steam sterilization; similar compounds
with higher alkyl group substituents (e.g., 15 carbon atoms and up)
are so insoluble as to interfere with their incorporation into the
binder latex, or, when incorporated, do not impart permanent
absorbent properties to the fabric.
The amount of surfactant used is from about 0.2 to about 10.0,
preferably about 0.3 to about 2.0 weight percent based on the
combined weight of the fibers and binder. The surfactant may be
used alone or in combination with various emulsifying and/or
wetting agents. It may be added to the binder latex prior to
polymerization, added intermittently or continuously during
polymerization, or even added subsequent to polymerization.
THE CATALYST
Various free-radical forming catalysts can be used in carrying out
the polymerization of the monomers, such as peroxide compounds.
Combination type catalysts employing both reducing agents and
oxidizing agents can also be used. The use of this type of combined
catalyst is generally referred to in the art as "redox
polymerization" or "redox system". The reducing agent is also often
referred to as an activator and the oxidizing agent as an
initiator. Suitable reducing agents or activators include
bisulfites, sulfoxylates, or other compounds having reducing
properties such as ferrous salts and tertiary aromatic amines
(e.g., N, N-dimethyl aniline). The oxidizing agents or initiators
include hydrogen peroxide, organic peroxides such as benzoyl
peroxide, t-butyl hydroperoxide and the like, persulfates such as
ammonium or potassium persulfate, perborates, and the like.
Specific combination type catalysts or redox systems which can be
used include hydrogen peroxide and zinc formaldehyde sulfoxylate;
hydrogen peroxide, ammonium persulfate, or potassium persulfate,
with sodium metabisulfite, sodium bisulfite, ferrous sulfate,
dimethyl aniline, zinc formaldehyde sulfoxylate or sodium
formaldehyde sulfoxylate.
In general, it is advantageous to utilize more water-soluble
peroxides, such as hydrogen peroxide, rather than the more
oil-soluble peroxides, such as t-butyl hydroperoxide, in the redox
system catalyzing the monomer polymerization. Redox catalyst
systems are described, for example, in "Fundamental Principles of
Polymerization" by G. F. D'Alelio (John Wiley and Sons, Inc., New
York, 1952) pp. 333 et seq. Other types of catalysts that are
wellknown in the art can also be used to polymerize the monomers
according to this invention, with or without the addition of
reducing agents or other activating materials.
The activator is ordinarily added in aqueous solution and the
amount of activator is generally 0.25 to 1 times the amount of
catalyst.
EMULSIFYING AGENTS
The emulsifying agent can be any of the non-ionic or anionic
oil-in-water surface active agents. In the following discussion of
emulsifying agents, frequent reference will be made to a cloud
point of a particular agent. The cloud points which are recited are
based on 1 weight percent aqueous solutions of the agent. A
relatively hydrophobic agent is one having a cloud point below
190.degree.F. and a relatively hydrophilic agent is one having a
cloud point of 190.degree.F. or above.
A single emulsifying agent can be used or the emulsifying agents
can be used in combination. When combinations of emulsifying agents
are used, it is advantageous to use a relatively hydrophobic agent
or a relatively hydrophobic agent in combination with a relatively
hydrophilic agent. The amount of emulsifying agent used is
generally from about 0.1 to about 10, preferably 0.5-7.0, weight
percent of the monomers used in the polymerization.
Suitable nonionic emulsifying agents include polyoxyethylene
condensates represented by the following general formula:
where R is the residue of a fatty alcohol, acid, amide, or amine
having from 10 to 18 carbon atoms or an alkyl phenol having from 10
to 18 carbon atoms; and where n is an integer of 1 or above and
preferably between 5 and 30. Some specific examples of
polyoxyethylene condensates which can be used include
polyoxyethylene aliphatic ethers such as polyoxyethylene lauryl
ether, polyoxyethylene oleyl ether, polyoxyethylene hydroabietyl
ether and the like; polyoxyethylene alkaryl ethers such as
polyoxyethylene nonylphenyl ether, polyoxyethylene octylphenyl
ether and the like; polyoxyethylene esters of higher fatty acids
such as polyoxyethylene laurate, polyoxyethylene oleate and the
like as well as condensates of ethylene oxide with resin acids and
tall oil acids; polyoxyethylene amide and amine condensates such as
N-polyoxyethylene lauramide and N-lauryl-N-polyoxyethylene ethyl
amine and the like; and polyoxyethylene thioethers such as
polyoxyethylene n-dodecyl thioether.
Some examples of nonionic emulsifying agents which can be used
include a polyoxyethylene nonylphenyl ether having a cloud point of
between 126.degree. and 130.degree.F and marketed by GAF
Corporation under the trademark "Igepal CO-630," and a
polyoxyethylene nonylphenol ether having a cloud point of about
212.degree.F. and marketed under the trademark "Igepal CO-887." A
similar polyoxyethylene nonylphenyl ether having a cloud point of
about 86.degree.F. is marked under the trademark "Igepal CO-610"
and is also a good emulsifying agent. Another agent is a
polyoxyethylene octylphenyl ether having a cloud point of between
80.degree.F and 160.degree.F. and marketed by Rohm & Haas
Company under the trademark "Triton X-100." Yet another agent is
nonylphenoxy polyethoxyethanol marketed under the trademark "Triton
X-305." Other emulsifying agents include a polyoxyethylene oleyl
ether having a cloud point of between 80.degree.F. and
160.degree.F. and marketed under the trademark "Atlas G-3915," and
a polyoxyethylene lauryl ether having a cloud point above
190.degree.F. and marketed under the trademark "Brij 35".
The nonionic emulsifying agents which can be used according to this
invention also include a series of surface active agents known as
"Pluronics." The "Pluronics" have the general formula:
where a, b and c are integers between 1 and 100. As the ratio of b
to a and c increases, the compounds become less water soluble or
more oil soluble and thus more hydrophobic, while as the ratio
decreases the compounds become more water soluble and less oil
soluble. An example of this class is "Pluronic L-64" which has a
cloud point of about 140.degree.F. and a polyoxypropylene chain
having a molecular weight of 1,500 to 1,800 and a polyoxyethylene
content that is 40 to 50 percent of the total weight of the
molecule. Another useful example is "Pluronic F-68", a
polyoxyethylene-polyoxypropylene glycol having a cloud point of
about 212.degree.F. and a polyoxyethylene content of about 80 to 90
percent of the total weight of the molecule.
A class of suitable emulsifying agents are a series of ethylene
oxide adducts of acctylenic glycols sold commercially under the
name "Surfynols." This class of compounds can be represented by the
formula: ##EQU8## in which R.sub.1 and R.sub.2 are alkyl radicals
containing from three to 10 carbon atoms, R.sub.2 and R.sub.3 are
selected from the group consisting of methyl and ethyl, and x and y
are integers having the sum in the range of 3 to 60, inclusive.
Representative of the "Surfynols" are "Surfynol 465" which is an
ethylene oxide adduct of 2,4,7,9-tetramethyl decynediol containing
an average of 10 moles of ethylene oxide per mole of the surface
active agent. "Surfynol 485" corresponds to "Surfynol 465" but
contains an average of 30 moles of ethylene oxide per mole of
surface active agent. "Surfynol 485" has a cloud point about
212.degree.F.
Anionic emulsifying agents which can be employed herein include
anionic compounds obtained by sulfonation of fatty derivatives such
as sulfonated tallow, sulfonated vegetable oils and sulfonated
marine animal oils. Commercially available emulsifiers of this
group are "Tallosan RC," a sulfonated tallow marketed by General
Dyestuff Corporation; "Acidolate," a sulfonated oil marketed by
White Laboratories, Inc.; and "Chemoil 412," a sulfonated castor
oil marketed by Standard Chemical Company.
Various sulfonated and sulfated fatty acid esters of mono- and
polyvalent alcohols are also suitable such as "Nopco 2272R," a
sulfated butyl ester of a fatty ester marketed by Nopco Chemical
Company; "Nopco 1471," a sulfated vegetable oil marketed by Nopco
Chemical Company; "Sandozol N," a sulfated fatty ester marketed by
Sandoz, Inc.; and "Stantex 322," an ester sulfate marketed by
Standard Chemical Products, Inc.
Sulfated and sulfonated fatty alcohols are also useful as an
emulsifier and include anionic agents such as "Duponal ME," a
sodium lauryl sulfate; "Duponal L142," a sodium cetyl sulfate;
"Duponal LS," a sodium oleyl sulfate which is marketed by E. I.
DuPont de Nemours and Company; and "Tergitol 4," a sodium sulfate
derivative of 7-ethyl-2-methyl, 4-undecanol, "Tergitol 7," a sodium
sulfate derivative of 3,9-diethyl tridecanol-6, and " Tergitol 08,"
a sodium sulfate derivative of 2-ethyl-1-hexanol, which are
marketed by Union Carbide Corporation, Chemical Division.
A particular useful class of anionic agents which can be employed
comprises the C.sub.1 to C.sub.12 alkyl and C.sub.5 to C.sub.8
cycloalkyl esters of alkali metal sulfoalkanedioic acids having
from three to about six carbons. Examples of these include diethyl
sodium sulfosuccinate, di-n-octyl potassium sulfosuccinate,
dicyclohexyl lithium sulfoglutarate, di(methylcyclopentyl) sodium
sulfoadipate, dicycloheptyl cesium sulfomalonate, diamyl sodium
sulfoadipate, etc. A useful member of this class is di-octyl sodium
sulfosuccinate marketed by American Cyanamid Co. under the
trademark "Aerosol-OT."
The half esterified, half ethoxylated derivatives of the
aforementioned alkali metal sulfoalkanedioic acids are preferred
emulsifiers. These agents have one of the carboxylic acid sites
esterified with a C.sub.1 to C.sub.12 alkanol or C.sub.5 to C.sub.8
cycloalkanol, and the remaining carboxylic acid site condensed with
from two to about 20 (preferably from eight to 16, and most
preferably from 10 to 12) ethylene oxide units per mole to add a
polyethoxylol group. Examples of these are: hexyl polyethoxylol
sodium sulfosuccinate, isopropyl polyethoxylol potassium
sulfoglutarate, decyl polyethoxylol lithium sulfoadipate,
cyclohexyl polyethoxylol cesium sulfomalonate, cycloheptyl
polyethoxylol sodium sulfosuccinate, cyclooctyl polyethoxylol
potassium sulfosuccinate, etc.
Another preferred anionic emulsifying agent is sodium dodecyl
benzene sulfonate, commonly called "SDBS" and used in a 20 weight
percent solution.
OTHER POLYMERIZATION REAGENTS
A protective colloid may optimally be used to increase the
adhesiveness of film prepared from the latex. When the protective
colloid is used, it is desirable to decrease the amount of
emulsifying agent used by an amount equivalent to the weight of the
protective colloid, since the latter also aids the stability of the
latex. This agent can be any of a wide range of compounds that is
available for use as protective colloids, including many natural
substances such as casein, natural gums, gelatins, agar, dextrin
and globulin; suitably chemically modified polysaccharides such as
hydrolyzed starch, hydroxyethyl cellulose, methyl and carboxymethyl
cellulose; and synthetic colloids such as polyvinyl alcohol, alkali
metal or ammonium salts of sulfonated polystyrene, water soluble
interpolymers of acrylic acid and 2-ethylhexyl acrylate, copolymers
of acrylamide and acrylic acid, partially hydrolyzed polyacrylamide
having from 10 to 70 percent of its amide groups as carboxylic acid
or alkali metal carboxylate groups, etc. The polyvinyl alcohols,
which are prepared by hydrolysis of polyvinyl esters, typically
polyvinylacetate, are preferred protective colloids and can be used
with from 80 to 100 percent, preferably from about 90 to 100
percent of the ester groups hydrolyzed to hydroxyl groups.
A buffering agent can be used, to maintain the pH at a value from
about 2.0 to 7.0, preferably from about 2.5 to 5.0, by periodic
addition of the buffering agent. Suitable agents comprise the
alkali metal or ammonium salts of weak acids; e.g., sodium
carbonate, sodium bicarbonate, sodium acetate, potassium
bicarbonate, lithium carbonate, potassium acid phthalate, potassium
citrate, sodium acetate, potassium acid phosphate, and others
well-known in the polymerization art.
Various polymerization modifiers may optimally be used in small
quantities to modify the molecular weight of the copolymers formed
during polymerization. For example, various polyfunctional agents,
such as divinyl benzene and allyl methacrylate, may be used to
increase molecular weight; various chain transfer agents, such as
the mercaptans and alcohols, may be used to decrease molecular
weight.
THE POLYMERIZATION PROCESS
The polymerization of the aforementioned monomers is performed by
emulsion polymerization, generally under batch conditions; however,
continuous processing can be employed if desired. The reactor used
for the polymerization can be a jacketed kettle having stirring
means with provisions to circulate a cooling medium through the
jacket of the kettle to maintain the desired temperature. The
aqueous medium is stirred to maintain dispersion of the monomers
and the copolymer in the aqueous medium.
A suitable emulsifying agent of the anionic or nonionic types, or
combinations thereof, is used in the polymerization. The amount of
emulsifying agent is generally from about 0.1 to about 10,
preferably from about 1 to about 5, weight percent of the monomers
used in the polymerization.
A water soluble, free radical catalyst such as a water soluble
peracid or salt thereof is used as the initiating catalyst and this
can be used alone or in combination with an active reducing agent
in a redox couple. The catalyst is used in concentration from about
0.01 to about 2, preferably from about 0.1 to about 0.5, weight
percent of the monomers used in the polymerization.
The surfactant of the present invention is generally added to the
polymerization latex in an amount of from about 0.2 to about 10.0,
preferably 0.3-2.0, weight percent based on the combined weight of
binder monomers and fibers.
If desired, the polymerization medium can also contain a minor
quantity of a protective colloid to improve the adhesiveness of the
product, generally from about 0.1 to about 3.0, preferably 0.5-1.5,
weight percent based on the monomers used in the
polymerization.
If desired, the polymerization medium can also contain a minor
quantity of a buffering agent, generally from about 0.1 to about
0.5, preferably 0.2-0.4, weight percent of the monomers used in the
polymerization.
Polymerization is performed conventionally--typically at a
temperature of about 30.degree.-90.degree.C, preferably
40.degree.-70.degree.C, for sufficient time to achieve a low free
monomer content; e.g., from 1 to about 10 hours, preferably from 5
to about 8 hours, to produce a latex having less than 3, preferably
less than 1.5, weight percent free monomer.
The preferred procedure is a modified batch processing wherein the
major amounts of some or all the comonomers and emulsifier are
charged to the reaction vessel after polymerization has been
initiated. In this manner, control over the copolymerization of
monomers having widely varied degrees of reactivity can be
ahieved.
It is preferred to add the .alpha.,.beta.-monoethylenically
unsaturated monomers (e.g., vinyl acetate) intermittently or
continuously over the polymerization period. The
.alpha.,.beta.-monoethylenically unsaturated polyfunctional
crosslinking comonomers (e.g., N-alkyl methacrylamide or
acrylamide) are preferably slowly added during polymerization to
avoid an excessive increase in viscosity of the latex which
otherwise occurs when the entire amount of these comonomers is
added to the initial charge to the polymerization vessel. (The
catalyst is also preferably continuously or intermittently added
during the polymerization.) From 40 to 100 percent of the amount of
these comonomers can be added in this fashion, the balance, if any,
being introduced with the initial charge.
The emulsifier used in the polymerization can also be added, in its
entirety, to the initial charge to the polymerization zone or a
portion of the emulsifier (e.g., from 90 to 25 percent thereof) can
be added continuously or intermittently during polymerization.
The surfactant is preferably continuously or intermittently added
during the polymerization, although at least a portion thereof may
be charged to the reactor at the start of polymerization.
The latex produced by this polymerization can contain from about 35
to 65 weight percent solids comprised chiefly of the interpolymers.
The preferred contents of solids are from 40 to 60, and most
preferably from 50 to 60, weight percent.
APPLICATION OF BINDER TO FIBERS
The binder described above is suitably used to prepare nonwoven
fabrics by a variety of methods known to the art which, in general,
involve the impregnation of a loosely assembled mass of fibers with
the binder latex followed by moderate heating to dry the mass. In
the case of the present invention this moderate heating also serves
to cure the binder by forming a cross-linked interpolymer.
The amount of binder, calculated on a dry basis, applied to the
fibrous starting web, suitably ranges from about 5 to about 100
weight percent of the starting web, preferably from about 10 to
about 70 weight percent.
If the surfactant has not been added already as part of the binder
polymerization process, it is incorporated physically into the
binder latex prior to application of the binder latex to the fiber
mass. Thus an alcohol solution of the surfactant (with or without a
plasticizer) may even be stirred into an available polymerized
commercial binder latex formulated from the aforementioned
monomers, cross-linking comonomers, and possibly additional
surfactants to increase the longevity of the absorbency of the
fabric to be produced.
The binder dispersion may be applied to the dry fibers after the
formation or deposition of the web or mat so as to penetrate
partially into or completely through the interior of the fibrous
products. Alternatively, the binder dispersion may be applied to
the fibers as they fall through the settling chamber to their point
of deposition. This is advantageously obtained by spraying the
binder dispersion into the settling chamber at some intermediate
point between the top and the bottom thereof. By so spraying the
fibers as they descend to the point of collection, it is possible
to effect a thorough distribution of the binder among the fibers
before they are collected into the product. In the production of
certain fibrous products wherein a hot molten mass of a polymer,
such as nylon or a fused siliceous mass or glass, is disrupted by
jets of heated air or steam, the binder dispersion may be sprayed
directly on the fibers -- while still hot and very shortly before
their deposition -- so that quickly after deposition the binder
sets and so bonds the fibers in proper relationship. Preferably,
however, application of the binder dispersion to the fibrous
product is made at room temperature to facilitate cleaning of the
apparatus associated with the application of the binder dispersion.
The binder dispersion may be applied to one or both surfaces of the
fibrous product, or it may be distributed through the interior as
well.
The binder of the present invention may be applied in conjunction
with other binders, such as glue. Similarly, the use of potentially
adhesive fibers within the fibrous product may also be resorted to
in conjunction with the use of a binder of the present
invention.
The aqueous dispersion of the binder may optionally contain from
about 1/2 to 3% by weight of a wetting agent to assist penetration
of the fibrous web or mat to which it is applied, and also it may
optionally contain either a foaming agent to provide the binder in
a foamed condition in the final product, or a defoamer when the
ingredients of the aqueous dispersion have a tendency to give rise
to foaming and in a particular case such foaming is undesirable.
The conventional wetting agents, including the alkali metal salts
of di(C.sub.6 -C.sub.12) alkyl sulfosuccinic acid, such as the
sodium salt of dioctylsulfosuccinic acid, may be used. The wetting
agent may also serve as the emulsifier in preparing the polymer
latex or it may be added after production of the latex.
Conventional foaming and defoaming agents may be employed, such as
sodium soaps including sodium oleate for foaming and octyl alcohol
or certain silicones for defoaming.
Optionally the flexibility and softness of the fabric can be
increased by the addition of a hydrophobic external plasticizer to
the binder composition without loss of desirable properties.
Examples of external plasticizers which are suitably used include
dibutoxyethylphthalate, dibutyl phthalate, tricresyl phosphate and
low molecular weight polyesters. A typical plasticizer as isodecyl
diphenyl phosphate marketed by Monsanto Chemical Company under the
trademark "Santocizer 148." These external components may be added
just before application if their stability in the dispersion or
solution is low, or they may be formulated into the aqueous
dispersion of the binder and stored if their stability in aqueous
dispersion is high.
Various thermosetting resins may optionally be added to the binder
latex to improve the strength of the resultant fabric. Typical of
the useful thermosetting resins are the condensates such as the
melamine-formaldehyde and ureaformaldehyde condensates, the
methylated and methoxy alkyl cyclic ureas, and the methylolated and
methoxyalkyl carbamates. Typically the thermosetting resins are
used in quantities not exceeding 20 weight percent, based on the
monomers used in the polymerization, the resins being added in
solution to the binder latex with agitation before, during or after
polymerization.
An acid catalyst may be optionally included in the aqueous
dispersion at the time it is applied to the fibrous web or it may
be applied to the fibrous web before or after the copolymer is
applied. Examples of acidic catalysts that may be employed include
oxalic acid, dichloroacetic acid, para-toluenesulfonic acid, and
acidic salts such as ammonium sulfate or chloride and amine salts,
such as the hydrochloride of 2-methyl-2-aminopropanol-1.
The impregnated web is then drried and cured. Thus, the fabrics are
suitably dried by passing them through an air oven or the like and
then through a curing oven. Ordinarily, drying is effected at
150.degree.-200.degree.F. for 4-6 min., followed by curing at
300.degree.-310.degree.F. for 3-5 min. or more. However, other
time-temperature relationships can be employed as is well known in
the art, shorter times at higher temperatures or longer times at
lower temperatures being used. For example, the curing step can be
carried out at 280.degree.F. for about 15 min. or more. However,
economic considerations make the use of excessively long times
undesirable, and the upper temperature limit is governed by the
nature of the fibers. Temperatures which degrade the fibers are, of
course, avoided. However, if the fibers are heat resistant,
temperatures even as high as 350.degree.F. or higher can be used
with times of 5-10 min. or more. In some cases, if desired, the
drying and curing can be effected in a single exposure or step,
e.g., at 300.degree.F. for 5-10 min.
A preferred binder composition (including the surfactant of the
present invention) is set forth below, all parts being by weight:
60-80 parts butyl acrylate 40-20 parts vinyl acetate 1.0-3.0 parts
acrylamide 1.0-4.0 parts N-methylol acrylamide 1.5-3.5 parts
bis-tridecyl sodium sulfosuccinate
EXAMPLES
The following examples illustrate the efficacy of the present
invention, and are intended to be illustrative only and not
limitative of the invention. All parts are by weight unless
otherwise indicated.
The procedures utilized in Examples 14-15 to determine fabric
absorbency are based on the following test format. A sample (4 in.
.times. 4 in.) of the fabric is folded twice to give a 2 in.
.times. 2 in. square which is then passed between steel rollers at
60 p.s.i. A paper clip is attached to weight the sample, which is
then placed on the top of a water bath in a 400 ml beaker at
ambient temperature. The time required for the sample to become
saturated is the "wet" time and the time required for the sample to
sink completely below the surface of the water is the "sink" time.
The recorded "wet" and "sink" times are the average of four
tests.
The initial absorbency test is conducted on a sample which has been
conditioned to ambient or room temperature. The absorbency test
after two extractions is conducted on a sample which has undergone
two of the following extraction cycles. The sample (approximately 3
grams) is soaked while tumbling for 30 minutes in a half gallon jar
containing 1,500 ml of distilled water, after which the liquid is
squeezed out and the web is dried at room temperature. The
absorbency test after steam sterilization is conducted on a sample
which has been steam sterilized for 30 minutes at 130.degree.C
prior to testing.
EXAMPLES 1-12
The identity and quantity of each of the additions utilized in each
"addition" of these examples are indicated in Table I. Addition "A"
is added to a 2 liter flask equipped with agitator, condenser and
nitrogen purge. 10% of Addition "B" is also added to the flask, and
the contents are then purged with nitrogen while heating to
70.degree.C. The contents are maintained for 15 minutes at
75.degree.C to insure initiation of polymerization, after which
Additions "C" and "D," and the remainder of Addition "B" are added
uniformly over a 4 hour period, the temperature of the contents
being maintained at 75.degree.C. After the slow additions are
completed, the contents are maintained for an additional 90 minutes
at 75.degree.C, after which the contents are cooled (30.degree.C)
and discharged.
EXAMPLE 13
The identity and quantity of the ingredients utilized in each
"addition" of this example are indicated in Table II. Addition "A"
is added to a 1 liter Paar reactor capable of withstanding 1,000
psig, and equipped with two pumps, a nitrogen purge, and evacuating
means. The contents are then subjected to two purging cycles, each
purging cycle consisting of a nitrogen purge to 100 psig, followed
by evacuation to 25 inches of mercury. After completion of the two
purging cycles, and while the contents are still under vacuum, mild
agitation is commmenced and Addition "B" is permitted to be sucked
into the reactor. The contents are then heated to 70.degree.C while
adding a sufficient quantity of ethylene (Addition "C") to maintain
a pressure of 750 psig. When the contents reach 70.degree.C, 10% of
Addition "E" is added; after a 20 minute hold, Addition "C" is
added uniformly over 4 hours, and Addition "E" is added uniformly
over 6 hours, the pressure being maintained at 750 psig throughout
the slow additions by the addition of ethylene (Addition "C").
After the slow additions are completed, the contents are held at
75.degree.C for 1 hour, and finally cooled, vented and
discharged.
EXAMPLE 14
The identity and quantity of the ingredients utilized in each
"addition" of this example are indicated in Table II. Addition "A"
is added to the reactor of Example 13, and two purging cycles
similar to those of Example 13 are performed. Thereafter Addition
"B" is allowed to be sucked into the reactor. Next the contents are
heated to 50.degree.C., with sufficient ethylene (Addition "C")
being introduced to maintain a pressure of 500 psig. Immediately
upon the contents reaching the temperature of 50.degree.C.,
Addition "D" is uniformly added over a period of 6.5 hours, and 30
minutes after that temperature is reached, Additions "E" and "F"
are added uniformly over a period of 5.0 hours. Upon completion of
the slow additions, the contents are held for 15 minutes, and then
Addition "G" is added over a 50 minute period. The contents are
then agitated at 50.degree.C for 30 minutes, and finally cooled to
45.degree. C before venting and discharge.
EXAMPLE 15
Each of the binder latices prepared according to Examples 1-14 is
diluted with water to 13 weight percent solids. Carded rayon test
webs weighing 200 grains per sq. yard are then saturated with the
diluted binder latices to provide a 20 weight percent dry resin
add-on (i.e., 20 parts dry binder per 100 parts of web). The
impregnated webs are then dried at room temperature, and cured for
2 minutes at 130.degree.C in a forced hot air oven. The dried and
cured test webs are then tested, the results being indicated in
Table III.
Table III illustrates that while all fabrics (except those formed
with the binders of Examples 8 and 12) displayed a good initial
absorbency of less than 300 seconds, only the fabrics containing
the surfactant of the present invention also displayed a good
absorbency of less than 300 seconds after two extractions or steam
sterilization. More particularly, Examples 8 and 9 illustrate that
the use of normal and even excessive amounts of a conventional
anionic emulsifying agent such as SDBS (sodium dodecyl benzene
sulfonate) does not provide permanent absorbency. Examples 10-12
illustrate that the addition of a second conventional anionic
emulsifying or wetting agent such as Aerosol OT (di-octyl sodium
sulfosuccinate), di-decyl sodium sulfosuccinate, and di-dodecyl
sodium sulfosuccinate, respectively, does not provide permanent
absorbency.
EXAMPLE 16
This example illustrates the utility of bistridecyl sodium
sulfosuccinate as an additive for commercially available latex
binders to improve the longevity of their absorbency
characteristics.
Four commercial binder latices of the National Starch and Chemical
Corporation of Plainfield, N.J. are tested according to the
procedures of Example 15 for their utility in forming permanent
absorbing fabrics. Each of the samples tested had sink times in
excess of 300 seconds after two extractions. Next the same
commercial binder latices are modified by the addition of 1.53
weight percent of a surfactant (based on the resin solids), the
surfactant being added as a 20% active mixture of surfactant,
benzyl butyl phthalate, and isopropanol (20/60/20 on a weight
basis). When the solution contained di-octyl sodium sulfosuccinate
as surfactant, the samples produced had sink times in excess of 300
seconds after two extractions. When the solution contained
bistridecyl sodium sulfosuccinate as surfactant, the samples had
the low sink times indicated in Table IV.
This example also illustrates the efficacy of bisalkyl sodium
sulfosuccinates having higher molecular weight alkyl group
substituents relative to those having lower molecular weight alkyl
group substituents. This example further illustrates that the
surfactant of the present invention may be added to the binder
latex after polymerization of the binder latex has been
completed.
To summarize, a permanently absorbent nonwoven fabric has been
described which is particularly well suited for the industrial,
hospital and consumer usages where high absorbency after repeated
usage is required. The permanent absorbency is achieved by
utilization of a specific surfactant which may be incorporated into
the fabric either as a component of the crosslinkable binder during
polymerization or as a blend of a crosslinkable polymeric binder
and the special surfactant.
Now that the preferred embodiments of the present invention have
been described in detail, various modifications and improvements
thereon will become readily apparent to those skilled in the art.
Accordingly, the spirit and scope of the present invention is to be
considered as defined not by the foregoing disclosure, but only by
the appended claims.
TABLE I
__________________________________________________________________________
EXAMPLES 1 2 3 4 5 6 7 8 9 10 11 12
__________________________________________________________________________
INGREDIENTS ADDITION "A" WATER 430 430 430 430 430 430 430 430 430
430 430 430 SDBS (20%) 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0
1.0 TRITON X-305 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8 1.8
AMMONIUM PERSULFATE 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4 0.4
ADDITION "B" VINYL ACETATE 400 -- 200 80 -- 200 200 200 200 200 200
200 BUTYL ACRYLATE -- -- 200 -- 240 200 200 200 200 200 200 200
ETHYL ACRYLATE -- 400 -- 320 120 -- -- -- -- -- -- -- ACRYLONITRILE
-- -- -- -- 40 -- -- -- -- -- -- -- BIS-TRIDECYL SODIUM
SULFOSUCCINATE (80%) 10.0 15.0 25.0 7.5 25.0 25.0 25.0 -- -- -- --
-- DI-DODECYL SODIUM SULFOSUCCINATE (100%) -- -- -- -- -- -- -- --
-- -- -- 6.0 DI-DECYL SODIUM SULFO- SUCCINATE (50%) -- -- -- -- --
-- -- -- -- -- 25.0 -- GLYCIDYL METHACRYLATE -- -- -- -- 10.0 -- --
-- -- -- -- -- ACRYLIC ACID -- -- -- -- -- 15.0 -- -- -- -- -- --
ADDITION "C" WATER 120 120 120 120 100 100 100 120 120 120 120 100
SDBS (20%) 15.0 15.0 15.0 15.0 15.0 15.0 15.0 15.0 60.0 15.0 15.0
15.0 TRITON X-305 6.5 6.5 6.5 6.5 6.5 6.5 6.5 6.5 6.5 6.5 6.5 6.5
ACRYLAMIDE -- -- -- -- -- -- 15.0 -- -- -- -- -- N-METHYOL
ACRYLAMIDE (60%) 10.0 20.0 25.0 7.5 -- -- -- 20.0 20.0 20.0 20.0
25.0 AEROSOL-OT -- -- -- -- -- -- -- -- -- 5.0 -- -- ADDITION "D"
WATER 50 50 50 50 50 50 50 50 50 50 50 50 AMMONIUM PERSULFATE 1.0
1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0 1.0
__________________________________________________________________________
TABLE II ______________________________________ EXAMPLE 13 14
______________________________________ INGREDIENTS ADDITION A WATER
330 260 SODIUM ACETATE 0.85 0.5 IGEPAL CO-977 8.5 SDBS (20%) 3.2
2.2 SODIUM BISULFATE 2.40 FERROUS SULFATE 44 ppm SODIUM PERSULFATE
1.7 ADDITION B VINYL ACETATE 20 VINYL CHLORIDE 30 ADDITION C
ETHYLENE (cp GRADE) 750 psig 500 psig ADDITION D VINYL ACETATE 280
BIS-TRIDECYL SODIUM SULFOSUCCINATE 15.0 N-METHYLOL ACRYLAMIDE (60%)
16.7 IGEPAL CO-977 4.0 SDBS (20%) 2.0 WATER 130 45 SODIUM ACETATE
1.0 SODIUM FORMALDEHYDE SULFOXYLATE 0.41 ADDITION E WATER 40 1.5
AMMONIUM FERSULFATE 2.40 VINYL CHLORIDE 30 ISO-BUTOXY METHYL
ACRYLAMIDE 8.5 BIS-TRIDECYL SODIUM SULFOSUCCINATE 10 ADDITION F
WATER 35 SDBS (20%) 35 ADDITION G BIS-TRIDECYL SODIUM
SULFOSUCCINATE 10 SANTOCIZOR 140 15 ISOPROPYL ALCOHOL 5
______________________________________
TABLE III
__________________________________________________________________________
INITIAL ABSORBENCY ABSORBENCY AFTER 2 ABSORBENCY AFTER STEAM
EXTRACTIONS STERILIZATION EXAMPLE NO. WET SINK WET SINK WET SINK
__________________________________________________________________________
1 <1 2.0 6.6 12.9 2 <1 1.9 5.9 107 3 <1 2.5 26.2 40.8 2.0
<10 4 <1 2.1 25.5 70.5 5 <1.0 1.5 <1 5.4 6 <1 1.7
2.7 58.1 7 <1 1.5 1.5 7.6 8 >300 >300 >300 >300 9
<1.0 2.8 >300 >300 10 2.0 5.0 >300 >300 >300
>300 11 <1.0 2.05 >300 >300 12 >300 >300 >300
>300 13 <1 3.0 4.1 7.4 14 <1 3.0 37.5 37.5
__________________________________________________________________________
TABLE IV ______________________________________ SINK TIME BINDER
LATICES After 2 Extractions ______________________________________
25-4280* 215 25-4445* 54 25-4260* 200 25-2833** 80
______________________________________ *A crosslinkable binder
latex containing an acrylate copolymer, and at least one
conventional emulsifier. **A crosslinkable binder latex containing
a vinyl acetate/acrylate copolymer, and at least one conventional
emulsifier.
* * * * *