[0001] This invention relates to the use of polymers as barrier coatings in paper applications.
By barrier coating is meant a layer or coating that prevents the penetration of oil,
water, or moisture through paper products. Barrier coatings are typically applied
to cardboard, paperboard, corrugated paperboard, Kraft paper, and ream wrap.
[0002] Containers made from paper may be used to transport fruits, meats, vegetables, candy,
and the like. There are several problems associated with the use of these containers.
One problem is that the containers may become wet when the materials transported in
the container are wet or when the container is exposed to rain or a humid environment.
The paper the containers are made from generally weakens and stains as a result of
exposure to water. This may lead to the container breaking open and the spilling of
the contents of the container. In order to avoid this problem, containers are generally
coated with a material such as wax to prevent water from contacting the paper.
[0003] One problem with wax coated containers is that although wax is effective at preventing
water and oil from contacting the paper, the wax generally must be applied as a thick
coating. By thick is meant a dry coating of from 55 microns to 125 microns. The thick
coating adds significantly to the weight of the container. In fact, the wax may account
for from 20% to 40% by weight of the coated container. Therefore, it is desirable
to provide a barrier coating that is more efficient than wax so that a thinner coating
may be applied without sacrificing barrier coating properties.
[0004] For economic reasons as well as the preservation of natural resources, it is desirable
to recycle the containers used to transport fruits, meats, vegetables, candy, and
the like. However, a second problem with wax coated containers is that the wax coating
makes it difficult to recycle the paper the container is made from. The wax adheres
to the paper fibers, making it difficult to re-pulp the fibers. There is a continuing
need for a barrier coating that is more efficient than wax and easier to remove from
paper fibers than wax.
[0005] We have surprisingly found that the use of a polymer as a barrier coating allows
a reduction in the amount of coating used without sacrificing barrier coating properties,
while improving the ability to re-cycle the coated paper.
[0006] U.S. Pat. No. 5,521,266 discloses a method for forming polymers from hydrophobic
monomers. The disclosed method utilizes macromolecular organic compounds which have
a hydrophobic cavity to complex monomers which have low water solubility. This enables
the formation of polymers from low water solubility monomers by emulsion polymerization.
Suitable monomers for use in the method for forming polymers include lauryl methacrylate
and stearyl methacrylate. The patent does not disclose the utility of the polymers
as barrier coatings.
[0007] WO 94/26513 patent application discloses recyclable paper stock coated with an emulsion
containing an acrylic-styrene copolymer and a wax. The copolymers tested are limited
to lower alkyl acrylic-styrene copolymers.
[0008] Despite these disclosures, there is a continuing need for a barrier coating that
is more efficient than wax and easier to remove from paper fibers than wax.
[0009] As used throughout this specification, by the term (meth)acrylic is meant acrylic
or methacrylic and by the term (meth)acrylate is meant acrylate or methacrylate.
[0010] The present invention provides a method of modifying paper substrates including:
applying a polymer to the paper substrate wherein the polymer contains as polymerized
units: a) from 1 to 100 parts by weight of at least one C
12 to C
40 alkyl ester of (meth)acrylic acid, b) from 0 to 99 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 0 to 15 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
[0011] The polymer may be applied as is to a paper substrate to modify the paper substrate.
The modification of the paper substrate results in good barrier coating and recycle
properties. Alternatively, the polymer may be used as an additive to improve barrier
coating and recycle properties of latexes such as, but not limited to butyl acrylate/methyl
methacrylate, butyl acrylate/styrene, styrene/butadiene, and vinyl acetate latexes.
[0012] The present invention also provides an article including a paper substrate coated
with the polymer described above. An article including a paper substrate coated with
the admixture described above is also within the scope of the present invention.
[0013] The polymer used in this invention may be prepared by a single stage or multi-stage
process. The process may be an emulsion polymerization. See U.S. Pat. No. 5,521,266
for a detailed description of emulsion polymerization processes. The process may also
be solution polymerization followed by emulsification. See U.S. Pat. No. 5,539,021
for detailed descriptions of a solution polymerization followed by mini-emulsion polymerization
or micro-emulsion polymerizations. The emulsion polymerization process of U.S. Pat.
No. 5,521,266 is preferred.
[0014] The morphology of the polymer utilized in this invention may be designed to optimize
certain properties of the polymer. For example, the polymer may be made in a core-shell
morphology wherein the core polymer is designed to have a lower glass transition temperature
than the polymer that creates the shell. This type of morphology may improve barrier
properties as well as blocking properties. Alternatively, the polymer that makes up
the core may be designed to have a higher glass transition temperature than the polymer
that makes up the shell. In this case, the core may act as a filler and the shell
may bind the harder cores together to aid in film formation. The core-shell polymers
may be prepared by methods well known in the art.
[0015] In the process utilized for preparing the samples within this application, a first
stage was prepared by adding a monomer emulsion and sodium persulfate to a solution
containing methyl-β-cyclodextrin ("CD"), deionized water, and surfactant. The first
stage was reacted at 85°C. A second stage was prepared by making a second monomer
emulsion and feeding the second monomer emulsion and a sodium persulfate solution
to the reacted first stage. The second stage was reacted at 85°C.
[0016] The polymer used in this invention is a composition which contains as polymerized
units from 1 to 100 parts by weight, preferably from 5 to 95 parts by weight, more
preferably 10 to 90 parts by weight of at least one C
12 to C
40 alkyl ester of (meth)acrylic acid. It is further preferred that the polymer used
in this invention contains as polymerized units from 20 to 80 parts by weight, preferably
30 to 70 parts by weight, more preferably 40 to 60 parts by weight of at least one
C
12 to C
40 alkyl ester of (meth)acrylic acid. It is preferred that the alkyl ester of (meth)acrylic
acid be a C
12 to C
30 alkyl ester of (meth)acrylic acid. It is more preferred that the alkyl ester of (meth)acrylic
acid be a C
12 to C
18 alkyl ester of (meth)acrylic acid. Suitable alkyl esters of (meth)acrylic acid include,
but are not limited to lauryl (meth)acrylate, cetyl (meth)acrylate, stearyl (meth)acrylate,
behenyl (meth)acrylate, and eicosyl (meth)acrylate. Beneficial properties may be obtained
by utilizing more than one C
12 to C
40 alkyl ester of (meth)acrylic acid.
[0017] The polymer used in this invention may also contain as polymerized units from 0 to
99 parts by weight, preferably 4 to 94 parts by weight, more preferably 9 to 89 parts
by weight of at least one ethylenically unsaturated monomer. It is further preferred
that the polymer used in this invention contains as polymerized units from 18 to 80
parts by weight, preferably 28 to 70 parts by weight, more preferably 38 to 60 parts
by weight of at least one ethylenically unsaturated monomer. Suitable ethylenically
unsaturated monomers for use in the preparation of the polymer compositions of this
invention include, but are not limited to (meth)acrylic ester monomers including methyl
acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, decyl acrylate, methyl
methacrylate, butyl methacrylate, hydroxyethyl methacrylate, and hydroxypropyl acrylate;
acrylamide or substituted acrylamides; styrene or substituted styrene; vinyl acetate
or other vinyl esters; vinyl monomers such as vinyl chloride, vinylidene chloride,
N-vinyl pyrolidone; and acrylonitrile or methacrylonitrile. Butyl acrylate, methyl
methacrylate, and styrene are preferred.
[0018] The polymer used in this invention may also contain as polymerized units from 0 to
15 parts by weight, preferably 1 to 10 parts by weight, more preferably 1 to 5 parts
by weight ethylenically unsaturated acid containing monomer or salts thereof. Suitable
ethylenically unsaturated acid containing monomers include, but are not limited to
acrylic acid, methacrylic acid, crotonic acid, phosphoethyl methacrylate, 2-acrylamido-2-methyl-1-propanesulfonic
acid, sodium vinyl sulfonate, itaconic acid, fumaric acid, maleic acid, monomethyl
itaconate, monomethyl fumarate, monobutyl fumarate, and maleic anhydride. Acrylic
acid and methacrylic acid are preferred. Methacrylic acid is more preferred.
[0019] The polymer used in this invention may also contain as polymerized units from 0 to
25 parts by weight, preferably 0 to 15 parts by weight, more preferably 0 to 10 parts
by weight of a fluorinated (meth)acrylate ethylenically unsaturated monomer, such
as Zonyl™ products (Trademark of DuPont Chemical Company).
[0020] The polymer used in this invention may also contain as polymerized units from 0 to
25 parts by weight, preferably 0 to 15 parts by weight, more preferably 0 to 10 parts
by weight of a silicone containing ethylenically unsaturated monomer, such as vinyl
trimethoxy silane and methacryloxy propyl trimethoxy silane.
[0021] The polymer used in this invention may also contain as polymerized units from 0 to
80 parts by weight, preferably 0 to 50 parts by weight, more preferably 1 to 15 parts
by weight of a monomer selected from C
6-C
20 alkyl styrene and alkyl-alpha-methyl styrene, C
6-C
20 alkyl dialkyl itaconate, C
10-C
20 vinyl esters of carboxylic acids, C
8-C
20 N-alkyl acrylamide and methacrylamide, C
10-C
20 alkyl alpha-hydroxymethylacrylate, C
8-C
20 dialkyl 2,2'-(oxydimethylene) diacrylate, C
8-C
20 dialkyl 2,2'-(alkyliminodimethylene)diacrylate, C
8-C
20 N-alkylacrylimide, and C
10-C
20 alkyl vinylether.
[0022] The compositions of this invention may also contain as polymerized units from 0.1
to 10 parts by weight, preferably 0.1 to 5 parts by weight, more preferably 0.1 to
3 parts by weight, based on the polymer weight of a cross-linker selected from a cross-linking
agent and a cross-linking monomer. By cross-linker is meant a compound which has at
least 2 reactive groups which will react with acid groups found on the monomers of
the compositions of this invention. Cross-linking agents useful in this invention
include a polyaziridine, polyisocyanate, polycarbodiimide, polyamine, and a polyvalent
metal. The cross-linking agent is optional, and may be added after polymerization
has been completed.
[0023] Cross-linking monomers are cross-linkers which are incorporated with the monomers
of the compositions of this invention during polymerization. Cross-linking monomers
useful in this invention include acetoacetate-functional monomers such as acetoacetoxyethyl
acrylate, acetoacetoxypropyl methacrylate, acetoacetoxyethyl methacrylate, allyl acetoacetate,
acetoacetoxybutyl methacrylate, and 2,3-di(acetoacetoxy)propyl methacrylate; divinyl
benzene, (meth)acryloyl polyesters of polyhydroxylated compounds, divinyl esters of
polycarboxylic acids, diallyl esters of polycarboxylic acids, diallyl dimethyl ammonium
chloride, triallyl terephthalate, methylene bis acrylamide, diallyl maleate, diallyl
fumarate, hexamethylene bis maleamide, triallyl phosphate, trivinyl trimellitate,
divinyl adipate, glyceryl trimethacrylate, diallyl succinate, divinyl ether, the divinyl
ethers of ethylene glycol or diethylene glycol diacrylate, polyethylene glycol diacrylates
or methacrylates, 1,6-hexanediol diacrylate, pentaerythritol triacrylate or tetraacrylate,
neopentyl glycol diacrylate, cyclopentadiene diacrylate, the butylene glycol diacrylates
or dimethacrylates, trimethylolpropane di- or tri-acrylates, (meth)acrylamide, n-methylol
(meth)acrylamide, mixtures thereof, and the like. (Meth)acrylamide, n-methylol (meth)acrylamide,
and mixtures thereof are preferred. The amount of cross-linker utilized is chosen
such that the cross-linker does not interfere with film formation.
[0024] Chain transfer agents may be used to control the molecular weight of the polymer
composition. Suitable chain transfer agents include mercaptans, such as, for example,
dodecylmercaptan. The chain transfer agent may be used at from 0.1% to 10% based on
the total weight of the polymeric composition.
[0025] Fillers may be added to the polymers to be used in this invention. The fillers may
improve the barrier coating properties such as water resistance, oil resistance, and
blocking resistance of the polymer. By blocking is meant tackiness of the coated surface.
Blocking is undesirable because the coated paper is frequently rolled, and blocking
leads to difficulty in unrolling the coated paper. Suitable fillers include talc (magnesium
silicate), calcium carbonate, titanium dioxide, clay (aluminum silicate), and plastic
pigments such as polystyrene. The fillers may be admixed with the polymer to be used
in this invention at levels ranging from 10% to 150% by weight based on the dry weight
of the polymer.
[0026] The polymer used in this invention is typically used to modify paper substrates by
applying the polymer to a paper substrate. The paper substrate may be selected from
cardboard, paperboard, corrugated paperboard, Kraft paper, ream wrap and the like.
The polymer may be applied to the paper substrate by a blade, knife, rod, or roll,
or by spray applying, dipping, gravure, flexo, or kiss coating. Other coating methods
known in the art may also be utilized. The polymer may be applied at from 1g/m
2 to 50g/m
2, preferably 5g/m
2 to 25g/m
2 to yield a dry thickness of from 1 micron to 50 microns, preferably 5 microns to
25 microns. The polymer is then dried. The polymer may be dried under ambient conditions.
Forced air may be utilized to aid in the drying of the polymer. Heat may also be utilized
in the drying of the polymer. The forced air may be heated, or the polymer coated
substrate may be placed in a heated oven. The temperature of the heat may range from
35°C to 200°C. Other methods of drying known in the art such as the use of ultra violet
or infra red, a steam heated cylinder, or an electrically heated bar may also be utilized.
[0027] The polymer may also be admixed with latexes in barrier coating applications to improve
water repellency and recycle properties. Any latex may be used. Suitable latexes include,
but are not limited to butyl acrylate/methyl methacrylate, butyl acrylate/styrene,
styrene/butadiene, and vinyl acetate latexes. The amount of polymer admixed with the
latex is typically from 1 to 50 parts by weight, preferably 5 to 45 parts by weight,
more preferably 10 to 40 parts by weight. The admixture is typically applied to paper
substrates as described above.
[0028] The following abbreviations are used throughout this patent application:
LMA = lauryl methacrylate SMA = stearyl methacrylate St = styrene MMA = methyl methacrylate BA
= butyl acrylate MAA = methacrylic acid CD = methyl-β-cyclodextrin
[0029] The following Examples are intended to demonstrate the polymers that are useful in
this invention and the benefits obtained when using the polymers in barrier coating
applications. The Examples should not be construed as limiting the scope of the invention.
Example 1
[0030] For stage 1, 400 g deionized water, Triton® XN-45S (Trademark of Union Carbide Chemical
Company) anionic surfactant, and 28.6 g CD were introduced into a 4-liter round bottom
flask with four necks equipped with a mechanical stirrer, temperature control device,
condenser, monomer and initiator feed lines, and a nitrogen inlet at room temperature.
The contents were heated to 85°C while stirred under a nitrogen purge. A monomer emulsion
was prepared separately. Solutions of 0.35% by weight sodium carbonate (based on the
total monomer weight in stage 1 and stage 2) in 25 g deionized water and 0.35% by
weight sodium persulfate (based on the total monomer weight in stage 1 and stage 2)
in 30 g deionized water were introduced into the reaction kettle. The monomer emulsion
was fed over a period of 20 minutes together with an initiator solution of 0.05% sodium
persulfate (based on the total monomer weight in stage 1 and stage 2) in 210 g deionized
water.
[0031] For stage 2, a second monomer emulsion was prepared using 625 g deionized water,
7.8 g Triton® XN-45S anionic surfactant, and monomers. Immediately after the end of
the stage 1 monomer emulsion feed, the stage 2 monomer emulsion was fed over a period
of 3 hours together with the sodium persulfate initiator solution. The monomers of
the first and second monomer emulsions were selected such that the polymers of Table
1 (based on weight percent monomer) were obtained.
Table 1
Polymer |
SMA |
LMA |
BA |
MMA |
St |
MAA |
AN |
Zonyl |
1 |
40 |
0 |
10 |
0 |
49 |
1 |
0 |
0 |
2 |
0 |
40 |
10 |
0 |
49 |
1 |
0 |
0 |
31 |
40 |
0 |
10 |
0 |
47 |
1 |
0 |
0 |
41 |
0 |
40 |
10 |
0 |
47 |
1 |
0 |
0 |
51 |
40 |
0 |
0 |
0 |
57 |
1 |
0 |
0 |
61 |
0 |
40 |
0 |
0 |
57 |
1 |
0 |
0 |
7* |
0 |
0 |
50 |
0 |
49 |
1 |
0 |
0 |
Sample |
SMA |
LMA |
BA |
MMA |
St |
MAA |
AN |
Zonyl |
8*1 |
0 |
0 |
50 |
0 |
47 |
1 |
0 |
0 |
92 |
40 |
0 |
0 |
0 |
57 |
1 |
0 |
0 |
10 |
93 |
0 |
0 |
5 |
0 |
2 |
0 |
0 |
11 |
46 |
47 |
0 |
5 |
0 |
2 |
0 |
0 |
121 |
40 |
0 |
5 |
42 |
0 |
1 |
10 |
0 |
131 |
0 |
40 |
10 |
0 |
47 |
1 |
0 |
0 |
141 |
40 |
0 |
5 |
42 |
0 |
1 |
0 |
10 |
15*2 |
0 |
0 |
50 |
0 |
47 |
1 |
0 |
0 |
161 |
30 |
0 |
0 |
5 |
61 |
2 |
0 |
0 |
171 |
0 |
30 |
0 |
5 |
61 |
2 |
0 |
0 |
184 |
0 |
40 |
0 |
0 |
58 |
1 |
0 |
0 |
193 |
0 |
40 |
0 |
0 |
58 |
1 |
0 |
0 |
201,5 |
40 |
0 |
0 |
0 |
57 |
1 |
0 |
0 |
211,5 |
0 |
40 |
0 |
0 |
57 |
1 |
0 |
0 |
22 |
10 |
0 |
40 |
0 |
49 |
1 |
0 |
0 |
23 |
20 |
0 |
30 |
0 |
49 |
1 |
0 |
0 |
24 |
35 |
0 |
15 |
0 |
49 |
1 |
0 |
0 |
25 |
50 |
0 |
0 |
0 |
49 |
1 |
0 |
0 |
26 |
65 |
0 |
0 |
0 |
34 |
1 |
0 |
0 |
27 |
80 |
0 |
0 |
0 |
19 |
1 |
0 |
0 |
28 |
0 |
35 |
15 |
0 |
49 |
1 |
0 |
0 |
29 |
0 |
50 |
0 |
0 |
49 |
1 |
0 |
0 |
30 |
0 |
65 |
0 |
0 |
34 |
1 |
0 |
0 |
* polymer that typically may be used as a barrier coating
1 = contains 2% MOA (50% acrylamide / 50% n-methylol acrylamide) |
2 = contains 2% MAM (90% methacrylamide / 10% acrylamide) |
3 = contains 1% MOA (50% acrylamide / 50% n-methylol acrylamide) |
4 = contains 1% MAM (90% methacrylamide / 10% acrylamide) |
5 = contains 0.2% n-dodecyl mercaptan |
[0032] Standard tests to establish the usefulness for polymer compositions in barrier coating
applications include the Cobb test which measures water absorption on a polymer film
over a given time, the Water Vapor Transmission Rate (WVTR) test which measures the
amount of water vapor that permeates a polymer film over a given time, and a repulpability
test which indicates whether or not the polymer film is readily removed from the paper
substrate enabling the recycle of the paper. The polymers of Table 1 were tested by
some of these tests to determine their usefulness in barrier coating applications.
Cobb Test
[0033] For most samples to be tested, a single, wet coat was applied to the uncoated side
(back side) of a sheet of 224 g/m
2 basis weight, bleached paperboard using a wire-wound rod selected to give a dry coating
weight of 10-15 g/m
2 when the coating was dried for 20 seconds at the drying temperature indicated in
Table 2. For samples 22 through 30, a dry coating weight of 15-19 g/m
2 was applied to reduce the possibility of pinholes and the coating was dried at 150°C
for 1 minute. The specimens were conditioned at 25°C and 50% relative humidity prior
to testing. The coated samples were tested according to SCAN P 12:64, Water absorptiveness
of sized (non-bibulous) paper and paperboard (Cobb test), testing only the coated
side of the paperboard and using an exposure period of 30 minutes instead of 120 seconds.
For samples 1 through 21, four specimens per coating composition were tested. For
samples 22 through 30, two specimens per coating composition were tested. For samples
1 through 22, non cross-linkable polymers were tested on films dried at 60°C, 90°C,
120°C, and 150°C and cross-linkable polymers were tested on films dried at 90°C, 120°C,
150°C, and 180°C. The results of the tests are shown in Table 2. For the results of
this test, the lower the number, the better the performance.
Table 2
Cobb 30 Minutes Water Absorption (g/m2) |
Polymer |
60°C |
90°C |
120°C |
150°C |
180°C |
None1 |
250 |
250 |
250 |
250 |
NT |
1 |
4.4 |
3.7 |
3 |
3.5 |
NT |
2 |
4.7 |
3.9 |
4.1 |
4.1 |
NT |
3 |
NT |
3.8 |
3.8 |
3.4 |
3.3 |
4 |
NT |
6 |
4.1 |
4.1 |
3.7 |
5 |
NT |
15.1 |
4.8 |
4.4 |
3.9 |
6 |
NT |
43.7 |
11.5 |
5.3 |
3.4 |
7* |
76.8 |
33 |
21 |
20 |
NT |
8* |
NT |
7.1 |
7.5 |
7.2 |
7.7 |
9 |
NT |
NT |
NT |
NT |
NT |
10 |
NT |
NT |
NT |
NT |
NT |
11 |
4.6 |
4.9 |
5.3 |
5.4 |
NT |
12 |
NT |
74.8 |
47.0 |
13.2 |
9.7 |
13 |
NT |
7.1 |
7.5 |
7.2 |
7.7 |
14 |
NT |
12.3 |
12.3 |
10.9 |
11.4 |
15* |
NT |
6.5 |
6.2 |
6.4 |
6.1 |
16 |
NT |
NT |
NT |
87.9 |
83.0 |
17 |
NT |
NT |
NT |
84.0 |
83.8 |
18 |
NT |
36.5 |
10.4 |
4.6 |
3.5 |
19 |
NT |
45.7 |
26.2 |
7.9 |
3.1 |
20 |
NT |
4.3 |
3.7 |
3.1 |
3.9 |
21 |
NT |
6.0 |
3.9 |
3.3 |
3.7 |
22 |
NT |
NT |
NT |
2.5 |
NT |
23 |
NT |
NT |
NT |
1.3 |
NT |
24 |
NT |
NT |
NT |
1.5 |
NT |
25 |
NT |
NT |
NT |
1.3 |
NT |
26 |
NT |
NT |
NT |
1.5 |
NT |
27 |
NT |
NT |
NT |
2.3 |
NT |
28 |
NT |
NT |
NT |
2.1 |
NT |
29 |
NT |
NT |
NT |
1.1 |
NT |
30 |
NT |
NT |
NT |
1.9 |
NT |
* polymer that typically may be used as a barrier coating NT = not tested |
1 run for 5 minutes and extrapolated to 30 minutes |
[0034] The results above show that the non cross-linkable polymers have very low water absorption
at all drying temperatures tested. The cross-linkable polymers have lower water absorption
as the drying temperature increases. It is understood that sometimes coatings have
flaws that are termed pinholes. The presence of pinholes will allow water to penetrate
the coating and therefore increase both the water absorption and the WVTR. The inventors
inspected the coatings made from Polymers 16 and 17 by a staining technique where
an excess amount of stain was contacted with the coated specimen for 5 minutes and
the pinholes were counted. A large amount of pinholes were discovered.
WVTR Test
[0035] The WVTR test was run according to modified SCAN P 22:68. The test conditions were
25°C and 75% relative humidity. Non cross-linkable polymers were tested on films dried
at 60°C, 90°C, 120°C, and 150°C. Cross-linkable polymers were tested on films dried
at 90°C, 120°C, 150°C, and 180°C. For samples 22 through 30, a dry coating weight
of 15-19 g/m
2 was applied to reduce the possibility of pinholes. For samples 1 through 21, six
specimens per coating composition were tested. For samples 22 through 30, two specimens
per coating composition were tested. The results are shown in Table 3. For the results
of this test, the lower the number, the better the performance.
Table 3
WVTR (g/m2/24hours) |
Polymer |
60°C |
90°C |
120°C |
150°C |
180°C |
None |
600 |
600 |
600 |
600 |
NT |
1 |
180.3 |
152.6 |
145.7 |
140.3 |
NT |
2 |
157.6 |
138.3 |
133.5 |
142.4 |
NT |
3 |
NT |
133.8 |
130.9 |
123.4 |
123.8 |
4 |
NT |
145.9 |
133.6 |
131.6 |
122.7 |
5 |
NT |
374.4 |
130.1 |
101.2 |
93.7 |
6 |
NT |
348.8 |
142.5 |
120.5 |
108 |
7* |
505.8 |
393.7 |
353.7 |
346.8 |
NT |
8* |
NT |
238.6 |
235.1 |
230.2 |
229.9 |
9 |
NT |
NT |
NT |
NT |
NT |
10 |
568.3 |
550.2 |
543.3 |
502.5 |
NT |
11 |
157.5 |
161.6 |
164.8 |
167.4 |
NT |
12 |
NT |
454.0 |
350.6 |
184.7 |
145.6 |
13 |
NT |
238.6 |
235.1 |
230.2 |
229.9 |
14 |
NT |
194.5 |
176.2 |
165.7 |
156.6 |
15* |
NT |
219.3 |
218.4 |
216.4 |
204.0 |
16 |
NT |
NT |
NT |
536.8 |
545.7 |
17 |
NT |
NT |
NT |
564.8 |
563.9 |
18 |
NT |
434.3 |
284.1 |
135.6 |
104.3 |
19 |
NT |
438.7 |
229.7 |
152.7 |
122.7 |
20 |
NT |
98.5 |
95.7 |
93.1 |
106.1 |
21 |
NT |
134.5 |
111.4 |
105.3 |
109.2 |
22 |
NT |
NT |
NT |
114 |
NT |
23 |
NT |
NT |
NT |
101 |
NT |
24 |
NT |
NT |
NT |
78 |
NT |
25 |
NT |
NT |
NT |
64 |
NT |
26 |
NT |
NT |
NT |
74 |
NT |
27 |
NT |
NT |
NT |
88 |
NT |
28 |
NT |
NT |
NT |
90 |
NT |
29 |
NT |
NT |
NT |
64 |
NT |
30 |
NT |
NT |
NT |
73 |
NT |
* polymer that typically may be used as a barrier coating |
[0036] The results above show that the non cross-linkable polymers have very low WVTRs at
all drying temperatures tested as compared with samples 7 and 8. The cross-linkable
polymers have lower WVTRs as the drying temperature increases. As discussed in the
Cobb test results, the presence of pinholes will allow water to penetrate the coating
and therefore increase both the water absorption and the WVTR. The inventors inspected
the coatings made from Polymers 16 and 17 by a staining technique where an excess
amount of stain was contacted with the coated specimen for 5 minutes and the pinholes
were counted. A large amount of pinholes were discovered.
The Effect Of Coat Weight On Water Absorption And WVTR
[0037] The effect of coat weight on water absorption and WVTR was tested by coating paperboard
with different coat weights of Sample 5. Aliquots of Sample 5 were applied to paperboard
to provide coat weights of 8 g/m
2, 10 g/m
2, and 15 g/m
2. A sample of each coated paperboard was dried at 90°C, 120°C, 150°C, and 180°C. Each
sample was tested for Cobb 30 minutes and WVTR as described above. The results are
shown in Table 4.
Table 4
Polymer |
Cobb 30 Minutes (g/m2) |
WVTR (g/m2/24hours) |
5 8 g/m2 |
|
|
90°C |
75.4 |
587.1 |
120°C |
76.4 |
548.6 |
150°C |
66 |
511.7 |
180°C |
77.2 |
550.6 |
5 10 g/m2 |
|
|
90°C |
15.1 |
374.4 |
120°C |
4.8 |
130.1 |
150°C |
4.4 |
101.2 |
180°C |
3.9 |
93.7 |
5 15 g/m2 |
|
|
90°C |
4.2 |
101.1 |
120°C |
3.3 |
79.3 |
150°C |
3.3 |
77.5 |
180°C |
2.5 |
77.8 |
None |
NT |
599.6 |
[0038] The results above show that the polymers dramatically improve the WVTR when applied
at a coat weight of 10 g/m
2 or greater. The polymers also dramatically improve the resistance to water absorption
when applied at a coat weight of 10 g/m
2 or greater.
The Effect Of Fillers On Water Absorption And WVTR
[0039] The effect of fillers on water absorption and WVTR was tested by coating paperboard
with admixtures of talc and the polymers used in this invention. The talc was added
on a weight basis based on the dry weight of the polymer. Samples were applied to
paperboard and dried at 150°C for 20 seconds. Each sample was tested for Cobb 30 minutes
and WVTR as described above. The results are shown in Table 5.
Table 5
Polymer |
Cobb 30 minutes (g/m2) |
WVTR (g/m2/24hours) |
5 |
4.4 |
101.2 |
5 + 20% talc |
2.6 |
68.2 |
5 + 40% talc |
3.3 |
46.6 |
6 |
5.3 |
120.5 |
6 + 20% talc |
2.3 |
80.4 |
6 + 40% talc |
2.7 |
53.5 |
12 |
13.2 |
184.7 |
12 + 20% talc |
9.6 |
139.6 |
12 + 40% talc |
7.0 |
97.7 |
14 |
11.8 |
165.7 |
14 + 20% talc |
8.3 |
135.5 |
14 + 40% talc |
7.4 |
103.9 |
[0040] The results above indicate that the addition of fillers to the polymers used in this
invention improves both the water resistance and water permeability of the barrier
coating. An increase in the amount of filler added also improved the water resistance
and water permeability of the barrier coating.
Repulpability
[0041] The repulpability tests were done on uncoated Kraft paper and Kraft paper coated
with sample 9. The average coating weight was 10 g/m
2 and the coating was applied to the smoother side of the paper. The coated paper was
dried at 150°C for 20 seconds. Approximately 30 g of each paper was cut into 1.5 cm
x 1.5 cm pieces. To each set of pieces was added 2 liters (1) of water to achieve
a consistency of 15 g/l. The pH was adjusted to neutral by using hydrochloric acid
and sodium hydroxide. The paper was repulped in a British Wet Disintegration device.
The number of revolutions was 30,000. The pulp was diluted with water to a consistency
of 3 g/l. The drainability of the diluted pulp was measured according to the Canadian
Freeness method. Two parallel measurements were done and the results were expressed
as milliliters.
[0042] The small pieces of the coatings in the pulp were observed under a stereo microscope,
looking for the size of the pieces of coating and whether or not pulp fibers were
attached to the pieces of coating.
[0043] The pulp was again diluted to a consistency of 1.63 g/l in order to make laboratory
sheets of a grammage of approximately 60 g/m
2. The sheets were made with a special sheet mold and then dried in an oven for 2 hours
in a way that they could not shrink. The tensile strength and elongation of the sheets
were measured using 10 parallel samples. The results of the tests described above
are shown in Table 6.
Table 6
Test |
Uncoated |
Coated |
Energy Consumption (KWH) |
1.7 |
1.7 |
Canadian Freeness (ml) |
890 |
900 |
Grammage (g/m2) |
68.1 |
68.6 |
Elongation (%) |
3.4 |
3.9 |
Tensile Strength (kN/m) |
2.3 |
2.5 |
[0044] The data above demonstrates that the polymer coated paper performs as well as the
uncoated paper in tests designed to show repulpability. The small pieces of the coatings
observed under the stereo microscope showed tracks of fibers, but the fibers were
not attached to the coating. These results indicate that the polymer coated paper
is repulpable.
1. A method of modifying paper substrates comprising:
applying a polymer to the paper substrate wherein the polymer comprises as polymerized
units: a) from 1 to 100 parts by weight of at least one C12 to C40 alkyl ester of (meth)acrylic acid, b) from 0 to 99 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 0 to 15 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
2. The method according to Claim 1 wherein the polymer comprises as polymerized units:
a) from 5 to 95 parts by weight of at least one C12 to C40 alkyl ester of (meth)acrylic acid, b) from 4 to 94 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 1 to 10 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
3. The method according to Claim 1 wherein the polymer comprises as polymerized units:
a) from 10 to 90 parts by weight of at least one C12 to C40 alkyl ester of (meth)acrylic acid, b) from 9 to 89 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 1 to 5 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
4. The method according to Claim 1 wherein the polymer further comprises a cross-linker.
5. The method according to Claim 1 wherein the polymer further comprises a filler.
6. The method according to Claim 1 wherein the paper substrate is selected from cardboard,
paperboard, corrugated paperboard, Kraft paper, and ream wrap.
7. The method according to Claim 1 wherein the polymer is admixed with from 50 to 99
parts by weight of a latex and the admixture is applied to a paper substrate.
8. The method according to Claim 7 wherein the polymer comprises as polymerized units:
a) from 5 to 95 parts by weight of at least one C12 to C40 alkyl ester of (meth)acrylic acid, b) from 4 to 94 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 1 to 10 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
9. The method according to Claim 7 wherein the polymer comprises as polymerized units:
a) from 10 to 90 parts by weight of at least one C12 to C40 alkyl ester of (meth)acrylic acid, b) from 9 to 89 parts by weight of at least one
ethylenically unsaturated monomer, and c) from 1 to 5 parts by weight of at least
one ethylenically unsaturated acid containing monomer or salts thereof.
10. The method according to Claim 7 wherein the polymer further comprises a cross-linker.
11. The method according to Claim 7 wherein the polymer further comprises a filler.
12. The method according to Claim 7 wherein the latex is selected from the group consisting
of butyl acrylate/methyl methacrylate, butyl acrylate/styrene, styrene/butadiene,
and vinyl acetate latexes.
13. The method according to Claim 7 wherein the paper substrate is selected from cardboard,
paperboard, corrugated paperboard, Kraft paper, and ream wrap.
14. An article comprising:
a paper substrate coated with the polymer of Claim 1.
15. An article comprising:
a paper substrate coated with the admixture of Claim 7.