U.S. patent application number 09/843603 was filed with the patent office on 2003-02-06 for modified silane treated pigments or fillers and compositions containing the same.
Invention is credited to Christie, Robert E., Mei, Henry L., Panzer, Louis M., Pohl, Eric R., Ramdatt, Philbert E..
Application Number | 20030027897 09/843603 |
Document ID | / |
Family ID | 25290490 |
Filed Date | 2003-02-06 |
United States Patent
Application |
20030027897 |
Kind Code |
A1 |
Mei, Henry L. ; et
al. |
February 6, 2003 |
Modified silane treated pigments or fillers and compositions
containing the same
Abstract
The present invention is directed to a composition comprising a
white pigment or extended white pigment surface treated with a
silane having at least one functional group capable of reacting
with acids and anhydrides, at least one polymeric material and a
compatibilizer. Once treated, the pigment has improved
processability and dispersibility in polymeric materials.
Silanizing the pigment also enhances the brightness (increase
whiteness and reduce yellowness) of the pigment.
Inventors: |
Mei, Henry L.; (New City,
NY) ; Panzer, Louis M.; (Ridgefield, CT) ;
Pohl, Eric R.; (Mount Kisco, NY) ; Christie, Robert
E.; (North Salem, NY) ; Ramdatt, Philbert E.;
(New York, NY) |
Correspondence
Address: |
MICHAEL P DILWORTH
CROMPTON CORPORATION
199 BENSON ROAD
MIDDLEBURY
CT
06749
US
|
Family ID: |
25290490 |
Appl. No.: |
09/843603 |
Filed: |
April 26, 2001 |
Current U.S.
Class: |
523/216 ;
524/261; 524/445 |
Current CPC
Class: |
C01P 2006/60 20130101;
C09C 1/3676 20130101; C01P 2006/22 20130101; C01P 2006/10 20130101;
C09C 1/3692 20130101; C01P 2004/51 20130101; C09C 3/006 20130101;
C01P 2006/65 20130101; C01P 2006/66 20130101; C09C 1/3684 20130101;
C09C 3/12 20130101; C09C 3/10 20130101 |
Class at
Publication: |
523/216 ;
524/261; 524/445 |
International
Class: |
C08K 003/34; C08K
005/24; C08K 009/00 |
Claims
1. A composition comprising: a) a white pigment or extended white
pigment surface treated with a silane having at least one
functional group capable of reacting with acids and anhydrides; b)
at least one polymeric material; and c) a compatibilizer.
2. The composition of claim 1 wherein said silane has the following
general formula: R.sub.xSi(R').sub.4-x wherein R is a
nonhydrolyzable functional group directly or indirectly bonded to
the silicon atom selected from the group consisting of epoxy,
isocyanato, mercapto, and mixtures thereof; R' is a hydrolyzable
group selected from the group consisting of alkoxy, halogen,
acetoxy or hydroxy or mixtures thereof; and x=1 to 3.
3. The composition of claim 1 wherein said pigment is
TiO.sub.2.
4. The composition of claim 1 wherein said extended white pigment
is selected from clays, inorganic metal compounds and siliceous
materials.
5. The composition of claim 1 wherein said compatibilizer comprises
copolymers of ethylene or propylene with anhydride or acid groups
which are capable of reacting with the functional groups of the at
least one polymeric material.
6. The composition of claim 1 wherein said compatibilizer comprises
copolymers selected from the group consisting of ethylene maleic
anhydride copolymers, ethylene (meth)acrylic acid copolymers,
propylene maleic anhydride copolymers, propylene acrylic acid
copolymers, ethylene propylene copolymers with maleic anhydride or
acid functional groups, and olefinic ionomer resins.
7. The composition of claim 1 wherein said compatibilizer is
present at a concentration of about 0.5 wt. % to about 20 wt. %
based on a total weight of the composition.
8. The composition of claim 1 wherein said compatibilizer is
present at a concentration of about 1% to about 10% by weight of
the total composition.
9. The composition of claim 1 wherein said filler or pigment is
present at a concentration of about 40 wt. % to about 85 wt. %
based on a total weight of the Composition.
10. The composition of claim 1 further comprising at least one
lubricant selected from the group consisting of polysiloxanes,
silicone fluids, stearates, paraffinic oils, fluorocarbon fluids,
and mixtures thereof.
11. The composition of claim 10 wherein said lubricant is a
polysiloxane selected from the group consisting of
polydimethylsiloxane and organomodified polydimethylsiloxane.
12. The composition of claim 13 wherein said lubricant is present
from about 0.05 wt. % to about 5 wt. % based on a total weight of
the composition.
13. The composition of claim 1 wherein said silane is present on
the surface of said pigment or extended white pigment in an amount
of about 0.1 wt. % to about 5 wt. % based on a weight of said
pigment or extended white pigment.
14. The composition of claim 1 wherein said polymeric material is
selected from the group consisting of olefins and alphaolefins and
their copolymers and terpolymers, rubbery block copolymers,
polyamides, polyesters, vinylic polymers, acrylics, epoxies,
ionomeric resins, and mixtures thereof.
15. The composition of claim 14 wherein said polymeric material is
selected from the group consisting of polyethylene, ethylene
copolymers, polypropylene, propylene copolymers, and mixtures
thereof.
16. A white pigment surface treated with at least one silane
capable of reacting with acids and anhydrides and having the
following general structure: R.sub.xSi(R').sub.4-x wherein R is a
nonhydrolyzable functional group directly or indirectly bonded to
the silicon atom selected from the group consisting of epoxy,
isocyanato, mercapto, and mixtures thereof; R' is a hydrolyzable
group selected from the group consisting of alkoxy, halogen,
acetoxy or hydroxy or mixtures thereof; and x=1 to 3.
17. The white pigment of claim 16 wherein said white pigment is
selected from the group consisting of clays, inorganic metal
compounds and siliceous materials.
18. The white pigment of claim 16 wherein said white pigment is
selected from the group aluminum trihydroxide, magnesium hydroxide,
calcined clay, nanoclay, kaolin clay, oxidized brass, oxidized
aluminum, oxidized steel, alumina, aluminum trihydrate, fumed
silica, precipitated silica, silica aerogels, silica xerogels,
aluminum silicates, calcium magnesium silicates, asbestos,
molecular sieves, Wallostonite, calcium carbonate, titanium
dioxide, calcium sulphate, magnesium sulfate, calcium carbonates
having a silica coating, calcium carbonates agglomerated to silica,
and mixtures thereof.
19. The white pigment of claim 16 wherein said white pigment is
TiO.sub.2.
20. A white pigment or extended white pigment having enhanced
processability and dispersion in polymeric material surface treated
with a silane having a structure of: R.sub.xSi(R').sub.4-x wherein
R is a nonhydrolyzable functional group directly or indirectly
bonded to the silicon atom selected from the group consisting of
epoxy, isocyanato, mercapto, and mixtures thereof; R' is a
hydrolyzable group selected from the group consisting of alkoxy,
halogen, acetoxy or hydroxy or mixtures thereof; and x=1 to 3; and
a polysiloxane having a structure of:
(R".sub.nSiO.sub.(4-n)/2).sub.m wherein R" is an organic or an
inorganic group; n is 0to 3;and m is equal t o or greater than 2.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to the surface treatment of
pigments, particularly white pigments, to improve dispersibility in
polymeric materials, processability, and performance
characteristics of the pigments. The pigments are treated with an
organosilicon compound having at least one functional group that is
capable of reacting with an acid or an anhydride. More
specifically, the present invention relates to polymeric
compositions comprising the surface treated pigments of the present
invention.
BACKGROUND OF THE INVENTION
[0002] The treatment of titanium dioxide pigments with
organosilicon compounds to improve dispersibility in a polymer
matrix is well known in the art. For instance, U.S. Pat. No.
4,061,503 to Berger et al. and U.S. Pat. No. 4,151,154 to Berger
describe the treatment of particulate titanium dioxide to improve
its dispersibility in a resin or plastic medium. The titanium
dioxide contains on its surface a silane possessing at least two to
about three hydrolyzable groups bonded to the silicon, and an
organic group which contains a polyalkylene oxide group.
[0003] Further, U.S. Pat. No. 4,810,305 to Braun et al. discloses a
modified hydrophobic pigment or filler containing 0.05 to 10 wt. %
of an organopolysiloxane having improved dispersibility in
synthetic resins. U.S. Pat. Nos. 5,607,994 and 5,631,310, both to
Tooley et al., disclose white-pigmented polymers (particularly,
polyolefins such as polyethylene) containing white pigments treated
with at least one silane or a mixture of at least one silane and at
least one polysiloxane to improve processability in compounding and
to improve performance properties such as lacing resistance in a
polymeric matrix, as well as other physical characteristics.
SUMMARY OF THE INVENTION
[0004] The present invention relates to a pigment surface treated
with a silane having at least one functional group capable of
reacting with acids and anhydrides. The surface treated pigment or
extended white pigment can then be compounded with at least one
polymeric material and at least one compatibilizer.
[0005] The silane of the present invention useful for surface
treating the pigments or extended white pigments has the following
general structure:
R.sub.xSi(R').sub.4-x
[0006] wherein
[0007] R is a nonhydrolyzable functional group directly or
indirectly bonded to the silicon atom such as epoxy, isocyanato,
mercapto, and mixtures thereof;
[0008] R' is a hydrolyzable group such as alkoxy, halogen, acetoxy
or hydroxy or mixtures thereof; and
[0009] x is 1 to 3.
[0010] Preferably, the pigment or extended white pigment is
titanium dioxide.
[0011] The compatibilizer has at least one group which is acidic,
or is an anhydride thereof.
[0012] The resultant polymer composition may further comprise
lubricants, as well as a variety of other conventional
additives.
[0013] The silanized pigments of the present invention exhibit
improved processability, lower viscosity, increased lacing
resistance, improved dispersion in polymeric materials and
excellent optical properties including improved whiteness and
yellowness index over the untreated pigments. The polymeric
compositions of the present invention may be used in an endless
variety of articles and applications.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0014] In general, the present invention encompasses the whitening
treatment of potentially any inorganic oxide particulate material,
days, pigments, extended white pigments, and so forth. These
materials are typically from classes of materials referred to as
fillers, pigments, and reinforcing materials such as inorganic
particulate materials and fibers (such as glass fibers, aluminum
fibers and steel fibers), and so forth. Such materials include
aluminum trihydroxide, magnesium hydroxide, calcined clays, kaolin
clays, nanoclays, brass (with an oxidized surface), copper metal
(oxidized at its surface), aluminum metal (oxidized at its
surface), iron or steel (oxidized at its surface), alumina,
aluminum trihydrate, siliceous materials such as fumed silica,
hydrated silica (precipitated silica), silica aerogels, silica
xerogels, aluminum silicates, calcium magnesium silicate, asbestos,
glass fibers, molecular sieves, Wallostonite, calcium carbonate,
carbon black (including lamp black), titanium dioxide (including
titanium dioxide which contains HCl soluble alumina and/or silica),
calcium sulphate, magnesium sulfate, calcium carbonate containing a
silica coating or agglomerated to silica, and the like. In
particular, the present invention is especially useful for the
surface treatment of white pigments or extended white pigments, and
even more particularly for the surface treatment of titanium
dioxide pigments.
[0015] The titanium dioxide, TiO.sub.2, pigments useful in the
present invention generally are in the rutile or anatase
crystalline form and are commonly made by either a chloride process
or a sulfate process. The optimum average particle size can range
from about 0.005 to about 1 micron. The TiO.sub.2 pigments may also
contain ingredients added thereto to further improve dispersibility
characteristics or other properties such as durability.
[0016] It has been found that the silane treatment of this
invention can be used not only for TiO.sub.2 but also for so-called
extended white pigments such as calcium carbonate.
[0017] Additives and/or inorganic oxides are commonly added to the
pigments and include but are not limited to aluminum, silicon, tin,
triethanolamine, trimethylolpropane, phosphates, and so forth. Such
additives are known to one of skill in the art.
[0018] "Silanized TiO.sub.2" is defined herein as TiO.sub.2 treated
with either at least one silane, or a mixture of at least one
silane and at least one polysiloxane (collectively referred to
herein as organosilicon compounds).
[0019] The silanes useful herein are those that have a functional
group capable of reacting with anhydrides or acids, their
hydrolyzates or condensates thereof. Examples of such silanes
include those having epoxy, isocyanato, and mercapto groups. In
preferred embodiments, the silanes have epoxy groups.
[0020] Suitable silanes have the following general formula:
R.sub.xSi(R').sub.4-x
[0021] wherein
[0022] R is a nonhydrolyzable functional group directly or
indirectly bonded to the silicon atom;
[0023] R' is a hydrolyzable group such as alkoxy, halogen, acetoxy,
hydroxy or mixtures thereof; and
[0024] x=1 to 3.
[0025] Examples of suitable silanes useful in carrying out the
invention include but are not limited to
.gamma.-(3,4-epoxycyclohexyl)ethyltrimetho- xysilane such as
Silquest.RTM. A-186, .gamma.-glycidoxypropyltrimethoxysil- ane such
as Silquest.RTM. A-187, .gamma.-Glycidoxypropylmethyldiethoxysila-
ne such as Silquest.RTM. Y-15078,
2-(3,4-epoxycyclohexalethyltriethoxysila- ne such as Silquest.RTM.
Y-11870), .gamma.-isocyanatopropyltrimethoxysilan- e such as
Silquest.RTM. A-1310, .gamma.-mercaptopropyltrimethoxysilane such
as Silquest.RTM. A-189, and so forth. All of the above mentioned
Silquest.RTM. materials are available from Crompton Corporation of
Greenwich, Conn. Preferably, the silanes utilized include
Silquest.RTM. A-187, Silquest.RTM. Y-11870and Silquest.RTM.
Y-15078.
[0026] The silanes of the present invention may be used in
combination with a lubricant including, but not limited to,
polysiloxanes, silicone fluids, stearates, paraffin oils,
fluorocarbon lubricants, and so forth. The polysiloxanes useful
herein include polydimethylsiloxane and organomodified
polydimethylsiloxane. "Organomodified" refers to organic pendant
groups on the molecules that may include polyalkylene oxides such
as polyethylene oxide, polyether groups, vinylic groups, and so
forth.
[0027] In one embodiment, a mixture of at least one silane with at
least one polysiloxane is advantageous in carrying out the
invention. Suitable polysiloxanes for use in combination with at
least one silane have the following general formula:
(R".sub.nSiO.sub.(4-n)/2).sub.m
[0028] wherein
[0029] R" is an organic or an inorganic group;
[0030] n is 0to 3; and
[0031] m is equal to or greater than 2.
[0032] Examples of useful polysiloxanes in carrying out the present
invention include, but are not limited to, polydimethylsiloxane
(PDMS), vinyl phenylmethyl terminated dimethyl siloxanes,
divinylmethyl terminated PDMS and the like, PDMS with polyether
pendant groups including Silwet.RTM. PA-1 available from Crompton
Corporation. PDMS such as Silwet.RTM. L45, available from Crompton
Corporation, is an example of a particularly useful
polysiloxane.
[0033] The silanes preferable for use in combination with the
polysiloxanes include those silanes described above such as
2-(3,4-epoxycyclohexaethyl triethoxy silane such as Silquest.RTM.
Y-11870, and .gamma.-glycidoxypropyltrimethoxy silane such as
Silquest.RTM. A-187. The silane/polysiloxane mixture is useful from
about 0.1 wt. % to about 5.0 wt. %, and preferably from about 1.0
wt. % to about 3.0 wt. %, based on a total weight of the silanized
pigments. A preferred combination is about 0.5 wt. % to about 1.5
wt. % of the silane(s), and about 0.5 wt. % to about 1.5 wt. % of
the polydimethylsiloxane based on a total weight of the silanized
pigments. The ratio of silane(s) to polysiloxane may be from about
1:2 to about 2:1, with the preferred ratio being about 1:1.
[0034] In preparing the silanized pigment, the order of addition is
not especially critical and the pigment may be treated with the
silane using a number of different methods. For example, the silane
can be either added neat or in a pre-hydrolyzed form to a dry
pigmentary base, or it can be added into a slurry. The silane can
be added during filtration, during drying, at a sizing operation
such as a fluid energy mill, e.g. micronizer, or at a media mill.
The silane may also be post blended after micronizing. One of skill
in the art would be knowledgeable in treating the pigmentary base
with the silane(s). For instance, media milling first involves
reducing the viscosity of a high solids TiO.sub.2 pigment slurry by
adjusting the pH in the range of about 7.5 to about 11 with caustic
or the like, or by contacting the slurry with a reducent, and then
treating the slurry with an organosilicon reagent. The treating
step is either preceded by and/or followed by media milling the
high solids slurry to reduce the TiO.sub.2 particle size. The
slurry is then dried as a product thereby eliminating the post
drying manipulation to control pigment properties such as particle
size distribution.
[0035] The surface modification of pigments by may also be
effectuated by adding amino organosilane to a pigment dispersion
directly in a suitable solids mixing apparatus. Postblending
processes may also be employed as well.
[0036] The description of the various preparation methods described
herein is intended for guidance purposes only, and is in no way
intended as a limitation on the scope of the present invention. One
of skill in the art would realize that there are various methods
and modifications of such methods which may be utilized to prepare
the silanized pigments or fillers of the present invention. Such
methods and modifications are seen to be within the scope of the
present invention.
[0037] The polysiloxane addition may be made in conjunction with
the silane, or added to the already silanized pigment. The silane
addition and polysiloxane addition is described in greater detail
below.
[0038] If water, either liquid or vapor (steam), is present as a
component of the process stream, hydrolysis of the hydrolyzable
groups of the silane will occur and the silane coating will bond to
the TiO.sub.2 base. Pre-hydrolyzing the silane is a preferred step
in treating the TiO.sub.2 pigment with the silane. Hydrolysis of
silanes is described in greater detail in "Organofunctional
Silanes" by Union Carbide (1991).
[0039] The treated pigment compositions of the present invention
may further comprise a compatibilizer. The compatibilizer comprises
at least one reactive group capable of reacting with the functional
groups of the organosilicone compound. If, however, the polymeric
material itself comprises such a functional group, a compatibilizer
may not be utilized. For instance, if a modified polyolefin polymer
with such a functional group is used, a compatibilizer may be
superfluous. In the alternative, a compatibilizing compound may be
added in addition to the polymeric material being utilized. In the
case of a polymeric composition wherein the polymeric material is
an unmodified polyolefin without any reactive groups, then a
compatibilizer is additionally added to the composition.
[0040] Examples of useful compatibilizers include copolymers of
ethylene or propylene with anhydride or acid groups capable of
reacting with the functional groups of the organosilicon compound
such as an epoxy group. The copolymers useful herein include
ethylene maleic anhydride copolymers (EMAH), ethylene acrylic acid
copolymers (EAA), ethylene methacrylic acid copolymers (EMAA),
propylene maleic anhydride copolymers (PMAH), propylene acrylic
acid copolymers (PAA), ethylene propylene copolymers with maleic
anhydride or acid functional groups (EPMAH or EPAA), olefinic
ionomer resins such as ethylene ionomers, and so forth. Ethylene
maleic anhydride copolymers (EMAH) and ethylene-acrylic acid
copolymers (EAA) are preferred.
[0041] Some specific examples of useful compatibilizers include
ACX.RTM. ethylene-maleic anhydride copolymer resins from Allied
Signal Corporation of Morristown, N.J., Primacor.RTM.
ethylene-acrylic acid copolymer resins from The Dow Chemical
Company of Midland, Mich., Surlyn.RTM. ionomer resins available
from E.I. du Pont de Nemours and Company of Wilmington, Del., and
Nucrel.RTM. ethylene methacrylic acid (EMAA) copolymers also
available from E.I. du Pont de Nemours and Company. The
compatibilizer is present in an amount from about 0.5 wt. % to
about 20 wt. %, preferably from about 1.0 wt. % to about 10 wt. %,
more preferably from about 1.0 wt. % to about 6.0 wt. %, and most
preferably from about 3.0 wt. % to about 5.0 wt. % based on a total
weight of the mixture which include the treated TiO.sub.2, polymer,
compatibilizer, and any other components used in the mixture.
[0042] The silanized compounds of the present invention may be used
in combination with any polymeric material with which such
compounds are typically used. The silane acts, in a sense, as a
dispersion promoter, by increasing the compatibility or
dispersibility of the inorganic oxide or other particulate material
within the plastic or resin system in which it is supplied.
[0043] The polymers useful herein are known to those of skill in
the art. The general classes of polymers suitable for use herein
are thermoplastic or thermosetting polymeric resinous materials,
and include but are not limited to, the olefinic polymers including
polyethylene and its copolymers and terpolymers, polybutylene and
its copolymers and terpolymers, polypropylene and its copolymers
and terpolymers; alphaolefins including linear or substantially
linear interpolymers of ethylene and at least one .alpha.-olefin
and atactic polyalphaolefins; rubbery block copolymers; polyamides;
polyesters such as polyethyleneterephthalate and
polybutyleneterephthalate; vinylic polymers; acrylics; epoxies;
polycarbonates; and so forth; and mixtures thereof. Preferably, the
polymers are selected from the group consisting of polyethylene,
ethylene copolymers, polypropylene, propylene copolymers, and
mixtures thereof.
[0044] Olefinic polymers, such as polyethylene, polypropylene and
polybutylene, are from a broad class of polymers typically referred
to as polymers of ethylenically unsaturated monomers, and the
copolymers and terpolymers of such polymers with higher olefins
such as alpha olefins containing 4 to 10 carbon atoms, or vinyl
acetate, and the like.
[0045] Olefins, i.e. ethylene, are often copolymerized with vinyl
monomers such as acrylates or vinyl esters of carboxylic acid
compounds. Specific acrylate monomers include acrylic acid,
methacrylic acid, acrylamide, methacrylamide, methyl acrylate,
methyl methacrylate, methoxyethyl methacrylate, methoxyethyl
acrylate, and so forth. Vinyl esters of carboxylic acids include
vinyl acetate, vinyl butyrate and so forth. Commonly used polymers
of this variety include, for instance, ethylene vinyl acetate,
ethylene ethyl acrylate, ethylene n-butyl acrylate, and ethylene
methylacrylate.
[0046] Other useful polymeric resins include vinylic compounds such
as polyvinyl chloride; polyvinyl esters such as polyvinyl acetate;
polystyrene, acrylic homopolymers, copolymers and terpolymers;
phenolics; alkyds; amino resins; epoxy resins; polyamides;
polyurethanes; phenoxy resins; polysulfones; polycarbonates;
polyesters and chlorinated polyesters; polyethers; acetal resins;
polyimides; polyoxyethylenes; and so forth.
[0047] Other useful polymers include various rubbers and/or
elastomers including both natural and synthetic rubbers. Such
polymers may be copolymerized, grafted, physically blending with
various diene monomers, and so forth. Block copolymers are a
commonly used elastomer and include polymers formed of styrene,
butadiene, isoprene and so forth. More specifically,
styrene-butadiene-styrene, styrene-isoprene-styrene,
styrene-ethylene/butylene-styrene,
styrene-ethylene/propylene-styrene, and so forth. Other elastomers
include natural rubber, i.e. polyisoprene; polyisobutylene; butyl
rubbers; and so forth.
[0048] Some polymers preferable for use in combination with the
silanized compounds of the present invention include polyolefins
such as polyethylene, polypropylene, polyvinyl chloride,
polyamides, polyesters and copolymers and terpolymers thereof.
[0049] "High loaded" TiO.sub.2 may depend on the type of polymer
used and may be anywhere from about 40 wt. % TiO.sub.2, up to about
90 wt. % TiO.sub.2. For instance, in a polyolefin matrix, a high
loaded TiO.sub.2 would be about 50 wt. % or more of the TiO.sub.2
pigment, based on a total weight of polyolefin matrix.
[0050] A wide variety of conventional additives may be optionally
added to the polymeric compositions of the present invention as is
necessary, desirable or conventional for the intended end use. Such
additives include but are not limited to antioxidants, ultraviolet
(UV) stabilizers, lubricants, thermal processing additives, and so
forth. Such additives are known to those of skill in the art.
[0051] TiO.sub.2 coated with organosilicon compounds can be
incorporated with a polymer in a melted state to form the polymeric
compositions of the present invention by any melt compounding
technique known to those of skill in the art. Generally, TiO.sub.2
and polymeric resin are added together, and are subsequently mixed
in a blending apparatus that applies shear to the melted polymer.
The polymeric resin is typically commercially available in a
variety of forms including but not limited to powder, granules,
pellets, cubes, and so forth.
[0052] In a typical mixing operation, pigment and polymer are first
dry blended while the polymer is still in a solid, pre-melted
state. This can be accomplished with simple processes such as by
shaking in a bag or by tumbling in a closed container. More
sophisticated methods include blending apparatuses having agitators
or paddles. The pigment and the polymeric resin can be co-fed into
mixers having an internal screw, i.e. an extruder device, which
mixes the pigment and polymer prior to the polymer achieving a
molten state.
[0053] Melt blending the components may be accomplished using any
conventional equipment known to those of skill in the art including
single-screw extruders, twin-screw extruders including the broad
range twin screw extruders and corotating twin screw extruders,
high shear mixers, blender type mixers, and so forth. Twin-screw
extruders are commonly used. The melt blending can be accomplished
during formation of an article such as during a melt extrusion
process. Melt extrusion can also be combined with blow molding, for
instance.
[0054] Exemplary mixers include co-rotating twin screw extruders
manufactured by Werner & Pfleiderer in Ramsey, N.J., and by
Leistritz Extruder Corporation in Somerville, N.J. Farrel
Corporation in Ansonia, Conn. manufacturers the Farrel Continuous
Mixers (FCM).
[0055] There are numerous ways of preparing the polymeric
compositions of the present invention. A concentrate may first be
prepared having a high concentration of TiO.sub.2, commonly
referred to as a masterbatch, and then subsequently combining the
concentrate with polymeric resin.
[0056] The highly loaded polymer concentrates are made as described
above with the desirable weight % of pigment for the intended end
use. For example, in polyolefin concentrates, about 50 wt. % to 85
wt. % concentrate may be used to opacify the composition. The
TiO.sub.2 concentrate is "let down" into the polymer. As used
herein, "let down" refers to process of lowering the TiO.sub.2
concentration in a resultant polymer. For example, in optical
property evaluation, a concentrate having about 50 wt. % to about
87 wt. % TiO.sub.2 may be let down to about 0.2 wt. % to about 30
wt. % by dry mixing polyolefin, extruding at a specific
temperature, and casting it into a film. The pigment performance is
then evaluated in an end use application.
[0057] The highly loaded silanized pigmentary TiO.sub.2 exhibits
outstanding processibility in polyolefinic matrices, and excellent
lacing resistance. The torque and pressure can be utilized to
determine the relative ease with which the compositions are
processed through a mixer, e.g. an extruder, for instance. The
lower the torque and pressure required to mix and move the
composition through the equipment, the easier the processing.
Furthermore, typically, the higher the loading of pigment or
filler, i.e. TiO.sub.2, in a polymer concentrate, the slower the
processing rates.
[0058] The compositions of the present invention require lower
torque and pressure for processing, particularly through an
extruder, than do those polymeric compositions compounded with
untreated titanium dioxide, and faster processing rates can also be
obtained. Another advantage of the polymeric films made using the
pigmented compositions of the present invention, particularly those
made with the silanized TiO.sub.2 of the present invention, is
increased lacing resistance. Other advantages include increased
bulk density, lower viscosity, excellent dispersion, excellent
moisture resistance, and excellent optical properties such as high
whiteness and gloss.
[0059] The polymeric materials containing the treated pigments of
the present invention are useful in a variety of applications. The
polymeric compositions of the present invention may be employed,
for example, for molding (including extrusion, injection,
calendering, casting, compression, lamination, and/or transfer
molding), coating (including lacquers, film bonding coatings and
painting), inks, dyes, tints, impregnations, adhesives, caulks,
sealants, rubber goods, and cellular products. Thus, the choice and
use of the polymeric compositions with the treated particles of
this invention is essentially limitless.
[0060] One of ordinary skill in the art would understand that there
are a vast number of modifications which could be made without
changing the scope of the invention, those modifications and
embodiments thereof are contemplated to be within the scope of the
present invention.
[0061] The following non-limiting examples are further illustrative
of the present invention, and are in no way intended to limit the
scope of the present invention.
EXAMPLES
[0062] Test Methods
[0063] 1. Viscosity (Pascal/Second) and Melt Flow Index (g/10
Minutes)
[0064] The viscosity and melt flow index were measured at
190.degree. C. using a Tinius Olsen Extrusion Plastometer available
from Tinius Olsen Corporation in Willow Grove, Pa.
[0065] 2. Yellow Index and Whiteness
[0066] The yellowness index and whiteness were measured using the
films and plaques as prepared above using a Colorgard System.TM.
1000 calorimeter manufactured by Pacific Scientific Corporation in
Silver Spring, Md. Film thickness was about 4 mils.
[0067] 3. Gloss
[0068] The gloss of the film and plaque samples was measured with a
GL-4525 glossmeter manufactured by Paul N. Guard Co. in Pompano
Beach, Fla. Film thickness was about 4 mils.
[0069] 4. Hue and Chroma
[0070] The hue and chroma of the film and plaque samples were
measured using a Minolta.RTM. CR 231 chromameter available from
Minolta Corporation in Osaka, Japan. The films tested had a
thickness of about 4 mils.
[0071] 5. Dispersion
[0072] The dispersion of the pigment was tested using a light box.
Film thickness was approximately 1 mil. The dispersion is rated
according to the distribution and uniformity using a rating of
excellent, good, fair and poor.
[0073] The following examples were prepared using a masterbatch
concentrate prepared in the following manner. The masterbatch
concentrate contained 80 wt. % TiO.sub.2 in low density
polyethylene (LDPE). The TiO.sub.2 powder was treated with silane
or a silane/siloxane combination, and mixed with low density
Microthene.RTM. GMN 711-20 LDPE available from Equistar Corporation
in Houston, Tex., having a melt flow index (MFI) of 22, and a
compatibilizer which was an ethylene-maleic anhydride copolymer,
ACX.RTM. 575 available from Allied Signal Corporation in
Morristown, N.J., or Primacor.RTM. 2410, an ethylene-acrylic acid
copolymer available from The Dow Chemical Company, in Midland,
Mich. The composition was mixed in a Henschel dry mixer
manufactured by Prodex Corporation in Fords, N.J. The dry mix was
then fed into a twin screw extruder (ZSK 30 by Werner &
Pfleiderer of Ramsey, N.J.) for a melt compounding. The twin screw
extruder was equipped with recording equipment for recording
temperature, pressure, rotating speed, torque and power
consumption. The extruded rods were fed into a water bath, air
knife and pelletizer. The 80 wt. % high loaded TiO.sub.2/LDPE
pellets were dried at 140.degree. F. (60.degree. C.) for about 8
hours and then made into films using a Brabender PL-V302 single
extruder with a 6" wide slot die. The films were tested for
dispersion of TiO.sub.2 in LDPE using a light box.
[0074] The masterbatch was then let down to 8%. The balance of LDPE
(Petrotheneg NA206, MFI.TM. 13 available from Equistar
Corporation), antioxidant (1rganox.RTM. B-215 and 1010, from Ciba
Specialty Chemicals in Tarrytown, N.Y.) and ultraviolet stabilizer
(Tinuvin.RTM. 783FP, also from Ciba Specialty Chemicals) were added
into the Masterbatch pellets with a bag dry mixing. The dry mix was
fed into a 2" single screw extruder (Midland Ross Hartic) for a
melt compounding. The extruded strands went through a water bath
and pelletizer.
[0075] The let down pellets were made into film samples using a
Brabender model PL-V302 single extruder with a 6" wide slot die.
The dispersion of TiO.sub.2 in LDPE was checked for these film
samples with a light box. The film samples were also used for the
measurement of optical performance (whiteness, yellow index, gloss,
hue and chroma).
[0076] The let down pellets were also made into plaques by
compression molding. Film thicknesses were approximately 4
mils.
Example 1
[0077] RCL-9.TM. pigmentary rutile TiO.sub.2 supplied by Millenium
Inorganic Chemicals in Baltimore, Md. (2500 g) was added to a
Patterson-Kelly Twin shell V-Blender and sprayed with a solution of
25 g of A-187 .gamma.-glycidoxy propyltrimethoxysilane available
from Crompton Corporation. The solution was about 20 wt. % silane
in 90/10 methanol/water. The silanized TiO.sub.2 (2400 g) was then
dried in an oven at 140.degree. F. (60.degree. C.) for 8 hours.
[0078] The silanized TiO.sub.2 was then compounded with 450 g of
Microthene.RTM. GMN 711-20 LDPE having a MFI of 22 available from
Equistar, and 150 g of ACX.RTM. 575 ethylene-maleic anhydride
copolymer compatibilizer available from Allied Signal. The
compounding was accomplished using a twin screw extruder model ZSK
30 by Werner & Pfleiderer. The weight ratio of treated
TiO.sub.2 to LDPE to compatibilizer was 80:15:5. The composition
was formed into pellets and film samples were prepared using a
Brabender model PL V302 single screw extruder with a 6" wide slot
die.
Example 2
[0079] RCL-9 pigmentary rutile TiO.sub.2 was treated with 1%
.gamma.-glycidoxy propyltrimethoxysilane and 1% L-45
polydimethylsiloxane (PDMS) available from Crompton Corporation.
The TiO.sub.2 was first treated with the .gamma.-glycidoxy
propyltrimethoxysilane. The PDMS (24 g) was then mixed with the
silanized TiO.sub.2 (2400 g), LDPE (450 g) and compatibilizer (150
g) in a Henschel mixer for about one minute at 2200 RPM as in
Example 1. The dry mix was then compounded through a twin screw
extruder as in Example 1.
Example 3
[0080] Example 1 was repeated using
2-(3,4-epoxycyclohexal)ethyltriethoxys- ilane, Y-11870, available
from Crompton Corporation, instead of the
.gamma.-glycidoxypropyltrimethoxysilane.
Example 4
[0081] Example 2 was repeated using Silquest.RTM. Y-11870
2-(3,4-epoxycyclohexal)ethyltriethoxysilane, available from
Crompton Corporation, instead of the
.gamma.-glycidoxypropyltrimethoxysilane.
Comparative Example A
[0082] Untreated RCL-9 TiO.sub.2 was dry mixed with Microthene.RTM.
GMN-711-20 LDPE (MFI 22) using a plastic bag. The mix was then fed
into a twin screw extruder for compounding.
[0083] The results of the tests using Examples 1-4 and Comparative
A are summarized in Table I below.
1TABLE I Observations Torque during Example (ft-lb) Pressure (psi)
Dispersion extrusion 1 1640 <25 good low feed rate but
acceptable 2 1650 <25 good runs well, smooth surface 3 1780
<25 good low feed rate but acceptable 4 1750 20 excellent runs
well, smooth surface Comparative 2600 400 a film could Brittle,
rough A not be made Surface, very difficult to process
[0084] The data found in Table I demonstrates the processing
advantages of using TiO.sub.2 that has been treated with an
organosilicone compound (Examples 14) as compared to an untreated
TiO.sub.2 (Comparative A) as opposed to using an untreated
TiO.sub.2 pigment (Comparative A) in a high loaded 80 wt. %
TiO.sub.2/polyethylene masterbatch. The torque and pressure can be
used as a means of determining the relative ease with which each
composition is processed through the extruder. As can be seen from
the data, the comparative example with the untreated titanium
dioxide requires both higher torque and higher pressure for
processing the composition through the extruder.
[0085] Using the untreated TiO.sub.2 lead to compounding difficulty
in making a high loaded 80 wt. % TiO.sub.2 masterbatch with LDPE.
Films could not be made using the composition with the untreated
TiO.sub.2 Compounding was accomplished at a 30 wt. % level of
TiO2.
[0086] The 30 wt. % loaded compositions were selected due to the
incompatibility between untreated TiO.sub.2 and LDPE. This
incompatability resulted in difficulty in producing a masterbatch
of LDPE filled with untreated TiO.sub.2. Furthermore, films of LDPE
highly loaded with untreated TiO.sub.2 could not be successfully
made. The untreated TiO.sub.2could be used to successfully produce
a 30 wt. % loaded LDPE masterbatch, and films could be made
thereof. Consequently, compounding experiments were conducted at a
30 wt. % loading of both treated and untreated TiO.sub.2to ensure
accurate comparative results.
Comparative Example B
[0087] Untreated RCL-9 TiO.sub.2 was dry mixed with Microthene.RTM.
GMN 711-20 LDPE (MFI 22) at a weight ratio of 30:70 using a plastic
bag. The mixture was then fed into a twin screw extruder and
compounded as in Comparative Example A. The composition was formed
into pellets dried. Film samples were prepared using a Brabender
PL-V302 single extruder with a 6" wide slot die.
Example 5
[0088] Comparative example B was repeated except that the TiO.sub.2
was treated with 1% .gamma.-glycidoxy propyltrimethoxysilane
(A-187) available from Crompton Corporation, and a compatibilizer
(ACX.RTM. 575 ethylene-maleic anhydride copolymer available from
Allied Signal) was added. The weight ratio of treated TiO.sub.2 to
LDPE to compatibilizer was 30:67:3.
Example 6
[0089] Example 5 was repeated using TiO.sub.2 treated with 1%
.gamma.-glycidoxy propyltrimethoxysilane (A-187) and 1% PA-1
organomodified polydimethylsiloxane available from Crompton
Corporation The weight ratio of treated TiO.sub.2 to LDPE to
compatibilizer was 30:67:3.
Example 7
[0090] Comparative example B was repeated using TiO.sub.2 treated
with 1% 2-(3,4-epoxycyclohexyl)ethyltriethoxysilane (Y-11870), and
a compatibilizer (ACX 575, ethylene-maleic anhydride copolymer) was
added. The weight ratio of treated TiO.sub.2 to LDPE to
compatibilizer was 30:67:3.
Example 8
[0091] Example 7 was repeated using TiO.sub.2 treated with 1%
2-(3,4-epoxycyclohexal)ethyltriethoxysilane (Y-11870) and 1% PA-1
organomodified polydimethylsiloxane. The weight ratio of treated
TiO.sub.2 to LDPE to compatibilizer was 30:67:3.
[0092] The viscosity and melt flow rate of the pellets were
measured using an extrusion plastometer manufactured by Tinius
Olsen. The whiteness and yellowness index of the film samples were
measured using a Colorgard.RTM. System 05 colormeter manufactured
by Pacific Scientific. The results are summarized in Table 2
below.
2TABLE II Viscosity Flow Rate Whiteness Yellowness Example (Pa/sec)
g/10 minutes ASTM D 1925 ASTM D 1925 Comparative 841.5 12.6 71 7.32
B 5 869.1 12.3 90 2.56 6 746.2 13.1 89 2.52 7 776.6 13.0 86 3.36 8
696.3 14.8 86 3.0
[0093] The data found in Table II demonstrates the improved
processing parameters, lower viscosity, higher whiteness and lower
yellowness achieved using the organosilicone treated TiO.sub.2
pigments (Examples 5-8) versus using an untreated TiO.sub.2 pigment
(Comparative B) in a 30 wt. % TiO.sub.2/polyethylene masterbatch.
The viscosity and melt flow rate were measured using the pellets,
and the whiteness and yellowness index were measured using films
having a thickness of approximately 4 .mu.m.
Comparative Example C
[0094] Comparative Example B was repeated using untreated ground
CaCO.sub.3. The weight ratio of untreated CaCO.sub.3 and
Microthene.RTM. GMN 711-20 LDPE (MFI 22) was 30:70.
Example 9
[0095] Example 6 was repeated using ground CaCO.sub.3 treated with
1% .gamma.-glycidoxy propyltrimethoxysilane (A-187) and 1% L-45
polydimethylsiloxane available from Crompton Corporation at
Greenwich, Conn. The weight ratio of treated CaCO.sub.3 to LDPE to
compatibilizer (ACX 575) was 30:67:3.
3 TABLE III Whiteness Yellowness Example ASTM D 1925 ASTM D 1925
Comparative C 22 20.89 Example 9 40 14.52
[0096] The data found in Table III demonstrates the higher
whiteness and lower yellowness achieved using the organosilicone
treated CaCO.sub.3 (extended white pigment, Example 9) versus using
an untreated CaCO.sub.3 (Comparative Example C) in a 30 wt. %
CaCO.sub.3/polyethylene masterbatch.
Example 10
[0097] By weight, 20% of an epoxysilane (Silquest.RTM. A-187)
treated TiO.sub.2 was compounded with 2% EMAH and balance
polyethylene. Material was extruded on a Brabender PL-V302 single
screw extruder through a slit film die at 620.degree. F. Evaluation
of the film on a light box revealed superior integrity with no thin
spots or pin-holes. Rating of material equaled 10. Lacing
resistance was comparable to the industry standard Ti-Pure.RTM.
R-104, available from E.I. du Pont de Nemours and Company.
Comparative Example D
[0098] By weight, 20% of an untreated TiO.sub.2 pigment RCL-9
available from Millenium Chemicals, Inc. in Baltimore, Md., was
compounded into balance polyethylene. Material was extruded on a
Brabender PL-V302 single screw extruder through a slit film die at
620.degree. F. The film exhibited thin spots and pin-holes under a
light box. The material was rated as a 6.
[0099] Lacing occurs as a function of pigment volatility at
specific wt-% pigment loadings and processing temperature. For
polyethylene films pigmented with titanium dioxide, 20% wt. %
TiO.sub.2 in the film processed at temperature of 620.degree. F. or
greater will readily exhibit lacing of the film. Typically,
materials are rated 10 if they do not lace, and below 10 if they
begin to lace. Example 10 and comparative example D were compared
above for lacing.
[0100] Having thus described and exemplified the invention with a
certain degree of particularity, it should be appreciated that the
following claims are not to be so limited but are to be afforded a
scope commensurate with the wording of each element of the claim
and equivalents thereof.
* * * * *