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| United States Patent Application |
20070010634
|
| Kind Code
|
A1
|
|
Ziegler; Michael J.
;   et al.
|
January 11, 2007
|
Polymer additives for powder coatings
Abstract
Comb polymers prepared by reacting an acrylic polyol or a siloxane polyol
with a lactone are disclosed. These comb polymers find particular
application as additives for powder coating compositions, to improve
various performance properties thereof. Powder coating composition
comprising the described comb polymers are also disclosed.
| Inventors: |
Ziegler; Michael J.; (Cranberry Township, PA)
; Retsch; William H. JR.; (Castle Shannon, PA)
; Chasser; Anthony M.; (Allison Park, PA)
; Ambrose; Ronald R.; (Pittsburgh, PA)
; Kulfan; Jackie L.; (Mars, PA)
|
| Correspondence Address:
|
PPG INDUSTRIES INC;INTELLECTUAL PROPERTY DEPT
ONE PPG PLACE
PITTSBURGH
PA
15272
US
|
| Serial No.:
|
522243 |
| Series Code:
|
11
|
| Filed:
|
September 15, 2006 |
| Current U.S. Class: |
525/446; 525/474 |
| Class at Publication: |
525/446; 525/474 |
| International Class: |
C08L 67/00 20070101 C08L067/00; C08L 83/00 20060101 C08L083/00 |
Claims
1. A curable powder coating composition comprising: (a) a compound that
comprises the reaction product of a polyol having at least one hydroxyl
group and a lactone, wherein the polyol comprises a siloxane polyol; (b)
a film-forming resin; and (c) a crosslinker.
2-17. (canceled)
18. The composition of claim 1, wherein the siloxane polyol has a number
average molecular weight of 500 to 5000.
19. The composition of claim 18, wherein the siloxane polyol has a number
average molecular weight of 750 to 3000.
20. The composition of claim 1, wherein 1 to 100 percent of the hydroxyl
functional groups on the siloxane polyol have a lactone grafted thereto.
21. The composition of claim 1, wherein greater than 90 percent of the
hydroxyl functional groups on the siloxane polyol have a lactone grafted
thereto.
22. The composition of claim 1, wherein the reaction product of the
siloxane polyol and the lactone has a weight average molecular weight of
1,000 to 500,000.
23. The composition of claim 22, wherein the reaction product of the
siloxane polyol and the lactone has a weight average molecular weight of
20,000 to 140,000.
24. The composition of claim 1, wherein the lactone comprises
epsilon-caprolactone.
25. The composition of claim 1, wherein the reaction product of the
siloxane polyol and the lactone comprises lactone chains comprising 1 to
50 lactone derived units.
26. The composition of claim 1, wherein the film-forming resin is hydroxy
functional.
27. The composition of claim 26, wherein the film-forming resin comprises
polyester.
28. The composition of claim 1, wherein the film-forming resin is present
in an amount of 50 weight percent or greater, based on total weight of
the composition.
29. The composition of claim 1, wherein the reaction product of the
siloxane polyol and the lactone is present in an amount of 0.1 to 20
weight percent.
30. The composition of claim 29, wherein the reaction product of the
siloxane polyol and the lactone is present in an amount of 0.1 to less
than 10 weight percent.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to powder coatings comprising a
polymer additive. More specifically, the polymer additive comprises a
polyol to which is grafted linear moieties comprising lactone.
BACKGROUND INFORMATION
[0002] In recent years, powder coatings have become increasingly popular;
because these coatings are inherently low in volatile organic content
(VOC), their use significantly reduces air emissions during the
application and curing processes. Powder coatings are typically cured by
heating the coated substrate to an elevated temperature, such as higher
than 125.degree. C. During the curing process, the powder particles melt
and spread, and the components of the powder coating react.
[0003] Powder coatings used today can be classified broadly in two
distinct categories, ultraviolet durable and ultraviolet non-durable.
Often, the durable powder compositions are brittle and the non-durable
films, while flexible, may not give the desired durability. There is a
need in the marketplace to have powder coatings that give flexible and
durable films when cured. Such coatings would have widespread
application, such as in high impact areas or environments requiring
secondary post-forming stages, something that is not currently possible.
In addition, good flow, leveling and/or handling of the powder is
desired.
SUMMARY OF THE INVENTION
[0004] The present invention is generally directed to powder coatings
comprising a film-forming resin, a crosslinker, and polymers that are the
reaction product of a polyol and a lactone. The polyol is typically ether
an acrylic polyol or a siloxane polyol, and is generally linear with one
or more pendant hydroxyl groups. One or more of these hydroxyl groups are
reacted with lactone, as described below.
[0005] The powder coatings of the present invention will often demonstrate
increased flexibility and may have increased toughness; the present
powder coatings also may have improved flow and leveling characteristics
and decreased gassing as compared with powder coatings lacking the
polymer additives described herein.
DETAILED DESCRIPTION OF THE INVENTION
[0006] The present invention is directed to powder coating compositions
that comprise a film-forming resin, a crosslinker, and a polymer
additive. Use of one or more film-forming resins, crosslinkers and/or
polymer additives are within the scope of the present invention. The
polymer additive comprises the reaction product of a linear polyol having
pendant hydroxyl groups and a lactone. The reaction product of the linear
polyol and the lactone is sometimes referred to herein as the "comb
polymer". In one embodiment of the present invention, the polyol is an
acrylic polyol and in another embodiment the polyol is a siloxane polyol.
[0007] The polyols used herein are ungelled polyols comprised of monomers,
wherein at least one of the monomers provides a pendant hydroxyl group to
the polymer. The polyol can be, for example, an acrylic polyol having
pendant hydroxyl groups attached to the acrylic backbone through some
means, such as an ester linkage. Acrylic polyol" can refer to an acrylic
polymer with a degree of polymerization greater than 5 and an average
functionality greater than 2. Such polyols are commercially available
from Johnson Polymer as "hydroxyl acrylics" in their JONCRYL line.
Acrylic polyols can be prepared through normal free radical
polymerization procedures of acrylate monomers using standard techniques.
Suitable monomers for use in preparing the acrylic polyol include
ethylenically unsaturated monomers such as hydroxyethyl(meth)acrylate,
hydroxypropyl(meth)acrylate, hydroxybutyl(meth)acrylate,
methyl(meth)acrylate, ethyl(meth)acrylate, butyl(meth)acrylate,
2-ethylhexyl(meth)acrylate, (meth)acrylic acid, vinyl aromatic compounds
such as styrene, para-hydroxy styrene and vinyl toluene, nitriles such as
(meth)acrylonitrile, and vinyl esters such as vinyl acetate. Any other
acrylic monomers known to those skilled in the art could also be used.
The term "(meth)acrylate" and like terms are used conventionally and
herein to refer to both methacrylate and acrylate. Two or more monomers
can be used; at least one polymer should be selected so as to provide the
acrylic polyol with one or more pendant hydroxyl groups. Hydroxyethyl
methacrylate ("HEMA") is particularly suitable for this purpose.
[0008] The acrylic polyols used herein will typically have weight average
molecular weights of 500 to 200,000, such as 5,000 to 80,000 or 12,000 to
50,000, as determined by gel permeation chromatography using linear
polystyrene standards. The hydroxy value of these polyols can range from
5 to 200, such as 30 to 100.
[0009] Alternatively, the polyol can be a siloxane polyol. A "siloxane
polyol", as that term is used herein, refers to organic/inorganic hybrid
oligomers containing siloxane segments, carbon-silicon bonds and organic
segments terminated with hydroxy groups. Such polyols are commercially
available from Dow Corning as Z-6018. Alternatively, the siloxane polyols
can be prepared by hydrosilation of allyl glycol ethers with silicon
hydrides. U.S. Pat. No. 6,387,519, incorporated by reference herein,
describes suitable siloxane polyols such as those depicted as Formulas
II, III or VI, wherein one or more of the "R.sup.a" groups are
hydroxyl/alkyl groups.
[0010] The siloxane polyols used according to the present invention will
typically have a number average molecular weight of about 500 to 5000,
such as 750 to 3000, as determined by gel permeation chromatography. The
hydroxy value of these polyols can range from 50 to 500, such as 100 to
300.
[0011] The polyol having pendant hydroxyl groups is then further reacted
with a lactone. The lactone can be substituted or unsubstituted. It will
be appreciated that lactides are specific lactones and are within the
present invention. Particularly suitable lactones are
epsilon-caprolactones, such as methyl epsilon-caprolactone, a mixture of
isomeric methyl caprolactones or a mixture of isomeric methyl
epsilon-caprolactones with epsilon-caprolactone. Other examples include
but are not limited to octanoic lactones, butyrolactones, valerolactones,
gluconolactones, oxycyclotridecane-2-ones, and pentadeca-lactones.
[0012] The lactone is attached or grafted to the polyol through the ring
opening polymerization of the lactone initiated by the hydroxyl
functional group(s) of the polyol. The results of the grafting is the
"comb polymer" according to the present invention. The grafting step is
accomplished by charging the lactone to the reaction vessel and heating
the mixture to a temperature suitable for the ring opening reaction,
typically 80 to 250.degree. C. An additional catalyst can also be added.
As a result of the grafting procedure, between 1 and 100 percent of the
hydroxyl functional groups on the polyol will have a linear polymer chain
comprised of at least one lactone molecule attached thereto. Typically,
the large majority (i.e. greater than 70 percent, such as greater than 90
percent or 95 percent or greater) of the groups will be reacted. The
linear polymer chains comprised of at least one lactone molecule that
become attached will have a terminal hydroxyl group. Thus, the comb
polymer itself also has hydroxyl functionality. Using a large excess of
lactone can force the grafting to occur at .about.100% of the hydroxyl
groups on the polyol. A 5 to 50 fold excess of lactone to hydroxyl
functional groups can be used, as can about a 20 fold excess. It will be
understood by those skilled in the art that there are other ways to graft
the lactone moieties to the backbone polymer, all of which are within the
scope of the present invention.
[0013] The reaction between the hydroxyl group(s) on the polyol with the
lactone will result in opening of the lactone ring in the normal manner
to produce a hydroxyl terminated lactone, the other end of which will be
attached to the polyol. The hydroxyl terminated lactone chain may react
with further lactone molecules to produce a hydroxyl terminated
polylactone side chain. A "lactone chain" therefore refers to a hydroxyl
terminated side chain that results from "ring opening" the lactone; a
lactone chain according to the present invention can contain one or more
lactone-derived units. In determining the ratio of lactone to polyol to
use, consideration should be given to the amount of lactone needed to
give the desired average lactone chain length. Generally, the lactone
chain length may be increased indefinitely. Typically, the lactone does
not merely polymerize on to a few hydroxyl groups of the polyol to
produce several long lactone chains but rather the lactone molecules are
distributed among a large number of hydroxyls. As noted above, typically
greater than 70 percent, such as greater than 90 percent or even 95
percent or greater of the hydroxyl functional groups of the polyol have a
lactone chain attached thereto, although the invention is not so limited.
The amount of lactone added (expressed as a weight percentage of the
total weight of the comb polymer--both polyol and lactone side-chains) is
typically from 10 to 95 percent, such as 65 to 95 percent. Lactone chains
comprised of 2 to 50 lactone units are particularly suitable for use in
powder coatings.
[0014] The weight average molecular weight of the comb polymer of the
present invention will typically be about 5,000 to about 500,000, such
about 25,000 to 250,000, as determined by gel permeation chromatography
using linear polystyrene standards. These comb polymers are also
characterized in certain embodiments by melting temperatures in the range
of about 40 to about 65.degree. C.
[0015] In addition to one or more of the comb polymers described above,
the present powder coatings further comprise a film-forming resin. Any
resin that forms a film can be used according to the present invention,
absent compatibility problems. A particularly suitable resin for use in
the present powder compositions is one formed from the reaction of a
polymer having at least one type of reactive functional group and a
curing agent having functional groups reactive with the functional group
of the polymer. The polymers can be, for example, acrylic, polyester,
polyether or polyurethane, and can contain functional groups such as
hydroxyl, carboxylic acid, carbamate, isocyanate, epoxy, amide and
carboxylate functional groups.
[0016] The use in powder coatings of acrylic, polyester, polyether and
polyurethane polymers having hydroxyl functionality is known in the art.
Monomers for the synthesis of such polymers are typically chosen so that
the resulting polymers have a glass transition temperature ("Tg") greater
than 50.degree. C. Examples of such polymers are described in U.S. Pat.
No. 5,646,228 at column 5, line 1 to column 8, line 7, incorporated by
reference herein.
[0017] Acrylic polymers and polyester polymers having carboxylic acid
functionality are also suitable for powder coatings. Monomers for the
synthesis of acrylic polymers having carboxylic acid functionality are
typically chosen such that the resulting acrylic polymer has a Tg greater
than 40.degree. C., and for the synthesis of the polyester polymers
having carboxylic acid functionality such that the resulting polyester
polymer has a Tg greater than 50.degree. C. Examples of carboxylic acid
group-containing acrylic polymers are described in U.S. Pat. No.
5,214,101 at column 2, line 59 to column 3, line 23, incorporated by
reference herein. Examples of carboxylic acid group-containing polyester
polymers are described in U.S. Pat. No. 4,801,680 at column 5, lines 38
to 65, incorporated by reference herein.
[0018] The carboxylic acid group-containing acrylic polymers can further
contain a second carboxylic acid group-containing material selected from
the class of C4 to C20 aliphatic dicarboxylic acids, polymeric
polyanhydrides, low molecular weight polyesters having an acid equivalent
weight from about 150 to about 750, and mixtures thereof. This material
is crystalline and is preferably a low molecular weight crystalline or
glassy carboxylic acid group-containing polyester.
[0019] Also useful in the present powder coating compositions are acrylic,
polyester and polyurethane polymers containing carbamate functional
groups. Examples are described in WO Publication No. 94/10213,
incorporated by reference herein. Monomers for the synthesis of such
polymers are typically chosen so that the resulting polymer has a high
Tg, that is, a Tg greater than 40.degree. C. The Tg of the polymers
described above can be determined by differential scanning calorimetry
(DSC).
[0020] Suitable curing agents generally include blocked isocyanates,
polyepoxides, polyacids, polyols, anhydrides, polyamines, aminoplasts and
phenoplasts. The appropriate curing agent can be selected by one skilled
in the art depending on the polymer used. For example, blocked
isocyanates are suitable curing agents for hydroxy and primary and/or
secondary amino group-containing materials. Examples of blocked
isocyanates are those described in U.S. Pat. No. 4,988,793, column 3,
lines 1 to 36, incorporated by reference herein. Polyepoxides suitable
for use as curing agents for COOH functional group-containing materials
are described in U.S. Pat. No. 4,681,811 at column 5, lines 33 to 58,
incorporated by reference herein. Polyacids as curing agents for epoxy
functional group-containing materials are described in U.S. Pat. No.
4,681,811 at column 6, line 45 to column 9, line 54, incorporated by
reference herein. Polyols, materials having an average of two or more
hydroxyl groups per molecule, can be used as curing agents for NCO
functional group-containing materials and anhydrides, and are well known
in the art. Polyols for use in the present invention are typically
selected such that the resultant material has a Tg greater than about
30.degree. C.
[0021] Anhydrides as curing agents for epoxy functional group-containing
materials include, for example, trimellitic anhydride, benzophenone
tetracarboxylic dianhydride, pyromellitic dianhydride, tetrahydrophthalic
anhydride, and the like as described in U.S. Pat. No. 5,472,649 at column
4, lines 49 to 52, incorporated by reference herein. Aminoplasts as
curing agents for hydroxy, COOH and carbamate functional group-containing
materials are well known in the art. Examples of such curing agents
include aldehyde condensates of glycoluril, which give high melting
crystalline products useful in powder coatings. While the aldehyde used
is typically formaldehyde, other aldehydes such as acetaldehyde,
crotonaldehyde, and benzaldehyde can be used.
[0022] The film-forming resin described above is generally present in the
powder coatings of the invention in an amount greater than about 50
weight percent, such as greater than about 60 weight percent, and less
than or equal to 95 weight percent, with weight percent being based on
the total weight of the composition. For example, the weight percent of
resin can be between 50 and 95 weight percent. When a curing agent is
used, it is generally present in an amount of up to 30 weight percent;
this weight percent is also based on the total weight of the coating
composition.
[0023] It will be appreciated that the hydroxyl functionality that results
from the lactone addition may react with one or more of the other
components of the powder coating composition. For example, if the comb
polymer has hydroxyl functionality at the end of a lactone chain, a
blocked isocyanate crosslinker and a hydroxy functional film-forming
resin can be used.
[0024] It is also possible, according to the present invention, to modify
the functionality that is present on the comb polymer. For example, the
hydroxy functionality that results from lactone grafting can be converted
to an acidic functionality, by reacting the hydroxy, for example, with a
cyclic carboxylic acid anhydride. This reaction can be carried out by
charging the hydroxy functional comb polymer to the reaction vessel and
heating the mixture to a temperature suitable for the ring opening of the
cyclic anhydride, such as 80 to 150.degree. C. In this manner, the
hydroxy functional comb polymer is converted to an acidic functional comb
polymer. This conversion may be relevant in a system wherein a curing
agent that is reactive with a carboxylic acid functional group is desired
rather than a curing agent that is reactive toward a hydroxy functional
group, such as in a system using triglycidyl isocyanurate. Other moieties
as desired by the user could also be introduced through reaction with the
terminal hydroxy on the comb polymer.
[0025] The polymer additive of the present invention is typically present
in the curable powder coating composition in an amount ranging from 0.1
to 20 weight percent, such as 1 to 10 weight percent, or about 5 weight
percent, with weight percent based on total weight of the coating
composition; in one embodiment, the weight percent is less than 20 weight
percent. In one embodiment wherein the polyol is acrylic polyol, the
weight percent of polymer additive is less than 10 weight percent of the
total powder composition, such as less than 10 weight percent to 0.1
weight percent. As used herein, "curable coating composition", "cured
coating composition" and like terms will be understood as referring to a
composition in which the components react with each other so as to resist
melting upon heating. It will be appreciated that inclusion of the
present additives or comb polymers in the powder coatings of the present
invention will result in at least one improvement to the performance
characteristics of the present powder coatings, such as improved flow
and/or improved leveling, decreased gassing, increased flexibility,
and/or improved appearance. Even slight improvements in any of these
characteristics is deemed an improvement according to the present
invention. In some embodiments, dramatic improvement to impact resistance
is seen with even slight additions of these comb polymers. Moreover,
gloss can be more easily varied with the coatings of the present
invention. It will be further appreciated that the polymer additives or
comb polymers used in the powder coatings of the present invention are
used in additive quantities. That is, they are in quantities sufficient
to form a film themselves; an additional quantity of a separate
film-forming resin should be used in sufficient quantity to form a film.
Thus, the "film-forming resin" as used herein does not refer to the comb
polymer.
[0026] The powder coating compositions of the present invention may
optionally contain other additives such as waxes for flow and wetting,
flow control agents, such as poly(2-ethylhexyl)acrylate, degassing
additives such as benzoin and MicroWax C, adjuvant resin to modify and
optimize coating properties, antioxidants, ultraviolet (UV) light
absorbers and catalysts. Examples of useful antioxidants and UV light
absorbers include those available commercially from Ciba Specialty
Chemicals Corporation under the trademarks IRGANOX and TINUVIN. These
optional additives, when used, can be present in amounts up to 20 percent
by weight, based on total weight of the coating.
[0027] The compounds of the present invention, as well as any additional
additives, can be added at any time during the formulation of the powder
coating. For example, curable powder coating compositions of the present
invention can be prepared by first dry blending the film-forming resin,
and any of the additives described above including the present compounds,
in a blender, such as a Henschel blade blender. The blender is operated
for a period of time sufficient to result in a homogenous dry blend of
the materials. The blend is then melt blended in an extruder, such as a
twin screw co-rotating extruder, operated within a temperature range
sufficient to melt but not gel the components. The melt blended curable
powder coating composition is typically milled to an average particle
size of from, for example, 15 to 80 microns. Other methods known in the
art for preparing powder coatings can also be used.
[0028] The powder coating compositions are most often applied by spraying,
and in the case of a metal substrate, by electrostatic spraying, or by
the use of a fluidized bed. The powder coating can be applied in a single
sweep or in several passes to provide a film having a thickness after
cure of from about 1 to 10 mils, usually about 2 to 4 mils. Other
standard methods for coating application can be employed such as
brushing, dipping or flowing.
[0029] Generally, after application of the coating composition, the coated
substrate is baked at a temperature sufficient to cure the coating.
Metallic substrates with powder coatings are typically cured at a
temperature ranging from 230.degree. F. to 650.degree. F. for 30 seconds
to 30 minutes.
[0030] In certain embodiments, the present coating compositions comprise
comb polymers that are the reaction product of the polyol and lactone
that has terminal hydroxy groups or whose terminal hydroxy groups have
been converted to acid groups; the comb polymers do not have any
additional moieties attached thereto. In certain embodiments the comb
polymer used in the present coatings does not contain a UV curable
moiety, such as (meth)acrylate.
[0031] As used herein, unless otherwise expressly specified, all numbers
such as those expressing values, ranges, amounts or percentages may be
read as if prefaced by the word "about", even if the term does not
expressly appear. Any numerical range recited herein is intended to
include all sub-ranges subsumed therein. Plural encompasses singular and
vice versa. Also, as used herein, the term "polymer" is meant to refer to
oligomers and both homopolymers and copolymers; the prefix "poly" refers
to two or more.
EXAMPLES
[0032] The following examples are intended to illustrate the invention,
and should not be construed as limiting the invention in any way.
Example 1
[0033] An acrylic polymer grafted with caprolactone-based chains modified
with anhydride was prepared as follows:
[0034] To 325 parts by weight of a commercially available hydroxyl
functional acrylic polymer (JONCRYL 587, from S.C. Johnson & Son) was
added 3.25 parts by weight of stannous octoate and 1235 parts by weight
of .epsilon.-caprolactone. The resultant mixture was heated to react in a
nitrogen atmosphere at a temperature of 180.degree. C. The reaction was
allowed to progress for 4 hours at that temperature. The reaction was
then cooled to 120.degree. C. and 62.6 parts by weight of
hexahydrophthalic anhydride were added. The reaction was allowed to
progress until no anhydride groups were detected by infrared spectroscopy
analysis of the material.
[0035] The reaction product was then cooled, discharged and analyzed. The
determined acid value was 17.9 mg KOH/gram, and hydroxy value was 4.9 mg
KOH/gram. Analysis of the polymer by GPC (using linear polystyrene
standards) showed the polymer to have an Mw value of 90,893, and an Mn
value of 4308. The melting temperature was determined to be 48.5.degree.
C. by differential scanning calorimetry.
Example 2
[0036] An acrylic polymer grafted with caprolactone-based chains modified
with anhydride was prepared as follows:
[0037] To 160 parts by weight of JONCRYL 587 was added 3.42 parts by
weight of stannous octoate and 1520 parts by weight of
.epsilon.-caprolactone. The resultant mixture was heated to react in a
nitrogen atmosphere at a temperature of 170.degree. C. The reaction was
allowed to progress for 4 hours at that temperature. The reaction was
then cooled to 120.degree. C. and 30.8 parts by weight of
hexahydrophthalic anhydride were added. The reaction was allowed to
progress until no anhydride groups were detected by infrared spectroscopy
analysis of the material.
[0038] The reaction product was then cooled, discharged and analyzed. The
determined acid value was 9.7 mg KOH/gram, and hydroxy value was 3.2 mg
KOH/gram. Analysis of the polymer by GPC (using linear polystyrene
standards) showed the polymer to have an Mw value of 215,933, and an Mn
value of 9293. The melting temperature was determined to be 53.degree. C.
by differential scanning calorimetry.
Example 3
[0039] An acrylic polymer grafted with caprolactone-based chains was
prepared as follows:
[0040] To 355 parts by weight of JONCRYL 587 was added 3.41 parts by
weight of stannous octoate and 1349 parts by weight of
.epsilon.-caprolactone. The resultant mixture was heated to react in a
nitrogen atmosphere at a temperature of 180.degree. C. The reaction was
allowed to progress for 4 hours at that temperature.
[0041] The reaction product was then cooled, discharged and analyzed. The
determined acid value was 2.7 mg KOH/gram, and hydroxy value was 20.7 mg
KOH/gram. Analysis of the polymer by GPC (using linear polystyrene
standards) showed the polymer to have an Mw value of 66,489, and an Mn
value of 4,877. The melting temperature was determined to be 56.3.degree.
C. by differential scanning calorimetry, and no glass transition
temperature was observed.
Example 4
[0042] A polysiloxane polyol grafted with caprolactone-based chains
modified with anhydride was prepared as follows:
Part 1
[0043] To a suitable reaction vessel equipped with a means for maintaining
a nitrogen blanket, the following components were charged under nitrogen
flow: 116 grams of 2-allyloxypropanol, 428 grams of trimethylol propane
diallyl ether, 0.04 grams of sodium acetate, and a solution of
chloroplatinic acid in isopropanol equivalent to 10 ppm of active
platinum based on total monomer solids. The temperature of the initial
charge was increased to 80.degree. C. and 14 grams of
1,1,3,3-tetramethyldisiloxane was added. An increase in temperature was
indicative of initiation of the reaction. The temperature of the reaction
mixture was increased to 95.degree. C. and the addition of 277 grams of
1,1,3,3-tetramethyldisiloxane was completed over 60 minutes. The reaction
was exothermic and the temperature was controlled between 90 and
100.degree. C. using a cool water bath. The reaction was held at
98.degree. C. for one hour after complete addition of all reactants. The
reaction was monitored by infrared spectroscopy for the disappearance of
a silicon hydride absorption at 2150 cm-1. The reaction product was
purified by filtration and isolated as a neat polymer with a hydroxyl
number of 176 OH/gram of material.
Part 2
[0044] To 200 parts by weight of the product prepared in Part 1 was added
3.25 parts by weight of stannous octoate and 1427.2 parts by weight of
.epsilon.-caprolactone. The resultant mixture was heated to react in a
nitrogen atmosphere at a temperature of 175.degree. C. The reaction was
allowed to progress for 4 hours at that temperature. The reaction was
then cooled to 120.degree. C. and 30.8 parts by weight of
hexahydrophthalic anhydride were added. The reaction was allowed to
progress until no anhydride groups were detected by Infrared spectroscopy
analysis of the material.
[0045] The reaction product was then cooled, discharged and analyzed. The
determined acid value was 17.6 mg KOH/gram, and hydroxy value was 15.8 mg
KOH/gram. Analysis of the polymer by GPC (using linear polystyrene
standards) showed the polymer to have an Mw value of 25,564, and an Mn
value of 8961. The melting temperature was determined to be 51.3.degree.
C. by differential scanning calorimetry.
Example 5
[0046] Powder coating samples were prepared using the ingredients and
amounts (in grams) shown in Table A. The samples were prepared as
follows. The ingredients were weighed together and processed for
.about.20 s in a Prism blender at 3500 rpm's. This premix was then
extruded through a b&p Process Equipment and Systems 19 mm, co-rotating,
twin screw extruder at 450 rpm's, at temperatures ranging from
100.degree. C. to 115.degree. C. The resultant chip was milled and
classified to a median particle size of 30 to 50 .mu.m on a Hosokawa
Micron Powder Systems Air Classifying Mill I. The formulas were then
electrostatically sprayed using Nordson corona equipment onto panels
supplied by ACT Laboratories as B-1000 P60 DIW, nonpolished panels which
were first coated in the lab with P-590 electrocoat available from PPG
Industries, Inc. The powder formulations were baked for a dwell time of
25 minutes at 375.degree. F. All testing was run at a dry film thickness
of 2.5 to 3.0 mils.
TABLE-US-00001
TABLE A
Material Sample 1 Sample 2 Sample 3 Sample 4
CRYLCOAT 630.sup.1 502.8 487.3 496.8 487.8
Product from Example 1 -- 30.0 -- --
Product from Example 2 -- -- 30.0 --
Product from Example 4 -- -- -- 30.0
Triglycidylisocyanurate.sup.2 37.8 37.8 37.8 37.8
VESTAGON BF 1540.sup.3 21.0 21.0 21.0 21.0
ACTIRON 32-057.sup.4 1.4 1.4 1.4 1.4
Benzoin 5.6 5.6 5.6 5.6
RESIFLOW PL-200.sup.5 7.0 7.0 7.0 7.0
LICOWAX C.sup.6 2.6 2.6 2.6 --
IRGANOX 1076.sup.7 8.4 8.4 8.4 8.4
TiO.sub.2 R706.sup.8 150.0 150.0 150.0 150.0
Impact 20/<20 90/160 40/30 50/30
(direct/reverse)(in-lbs).sup.9
MEK (50 double rubs).sup.10 4 3 5 4
.sup.1Superdurable carboxylic acid functional polyester from UCB Surface
Specialties.
.sup.2Available from Vantico Inc.
.sup.3Self-blocked isophorone diisocyanate from Degussa CRM.
.sup.4Dimethyl lauryl amine on silica support, from Synthron Inc.
.sup.5Acrylic flow additive dispersed on silica, from Estron Chemical.
.sup.6Ethylene bis(stearamide), from Clariant Additives.
.sup.7Antioxidant, from CIBA Additives.
.sup.8Available from DuPont.
.sup.9Impact testing was run according to ASTM D 2794 using a Byk-Gardner
Falling Dart Impact tester.
.sup.10MEK resistance was run by rubbing a Q-tip soaked with methyl ethyl
ketone back and forth across a panel (one double rub) 50 times and then
rating the resulting marks as follows: MEK rating system:
0 No change
1 Slight gloss loss around test area
2 Barely detectable gloss loss in test area
3 Barely detectable scuffing of test area
4 Slightly detectible scuffing of test area
5 Noticeable scuffing of test area
6 Marring of test area
7 Smearing of test area
Readings of 0-5 are generally regarded as acceptable.
[0047] Table A demonstrates that coatings prepared with the additives of
the present invention gave better impact resistance and comparable if not
better solvent resistance as compared with a control sample.
[0048] Whereas particular embodiments of this invention have been
described above for purposes of illustration, it will be evident to those
skilled in the art that numerous variations of the details of the present
invention may be made without departing from the invention as defined in
the appended claims.
* * * * *