U.S. patent application number 09/922243 was filed with the patent office on 2003-05-15 for high strength pultrusion resin.
Invention is credited to Dixon, Harvey G., Qureshi, Shahid P..
Application Number | 20030092866 09/922243 |
Document ID | / |
Family ID | 25446755 |
Filed Date | 2003-05-15 |
United States Patent
Application |
20030092866 |
Kind Code |
A1 |
Qureshi, Shahid P. ; et
al. |
May 15, 2003 |
High strength pultrusion resin
Abstract
A pultrusion resin composition comprising about 75 wt % to about
85 wt % of a phenolic resin, about 9 wt % to about 20 wt % of the
reaction product of a polyhydroxy compound and an epoxy-functional
polysiloxane, about 6 wt % to about 15 wt %, of a phenolic epoxy,
and about 0.2 wt % to about 1 wt % of a catalyst, based on total
weight of the composition. Pultruded products are formed by drawing
fibrous reinforcement through a bath of the pultrusion resin
composition.
Inventors: |
Qureshi, Shahid P.; (Duluth,
GA) ; Dixon, Harvey G.; (Covington, GA) |
Correspondence
Address: |
BANNER & WITCOFF
1001 G STREET N W
SUITE 1100
WASHINGTON
DC
20001
US
|
Family ID: |
25446755 |
Appl. No.: |
09/922243 |
Filed: |
August 6, 2001 |
Current U.S.
Class: |
528/27 |
Current CPC
Class: |
Y10T 428/31663 20150401;
C08L 61/06 20130101; C08L 61/06 20130101; C08L 61/06 20130101; C08L
83/08 20130101; C08L 61/12 20130101; C08L 2205/035 20130101; C08L
2205/03 20130101; C08L 61/12 20130101; C08L 2666/22 20130101; C08L
2666/14 20130101; C08L 63/00 20130101; Y10T 428/31511 20150401;
C08L 83/00 20130101 |
Class at
Publication: |
528/27 |
International
Class: |
C08G 077/04 |
Claims
We claim:
1. A pultrusion resin composition comprising about 75 wt % to about
85 wt % of a phenolic resin, about 9 wt % to about 20 wt % of the
reaction product of a polyhydroxy compound and an epoxy-functional
polysiloxane, about 6 wt % to about 15 wt %, of a phenolic epoxy,
and about 0.2 wt % to about 1 wt % of a catalyst, based on total
weight of the composition.
2. The pultrusion resin composition of claim 1 wherein the resin
composition comprises about 80 wt % to about 85 wt % of the
phenolic resin, about 10 wt % to about 15 wt % of the reaction
product of a polyhydroxy compound and an epoxy-functional
polysiloxane based on total weight of the composition.
3. The pultrusion resin composition of claim 1 wherein the resin
composition comprises about 8 wt % to about 10 wt % of phenolic
epoxy based on total weight of the composition.
4. The pultrusion resin composition of claim 1 wherein the phenolic
resin has a formaldehyde to phenol mole ratio of about 1:1 to about
2:1.
5. The pultrusion resin composition of claim 1 wherein the
polyhydroxy compound and an epoxy-functional polysiloxane are first
reacted in the presence of a catalyst, and then blended with an
epoxy.
6. The pultrusion resin composition of claim 1 wherein the
polyhydroxy compound is reacted with an epoxy-functional
polysiloxane at a temperature of between about 180.degree. C. and
about 250.degree. C.
7. The pultrusion resin composition of claim 6 wherein the
polyhydroxy compound is reacted with an epoxy-functional
polysiloxane for about 1 to about 7 hours.
8. The pultrusion resin composition of claim 1 wherein the
polyhydroxy compound is selected from the group consisting of
resorcinol, phenol-formaldehyde novolac, cresol novolac, t-butyl
novolac or bis A novolac.
9. The pultrusion resin composition of claim 8 wherein the
polyhydroxy compound is resorcinol.
10. The pultrusion resin composition of claim 1 wherein the
epoxy-functional polysiloxane is epoxy silane or a compound of
formula (I) or (II): 2
11. The pultrusion resin composition of claim 1 wherein from about
0.1 to about 10 moles of polyhydroxy compound is present per mole
of epoxy in the polysiloxane.
12. The pultrusion resin composition of claim 11, wherein from
about 2 to about 3 moles of polyhydroxy compound is present per
mole of epoxy in the polysiloxane.
13. The pultrusion resin composition of claim 1 wherein the
phenolic epoxy is bis-phenol F epoxy or bis-phenol A epoxy.
14. The pultrusion resin composition of claim 13 wherein the
phenolic epoxy is bis-phenol F epoxy.
15. The pultrusion resin composition of claim 1 wherein the
catalyst is selected from the group consisting of 2-methyl
imidazole, 4-methyl imidazole, triethyl amine, benzyldimethylamine,
and triethanolamine.
16. The pultrusion resin composition of claim 15 wherein the
catalyst is 2-methyl imidazole.
17. A pultruded product comprising fibrous reinforcement and the
pultrusion resin composition of claim 1 prepared by drawing the
fibrous reinforcement through a bath of the pultrusion resin
composition.
18. A process of forming a pultruded product comprising drawing a
plurality of fibrous reinforcement through a bath of the pultrusion
resin composition of claim 1 to form a resin impregnated fiber
reinforcement.
19. The process of claim 18 further comprising shaping the resin
impregnated fiber reinforcement in a pultrusion die.
20. The process of claim 18 wherein the pultrusion resin
composition is formed in situ in the bath.
Description
FIELD OF THE INVENTION
[0001] The invention relates to high strength phenolic composites
made by pultrusion process.
BACKGROUND OF THE INVENTION
[0002] The term "pultrusion" means a method of drawing a plurality
of fibrous reinforcement coated with a binder solution through a
heated die in order to shape the fibrous reinforcement and binder
into a unitary article of desired shape.
[0003] Fibrous reinforcement, such as glass fibers, allows the
formation of varying shapes by the pultrusion process. This process
provides a composite structural member, which is typically stronger
and lighter and may be less expensive than similarly sized single
material members, such as wood. Such fiber-reinforced structures
can be used as a substitute product to conventional wood or metal
structural materials.
[0004] A schematic for a pultrusion process is shown in U.S. Pat.
No. 5,456,781. A plurality of fiber rovings is pulled through a
resin bath and then a forming die and subsequently through a heated
die that cures the resin materials and shapes the rovings and
resin. Although glass fiber has been mentioned as the fiber
filaments or rovings, other materials, including synthetic fibers,
carbon fibers, natural fibers and inorganic fibers, e.g. ceramic,
can be used in the form of filaments, rovings or mats. Suitable for
use as synthetic fibers in tension are aramid fibers, which are
commercially available from E.I. Dupont de Nemours & Company of
Delaware under the trademark "KEVLAR" and high modulus
polyethylene, which is available under the trademark "SPECTRA" from
Allied Fibers of Allied Signal, Petersburg, Va.
[0005] Phenolic resin systems containing resorcinol, such as a
commercially available phenolic resin system containing about 0-60%
resorcinol, suitable for the protrusion process are commercially
available under the trade designation GP4221 from Georgia-Pacific
Resins Inc.
[0006] Other phenolic resin systems for pultrusion composites are
described in U.S. Pat. Nos. 5,075,413; 5,075,414; and 159,405. This
patent discloses a reaction product of a resorcinol component such
as a resorcinol formaldehyde novolac resin formed as the reaction
product of resorcinol, an aldehyde and an acidic catalyst. The
resorcinol component is reacted with a phenolic resole resin such
as phenol-formaldehyde. The resulting compositions are suitable for
pultrusion processes and exhibit fire resistance.
BRIEF SUMMARY OF THE INVENTION
[0007] The invention is directed to a high strength pultrusion
resin composition comprising a phenolic resin and an elastomeric
component. In particular the present invention is directed to a
pultrusion resin composition comprising about 75 wt % to about 85
wt % of a phenolic resin, about 9 wt % to about 20 wt % of the
reaction product of a polyhydroxy compound and an epoxy functional
polysiloxane, about 6 wt % to about 15 wt %, of a phenolic epoxy,
and about 0.2 wt % to about 1 wt % of a catalyst, based on total
weight of the composition.
[0008] The invention is further directed to a pultruded product
prepared with the high strength pultrusion resin composition and a
plurality of fibrous reinforcement.
[0009] The invention is also directed to a method of preparing a
pultruded product comprising drawing a plurality of fibrous
reinforcement through a bath of the high strength resin composition
bath wherein the elastomeric component is added to the phenolic
resin prior to or during the pultrusion process.
BRIEF DESCRIPTION OF THE DRAWINGS
[0010] FIG. 1 depicts a graph of viscosity versus temperature for
two resins of the invention.
DETAILED DESCRIPTION OF THE INVENTION
[0011] The present invention is directed to a new high strength
pultrusion resin composition comprising a phenolic resin modified
with an elastomeric component. More particularly, the pultrusion
resin composition comprises a phenolic resin, the reaction product
of a polyhydroxy compound and an epoxy functional polysiloxane, a
phenolic epoxy resin, and a catalyst.
[0012] The elastomeric component of the pultrusion resin provides
flexural strength to the pultruded product. The elastomeric
component may be incorporated into the phenolic resin prior to, or
during, the pultrusion process. The elastomeric component
preferably has novolac hydroxyl functionality to allow the hydroxyl
to react with an epoxy to become part of the cured phenolic
resin.
[0013] In an embodiment of the invention, the high strength
phenolic resin composition comprises about 75 wt % to about 85 wt
%, preferably about 80 wt % to about 85 wt %, of a phenolic resin,
about 9 wt % to about 20 wt %, preferably about 10 wt % to about 15
wt %, of the reaction product of a polyhydroxy compound and an
epoxy functional polysiloxane, about 6 wt % to about 15 wt %,
preferably about 8 wt % to about 10 wt %, of a phenolic epoxy, and
about 0.2 wt % to about 1 wt %, preferably about 0.4 wt % to about
0.6 wt %, of a catalyst.
[0014] Any phenolic resole systems used in pultrusion processes can
be used with the present invention. For example, the phenolic
resole resin may be prepared, for example, by reacting phenol and
formaldehyde typically in the presence of a basic catalyst, such as
sodium hydroxide or an amine such as hexamine, at a temperature
below about 95.degree. C., preferably between about 45.degree. C.
and about 85.degree. C. Generally, the formaldehyde to phenol mole
ratio in the phenolic resole resin is about 0.8 to about 4,
preferably about 1 to about 2 moles. The basic catalyst to phenol
mole ratio in preparing the phenolic resole resin is from about
0.001 to about 0.1 moles of catalyst per mole of phenol, preferably
from about 0.005 to about 0.05. The term phenol is used generically
to encompass any suitable phenolic compound.
[0015] The elastomeric component is formed from the reaction
product of a polyhydroxy compound and an epoxy-functional
polysiloxane in the presence of a catalyst. Preferably, the
polyhydroxy compound is reacted with an epoxy-functional
polysiloxane in the presence of the catalyst at a temperature of
between about 180.degree. C. and about 250.degree. C. for about 1
to about 7 hours.
[0016] The resulting reaction product is then blended with a
phenolic epoxy. The phenolic resin may be combined with a phenolic
epoxy prior to or after the addition of the reaction product.
[0017] The polyhydroxy compound may be any suitable polyhydroxy
compound such as resorcinol, phenol-formaldehyde novolac, cresol
novolac, t-butyl novolac or bis A novolac. Preferably the
polyhydroxy compound is resorcinol.
[0018] The epoxy-functional polysiloxane include those described in
EP 0 428 871 which is hereby incorporated by reference in its
entirety. Specifically, the formulas identified as formulas (I) and
(II) and specific epoxy-functional polysiloxanes as identified by
organopolysiloxanes I-1 to I-8, II-1 to II-7, III-1 to III-7, IV-I
to IV-7, and V-1 to V-7. 1
[0019] The epoxy-functional polysiloxane also include OSI Witco
Y-12940 and OSI Witco Y-14362. Other epoxy-functional polysiloxanes
include, but are not limited to, Dow Corning 2-8065, DC Toray
Silicones BY 1-2940, ShinEtsu KF-105, ShinEtsu X-22-163A, Shin Etsu
X-22-163B, and ShinEtsu X-22-163C
[0020] Generally, from about 0.1 to about 10 moles, preferably from
about 2 to about 3, of polyhydroxy compound is present per mole of
epoxy in the polysiloxane.
[0021] An example of reacting resorcinol with an epoxy-functional
polysiloxane may be found in copending application Ser. No.
09/511,350, which is hereby incorporated by reference in its
entirety. In this example, 100 parts of resorcinol are heated to
195.degree. C., and a blend of 2 parts of benzyldimethylamine and
222 parts of epoxy-functional polysiloxane are added over 5 hours
while maintaining a temperature of 195.degree. C. The material is
then further heated for 2 hours to make a phenolic-functionalized
polysiloxane.
[0022] The phenolic epoxy may be a bis-phenol epoxy such as
bis-phenol F epoxy or bis-phenol A epoxy. Preferably the epoxy is
bis-phenol F epoxy. Other epoxy resins are described in U.S. Pat.
No. 4,086,250, which is hereby incorporated by reference in its
entirety.
[0023] The catalyst promotes the reaction of phenolic-functional
polysiloxane and phenolic epoxy. The catalyst may be any suitable
base catalyst such as 2-methyl imidazole, 4-methyl imidazole, and
tertiary amines such as triethyl amine, benzyldimethylamine,
triethanolamine. Preferably, the catalyst is 2-methyl
imidazole.
[0024] The resin composition is used in the pultrusion process. The
ingredients may be mixed prior to or during the pultrusion process
For example, the phenolic resole resin and phenolic epoxy are mixed
and then phenolic-functional siloxane is blended. This mixture is
stored as stock solution at 5.degree. C. for future production.
Prior to the pultrusion process, the mixture is warmed to ambient
conditions and then the imidazole catalyst is added. The mixture is
kept at 40.degree. C. in an oven and then poured into resin bath of
pultrusion equipment. During the pultrusion process implies that
only phenolic resin is stored as stock product and then prior to
the pultrusion process, the resin is mixed with phenolic-functional
polysiloxane, phenolic epoxy and catalyst.
[0025] The fibrous reinforcement may be prepared by grouping
filaments together into strands or fibers, which then may be
grouped together into twisted strands to form yams, or untwisted
strands to form rovings of a fibrous material or which may be bound
together as continuous or chopped strands to form mat, such as of a
glass, ceramic, carbon, metal, thermosetting or thermoplastic
resin, or natural fibers. The fiber reinforcement, whether strands,
fibers, yams, rovings, or mats, are drawn through a bath of liquid
resin and then through a pultrusion die to shape the fibrous
reinforcement and resin. The resin is then cured.
[0026] Suitable fibers include any of the fibers known for
pultrusion processes in the prior art, including but not limited to
natural fibers, paper fibers, carbon fibers, ceramic fibers, metal
fibers, synthetic resin fibers, including thermosetting and
thermoplastic types, especially aramid fibers and high modulus
polyethylene, glass fibers, other inorganic fibers including
composite ceramic fibers and metal fibers, and combinations
thereof. Specific fibers include KEVLAR, and NOMEX honeycomb.
[0027] The content of the fibrous reinforcement and nature thereof
will vary according to the desired strength but usually is in a
range of 60-85% by weight, preferably 70-80% by weight.
[0028] During the pultrusion process, the viscosity of the
pultrusion resin composition is preferably controlled by increasing
or decreasing the temperature of the resin bath. Alternatively, a
solvent may be added to the resin. Preferably, the resin does not
contain a solvent.
EXAMPLE 1
[0029] Six-inch wide 1/4 inch thick pultruded composites were
prepared with compositions described in Table 1. The gel time is
the time when the resin is no longer stringy on the hot plate and
is no longer workable. The cure time is the time when the resin is
and is hard on the hot plate.
1TABLE 1 Formula: 1 2 3 4 5 6 7 Phenolic resole resin 80 g 80 g 80
g 80 g 80 g 100 g 80 g Reaction product of 13 g 13 g 13 g 13 g 13 g
13 g 13 g resorcinol and epoxy siloxane Bis-phenol A epoxy 7g -- 7
g Bis-phenol F epoxy 7 g 7 g 7 g 4-methyl imidazole .5 g .5 g
2-methyl imidazole .5 g Gel Time @ 180 175 190 200 250 270 138 150
.degree. C., sec Cure Time @ 350 450 680 680 780 700 483 150
.degree. C., sec Appearance @ RT milky, milky, milky, milky, milky,
trans- milky, tan, tan, tan, tan, tan, parent, tan, opaque opaque
opaque opaque opaque brown opaque
[0030] Formulas 1, 2, and 7 had the fastest gel and cure times.
Formulas 3 and 4 were the same as formulas 1 and 2 except formulas
3 and 4 do not have a catalyst. Formulas 3 and 4 had higher gel
times and cure times. It is believed that the gel and cure times
were higher due to the lack of catalyst in formulas. Formula 7 had
a different catalyst than the catalyst used in Formulas 1 and 2.
The catalyst 2-methylimidazole is a more reactive catalyst than
4-methylimidazole. Although the melting point of the
2-methylimidazole (142.degree. C.) is much higher than the melting
point of the 4-methylimidazole (54.degree. C.), the
2-methylimidazole is preferred because temperature of the
pultrusion is in excess of 225.degree. C. and thus melting point
temperature is not a factor.
[0031] Formulas 1 and 2 were tested for viscosity versus
temperature. The bis-phenol F epoxy had a lower viscosity than the
bis-phenol A epoxy. Moreover, in both formulas, as the temperature
increases, the viscosity decreases. See FIG. 1. Thus, the viscosity
can be controlled by changing the temperature of the resin bath
during the pultrusion process instead of adding solvent to the
bath. Formula 7 should have viscosities comparable to Formula 2
since they are the same except for the catalyst.
EXAMPLE 2
[0032] Neat resin castings were prepared using the reaction product
of resorcinol and epoxy silane, 0.5 pph of 4-methyl imidazole, and
either bis-phenol A epoxy or bis-phenol F epoxy. The pultruded
parts were tested for flexural strength and for flammability. The
castings of both formulas were tough but the castings made with bis
phenol A epoxy were translucent compared to the ones made with
bis-phenol F epoxy, which were opaque.
[0033] Based on the results of Examples 1 and 2, the following are
preferred formulas for the pultrusion resin.
2 TABLE 2 Formula: 8 9 Phenolic resole resin 79.6 g 79.6 g Reaction
product of 11.9 g 11.9 g resorcinol and epoxy siloxane Bis-phenol A
epoxy 8 g -- Bis-phenol F epoxy 8 g 2-methyl imidazole, gram 0.5 g
0.5 g
[0034] While the invention has been described with respect to
specific examples including presently preferred modes of carrying
out the invention, those skilled in the art will appreciate that
there are numerous variations and permutations of the above
described systems and techniques that fall within the spirit and
scope of the invention as set forth in the appended claims.
* * * * *