U.S. patent application number 09/832228 was filed with the patent office on 2002-12-19 for block copolymers of lactone and lactam, compatabilizing agents, and compatibilized polymer blends.
This patent application is currently assigned to University of Akron. Invention is credited to Kim, Byong-Jun, White, James L..
Application Number | 20020193518 09/832228 |
Document ID | / |
Family ID | 25261048 |
Filed Date | 2002-12-19 |
United States Patent
Application |
20020193518 |
Kind Code |
A1 |
White, James L. ; et
al. |
December 19, 2002 |
BLOCK COPOLYMERS OF LACTONE AND LACTAM, COMPATABILIZING AGENTS, AND
COMPATIBILIZED POLYMER BLENDS
Abstract
This invention relates to high molecular weight block copolymers
of .epsilon.-caprolactone and .omega.-lauryl lactam prepared by
sequential bulk polymerization using a mixture of at least one
anionic polymerization initiator and optionally at least one
co-initiator. A preferred continuous sequential bulk reactive
extrusion process comprises feeding a mixture of .omega.-lauryl
lactam, at least one anionic polymerization initiator, and at least
one co-initiator into the first (i.e., upstream) hopper of an
extruder, and thereafter feeding .epsilon.-caprolactone into a
second (i.e., downstream) hopper of the extruder. The preferred
continuous sequential bulk reactive extrusion is solvent free,
rapid (typical mean and maximum residence times in the extruder
being no more than about 20 minutes and 30 minutes respectively),
and produces a high conversion of monomers to block copolymer. The
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block copolymers
compatibilize the blending of otherwise immiscible or poorly
miscible polymers to form polymer blends having improved mechanical
and thermal properties. Accordingly, the block copolymers can be
compounded with chlorine containing polymers and other polymers
such as polyamides, anhydride polymers such as maleic anhydride,
and the like. To improve the impact resistance of the
compatibilized blend, impact modifiers can be utilized such as
maleic anhydride modified EPM, EPDM, and the like. To improve
thermal and mechanical properties, thermal performance modifiers
can be utilized such as maleic anhydride polyolefins or maleic
anhydride modified polymers made from vinyl substituted aromatic
monomers.
Inventors: |
White, James L.; (Akron,
OH) ; Kim, Byong-Jun; (Akron, OH) |
Correspondence
Address: |
HUDAK & SHUNK CO., L.P.A.
Daniel J. Hudak
Suite 808
7 West Bowery Street
Akron
OH
44308-1133
US
|
Assignee: |
University of Akron
|
Family ID: |
25261048 |
Appl. No.: |
09/832228 |
Filed: |
April 10, 2001 |
Current U.S.
Class: |
525/88 |
Current CPC
Class: |
C08G 69/44 20130101;
C08L 77/12 20130101; C08L 77/12 20130101; C08L 77/12 20130101; C08L
2666/08 20130101; C08L 51/00 20130101 |
Class at
Publication: |
525/88 |
International
Class: |
C08L 053/00 |
Claims
What is claimed is:
1. A compatibilized polymer blend of at least two polymers
comprising: a carbonyl containing polymer, a chlorine containing
polymer, and an effective amount of a lactone/lactam block
copolymer compatibilizing agent.
2. A compatibilized polymer blend according to claim 1, wherein
said carbonyl containing polymer comprises polyamide, wherein said
polyamide is derived from an internal lactam having from about 4 to
about 20 carbon atoms, or is derived from the reaction of a diamine
having from 4 to about 15 carbon atoms and a dicarboxylic acid
having from about 4 to about 15 carbon atoms, and wherein the
amount of said chlorine containing polymer is from about 15% to
about 90% by weight based upon the total weight of said chlorine
containing polymers and said carbonyl containing polymers.
3. A compatibilized polymer blend according to claim 2, wherein the
amount of said compatibilizing agent is from about 1 to about 30
parts by weight per 100 parts by weight of said polymer blend,
wherein said chlorine containing polymer is polyvinyl chloride,
chlorinated polyvinyl chloride, a copolymer of polyvinyl chloride,
a copolymer of chlorinated polyvinyl chloride, polyvinylidene
chloride, or a chlorinated polyolefin, or blends thereof, and
wherein the amount of said chlorine containing polymer is from
about 50% to about 90% by weight based upon the total weight of
said chlorine containing polymers and said carbonyl containing
polymers.
4. A compatibilized polymer blend according to claim 3, wherein
said chlorine containing polymer is polyvinyl chloride, chlorinated
polyvinyl chloride, a copolymer of polyvinyl chloride, or blends
thereof, and wherein said carbonyl containing polymer is polyamide
12, polyamide 6-12, Polyamide 12-12.
5. A compatibilized polymer blend according to claim 4, wherein
said block copolymer is a lactone/lactam diblock copolymer, and
wherein the amount of said block copolymer is from about 5 to about
15 parts by weight per 100 parts by weight of said polymer
blend.
6. A compatibilized polymer blend according to claim 1, wherein
said lactone block is made from lactone monomers having from 4 to
10 carbon atoms, and wherein said lactam block is made from lactam
monomers having from 4 to 20 carbon atoms.
7. A compatibilized polymer blend according to claim 2, wherein the
amount of said lactam in said block copolymer is from about 30% to
90% by weight, wherein the amount of lactone is said block
copolymer is from about 10% to about 70% by weight based upon the
total weight of said lactam-lactone block copolymer, and wherein
the number average molecular weight of at least one lactam block
and of at least one lactone block, independently, is from about
5,000 to about 180,000.
8. A compatibilized polymer blend according to claim 2, wherein
said block polymer is an AB or an ABA block copolymer wherein said
A block is derived from lactone monomers and wherein said B block
is derived from lactam monomers.
9. A compatilibized polymer blend according to claim 2, wherein
said block copolymer is an AB block copolymer wherein said A block
is derived from .epsilon.-caprolactone monomers and said B block is
derived from lauryl lactam, wherein the amount of said lactone
block is from about 10% to about 70% by weight based upon the total
weight of said AB block copolymer, and wherein the number average
of molecular weight of said lactam block and said lactone block,
independently, is from about 30,000 to about 100,000.
10. A compatilibized polymer blend according to claim 3, wherein
said block copolymer is an AB or an ABA block copolymer wherein
said A block is derived from lactone monomers and wherein said B
block is derived from lactam monomers.
11. A compatilibized polymer blend according to claim 3, wherein
said block copolymer is an AB block copolymer wherein said A block
is derived from .epsilon.-caprolactone monomers and said B block is
derived from lactam monomers having 11 or 12 total carbon
atoms.
12. A compatilibized polymer blend according to claim 4, wherein
said block copolymer is an AB or an ABA block copolymer wherein
said A block is derived from lactone monomers and wherein said B
block is derived from lactam monomers, wherein the amount of said
lactone block is from about 20% to about 65% by weight based upon
the total weight of said AB or said ABA block copolymer, and
wherein the number average of molecular weight of said lactam block
and said lactone block, independently, is from about 30,000 to
about 100,000.
13. A compatilibized polymer blend according to claim 5, wherein
said block copolymer is an AB block copolymer, wherein said A block
is derived from .epsilon.-caprolactone and said B block is derived
from lauryl lactam, wherein the amount of said lactone block is
from about 25% to about 55% by weight based upon the total weight
of said AB block copolymer, and wherein the number average of
molecular weight of said lactam block and said lactone block,
independently, is from about 30,000 to about 100,000.
14. A compatibilized polymer blend according to claim 5, wherein
said block copolymer is an AB or an ABA block copolymer wherein
said A block is derived from lactone monomers and wherein said B
block is derived from lactam monomers.
15. A process for continuous making a
poly(.epsilon.-caprolactone/.omega.-- lauryl lactam) block
copolymer comprising: bulk polymerizing .omega.-lauryl lactam in
order to form a poly(.omega.-lauryl lactam) polymer, and thereafter
bulk copolymerizing .epsilon.-caprolactone in the presence of said
poly(.omega.-lauryl lactam) polymer, wherein said process uses at
least one anionic polymerization initiator and optionally at least
one polymerization co-initiator.
16. A process according to claim 15, including: feeding a mixture
of said (.omega.-lauryl lactam, at least said one anionic
polymerization initiator, and at least said optional co-initiator
into a first, upstream hopper of an extruder and forming said
poly(.omega.-lauryl lactam) polymer, and thereafter feeding
.epsilon.-caprolactone into a second, downstream hopper of said
extruder, and continuing copolymerization and forming said
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block
copolymer.
17. A process according to claim 16, wherein said initiator
comprises at least one Group IA (periodic table IUPAC notation)
metal, hydride, or salt; or Group IIA (periodic table IUPAC
notation) hydride or salt.
18. A process according to claim 17, wherein said initiator
comprises at least one Group IA metal or hydride; and said
co-initiator comprises at least one isocyanate having the formula
R--(NCO).sub.n, wherein R is a hydrocarbon having from 1 to about
10 carbon atoms, and n is from about 1 to about 3.
19. A process according to claim 18, wherein said metal hydride
comprises sodium hydride, and said isocyanate comprises
1,6-hexamethylene diisocyanate.
20. A process according to claim 17, wherein said initiator
comprises at least one Group IA metal or hydride, and said
co-initiator comprises at least one acylated derivative of
caprolactam having the formula: 2or a Group IA (periodic table
IUPAC notation) salt of said derivative, or a mixture thereof,
wherein R and R' independently are hydrogen or an alkyl group
having from 4 to 10 carbon atoms, wherein R and R' can join
together to form an alkylene group in a cyclic structure, and X is
a polar substituent.
21. A process according to claim 20, wherein said R and R'
independently join together to form an alkylene group having 4 to 7
carbon atoms in a cyclic structure, and X is an acyl, carbonyl or
cyano group.
22. A process according to claim 21, wherein said metal hydride
comprises sodium hydride, and said acylated derivative of
caprolactam comprises N-acetyl-6-caprolactam.
23. A process according to claim 16, wherein said extruder has twin
screws.
24. A composition comprising: a block copolymer of
.epsilon.-caprolactone and .omega.-lauryl lactam, wherein the
amount of polymerized .epsilon.-caprolactone is from about 1 wt. %
to about 80 wt. % of the total weight of said block copolymer.
25. A composition according to claim 24, wherein the amount of
polymerized .epsilon.-caprolactone comprises from about 10 wt. % to
about 70 wt. % of the total weight of said block copolymer, and
wherein the number average molecular weight (M.sub.n) of each said
block, independently, is from about 5,000 to about 180,000 as
measured by gel permeation chromatography.
26. A composition according to claim 25, wherein the amount of
polymerized .epsilon.-caprolactone comprises from about 20 wt. % to
about 65 wt. % of the total weight of said block copolymer.
27. A composition according to claim 26, wherein the amount of
polymerized .epsilon.-caprolactone comprises from about 35 wt. % to
about 55 wt. % of the total weight of said block copolymer, and
said number average molecular weight (M.sub.n) is from about 20,000
to about 150,000.
28. A composition according to claim 26, wherein said block
copolymer comprises a di-block copolymer.
29. A composition according to claim 26, wherein said block
copolymer comprises a tri-block copolymer.
30. A compatibilized polymer blend according to claim 1, including
an impact modifier, wherein said impact modifier is an unsaturated
anhydride modified flexible polymer.
31. A compatibilized polymer blend according to claim 3, including
an unsaturated anhydride modified polymeric impact modifier,
wherein said unsaturated anhydride contains from 4 to 15 carbon
atoms, wherein said polymer is EPDM, or EPM, and wherein the amount
of said anhydride is from about 0.1 to about 10% by weight based
upon the total weight of said impact modifier.
32. A compatibilized polymer blend according to claim 4, including
a maleic anhydride modified polymeric impact modifier, wherein said
polymer is EPDM, wherein the amount of said maleic anhydride is
from about 0.2 to about 7% by weight based upon the total weight of
said impact modifier, and wherein the amount of said impact
modifier is from about 5 to about 30 parts by weight per 100 parts
by weight of said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
33. A compatibilized polymer blend according to claim 5, including
a maleic anhydride modified polymeric impact modifier, wherein said
polymer is EPDM, wherein the amount of said maleic anhydride is
from about 0.5 to about 3% by weight based upon the total weight of
said impact modifier, and wherein the amount of said impact
modifier is from about 5 to about 30 parts by weight per 100 parts
by weight of said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
34. A compatibilized polymer blend according to claim 7, including
an unsaturated anhydride modified polymeric impact modifier,
wherein said unsaturated anhydride contains from 4 to 15 carbon
atoms, wherein said polymer is EPDM, or EPM, and wherein the amount
of said anhydride is from about 0.3 to about 7% by weight based
upon the total weight of said impact modifier.
35. A compatibilized polymer blend according to claim 9, including
a maleic anhydride modified polymeric impact modifier, wherein said
polymer is EPDM, and wherein the amount of said maleic anhydride is
from about 0.5 to about 5% by weight based upon the total weight of
said impact modifier.
36. A compatibilized polymer blend according to claim 11, including
a maleic anhydride modified polymeric impact modifier, wherein said
polymer is EPDM, wherein the amount of said maleic anhydride is
from about 0.3 to about 7% by weight based upon the total weight of
said impact modifier, and wherein the amount of said impact
modifier is from about 5 to about 30 parts by weight per 100 parts
by weight of said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
37. A compatibilized polymer blend according to claim 13, including
a maleic anhydride modified polymeric impact modifier, wherein said
polymer is EPDM, wherein the amount of said maleic anhydride is
from about 0.5 to about 5% by weight based upon the total weight of
said impact modifier, and wherein the amount of said impact
modifier is from about 5 to about 30 parts by weight per 100 parts
by weight of said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
38. A compatibilized polymer blend according to claim 1, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers.
39. A compatibilized polymer blend according to claim 3, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers, wherein said unsaturated anhydride contains from about 4
to about 15 carbon atoms, wherein said polyolefin is derived from
olefin monomers having 2 to about 6 carbon atoms, wherein said
vinyl substituted aromatic monomers have from about 8 to about 12
carbon atoms, and wherein the amount of said thermal performance
modifier is from about 5 to about 50 parts by weight per 100 parts
by weight of said said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
40. A compatibilized polymer blend according to claim 4, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers, wherein said unsaturated anhydride is maleic anhydride,
wherein said polyolefin is polyethylene, polypropylene, or
combinations thereof, and wherein said polymer derived from vinyl
substituted aromatic monomers is polystyrene.
41. A compatibilized polymer blend according to claim 7, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers, wherein said unsaturated anhydride contains from about 4
to about 15 carbon atoms, wherein said polyolefin is derived from
olefin monomers having 2 to about 6 carbon atoms, wherein said
vinyl substituted aromatic monomers have from about 8 to about 12
carbon atoms, and wherein the amount of said thermal performance
modifier is from about 5 to about 40 parts by weight per 100 parts
by weight of said said chlorine containing polymer, said carbonyl
containing polymer, and said block copolymer compatiblizing
agent.
42. A compatibilized polymer blend according to claim 9, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers, wherein said unsaturated anhydride is maleic anhydride,
wherein said polyolefin is polyethylene, polypropylene, or
combinations thereof, and wherein said polymer derived from vinyl
substituted aromatic monomers is polystyrene.
43. A compatibilized polymer blend according to claim 13, including
a thermal performance modifier, wherein said thermal performance
modifier is an unsaturated anhydride modified polyolefin or an
anhydride modified polymer derived from vinyl substituted aromatic
monomers, wherein said unsaturated anhydride is maleic anhydride,
wherein said polyolefin is polyethylene, polypropylene, or
combinations thereof, wherein said polymer derived from vinyl
substituted aromatic monomers is polystyrene, and wherein the
amount of said thermal performance modifier is from about 15 to
about 30 parts by weight per 100 parts by weight of said chlorine
containing polymer, said carbonyl containing polymer, and said
block copolymer compatiblizing agent.
Description
FIELD OF THE INVENTION
[0001] This invention relates to compatibilizing agents for blends
of chlorine containing polymers and carbonyl containing compounds
such as polyamide having improved mechanical and thermal
properties. The compatibilizing agents are block copolymers of
lactones and lactams prepared by sequential bulk polymerization
using a mixture of at least one anionic polymerization initiator
and optionally at least one co-initiator. Various thermal
performance modifiers and impact modifiers can be utilized to
improve the thermal properties as well as the impact resistance of
a compatibilized blend.
BACKGROUND OF THE INVENTION
[0002] The first studies of the polymerization of lactones were in
the 1930s by W. H. Carothers and his coworkers. Subsequently, the
mechanisms of cationic, anionic, and coordination polymerization of
various lactones were studied throughout the 1950's to the present.
It is well known that polylactones, notably
poly(.epsilon.-caprolactone), of high molecular weight mass exhibit
a high compatibility and miscibility with many thermoplastics and
elastomeric polymers. Polylactones having melting points lower than
polyethylene are thermally stable up to 220.degree. C. Above this
temperature, they slowly depolymerize to yield lactone monomer and
oligomer. Union Carbide, Solvay, and Daicel are commercial
producers of a series of polycaprolactones possessing various
ranges of molecular weights.
[0003] The first commercial polyamides also were developed by W. H.
Carothers at the DuPont Company. He obtained many patents on
polyamides produced from dicarboxylic acids and diamines. Shortly
after DuPont's entry into the field, I. G. Farbenindustrie obtained
patents for polymers based on the ring-opening polymerization of
.epsilon.-caprolactam. Linear aliphatic polyamides, frequently
referred to generically as nylons, rank among the most important
commercial polymers.
[0004] They were introduced in the 1930s as the first synthetic
fiber, and subsequently as the first crystalline engineering
thermoplastic.
[0005] Lactone and lactam polymerization caused by a ring-opening
process can lead to high molecular weight polymers. Such
polymerization of lactones usually has been conducted at relatively
low temperatures in an appropriate solvent and at modest rates.
[0006] Solvent-free (i.e., bulk) polymerization has been of
interest to industry because of its great economic savings.
However, one of the problems of bulk polymerization is a difficulty
of temperature control caused by exothermic reaction. U.S. Pat. No.
3,021,313 relates to aluminum alkoxides as initiators of the
polymerization of monomeric cyclic esters in a conventional
reactor. U.S. Pat. No. 3,021,016 relates to metal hydrides as
initiators of the polymerization of monomeric cyclic esters in a
conventional reactor. The polymers of the patents can be prepared
via bulk, suspension, or solution polymerization.
[0007] Advantages of the screw extruder as a chemical reactor
include fewer processing steps and no need for a solvent. On-line
(i.e., in-situ) polymerization, mixing and compounding allow
continuous downstream processing, easy devolatilization of
by-product, and easy recycling of products. Thus continuous
polymerization using a screw extruder (i.e., reactive extrusion) is
attractive as an alternative to both bulk and solvent
polymerization.
[0008] Continuous monomer polymerization of certain urethanes,
lactams, acrylates, and styrene using a screw extruder is known in
the prior art. Co-rotating and counter-rotating twin screw
extruders are considered to be attractive chemical reactors
providing good technical and economical means for polymerization
and polymer modification.
[0009] In particular, continuous polymerization of
.epsilon.-caprolactone in a screw extruder has become possible with
alkoxymetallic complexes as initiators that result in short
reaction times. U.S. Pat. No. 5,468,837 relates to reactive
extrusion of .epsilon.-caprolactone using aluminum alkoxides. U.S.
Pat. No. 5,801,224 relates to reactive extrusion of a cyclic
aliphatic ester (e.g. a lactone monomer such as
.epsilon.-caprolactone), optionally together with a secondary
component containing hydroxyl or amino group functionality, using
coordination insertion catalysts and/or initiators such as Lewis
acids and metal alkoxides. The ester must contain less than 100 ppm
water and have an acid value less than 0.5 mg KOH/g and preferably
less than 0.2 mg KOH/g. It is indicated that higher water and acid
content reduces overall polymerization rate and ultimately leads to
lower conversion of monomer to polymer. Further, Gimenez et al.
reported the reactive extrusion of .epsilon.-caprolactone catalyzed
by tetrapropoxytitanium in Polymer Processing Society 14.sup.th
Annual Meeting (Yokohama, Japan), PPS-14, pp. 629-630 (1998), and
also in International Polymer Processing 15, pp. 20-27 (2000).
[0010] U.S. Pat. No. 2,251,519 relates to random polymerization of
cyclic amides such as caprolactam, optionally together with cyclic
esters such as caprolactone, using any of the alkali or alkali
earth metals. However, the reaction was slow, e.g., 1/2 hour to 5
hours. U.S. Pat. No. 3,017,391 relates to faster polymerization of
.epsilon.-caprolactam at lower temperatures using certain
nitrogen-containing promoters together with alkali and alkali earth
metal catalysts. U.S. Pat. No. 3,200,095 relates to reactive
extrusion of 6-caprolactam using a mixture of an alkali metal salt
of 6-caprolactam and certain N-substituted compounds free of
primary amino groups, such as N-acetyl-6-caprolactam. U.S. Pat. No
3,371,055 relates to reactive extrusion of lactams using a catalyst
such as certain alkali or alkali earth metal compounds or certain
organometallic compounds of the first to third main group of the
Periodic Table, together with certain activators such as acylated
lactams and lactams having groups with acylating activity attached
to the lactam nitrogen. An article by Kye et al. (Journal of
Applied Polymer Science, Vol. 52, pp. 1249-1262 (1994)) relates to
reactive anionic polymerization of caprolactam integrated with
continuous melt spinning of polyamide-6 fiber.
[0011] U.S. Pat. No. 3,758,631 relates to block copolymers prepared
by (1) end-capping and optionally chain-extending a polylactone
diol with a diisocyanate and (2) thereafter reacting the first step
reaction product with caprolactam in the presence of an anionic
catalyst for the polymerization of caprolactam. The first step is
said to take from about 15 minutes to 3 or 4 hours and the second
step from 0.1 to 18 hours. However, the examples show reaction
times of hours, making the process impractical for reactive
extrusion.
[0012] British Patent No. 1,099,184 relates to
poly(lactone-lactam)s in which as few as 5 for every 100 units of
the polymer chain are amide units. The copolymers are solid
crystalline materials having high melting temperature and being
substantially insoluble in hydrocarbons. Although the patent states
that it includes both random and block copolymers, it is apparent
that only random copolymers were envisaged, since each example
produced a material with a single, narrow melting point range. The
patent also states that the polyesteramides can be blended with
other polymers, but there is no teaching as to why or how this
might be done.
[0013] An article by Goodman et al. (Eur. Polym. J., Vol. 20, No.
3, pp. 241-247 (1984)) relates to copolymers of
.epsilon.-caprolactone and .omega.-lauryl lactam prepared via
anionic polymerization. The products are said to have relatively
random structures. However, it is known by those skilled in the art
that random .epsilon.-caprolactone/.omega.-laury- l lactam
copolymers do not work well if at all to compatibilize blending of
PVC with other thermoplastics.
[0014] An abstract by Ha et al. presented at the Polymer Processing
Society's Aug. 17-19, 1998 meeting in Toronto, Ontario relates to a
simultaneous and to a continuous sequential bulk polymerization of
lauryl lactam, caprolactone, caprolactam/lauryl lactam, and
caprolactone/caprolactam using several anionic catalysts.
[0015] New block copolymers are desired that are both relatively
easy to prepare, especially via reactive extrusion, as well as
suitable for compatibilizing (i.e., facilitating or enhancing)
blending of chlorine containing polymers (such as vinyl chloride
polymers and the like) with other polymers (such as nylons, maleic
anhydride polymers, and the like) in order to produce blends having
improved mechanical and thermal properties.
SUMMARY OF THE INVENTION
[0016] This invention relates to compatibilized blends of chlorine
containing polymers and carbonyl containing polymers utilizing high
molecular weight block copolymers of lactones and lactams such as
.epsilon.-caprolactone (also known as 6-caprolactone) and
.epsilon.-lauryl lactam (also known as .omega.-lauryl lactam)
prepared by a sequential bulk polymerization using at least one
anionic polymerization initiator and optionally at least one
co-initiator block. The block copolymerization of the
compatibilizing agent can be performed sequentially in a single
reaction vessel by preferably (1) feeding a mixture of
.omega.-lauryl lactam, at least one anionic polymerization
initiator, and optionally at least one co-initiator into the vessel
and allowing polymerization to occur, and (2) thereafter feeding
.epsilon.-caprolactone into the same vessel and allowing the block
copolymer to form. Alternatively, the first step can be performed
in one reaction vessel and the reacted contents transferred to a
second reaction vessel before addition of .epsilon.-caprolactone
and formation of the block copolymer.
[0017] In a preferred embodiment, a single or preferably a twin
screw extruder is used as the polymerization reactor in a
continuous sequential bulk reactive extrusion process to prepare
the poly(.epsilon.-caprolacton- e/.omega.-lauryl lactam) block
copolymers of this invention. The continuous reactive extrusion
process comprises (1) feeding a mixture of .omega.-lauryl lactam,
at least one anionic polymerization initiator, and at least one
co-initiator into the first (i.e., upstream) hopper of a heated,
operating extruder, and (2) thereafter feeding
.epsilon.-caprolactone into a second (i.e., downstream) hopper of
said extruder.
[0018] The invention further relates to utilizing thermal
performance modifiers as well as impact modifiers to improve
thermal properties such as heat resistance and to improve the
impact resistance of the compatibilized blends.
DETAILED DESCRIPTION OF THE INVENTION
[0019] The present invention relates to compatabilized blends of a
chloride containing polymer and at least a carbonyl containing
polymer. Chlorine containing polymers suitable for use in the
present invention are thermoplastics well known to those skilled in
the art. The term "chlorine containing polymers" includes both
polymers derived from chlorine-containing monomers, as well as
polymers that are chlorinated during or after polymerization.
Examples of such chlorine containing polymers include vinyl
chloride homopolymers (PVC), chlorinated PVC (CPVC), polyvinylidene
chloride, chlorinated olefins such as chlorinated polyethylene,
chlorinated polypropylene, and the like. Other examples include
copolymers of vinyl chloride with vinyl acetate; with olefins
containing from 2 to about 6 carbon atoms such as ethylene,
propylene, chlorinated propylene, butalyene, or, isobutylene; with
vinylidene chloride; with acrylonitrile; with a conjugated diene
having from 4 to 8 carbon atoms such as butadiene; with a vinyl
substituted aromatic having from 8 to 12 carbon atoms such as
styrene, and the like. Mixtures of such polymers can also be used.
Vinyl chloride homopolymers and copolymers are preferred. The
amount of such comonomers when utilized is generally from about 5
to about 95 and desirably from about 30 to about 70 percent by
weight based upon the total weight of the copolymer. The above
polymer or copolymers can contain various additives known to the
literature and to the art, such as plasticizers, in conventional
amounts.
[0020] Examples of thermoplastics carbonyl containing polymers
include polyamides (nylons) such as those made from internal amides
having a total of from about 4 to about 20 carbon atoms such as
polyamide 4 (polybutyrolactam), polyamide 6 (polycaprolactam),
polyamide 12 (polylauryl lactam), or polyamides made by the
condensation reaction of a diamine monomer having a total of from
about 4 to about 15 carbon atoms with a dicarboxylic acid having
from about 4 to about 15 carbon atoms such as polyamide 66 (a
condensation product of adipic acid and hexamethylenediamine),
polyamide 610 (a condensation product of sebacic acid and
hexamethylenediamine), polyamide 6-12, polyamide 12-12, and the
like with polyamide 12 (polylauryl lactam) being especially
preferred. Such polymers can contain conventional additives known
to the literature and to the art in conventional amounts.
[0021] The amount of the one or more chlorine containing polymers
is generally from about 10% or 20% to about 99%, and preferably
from about 15%, 35% or 50% to about 90% by weight based upon the
total weight of the one or more chlorine containing polymers and
the one or more carbonyl containing polymers forming the blend.
[0022] The compatibilizing agents relate to block copolymers made
from cyclic esters such as lactones having a total of from about 4
to about 10 carbon atoms with about six carbon atoms, i.e.
.epsilon.-caprolactones being preferred. The lactams generally can
have a total of from about 8 to about 20 carbon atoms with about 11
or 12 carbon atoms being preferred, for example .omega.-lauryl
lactam.
[0023] The compatabilizing agents are generally block copolymers of
a lactone and a lactam preferably prepared by sequential bulk
polymerization using at least one anionic polymerization initiator
and optionally at least one co-initiator. The sequential bulk
polymerization generally is a sequential anionic living
polymerization in which the lactam such as .omega.-lauryl lactam
monomer is polymerized using the initiator and co-initiator,
followed by chemical attachment of the lactone such as
.epsilon.-caprolactone to the propagation chain end of the living
poly(lauryl lactam) anion. The block copolymers typically are
di-block (AB) copolymers having repeating units such as
follows:
--(O(CH.sub.2).sub.5CO).sub.x--(NH(CH.sub.2).sub.11CO).sub.Y--
[0024] wherein "x" and "y" represent the number of units in the
respective "A" (polymerized .epsilon.-caprolactone) and "B"
(polymerized .omega.-lauryl lactam) blocks. However, other block
copolymers also can be produced, such as the ABA tri-block
copolymers described below. The amount of .epsilon.-caprolactone
polymerized in the block copolymers of the invention can range from
about 1 wt. % to about 80 wt. %. However, for the compatibilizing
purposes described herein, the amount of .epsilon.-caprolactone in
said block copolymers can range from about 10 wt. % to about 70 wt.
%, preferably from about 20 wt. % to about 65 wt. %, and more
preferably from about 25 wt. % or 30 wt. % to about 55 wt. % or 65
wt. %, based upon total weight of the block copolymer. Naturally,
the difference is the amount of the one or more lactam blocks.
[0025] Suitable initiators for use in this invention are well known
to those skilled in the art and include Group IA (periodic table
IUPAC notation, i.e., so-called "alkaline") metals, hydrides, and
salts, and preferably Group IA metals and hydrides. Lithium,
sodium, and potassium metals and hydrides are more preferred, such
as Li, Na, K, lithium hydride, sodium hydride, and the like. Other
suitable initiators include Group IIA (periodic table IUPAC
notation, i.e., so-called "alkaline earth") hydrides and salts, and
preferably Group IIA hydrides, such as calcium hydride, and the
like. Mixtures of initiators can also be used. Typical initiator
concentrations can vary from about 1 mmol/mol to about 30 mmol/mol,
and preferably from about 4 mmol/mol to about 15 mmol/mol, based on
total moles of .epsilon.-caprolactone and .omega.-lauryl lactam
monomers.
[0026] Typically at least one co-initiator is used in an amount of
molar concentration in order to keep reaction time of
polymerization below about 20 minutes, especially when an extruder
is used as the reaction vessel. However, longer reaction times can
be suitable in other reaction vessels such as stirred tank
reactors, in which case a co-initiator need not be used. The amount
of the at least co-initiator is generally from 1 to about 30 and
preferably from about 5 to about 20 mmol/mol of total lactam and
lactone monomers.
[0027] Co-initiators suitable for use in the sequential
polymerization include acylated lactam derivatives having the
formula: 1
[0028] as well as Group IA (periodic table IUPAC notation) salts of
said derivatives, and mixtures thereof, wherein R and R'
independently are hydrogen or an alkyl group having from 4 to 10
carbon atoms, preferably 4 to 7 carbon atoms, wherein R and R' can
join together form an alkylene group in a cyclic structure, and X
designates a polar substituent such as an acyl, carbonyl, or cyano
group, or the like. Examples of such acylated lactam derivatives
are set forth in U.S. Pat. No. 3,200,095, hereby fully incorporated
by reference, and include N-acetyl-6-carprolactam, and the like,
and mixtures thereof.
[0029] Other suitable co-initiators include an isocyanate, such as
those having the formula
R--(NCO).sub.n
[0030] wherein R is a hydrocarbon, halohydrocarbon or other
generally inert organic group containing carbon atoms, preferably a
hydrocarbon group containing from 1 to 10 carbon atoms. The term
"generally inert" refers to organic radicals that do not tend to
interfere with the sequential bulk polymerization of this
invention. Isocyanates typically are mixtures rather than pure
monoisocyanates, diisocyanates, or the like; thus "n" in the above
formula can be from about 1 to about 3, and preferably is about 2.
Use of a monoisocyanate as a co-initiator ideally produces an AB
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) di-block
copolymer. Use of a diisocyanate as a co-initiator ideally produces
an ABA tri-block copolymer, which is a caprolactone-lauryl
lactam-caprolactone block copolymer.
[0031] Examples of suitable diisocyanates include tolylene 2,4-
and/or 2,6-diisocyanate, 4,4'-diisocyanato-diphenylmethane,
diphenyl-4,4'- diisocyanate, m-phenylene diisocyanate, p-phenylene
diisocyanate, xylylene diisocyanate, 4-chloro-1,3-phenylene
diisocyanate, benzophenone-naphthalene diisocyanate,
1,5-tetrahydronaphthalene diisocyanate, 1,4-cyclohexylene
diisocyanate, 1,4-tetramethylene diisocyanate, 1,6-hexamethylene
diisocyanate, 1,10-decamethylene diisocyanate, and
4,4'-methylene-bis(cyclohexyl isocyanate). 1,6-hexamethylene
diisocyanate is preferred. Isocyanate mixtures can also be
used.
[0032] Sequential bulk polymerization in a single reaction vessel
can be performed by a process comprising (1) feeding a lactam such
as mixture of .omega.-lauryl lactam, at least one anionic
polymerization initiator, and optionally at least one co-initiator
into a single reaction vessel and allowing polymerization to occur,
and (2) thereafter feeding a lactone such as .epsilon.-caprolactone
into the same reaction vessel and allowing the block copolymer to
form. Alternatively, the first step can be performed in one
reaction vessel and the contents transferred to a second reaction
vessel before addition of the lactone and formation of the block
copolymer. It is preferred that the total amount of initiator and
optional co-initiator be added during step (1) of the
polymerization, and that no initiator and/or co-initiator be added
during step (2) (e.g., not pre-mixed with .epsilon.-caprolactone)
so as to avoid undesirable formation of .epsilon.-caprolactone
oligomers and homopolymers.
[0033] In a preferred embodiment, a single or preferably a twin
screw extruder is used as the polymerization reactor in a
continuous sequential bulk reactive extrusion process to prepare
the preferred poly(.epsilon.-caprolactone/.omega.-lauryl lactam)
block copolymers of this invention. The reactive extrusion process
comprises (1) feeding a mixture of .omega.-lauryl lactam, at least
one anionic polymerization initiator, and at least one co-initiator
into the first (i.e., upstream) hopper of a heated, operating
extruder, and (2) thereafter feeding .epsilon.-caprolactone into a
second (i.e., downstream) hopper of said extruder. The preferred
reactive extrusion process of the present invention is
substantially solvent free, rapid (typical mean and maximum
residence times being no more than about 20 minutes and about 30
minutes respectively), and produces a high conversion of monomers
to block copolymer. By the term "substantially solvent free" it is
meant that the amount of solvent is generally less than 50% or 25%,
desirably less than 15%, and preferably less than 5%, 3%, 2%, or 1%
by weight based upon the total weight of the monomers added to form
the block copolymer. Said process produces a block copolymer
wherein each block (A or B) typically has a number average
molecular weight (M.sub.n) from about 5,000 or 10,000 to about
180,000, and more desirably from about 20,000 to 30,000 to about
100,000 or 150,000 (as measured by the method described
hereinafter).
[0034] Suitable extruders for the process of this invention must
accomplish the following functions: (1) mixing the substances
introduced (in this case comprising the mixtures of monomers,
initiator(s) and co-initiator(s)), (2) conveying the substances as
they form a block copolymer from their respective feed zones to a
discharge zone such as a die, and (3) maintaining appropriate
reaction temperatures. Suitable extruders advantageously will be
provided with a degassing vent located near the die. Any known and
conventional extruders based on the work of one, two, or a number
of screws, whether rotating in the same (co-rotating) or opposite
(counter-rotating) directions, are suitable for reactive extrusion
to prepare the block copolymers of the invention. The screws can be
intermeshing or non-intermeshing (i.e., tangential). Excellent
results have been obtained using extruders having two co-rotating,
intermeshing screws. Modular twin screw extruders are preferred,
i.e., extruders in which screw segments can be assembled (i.e.,
configured) in customized order in order maximize conversion of
monomers to block copolymers. The design of modular screw
configurations is well understood by those skilled in the art.
Examples of suitable extruders include the Japan Steel Works model
TEX-30, which is a 30-mm diameter co-rotating, intermeshing twin
screw extruder. Other examples of suitable extruders include the
Werner and Pfleiderer model ZSK-30, and the Berstorff model ZE-60.
Extruders containing larger screws can also be utilized.
[0035] Feed rates to the extruder of monomers, initiators and
co-initiators are determined according to the size of the extruder,
as well as the desired mean and maximum residence time of reactants
in the extruder, according to principles well understood by those
skilled in the art. Higher feed rates will result in shorter mean
and maximum residence times. Extruder screw speeds can be chosen
with consideration of shear level, residence time, and heat
generation. For example, a feed rate of about 2 to about 10 kg/hr
and a screw speed of about 50 to about 300 rpm are preferred for
higher conversion of monomers to block copolymers in a 30-mm
diameter screw extruder, such as the Japan Steel Works model TEX-30
and the Werner and Pfleiderer model ZSK-30. Extruder barrel
temperature will also affect polymerization rates and can be from
about 175.degree. C. to about 300.degree. C. for the lactam monomer
and from about 180.degree. C. to about 250.degree. C. for the
lactone monomer.
[0036] The block copolymer can be prepared by feeding the preheated
.epsilon.-carprolactone into the second hopper. It can be preheated
from about 25.degree. C. to about 200.degree. C. in a stirred
vessel under a nitrogen atmosphere. A lactam reaction mixture
containing the lactam, initiator, and co-initiator is fed into the
first (i.e., upstream) hopper of a screw extruder, and subsequently
the preheated lactone is fed into a second (i.e., downstream)
hopper. It is preferred that the two hoppers be separated by a
distance allowing at least about one minute of residence time in
the extruder of the first-step materials in order to allow
formation of the .omega.-lauryl lactam "B" block portion before
addition of .epsilon.-carprolactone to form the "A" block of the
block copolymer. The extruder is purged with an inert gas such as
nitrogen, argon, etc., during the reactive extrusion process.
[0037] The reactive extrusion process produces a yield of at least
about 50%, desirably about 60% or 70% and preferably at least about
80%, 90%, or 95% by weight of the block copolymer. Usually, no
purification step typically is needed to remove oligomers,
homopolymers, and unreacted monomers. The gel permeation
chromatography (GPC) test method described hereinafter is used to
verify both the molecular weight (MW) and the substantial purity of
the block copolymers. After extraction using toluene to ensure
removal of polylactone homopolymer, differential scanning
calorimetry (DSC) using the test method described hereinafter shows
two distinct melting points, indicating production of a block
copolymer.
[0038] Downstream processing of the block copolymers of the
invention can be delayed or can be conducted immediately after the
reactive extrusion process. For example, the block copolymers can
be cooled, converted into particles, and stored for further
processing. Alternatively, the block copolymers can be processed
immediately, e.g., by compounding the block copolymers while they
are still warm with chlorine containing polymers and optionally
other ingredients to form polymer blends having improved mechanical
and thermal properties. Processing steps such as pelletizing, film
casting, fiber melt spinning, blow molding and injection molding
can be integrated into post-reactive extrusion processing.
Immediate processing following completion of the reactive extrusion
process has the advantage of reducing the thermal history of the
final product by eliminating at least one cooling and re-melting
step.
[0039] The polymers formed from lactams and lactones such as
poly(.epsilon.-caprolactone) homopolymer and poly(.omega.-lauryl
lactam) homopolymer are generally incompatible with one another in
their semi-crystalline states. Furthermore, polyamides generally
are incompatible with PVC, while poly(.omega.-caprolactone) is
miscible with PVC and certain other thermoplastics but does not
improve their mechanical and thermal properties. However, the
poly(lactone/lactam) block copolymers of the present invention have
been found to be good compatibilizing agents for blends of the
about noted chlorine containing polymers, and certain other
thermoplastics such as polyamides, and also improve the mechanical
and thermal properties of the blends.
[0040] Additives such as activators, curing agents, stabilizers
(such as the Mark series from Witco and the Thermolite series from
Elf Atochem), colorants, pigments, plasticizers, waxes, slip and
release agents, antimicrobial agents, antioxidants, UV stabilizers,
antiozonants, fillers, and the like, can be added optionally during
the manufacture of the block copolymers of this invention or during
subsequent processing into finished products.
[0041] The block copolymers of the present invention can be blended
with chlorine containing polymers, other compatible thermoplastics,
additives, and other ingredients by techniques well known to those
skilled in the art, such as by mixing of ingredients in an
electrical heater mixer, Brabender, or screw extruders. The blended
ingredients can be mixed further on heated two-roll mills to form a
viscous sheet, followed by cooling the sheet in a hot water tank,
granulizing or pelletizing the sheet, and packaging the granules or
pellets in bags, drums, or boxes for storage and shipment. The
pellets or granules subsequently can be processed to form shaped
articles, adhesives, and other products.
[0042] The amount of the one or more block copolymers of the
present invention which are compatibilizing agents for blends of
chlorine containing polymers and carbonyl containing polymers is
from about 1 to about 20 or 30 parts by weight, and desirably from
about 3, 5, or 8 parts to about 12, or 15 parts by weight for every
100 parts by weight of the total weight of the polymers being
blended. Such compatibilized polymer blends can be utilized in a
wide variety of applications, such as adhesives, wire insulation,
tubing, and gaskets. In particular, the block copolymers are useful
in compatibilizing (i.e., facilitating or enhancing) the blending
of otherwise immiscible or poorly miscible materials (for example,
polyamides blended with chlorine containing polymers) in order to
produce polymer blends having improved mechanical and thermal
properties for such applications. Of course, more than two
different types of polymers can be blended so that multiple polymer
blends, i.e. containing from 2 to about 5 or 6 polymers, are also
within the scope of the present invention.
[0043] In order to retain and/or improve thermal properties, such
as high heat stability, ultimate tensile strength, elongation at
break, and the like, thermal performance modifiers are used. The
thermal performance modifiers are often unsaturated anhydride
modified polyolefins or polymers made from vinyl substituted
aromatic monomers. Suitable polyolefins are generally made from
olefin monomers having from 2 to 6 carbon atoms, desirably 2 or 3
carbon atoms with 3 carbon atoms, i.e. propylene being preferred.
Suitable vinyl substituted aromatic monomers generally contain from
8 to 12 carbon atoms with 8 or 9 carbon atoms such as styrene or
a-methylstyrene being desired. The unsaturated anhydride monomers
contain from 4 to 15 carbon atoms, desirably 4 or 5 carbon atoms
with maleic anhydride being preferred. The amount of the
unsaturated anhydride which is reacted with the olefin or the vinyl
substituted aromatic monomers is such that the amount of anhydride
is generally from about 0.1, 0.2, 0.3 or 0.5 to about 3, 5, 7, or
10% by weight based upon the total weight of the anhydride modified
polymer
[0044] The thermal performance modifier preferably also contains a
significant amount of a polyolefin homopolymer derived from olefin
monomers having from 2 to 6 carbon atoms and thus can be
polypropylene or polyethylene, or a homopolymer made from vinyl
substituted aromatic monomers having from 8 to 12 carbon atoms and
thus can be polystyrene. The amount of such so-called base polymers
of the thermal performance modifier can vary greatly but often is
from about 10 or 20 to about 60 or 80% by weight based upon the
total weight of thermal performance modifier.
[0045] When utilized, the amount of the thermal performance
modifier is generally from about 5 or 10 to about 40 or 50 parts by
weight and preferably from about 15 to about 30 parts by weight for
every 100 parts by weight of the blended one or more chlorine
containing polymers, one or more carbonyl containing polymers, and
the block copolymer.
[0046] It is desirable to use various impact modifiers to improve
at least the impact resistance of the blend of various chloride
containing polymers and carbonyl containing polymers. Suitable
impact polymers are often various unsaturated anhydride modified
flexible polymers. The unsaturated anhydrides generally have from
about 4 to about 15 carbon atoms, desirably 4 or 5 carbon atoms
with 4 carbon atoms, for example maleic anhydride being preferred.
Flexible polymers include rubber polymers, EPM polymers, that is
polymers made from ethylene and propylene monomers; and EPDM
polymers, that is polymers made from ethylene, propylene, and a
conjugated diene monomer. Similar flexible rubbers include
ethylene, and other alpha olefins such as butylene and styrene.
When the amount of conjugated diene therein is generally from about
0.1 to about 5% and desirably from about 0.2 to about 4% by weight
based upon the total weight of the EPDM.
[0047] The unsaturated anhydride is added as a monomer during the
polymerization of the various flexible polymers and due to the
existence of an unsaturated group therein, reacts with the various
flexible polymer forming monomers and generally is located in the
backbone of the polymer with the anhydride portion being dependent
therefrom. The amount of unsaturated anhydride is generally low,
for example, from about 0.1, or 0.2, or 0.3, or 0.5 to about 3, 5,
7, or 10% by weight based upon the total weight of the impact
modifier.
[0048] The weight of the impact modifier is generally from about 1
to about 50 parts by weight, desirably from about 3 to about 40 and
preferably from about 5 to about 30 parts by weight for every 100
parts by weight of the blended one or more per se chlorinated
polymers, the one or more per se carbonyl containing polymers such
as a polyamide, and the block copolymer.
[0049] The mechanism by which the thermal performance and the
impact modifiers containing maleic and anhydride work is not fully
understood but it is believed that the maleic anhydride portion of
the modifier chemically reacts with the amine end group of the
polyamide and thus forms a polyamide-g-polymeric modifier which is
generally compatible with the polylactam portion of the
compatiblizing agent.
[0050] The following examples are presented for the purpose of
illustrating the invention disclosed herein in greater detail.
However, the examples are not to be construed as limiting the
invention here in any manner, the scope of the invention being
defined by the appended claims.
EXAMPLES
List of Chemicals Used
[0051] .epsilon.-Caprolactone as "ECEQ Tone Monomer" from Union
Carbide.
[0052] .omega.-Lauryl lactam from Ube Industries.
[0053] N-Acetyl-6-caprolactam from Aldrich Chemical Company.
[0054] Polyamide 12--poly(.omega.-lauryl lactam) having a
MW.sub.avg of about 50,000 from Ube Industries.
[0055] PVC--polyvinyl chloride having a MW.sub.avg of about 90,000
as "Geon 27" from Geon Company.
[0056] Maleic anhydride modified ethylene/propylene/non-conjugated
diene elastomer (M-EPDM) "Royaltuf 485" from Uniroyal Chemical-EPDM
E/P ratio :75/25
[0057] Maleic anhydride modified polypropylene (M-PP) "Epolene
G-3003" from Eastman Chemical
[0058] Polypropylene (PP) from Exxon Chemical "ESCORENE 1052"
[0059] Sodium hydride from Aldrich Company.
[0060] Tin stabilizer--"Thermolite 31-Super" from Elf Atochem.
List of Test Methods
[0061] 1. Differential Scanning Calorimetry (DSC) was performed
under a nitrogen blanket at a heating rate of 20.degree. C./minute
using a General V4.1C 2100 instrument from Dupont.
[0062] 2. Dynamic Mechanical Thermal Analysis (DMTA). ASTM No. D
5023-94 was applied in the three-point bending mode at a heating
rate of 4.degree. C./min and a frequency of 1 Hz. Testing was
performed using a Rheometric Scientific Dynamic Mechanical Analyzer
from Polymer Laboratories. The temperatures reported in these
examples (Table II) are the temperatures at which E' (bending
storage modulus) falls to 100 Mpa. Higher values of E' in Table II
demonstrate better mechanical performance, i.e., better mechanical
properties at elevated temperatures.
[0063] 3. Gel Permeation Chromatography for Molecular Weight
Measurement was performed at 100.degree. C. using a Waters 510
pump, three columns, and a Waters 410 refractive index detector
(all assembled by Millipore Company). The solvent used was
m-cresol, and the reference standard was polystyrene.
[0064] 4. Tensile Testing for % Elongation at Break and Tensile
Strength (Mpa)--ASTM D638 for plastics was used for specimen type V
(prepared by compression molding samples at 195.degree. C.).
Testing was performed using an Instron 4204 at room temperature and
a speed of 50 mm/min.
[0065] 5. Dynatup Dart Impact Testing--ASTM No. STP 936 was applied
at a head speed rate of 4.20 m/sec using Dynatup 8250 from General
Research Corp. Specimens were prepared by compression molding at
195.degree. C.
Examples 1 and 2
Preparation of Poly(caprolactone/lauryl lactam) Di-block
Copolymers
[0066] All reactive extrusions were performed under a nitrogen
atmosphere in a Japan Steel Works model TEX-30 modular intermeshing
co-rotating twin screw extruder. The screw diameter was 30 mm,
barrel length was 975 mm, and separation of the two screw axes was
26 mm. This twin screw extruder had 8 barrel sections with electric
heaters and water cooling systems.
[0067] In Examples 1 and 2, the screw configuration had three
different sets of kneading disk blocks. The first and second
kneading zones were located immediately before the second hopper,
while the third zone was located between the second hopper and
devolatilization vent near the die.
[0068] 16 mmol of sodium hydride and 16 mmol of
N-acetyl-6-caprolactam for every one mole of .omega.-lauryl lactam
(LA) were mixed. This mixture was fed into the first hopper of the
extruder at a constant rate of 1.5 kg/hr at ambient temperature.
.epsilon.-caprolactone ("CL") heated to 100.degree. C. was fed into
the second hopper at a rate of 1.5 kg/hr and 3 kg/hr for Examples 1
and 2 respectively. The temperature of barrel sections of the
extruder was maintained at 210.degree. C., and screw rotation speed
was 250 rpm. The extrudates were cooled by quenching in a water
bath and then granulated using a pelletizer.
[0069] Monomer conversions reported in Table I were measured as
follows. 20 grams of granulated product was dissolved in 200 ml
m-cresol solvent and subsequently poured into an excess amount of
cold, rapidly stirred methanol. The precipitated product was
filtered and then dried in a vacuum oven for 48 hours at
110.degree. C. The weight of the precipitated, dried polymer was
reported as "Monomer Conversion to Polymers (%)" relative to
starting monomers and included both block copolymers and
homopolymers, but excluded oligomers and residual monomers.
[0070] Yields of block copolymers reported in Table I were measured
as follows. Polycaprolactone homopolymer was extracted from 20
grams of the precipitated, dried polymer (described above) by
Soxhlet extraction for 24 hours using toluene. The residual polymer
was dried in a vacuum oven for 24 hours at 50.degree. C. and then
weighed as the final poly(.epsilon.-caprolactone/.omega.-lauryl
lactam) di-block copolymer. The yield of the residual, dried final
polymer was reported as "Yield of Di-block Copolymer (%)" relative
to starting monomers.
[0071] The weight percent of each component in block copolymers was
calculated after subtracting the weight ratio of extracted (by
Soxhlet extraction) polycaprolactone homopolymer from the weight
ratio of monomer feed rates.
[0072] GPC testing of the residual, dried final (i.e., following
Soxhlet extraction) poly(.epsilon.-caprolactone/.omega.-lauryl
lactam) di-block copolymers for Examples 1 and 2 confirmed that
there were no residual polylauryl lactam homopolymers or
polycaprolactone homopolymers. Furthermore, a single, narrow GPC
curve for each final poly(.epsilon.-caprolactone/.omega.-lauryl
lactam) di-block copolymer demonstrated that each was pure block
copolymer. Moreover, the GPC peak of polylauryl lactam (sampled
from the extruder's second hopper just before feeding caprolactone
monomer into that hopper) was not observed in the final products of
the poly(.epsilon.-caprolactone).omega.-lauryl lactam) di-block
copolymer.
[0073] Differential scanning calorimetry (DSC) testing of the final
di-block copolymers for Examples 1 and 2 showed that each di-block
copolymer had two different melting peaks at 55.degree. C. and
175.degree. C., which are the melting points of polycaprolactone
and polylauryl lactam respectively. After extraction of
homopolymers from the products, the existence of two separate
melting peaks clearly prove di-block copolymer.
[0074] Feed rates of .omega.-lauryl lactam and
.epsilon.-caprolactone (kg/hr), number average molecular weights
(M.sub.n), relative amounts of polymerized .omega.-lauryl lactam
and .epsilon.-caprolactone in the final polymers, weight percentage
monomer conversions to total polymers, and yields of
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) di-block
copolymers (as a weight percentage of total starting monomer
amounts) are shown in Table I. Examples 1 and 2 were
poly(.epsilon.-caprolactone/.omeg- a.-lauryl lactam) di-block
copolymers of the present invention.
1TABLE I Weight % Monomer Yield Feed Rates M.sub.n of in Di-block
Conversion of Di-block Example (kg/hr) Di-block Copolymer to
Polymers Copolymer # (1.sup.st LA/2.sup.nd CL) Copolymer (LA/CL)
(Wt. %) (Wt. %) 1 1.5 1.5 89,000 65/35 94 87 2 1.5 3 105,000 58/42
87 82
Examples 3 to 12
Testing of Poly(.epsilon.-caprolactone).omega.-lauryl lactam)
Di-block Copolymers as a Compatibilizing Agent for Mechanical and
Thermal Properties for Blending of PVC and Polyamide 12
[0075] The PVC and polyamide 12 compositions used in the
experiments below are described in the "List of Chemicals" above.
The poly(.epsilon.-carprolactone/.omega.-lauryl lactam) di-block
copolymer used as a compatibilizing agent in the ternary blends was
the copolymer prepared in Example 1. Prior to the experiments
below, the PVC was compounded with 3 phr of tin stabilizer (i.e., 3
parts by weight of tin stabilizer per 100 parts by weight of PVC)
by tumbling for 4 hours in a rotation tumbling apparatus in order
to form a PVC compound.
[0076] Binary 2-Polymer blends of PVC compound and polyamide 12
(poly(.omega.-lauryl lactam)) were prepared in ratios of 80/20,
60/40, 40/60, and 20/80 wt. % (based on the total weight of the
blend) without inclusion of
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block copolymer.
Comparison ternary polymer blends were prepared using a PVC
compound (i.e., PVC compounded with tin stabilizer as described
heretofore) and polyamide 12 in approximately the same weight
ratios to each other, but also including
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) di-block
copolymer in an amount of 10 wt. % of the total weight of each
ternary blend. Two control blends (Examples 3 and 12) also were
prepared containing 100 wt. % PVC compound and 100 wt. % polyamide
12 respectively.
[0077] Each blend or control was prepared by mixing ingredients in
a Brabender Plastograph internal mixer for about seven minutes at
195.degree. C. using a 100 rpm rotor speed. 70 grams total of each
blend was obtained and processed by compression molding at
195.degree. C. in order to prepare test samples for testing of
mechanical and thermal properties. Test results for mechanical
(elongation at break and ultimate tensile strength) and thermal
properties (using the Dynamic Mechanical Thermal Analyzer (DMTA))
are shown in Table II. Values in Table II were averaged after
testing was carried out 5 times for each example.
2TABLE II Temperature at Ultimate which E' falls PVC Block
Elongation Tensile to 100 Mpa in Compound Polyamide Co-Polymer at
Break Strength DMTA Example # (Wt. %) 12 (Wt. %) (Wt. %) (%) (Mpa)
Test (.degree. C.) 3 (Control) 100 0 0 150 43 80 4 (Control) 80 20
0 50 17 80 5 72 18 10 200 45 130 6 (Control) 60 40 0 119 29 125 7
54 36 10 243 44 160 8 (Control) 40 60 0 299 40 Not tested 9 36 54
10 320 43 Not tested 10 (Control) 20 80 0 412 53 Not tested 11 18
72 10 440 54 Not tested 12 (Control) 0 100 0 570 60 170
[0078] The data in Table II demonstrates substantial improvement in
mechanical and thermal properties of PVC compound when it is
blended with both Polyamide 12 and the
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block copolymers
of this invention. Surprisingly, side-by-side comparison of
Examples 5, 7, 9, and 11 with Control Examples 4, 6, 8, and 10
respectively shows that the block copolymers of the present
invention act as compatibilizers enhancing mechanical properties
(elongation at break and ultimate tensile strength) of the ternary
polymer blends over the mechanical properties of binary polymer
PVC/polyamide 12 blends made without the block copolymer,
especially at high levels of PVC. Also surprisingly, side-by-side
comparison of Examples 5 and 7 with Examples 4 and 6 respectively
shows that the block copolymers of the present invention act as
compatibilizers enhancing the thermal properties (DMTA) of the
ternary blends over the thermal properties of the binary
PVC/polyamide 12 blends made without the block copolymer.
Examples 13 to 17
Testing of Poly(.epsilon.-caprolactone/.omega.-lauryl lactam)
Di-block Copolymer as a Compatibilizing Agent for Blending of PVC
and Polyamide 12 Using M-EPDM as an Impact Modifier
[0079] The PVC, M-EPDM and polyamide 12 compositions used in the
experiments below are described in the "List of Chemicals" above.
The poly(.epsilon.-carprolactone/.omega.-lauryl lactam) di-block
copolymer used as a compatibilizing agent in 4-polymer component
blends was the copolymer prepared in Example 1.
[0080] 3-Polymer blends of PVC compound, M-EPDM, and polyamide 12
were prepared in ratios of 80/10/10 and 60/20/20 wt. % (based on
the total weight of the blend) without inclusion of
poly(.epsilon.-caprolactone/.om- ega.-lauryl lactam) block
copolymer. Comparison 4-polymer blends were prepared using PVC
compound, M-EPDM, and polyamide 12 in approximately the same weight
ratios to each other, but also including
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) di-block
copolymer in an amount of 10 wt. % of the total weight of each
4-polymer blend. Control blend (Example 13) was prepared containing
100 wt. % PVC.
[0081] Each blend or control was prepared by mixing ingredients in
a Brabender Plastograph internal mixer for about seven minutes at
210.degree. C. using a 100 rpm rotor speed. 70 grams total of each
blend was obtained and processed by compression molding at
195.degree. C. in order to prepare test samples for testing of
mechanical properties. Test results for mechanical (elongation at
break and ultimate tensile strength) and dart impact energy (using
Dynatup 8250) are shown in Table III. Values in Table III were
averaged after testing was carried out 5 times for each
example.
3TABLE III Block Ultimate Dart PVC Polyamide Co- Elonga- Tensile
Impact Com-pound M-EPDM 12 polymer tion at Strength Energy Example
# (Wt. %) (Wt. %) (Wt. %) (Wt. %) Break (%) (Mpa) (Joule) 13
(Control) 100 0 0 0 155 42 1.5 14 (Control) 80 10 10 0 40 30 0.65
15 72 9 9 10 225 40 7.8 16 (Control) 60 20 20 0 35 27 1.4 17 54 18
18 10 280 35 30.7
[0082] The data in Table III demonstrates substantial toughness
improvement in mechanical properties of PVC compound when it is
blended with M-EPDM, polyamide 12 and the
poly(.epsilon.-caprolactone/.omega.-lau- ryl lactam) block
copolymer of this invention. Surprisingly, side-by-side comparison
of Control Examples 14 and 16 with Examples 15 and 17 respectively
shows that the block copolymers of the present invention act as a
compatiblizer enhancing properties (elongation at break and
ultimate tensile strength and especially impact energy properties)
of polymer blends over properties of 3-polymer
(PVC/M-EPDM/polyamide12) blends made without the compatibilizing
block copolymer.
Examples 18 to 21
Testing of Poly(.epsilon.-caprolactone/.omega.-lauryl lactam)
Di-block Copolymer as a Compatibilizing Agent for Mechanical
Properties for Blending of PVC and Polyamide 12 Using a Maleic
Anhydride Modified Polypropylene (M-PP) as a Thermal Performance
Modifier
[0083] The PVC, PP, M-PP and polyamide 12 compositions used in the
experiments below are described in the "List of Chemicals" above.
The poly(.epsilon.-caprolactone/.omega.-lauryl lactam) di-block
copolymer used as a compatibilizing agent in 5-polymer component
blends was the copolymer prepared in Example 1.
[0084] First, a reactive 3-Polymer blend of PP, M-PP, and polyamide
12 (poly(.omega.-lauryl lactam)) was prepared in ratio of 50/17/33
wt. % (based on the total weight of the blend) as one of control
blends. This control blend is named "PP-based compound" hereafter.
This PP-based compound, which is composed of PP(50)/M-PP
(17)/polyamide 12(33%), was prepared by mixing ingredients in a
Brabender Plastograph internal mixer for about seven minutes at
230.degree. C. using a 100 rpm rotor speed.
[0085] A 4-Polymer blend of PVC compound and PP-based compound
(PP/M-PP-polyamide 12) was prepared in ratios of 70/30 wt. % (based
on the total weight of the blend) without inclusion of
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block copolymer.
Comparison 5-polymer blends were prepared using PVC compound,
PP-based compound (PP/M-PP/polyamide 12) in approximately the same
weight ratios to each other, but also including
poly(.epsilon.-caprolactone/.omega.-lau- ryl lactam) di-block
copolymer in an amount of 10 wt. % of the total weight of the
5-polymer blend. Therefore, three control blends (Examples 18, 19
and 21) contain PVC compound(100), PVC(70)/PP-based compound(30),
and PP-based compound(100), respectively.
[0086] Each blend or control was prepared by mixing ingredients in
a Brabender Plastograph internal mixer for about seven minutes at
200.degree. C. using a 100 rpm rotor speed. 70 grams total of each
blend was obtained and processed by compression molding at
195.degree. C. in order to prepare test samples for testing of
mechanical properties. Test results for mechanical (elongation at
break and ultimate tensile strength) are shown in Table IV. Values
in Table IV were averaged after testing was carried out 5 times for
each example.
4TABLE IV Temp at PP-Based Ultimate Which E' PVC Compound Block
Elongation Tensile falls to 20 Compound * Copolymer at Break
Strength Mpa in Example # (Wt. %) (Wt. %) (Wt. %) (%) (Mpa) DMTA
(.degree. C.) 18 (Control) 100 0 0 152 42 85 19 (Control) 70 30 0
19 8 112 20 63 27 10 180 40 125 21 (Control) 0 100 0 300 22 150 *
PP-based compound: PP (50)/M-PP (17)/Polyamide 12 (33%))
[0087] The data in Table IV demonstrates substantial improvement in
mechanical properties of PVC compound when it is blended with a
thermal performance modifier of a PP-based compound and the
poly(.epsilon.-caprolactone/.omega.-lauryl lactam) block copolymer
of this invention. Surprisingly, the comparison of Control Example
19 with Example 20 shows that the block copolymers of the present
invention act as a compatibilizer enhancing mechanical properties
(elongation at break and ultimate tensile strength) of 5-polymer
blend over the mechanical properties of 4-polymer
(PVC/PP/M-PP/Polyamide12) blend made without the block copolymer.
When PVC (63) is blended with PP-based Compound (27) with the block
copolymer (10 wt. %), the temperature at which storage modulus (E')
falls to 20 Mpa is 40 and 13.degree. C. higher, respectively than
those of PVC (Example 1) and PVC/PP-based compound without the
block copolymer (Example 2) as summarized in Table IV.
[0088] Naturally the block copolymers of the present invention, as
well as the compatibilized blends, can be used in numerous
applications where their properties are desired.
[0089] While in accordance with the patent statutes the best mode
and preferred embodiment has been set forth, the scope of the
invention is not limited thereto, but rather by the scope of the
attached claims.
* * * * *