2
Terpolymers of Tetrafluoroethylene, Perfluoro (Methyl Vinyl Ether), and Certain Cure Site Monomers
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G. H . K A L B , A. A. K H A N , R. W. Q U A R L E S , and A. L . B A R N E Y Research Laboratory, Elastomer Chemicals Department, E . I. du Pont de Nemours and Co., Inc., Wilmington, Del. 19898
Copolymers
of tetrafluoroethylene,
perfluoro(methyl
ether), and a third monomer—selected perfluoro(4-cyanobutyl oxbutyl
vinyl
vinyl ether),
ether),
perfluoro(4-carbometh-
perfluoro(2-phenoxypropyl
ether), or perfluoro(3-phenoxypropyl
vinyl
vinyl ether)—give vul-
canizable, high performance elastomers. cyano and the carbomethoxy
vinyl
from the group of
Syntheses of the
compounds from
perfluoro-
glutaryl chloride and the phenoxy compounds from pentafluorophenol are presented. three copolymer
Vulcanization methods for the
types include
catalytic
condensation of
the nitrile, interchange of dibasic amines or esters with the methyl ester, and nucleophilic displacement
of a fluorine
atom on the phenoxy ring with a diamine or an aromatic bisnucleophile.
A brief description of vulcanizate
ties demonstrates the outstanding
solvent and
properchemical
resistance that may be obtained with these new elastomers.
A
n e w h i g h - p e r f o r m a n c e elastomer, p r e p a r e d f r o m tetrafluoroethylene ( T F E ) a n d p e r f l u o r o ( m e t h y l v i n y l ether) ( P M V E ) , a n d c h a r a c t e r i z e d
b y o u t s t a n d i n g resistance to c h e m i c a l attack a n d excellent t h e r m a l sta b i l i t y , w a s r e p o r t e d r e c e n t l y b y B a r n e y et al. ( 1 ) o f o u r l a b o r a t o r y . That paper described
a rubbery perfluorinated dipolymer that c o u l d
not b e c r o s s l i n k e d u s i n g o r d i n a r y techniques because of its c h e m i c a l inertness, a n d also a t e r p o l y m e r i n w h i c h a n u n s p e c i f i e d t h i r d
monomer
was u s e d to i n t r o d u c e a c t i v e c r o s s l i n k i n g sites. T h e d i p o l y m e r , w h i c h loses o n l y 5 to 1% o f its w e i g h t i n a n a i r c i r c u l a t i n g o v e n at 316° C i n seven days ( a n d o n l y a f e w p e r cent m o r e a m o n t h at these conditions) is, h o w e v e r , a t h e r m o p l a s t i c .
I t is a p p a r e n t ,
13 In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
14
POLYMERIZATION REACTIONS A N D N E W POYLMERS
therefore, that a c r o s s l i n k e d structure is necessary to g a i n t h e m e c h a n i c a l strength at elevated temperatures r e q u i r e d f o r a true h i g h - p e r f o r m a n c e elastomer.
T h i s p a p e r describes w o r k a i m e d at: d e v e l o p m e n t of a
s u i t a b l e crosslink s t r u c t u r e a n d various c a n d i d a t e t h i r d m o n o m e r s that copolymerize
with T F E and P M V E
to i n t r o d u c e t h e necessary
cross-
l i n k i n g sites; t h e i r p r e p a r a t i o n a n d c o p o l y m e r i z a t i o n ; c r o s s l i n k i n g reac tions i n v o l v e d w i t h some of t h e m o n o m e r s ;
and a f e w of the physical
properties of the c r o s s l i n k e d ( " v u l c a n i z e d " ) The
dipolymer
has m a n y
compositions.
d e s i r a b l e properties,
a n d , to m a i n t a i n
these properties, the r e q u i r e m e n t s f o r the t h i r d m o n o m e r a n d the cross-
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l i n k i n g r e a c t i o n are q u i t e stringent.
T h e s e r e q u i r e m e n t s are:
( a ) T h e c u r e site m o n o m e r must c o p o l y m e r i z e r e a d i l y w i t h o u t a p p r e c i a b l e c h a i n transfer ( t h e p o l y m e r i z a t i o n is p a r t i c u l a r l y susceptible to c h a i n - t r a n s f e r r e a c t i o n s ) , a n d at a rate s u c h that reasonable a n d c o n t r o l l e d amounts of c r o s s l i n k i n g site are i n c o r p o r a t e d at a n adequate spacing. ( b ) T h e c r o s s l i n k i n g f u n c t i o n a l g r o u p m u s t not b e affected b y t h e p r e f e r r e d aqueous p o l y m e r i z a t i o n system. ( c ) T h e c r o s s l i n k i n g r e a c t i o n m u s t b e s u c h that t h e stock c a n b e f o r m e d i n t o d e s i r e d shapes at elevated temperatures ( b y m o l d i n g o r other m e a n s ) , t h e n b e c o n v e r t e d into a c r o s s l i n k e d structure. ( d ) T h e crosslink s h o u l d b e c o m p a r a b l e i n t h e r m a l , c h e m i c a l , a n d o x i d a t i o n resistance to t h e b a c k b o n e to m a i n t a i n t h e o u t s t a n d i n g p r o p erties of the d i p o l y m e r . CF
=CF - 0 -
2
where X = - C 0 0 R , and
(R )
Figure
f
1.
( R
f
) -
X
-CN,-0-C F 6
5
= PERFLUOROALKYL or P E R F L U 0 R 0 A L K Y L ETHER GROUP
Comonomer candidates—generalized structure
A survey o f a v a r i e t y o f p o l y m e r i z a b l e groups i n d i c a t e d that i n the preferred fluorovinyl
free-radical aqueous-emulsion
p o l y m e r i z a t i o n system, a p e r -
ether most n e a r l y fulfills these r e q u i r e m e n t s .
p e r f l u o r o v i n y l ethers c o p o l y m e r i z e
at a reasonable
I n general, the
rate.
T h e y change
l i t t l e i n rate w i t h variations i n c h a i n l e n g t h o r f u n c t i o n a l i t y i n the p e r fluoroalkyl
m o i e t y so l o n g as the t y p e of f u n c t i o n a l i t y o n the perfluoro-
a l k y l g r o u p is consistent w i t h requirements ( a ) a n d ( b ) .
I n addition,
s u c h ethers f u r n i s h t h e r m a l l y resistant structures i n t h e p o l y m e r . A
number
of m o n o m e r s
of t h e general
( 2 , 3 ) , w h e r e X is - C O O R , - C N , a n d - O C F 6
copolymerized with T F E and P M V E .
type 5
CF =CF-0-R X 2
f
( F i g u r e 1) have been
T h e i r c r o s s l i n k i n g reactions w i t h
d i f u n c t i o n a l v u l c a n i z a t i o n agents w e r e c a r r i e d o u t a n d t h e v u l c a n i z a t e
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
KALB E T AL.
15
Terpolymers
9 II
9 II
9 I
MnF
9 II
Cl-C-(CF ) -C-Cl ^ T ^ F - C - ( C F ) - C - F (89% YIELD) Perfluoroglutaryl Fluoride 1 n 2
3
2
9 II
HFPO
?3 F
'
F-C-(CF ) -CF 0-CF-CF0 (71% YIELD) 3-Oxa-perfluoro (2-methyl nonone dioyl) Fluoride (b.p.l06°C) ni
3
2
CsF
3
r
/
CH3OH
(near o°) 0
CF
0
3
0
K - 0- 8- (R )-0-CF-C-0" K • - g j g L (97,8% YIELD) Dipotassium 3-Oxa-perfluoro( 2-Methyl azelaoate )
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o
r
2
4
f
3
H00C-(R)-0-CF=CF
2
f
21
2
(b.p.80°C/2mm)
22
-KF
/
jx
K*0 -C-(R )-0-CF=CF 2
0
3
CH 0-C-(CF ) VcF-C-0CH
f
^ —
CF
SK
CH 0H,H S0 3
NC-(CF ) -0-CF=CF -^NH -C-(R )-0-CF=CF 2 4
2
2
f
2
r
(b.p.90-93°C) (m.p. 89.5-91.5°C) (YIELD 90 - 95 %) (Yl ELD 75-80 %) Perfluoro (4-cyanobutyl ^ vinyl ether) 1
Figure 2.
4
f
2
(b.p.60°C/40mm) Perfluoro (4-carbomethoxybutyl vinyl ether) ™:
Synthesis of perfiuoro(4-cyanobutyl
properties i n v e s t i g a t e d .
2
0 CH 0-C-(R )-0-CF=CF
T h e simplest phenoxy
vinyl ether) compound
(perfluoro-
p h e n y l v i n y l ether) has b e e n r e p o r t e d b y W a l l a n d P l u m m e r to p o l y m e r i z e w i t h great difficulty ( 6 ) .
In general, ionically bonded
cross-
l i n k i n g agents a n d g r o u p i n g s that t e n d to i n t e r c h a n g e easily ( s u c h as ester g r o u p s ) g i v e g o o d c h e m i c a l - r e s i s t a n t p o l y m e r s , b u t d o not g i v e v u l canizates w i t h attractive h i g h - t e m p e r a t u r e properties b e c a u s e these r u b bers suffer h i g h r e l a x a t i o n u n d e r stress at e l e v a t e d temperatures. Among
the m o r e
a t t r a c t i v e v i n y l ether c a n d i d a t e m o n o m e r s
perfluoro ( 4 - c a r b o m e t h o x y b u t y l
vinyl
ether),
vinyl ether), perfluoro(2-phenoxypropyl phenoxypropyl vinyl ether).
are
perfluoro ( 4 - c y a n o b u t y l
vinyl ether), and perfluoro(3-
C o m p o s i t i o n s c o n t a i n i n g these
monomers
are discussed i n this report. P o l y m e r i z a t i o n is c a r r i e d out e x p e d i t i o u s l y i n aqueous m e d i a u s i n g either redox
or t h e r m a l l y generated
techniques m a y b e also u s e d . difference ethers.
f r e e - r a d i c a l systems;
anhydrous
I n g e n e r a l , there appears to b e no gross
i n r e a c t i v i t y rates w i t h different substituents o n the
vinyl
H o w e v e r , w h e r e s l i g h t differences w e r e n o t e d , i t is l i k e l y that
differences i n s o l u b i l i t y i n the m i c e l l e affect c o n c e n t r a t i o n at the p o l y m e r i z a t i o n site a n d thus m o d i f y the final content of the t h i r d m o n o m e r i n the p o l y m e r .
D i f f e r e n t c r o s s l i n k i n g reactions are u s e d w i t h various
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
16
POLYMERIZATION REACTIONS A N D N E W POLYMERS
s u b s t i t u t e d v i n y l ether structures. the appropriate copolymer
T h e s e reactions a r e d i s c u s s e d u n d e r
type.
Studies with Perfluoro(4-Cyanobutyl The
Vinyl Ether)
synthesis o f this m o n o m e r
i n v o l v e s n i n e steps s t a r t i n g w i t h
p e r f l u o r o g l u t a r y l c h l o r i d e , as i n d i c a t e d i n F i g u r e 2 ( 3 ) . M o s t o f t h e steps g i v e g o o d y i e l d s except f o r t h e selective p y r o l y s i s step ( F i g u r e 2, c o m p o u n d s V - V I ) , w h e r e t h e y i e l d s a r e o n l y 10-20%.
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perfluoro(butenyl
vinyl
By-products are
a n d the hydrogen
fluoride
b o t h the desired a c i d a n d perfluoro ( b u t e n y l v i n y l
ether).
Polymerization. v i n y l ether)
ether)
adducts of
Copolymers of tetrafluoroethylene/perfluoro(methyl
a n d t h e n i t r i l e ( 1 - 4 m o l e %) h a v e b e e n p r e p a r e d b a t c h -
w i s e i n a s t i r r e d a u t o c l a v e u s i n g a n aqueous a m m o n i u m p e r s u l f a t e o r a m m o n i u m p e r s u l f a t e - s o d i u m sulfite redox c o u p l e system at 40°-100° C . The T F E / P M V E t h e pressure ethane.
gas m i x t u r e w a s p r e s s u r e d , as r e q u i r e d , t o m a i n t a i n
a n d the nitrile p u m p e d
i n solution i n trichlorotrifluoro-
After completion of t h e reaction, polymer was isolated
the latex
(25-30% s o l i d s )
from
b y c o a g u l a t i o n u s i n g e t h a n o l a n d aqueous
magnesium chloride solution.
It was washed w i t h alcohol/water solu
tions a n d d r i e d a t 7 0 ° C i n a n o v e n
under nitrogen.
Mass
balance
i n d i c a t e d that most o f t h e n i t r i l e h a d b e e n i n c o r p o r a t e d .
0-(CF ) CN 2
3--CF -CF-CF 2
4
-0-(CF )-C II 2
2
^C-(CF ) I 2
- 0 -
0 1 '— — 1
Figure 3. Crosslinking. action
Crosslinking
— -n
of polymer through the nitrile group
C r o s s l i n k i n g is b r o u g h t a b o u t b y t h e c a t a l y t i c i n t e r
of the pendant
n i t r i l e groups,
perhaps
to t h e t r i a z i n e , u s i n g
t e t r a p h e n y l t i n o r s i l v e r o x i d e ( F i g u r e 3 ) . T h e exact f o r m o f t h e cross l i n k has n o t b e e n e s t a b l i s h e d .
Henne ( 4 ) showed monomeric
perfluoro
c a r b o n i t r i l e s f o r m t r i a z i n e rings i n t h e presence o f t e t r a p h e n y l t i n o r other catalysts strongly
( 5 ) . T h e s e t r i a z i n e structures s o f o r m e d
a t 6.40-6.45/A
i n the infrared.
p a r e d f r o m t h e perfluoroelastomer
absorb
C r o s s l i n k e d g u m stocks
(polymer
a n d catalyst)
have
very pre been
e x a m i n e d i n t h e i n f r a r e d , a n d other u n a s s i g n e d b a n d s w e r e f o u n d , b u t the c h a r a c t e r i s t i c a b s o r p t i o n o f t h e t r i a z i n e s t r u c t u r e has n o t b e e n o b -
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
KALB E T AL.
17
Terpolymers
RAW
TERPOLYMER
100 pts.
MED. T H E R M A L
BLACK
TETRAPHENYL
TIN
10 pts. 4.5 pts.
Cure Conditions:
18 hours 160°C ( 3 2 0 ° F )
~ 1000
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Figure 4. Crosslinking for nitrite-containing served.
psi
formulation polymer
W h e n t h e viscous n a t u r e of t h e p o l y m e r stock is c o n s i d e r e d ,
c o u p l e d w i t h t h e f a c t t h a t t h e n i t r i l e is present i n t h e p o l y m e r to t h e extent o f o n l y 2 - 4 m o l e % o r less, i t appears u n l i k e l y t h a t c o m p l e t e
con
v e r s i o n t o a t r i a z i n e s t r u c t u r e is i n v o l v e d . I n p r a c t i c e , t h e c u r e i n g r e d i e n t s (see F i g u r e 4 ) a r e m i l l e d i n t o t h e p o l y m e r o n a r u b b e r m i l l ; c u r i n g is d o n e i n a press at 160° C a n d 1000 p s i f o r 18 h o u r s .
N o p o s t c u r i n g is r e q u i r e d .
Studies with Perfluoro(4'Carbomethoxybutyl S e v e r a l types
Vinyl Ether)
of c r o s s l i n k e d structures w e r e p r e p a r e d b y
m e r i z i n g v i n y l ethers c o n t a i n i n g 4 - c a r b o m e t h o x y p e r f l u o r o a l k y l
copolymoieties
i n t h e s t r u c t u r e a n d u s i n g v a r i o u s c r o s s l i n k i n g agents to b r i n g a b o u t vulcanization. Synthesis parent
of
Perfluoro(4-Carbomethoxybutyl
ester w a s p r e p a r e d f r o m
fluoropropylene
Vinyl
Ether).
The
fluoride
and hexa-
o x i d e b y t h e reactions s h o w n i n F i g u r e 2.
T h i s ester
h a d a b o i l i n g p o i n t o f 146°C,
perfluoroglutaryl
a n d showed
characteristic v i n y l
ether
i n f r a r e d absorptions a t 5.42/*, 5.55/A ( c a r b o n y l g r o u p ) , a n d 10.0/x ( - O C H
3
group). A c u t a l l y , b e t t e r y i e l d s of t h e m o n o c a r b o x y l i c
a c i d esters are o b
t a i n e d b y p y r o l y z i n g t h e h a l f - n e u t r a l i z e d a c i d i n s t e a d of t h e d i p o t a s s i u m salt.
E v e n so, t h e y i e l d of ester is o n l y a b o u t 25%.
Polymerization.
P o l y m e r i z a t i o n is c a r r i e d o u t i n t h e s a m e r e a c t o r
as i n d i c a t e d p r e v i o u s l y i n t h e s t a n d a r d persulfate-sulfite system.
The
presence o f t h e ester ( 1 m o l e % c h a r g e d ) i n t h e p o l y m e r is i n d i c a t e d b y t h e s t r o n g i n f r a r e d a b s o r p t i o n b a n d a t 5.55/x, a n d mass b a l a n c e i n d i c a t e s t h a t most o f t h e ester is i n c o r p o r a t e d . Crosslinking
the
Ester-Containing
b r o u g h t a b o u t easily u s i n g a c o n v e n t i o n a l
Polymer.
Crosslinking was
fluoroelastomer
hexamethyl-
enediamine carbamate cure, or b y using p-phenylenediamine. samples
tested, v u l c a n i z a t e p r o p e r t i e s
(hardness,
elongation)
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
I n the and re-
18
POLYMERIZATION REACTIONS A N D N E W POLYMERS
0 - C F - C F - 0 - C F = CF 2
2
F PERFLUORO (2-Phenoxypropyl Vinyl Ether)
F
F
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F
Figure 5.
Monomers containing the phenoxy group
perfluoro-
sistance t o c h e m i c a l s a n d fluids i n d i c a t e d a d e q u a t e c u r i n g . less, c o m p r e s s i o n
set values
Neverthe
( 7 0 hours a t 121° C ) o n stocks v a r i e d
b e t w e e n 87 a n d 100%, i n d i c a t i n g t h e extreme m o b i l i t y o f the c r o s s l i n k i n g b o n d a t m o d e r a t e l y h i g h temperatures.
M e t a t h e t i c a l reactions o f t h e
ester groups, w i t h a m i n e s , a m m o n i a , a n d h y d r a z i n e g a v e m o d e l cross l i n k structures.
Heat-loss studies o n these,
along with
model
com
p o u n d s p r e p a r e d f r o m the free a c i d , i n d i c a t e d that c a r b o n y l functions are not t h e r m a l l y stable e n o u g h .
Studies with Monomers Containing the Perfluorophenoxy T w o monomers
containing the perfluorophenoxy
Group
group have been
synthesized a n d copolymerized w i t h T F E a n d P M V E . these m o n o m e r s are s h o w n i n F i g u r e 5. ing
Structures o f
P o l y m e r i z a t i o n a n d crosslink
reactions a r e s i m i l a r f o r p o l y m e r s c o n t a i n i n g these t w o i s o m e r i c
monomers a n d , a c c o r d i n g l y , these p o l y m e r s are discussed together. Synthesis of the P h e n o x y - C o n t a i n i n g M o n o m e r s .
Perfluoro (2-phe-
n o x p r o p y l v i n y l ether) is p r e p a r e d b y t h e route s h o w n i n F i g u r e 6 ( 3 ) . T h e 2-phenoxy
compound
various monomers. glass e q u i p m e n t .
requires t h e l e a s t - i n v o l v e d s y n t h e s i s o f t h e
T h e first t w o steps w e r e c a r r i e d o u t i n o r d i n a r y T h e last r e a c t i o n w a s c a r r i e d o u t u s i n g a b e d o f
d r i e d s o d i u m carbonate. P e r f l u o r o ( 3 - p h e n o x y p r o p y l v i n y l ether) six-step r o u t e s h o w n i n F i g u r e 7. out w i t h o u t i s o l a t i n g the p r o d u c t s .
( 7 ) is s y n t h e s i z e d b y t h e
T h e first three steps m a y b e c a r r i e d T h e a c i d c h l o r i d e p r o d u c t of step
3 is s e p a r a t e d b y f r a c t i o n a l d i s t i l l a t i o n , as is the a c i d fluoride p r o d u c t o f step 4.
I n step 5, the p r o d u c t is separated as the l o w e r o f a t w o - l a y e r
p r o d u G t a n d is p u r i f i e d b y d i s t i l l a t i o n .
T h e upper layer, a complex of
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
Terpolymers
KALB ETAL.
C s F , the starting acid lyst.
19
fluoride,
a n d t e t r a g l y m e m a y b e r e u s e d as c a t a
B e t t e r p r o d u c t y i e l d s a r e o b t a i n e d w i t h reused catalyst t h a n w i t h
v i r g i n catalyst. fluidized
T h e last r e a c t i o n (step 6 ) is best c a r r i e d o u t u s i n g a
b e d of d r i e d s o d i u m c a r b o n a t e at 270°-300° C .
Polymerization. monomers
T e r p o l y m e r s of P M V E a n d T F E w i t h either of the
containing a phenoxy group have been prepared i n a pres
sure vessel u s i n g a n aqueous
redox p o l y m e r i z a t i o n system.
positional molar T F E / P M V E
ratio i n t h e p r e f e r r e d p o l y m e r is about
60/40.
T h e com
T h e t h i r d m o n o m e r p o l y m e r i z e s a t about t h e same rate as t h e
P M V E a n d is f e d either neat (as a l i q u i d ) o r i n F r e o n F - 1 1 3 s o l u t i o n . Downloaded by MONASH UNIV on November 26, 2014 | http://pubs.acs.org Publication Date: June 1, 1973 | doi: 10.1021/ba-1973-0129.ch002
I n f r a r e d analysis o f the b a n d at 10.0/x indicates 75-85% i n c o r p o r a t i o n o f the p h e n o x y
compound
over t h e 1-4 m o l e % m o n o m e r
change
range.
O n e t o 2 m o l e % of the crosslink m o n o m e r m u s t b e i n c o r p o r a t e d i n t h e elastomer to ensure g o o d v u l c a n i z a t e properties. 1. CcFc-OH + CsoC0 6
5
2
3
3
° » TETRAGLYME R
T
t 0
5 Q
0 / \ 2. C F - O C s + (n+1)CF -CF-CF 6
5
2
C
C F OCs + CsHCCU g
6
5
5
3
CF CF 0 I I II C F -0-(-CF-CF -0-KF-C-F 3
3
in-is°r ° ^ U
6
3
5
2
n= 1 BUT THERE MAY BE SOME n=2 CF
CF
3
3. C F - 0 - f C F - C F - 0 - ) t> o c 6
5
2
n
3
- C F - C 0 F r ^ ^ C F 0 - f C F - 0 + CF=CF 200-300°C B.R = 6 5 - 6 8 ° / 9 m m For n = 1 N 25°C = 1.3639 6
5
3
6
2
n
D
For n = 0
Figure
6.
Crosslinking
Synthesis
of perfluoro(2-phenoxypropyl
vinyl
Perfluorophenoxy-Containing Elastomers.
t i o n o f t h e perfluoroelastomer c a r r i e d o u t several w a y s . enediamine,
(Wall a Plummer, U.S. Patent 3,192,190, Unsatisfactory polymerization)
containing a phenoxy
ether) Vulcaniza
group
may be
O n e m e t h o d uses d i a m i n e s s u c h as p - p h e n y l -
tetraethylenepentamine,
or hexamethylenediamine
carba
m a t e ( D u P o n t D I A K N o . 1) (3). A t y p i c a l r e c i p e is s h o w n i n F i g u r e 8. T h e r u b b e r a n d t h e c o m p o u n d i n g ingredients a r e m i x e d o n a c o n ventional rubber
m i l l , a n d t h e d e s i r e d shape
molded
i n a press at
500-1000 p s i o n t h e s h a p e d p i e c e f o r 30 m i n u t e s at 160° C . T h e p i e c e is t h e n r e m o v e d f r o m t h e press a n d p o s t c u r e d stepwise o v e r five to s i x days t o c o m p l e t e v u l v a n i z a t i o n .
O u r present c o n c e p t o f this c r o s s l i n k
i n g r e a c t i o n i n v o l v e s r e a c t i o n of the d i a m i n e ( F i g u r e 9 ) w i t h the a c t i v e fluorine
a t o m p a r a t o the o x y g e n l i n k a g e o n the a r o m a t i c r i n g to l i b e r a t e
hydrogen
fluoride
(11).
T h i s , i n t u r n , reacts w i t h m a g n e s i u m o x i d e t o
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
20
POLYMERIZATION REACTIONS A N D N E W POLYMERS
1.
C F 0H + K C0 6
5
2
3
C
R
H
E
3
F
^
X
• C F -0K 6
+ KHC0
5
3
( 80% when isolated ) 0 2.
C F 0K + CF = CF +C0
3.
150 psig 0 II 3 C F - 0 - C F - C F - C - 0 K + POCI3
6
5
2
6
5
2
2
g
2
™ ' C F -0-CF -CF -C-0K
H
6
2
5
2
2
(95%) 0 II ^ • 3 C F - 0 - C F - C F - C - C l + K3PO4
c
6
5
2
(85%)
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4-
0 II C F - 0 - C F C F - C - C l + NaF 6
5
2
2
T
M
S
6
0
5
2
2
5
2
(B.P. 49°/11mm)
^(2)
CF 0
C F - 0 - C F - C F - C - F + CF -CF-CF 6
5 mm )
0 II ' C F - 0 - C F - C F - C - F + NaCl (85%)
5.
2
(BP. 54°/
2
2
• C F -0-(CF
3
6
5
) ~CF -0-CF-C-F
2
2
2
(>70%) (B.P. 7 7 ° / l l m m ) CF 0 I II C F -0-(CF ) -CF -0-CF-C-F 3
6.
6
5
2
2
2
Z
7
N00CO7 ^ . Q
' C F - 0 - ( C F ) - C F - 0 - C F = CF
C
6
5
2
2
2
2
(>85%)
Figure
7.
Synthesis of perfluoro(3-phenoxypropyl
vinyl
ether)
PARTS by WEIGHT POLYMER MEDIUM
100
THERMAL
MAGNESIUM
BLACK
OXIDE
HEXAMETHYLENE
20.0 15.0
DIAMINE CARBAMATE
1.5
Figure 8. Diamine formulation for curing perfluorophenoxy-containing polymer form water and magnesium
fluoride.
U n d e r the c o n d i t i o n s r e q u i r e d to
complete the vulcanization, water must b e expelled from t h e m o l d e d p i e c e , a n d , because o f the l o w p e r m e a b i l i t y o f the r u b b e r to m o i s t u r e , the step postcure must b e c a r r i e d o u t s l o w l y to p r e v e n t s p o n g i n g . Alternately, aromatic bisnucleophiles m a y b e used to cure perfluorophenoxy-containing polymers. agents are s h o w n i n F i g u r e 10. salts are also effective. to f u n c t i o n w e l l . are
p o l y ethers 2
P o t a s s i u m salts are s h o w n , b u t c a l c i u m
T h e s e c r o s s l i n k i n g agents r e q u i r e a n accelerator
I n g e n e r a l , the accelerators f o u n d to b e most efficient (Figure
11) such
CH -0-(CH -CH ) -OH—of 3
these
E x a m p l e s of t y p i c a l c r o s s l i n k i n g
2
n
as p o l y e t h y l e n e
ether
glycols—
m o l e c u l a r w e i g h t a b o u t 350 ( C a r b o w a x
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
KALB ET AL.
350)
21
Terpolymers
( 8 ) , or the cyclic polyether compounds of " c r o w n " structure ( 9 ) .
A t y p i c a l f o r m u l a t i o n is s h o w n i n F i g u r e 12. T h e r o l e of t h e accelerators is n o t k n o w n , b u t t h e y m a y serve as s o l u b i l i z i n g agents, c o m p l e x i n g agents, o r i o n i z a t i o n agents.
T h e com
p l e t e c u r i n g r e a c t i o n is q u i t e s l o w , a n d t h e content o f c r o s s l i n k i n g sites is l o w so that l o n g post c u r e s — u p t o five d a y s — a r e r e q u i r e d .
T h e last
24 hours o f t h e c u r e is c a r r i e d o u t at 290° C u n d e r n i t r o g e n t o o b t a i n t h e best h i g h - t e m p e r a t u r e p r o p e r t i e s .
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CF
CF
3
&
2
;
+
2
CF CF I I 0-CF-CF -0-CF 3
CH
9.
*
2
2
\
2
2
Figure
. '/ Mg0
2
i
F
Raw Polymer
H N-CH I CH + 2
2
0-CF-CF -0-CF
Diamine
+
\
(MgF )
curing of polymer
2
+ V H 0 2
2
phenoxy-containing
Properties
T h e p h y s i c a l properties o f r a w t e r p o l y m e r are essentially i d e n t i c a l w i t h t h a t o f t h e d i p o l y m e r d e s c r i b e d b y B a r n e y et al. ( I ) , w i t h a f e w exceptions.
L o w - t e m p e r a t u r e characteristics a r e essentially u n c h a n g e d ,
b u t u n c u r e d p o l y m e r s s h o w s o m e loss i n t h e r m a l s t a b i l i t y a t t r i b u t a b l e t o the third monomer.
F o r example, a perfluorophenoxy-containing
poly
m e r lost a b o u t 12% o f its w e i g h t after heat a g i n g i n a n a i r c i r c u l a t i n g o v e n a t 316° C i n s i x d a y s , whereas t h e d i p o l y m e r c o n t r o l lost o n l y 6.5% u n d e r s i m i l a r c o n d i t i o n s . Because of the similarity of the t h i r d monomers polymer
density
is essentially
constant
from
investigated, r a w
polymer
to polymer:
2.04 ± 0.01. C u r e d a n d p o s t c u r e d g u m stock has a d e n s i t y o f 2.01 a n d b l a c k stock c o n t a i n i n g 10 p h r .
S A F b l a c k has a d e n s i t y o f 2.02.
R a w p o l y m e r is i n s o l u b l e i n most fluids, m a k i n g t h e d e t e r m i n a t i o n of s o l u t i o n v i s c o s i t y v e r y difficult. be
prepared
Solutions o f 0.2 g / 1 0 0 g solvent m a y
i n 2,2,3-trichloroheptafluorobutane
(Halocarbon
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
437, b y
22
POLYMERIZATION REACTIONS A N DN E W POLYMERS O'K*
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DIPOTASSIUM SALT OF HYDROQUINONE
Figure
10.
DIPOTASSIUM SALT OF 2,2"BIS( 4-HYDROXYPHENYL) PROPANE ( BISPHENOL A )
Typical
CH3-O
0"K*
DIPOTASSIUM SALTOF 2,2-BIS(4-HYDROXYPHENYL) PERFLUOROPROPANE (BISPHENOL AF)
bisnucleophiles used in curing perfluoroelastomer
-(-CH -CH -0 2
2
phenoxy-containing
H
e.g."CARBOWAX
350"
DICYCLOHEXYL- 1 8 - C R 0 W N - 6 ( 2 , 5,8,15,18, 21 -HEXAOXATRICYCLO [ 2 0 . 4 . 0 . 0
Figure 11.
Accelerators
H a l o c a r b o n Products, Inc.)
9,18
j
for perfluoroelastomer
HEXACOSANE)
curing
o r i n a f e w other chlorofluorocarbons
con
t a i n i n g 2-3% b y w e i g h t of a p o l a r cosolvent s u c h as m e t h a n o l , t r i c h l o r o acetic a c i d , o r g l y m e .
I n these solvents, d e t e r m i n a t i o n s of s o l u t i o n v i s
cosity i n d i c a t e that i n h e r e n t viscosities
( 7 7 ^ ) o f 0.4 o r greater a r e
necessary to o b t a i n a d e q u a t e v u l c a n i z a t e properties.
Properties of the Cured Polymer Stocks E x p e r i m e n t a l studies to date i n d i c a t e that there is l i t t l e b a s i c differ ence i n the resistance to c h e m i c a l s o r s w e l l i n g b y fluids b e t w e e n c o m positions c o n t a i n i n g t h e different crosslink m o n o m e r s . T h i s is p r o b a b l y because t h e c u r e site m o n o m e r , a n d e v e n t h e c r o s s l i n k i n g agent i n the p o l y m e r , represent o n l y a s m a l l p a r t of the finished v u l c a n i z a t e . F u r t h e r m o r e , the i n h e r e n t resistance o f the p o l y m e r to various fluids a n d to c h e m i c a l attack, c o u p l e d w i t h its l o w p e r m e a b i l i t y , c o n t r i b u t e to the s i m i l a r i t y o f materials c u r e d w i t h various agents. O n l y the most d r a s t i c tests s h o w differences i n p e r f o r m a n c e .
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
23
Terpolymers
KALB E TA L .
A b r i e f t a b u l a t i o n o f the v u l c a n i z a t e properties t o i n d i c a t e the l e v e l of p e r f o r m a n c e t h a t c a n b e a c h i e v e d w i t h these n e w perfluoroelastomers is i n o r d e r (10): F i g u r e 13 tabulates some o f t h e p h y s i c a l properties. T h e d a t a s h o w n are for b l a c k stocks. F i g u r e 14, illustrates t h e o u t s t a n d i n g resistance o f b l a c k v u l c a n i zates to heat a g i n g i n a i r ( t h e r m a l o x i d a t i o n ) .
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POLYMER SUPER ABRASION FURNACE BLACK MAGNESIUM
BLACK STOCK
GUM STOCK
100
100
10
OXIDE
4
ACCELERATOR
3
BISPHENOL
3
4*
Cure 30 min at 177 ° C Oven Cure. ROOM TEMP to 290 ° C 5 DAY S T E P - N 2
Figure 12. Typical cure formulation for curing phenoxy-containing perfluoroelastomer with bisnucleophiles 90 DUROMETER STOCK Cure
30 mins. / 3 5 0 ° F
20phr SAF BLACK + CURATIVES
+ POSTCURE TO 4 0 0 ° F ( 5 0 0 ° F tor COMP. SET)
ORIGINAL PHYSICAL PROPERTIES STRESS / STRAIN at 7 5 ° F
Mioot Psi.
1350
T , psi.
2720
B
E
B
, %
160
HARDNESS (Durometer A )
89
COMPRESSION SET-METHOD B 70 hrs. at 121 °C
(250 °F )
23%
70 hrs. at 288 °C
(550 °F )
45%
CLASH -BERG STIFFNESS TEMP. (10,000 psi TORSIONAL MODULUS )
+28°F
BRITTLE TEMPERATURE
-38°F
TEMPERATURE T-IO T-50
RETRACTION
TEAR D-470 (pli)
Figure
13. Typical
+30 °F 46°F 13
physical properties of black vulcanizates
perfluoroelastomer
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
24
POLYMERIZATION REACTIONS A N D N E W POLYMERS
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500 |
400
5 (3
300
TEMP. 2 8 8 ° C AIR
(550°F)
CIRCULATING OVEN
12 16 T I M E , DAYS
Figure
14. Effect of heat aging on perfluoroelastomer (10 phr SAF) vulcanizate tensile properties
black
3*
It—
200
"X
o z
S
100
232°C (450 F) 30mm Hg of MOIST AIR W
V
cJT 24 b ~ 20 / o. 16 m
S
,2
o
T7~ V
V V
I"
8 4• 20
Figure
40 60 WEEKS at
80 232°C
100
15. Effect of heat aging under conditions for high-performance aircraft
120
140
of operation
F i g u r e 15 shows heat a g i n g characteristics at 30 m m a i r pressure a n d 232° C — c o n d i t i o n s s i m i l a r to w h a t a h i g h - p e r f o r m a n c e a i r c r a f t m i g h t encounter i n flight. F i g u r e 16 illustrates t h e excellent resistance of b l a c k v u l c a n i z e d stocks to s w e l l i n g w i t h various fluids.
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
2.
KALB ET AL.
25
Terpolymers
I n a d d i t i o n to b l a c k , t h e elastomer m a y b e c o m p o u n d e d w i t h other common
fillers
s u c h as s i l i c a , c l a y , a n d asbestos.
H o w e v e r , i n general,
t h e i r r e i n f o r c i n g properties a r e i n f e r i o r t o c a r b o n . is advantageous t o c o m p o u n d the r u b b e r w i t h o u t
F o r c e r t a i n uses, i t fillers.
This gum vul
c a n i z a t e has p o o r e r p h y s i c a l properties t h a n l o a d e d stock b u t is better i n c h e m i c a l resistance. perfluoro greases
B o t h r e i n f o r c e d a n d g u m recipes m a y i n c l u d e
o r oils as plasticizers t o soften v u l c a n i z a t e s w i t h o u t
affecting a p p r e c i a b l y c h e m i c a l resistance. F i g u r e 17 tabulates t h e e l e c t r i c a l properties o f t h e g u m stock i n
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c o m p a r i s o n w i t h those of T e f l o n
fluorocarbon
resin.
WT. INCREASED
TENSILE EL0N6. RETD..% RETD.,%
0
100
100
1.3
80
100
3.2
75
100
0
100
100
ACETONE
1.0
73
100
ETHYL
1.2
73
100
1.0
96
100
0.5
94
100
0
100
100
JP-5
JET-FUEL
BENZENE CARBON 2B
TETRACHLORIDE
ALCOHOL
ACETATE
PYRI DINE ACETIC
ANHYDRIDE
SODIUM
HYDROXIDE
(46%)
Figure 16. Resistance of black vulcanizate perfluoroelastomer (10 phr SAF black) to various fluids at 25° C and seven-day immersion
(i) ELASTOMER DIELECTRIC
CONSTANT " E "
2.8-3.2
DISSIPATION FACTOR "D" (50%RH, 7 3 ° F ) DC.
RESISTIVITY
"p"
DIELECTRIC STRENGTH ( BREAKDOWN )
1 x 10"
10
18
3
ohm-cm
> 2 0 0 0 volts/mil
TFE 2.1 3 x 10"
4
10
18
400
(1) GUM STOCK -VULCANIZED 2
Figure
PLASTICS
WORLD
17. Dielectric
(1965).
properties elastomer
of gum
perfluoro-
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.
26
POLYMERIZATION REACTIONS A N D N E W POLYMERS
Safety Notes ( 1 ) M a n y of perfluoro c o m p o u n d s m e n t i o n e d a r e toxic a n d s h o u l d be h a n d l e d o n l y b y c o m p e t e n t investigators i n w e l l v e n t i l a t e d areas. ( 2 ) T h e p o l y m e r i z a t i o n w o r k r e p o r t e d h e r e i n requires c o m p r e s s i o n of tetrafluoroethylene-perfluoro ( m e t h y l v i n y l e t h e r ) mixtures. T h i s o p e r a tion must b e considered potentially hazardous a n d should b e carried out o n l y i n a d e q u a t e l y b a r r i c a d e d areas. Acknowledgments
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T h e authors t h a n k A . F . B r e a z e a l e , D . F . B r i z z o l a r a , D . B . P a t t i s o n , a n d H . J . S t i n g e r for t h e i r c o n t r i b u t i o n s t o this study.
Literature
Cited
1. Barney, A. L . , Keller, W . J., van Gulick, N . M . , J. Polym. Sci., A-1 (1970) 8, 1091. 2. Gladding, E . K., Sullivan, R; U.S. Patent 3,546,186 (1970); Anderson, D. G . , Gladding, E . K., Sullivan, R.; French Patent 1,527,816 (1968). 3. Pattison, D. B.; U.S. Patent 3,467,638 (1969). 4. Henne, A., Pelley, R. L . , J. Amer. Chem. Soc. (1952) 74, 1426. 5. Graham, T. L . , Rubber Age (1960) 43; Fritz, C. G . ; U.S. Patent 3,317,484 (1967). 6. Wall, L . A., Plummer, W . J.; U.S. Patent 3,192,190 (1965). 7. Quarles, R. W., Jr., French Patent 71.09113 (1971); Brizzolara, D . F . , Quarles, R. W., Jr., French Patent 71.09114 (1971). 8. Barney, A. L . , Honsberg, W . U.S. Patent 3,524,836 (1970). 9. Barney, A. L . , Honsberg, W.; U.S. Patent 3,580,889 (1971). 10. Barney, A. L . , Kalb, G . H . , Khan, A. A., Rubber Chem. and Tech. (1971) 44, 660. 11. Brizzolara, D. F . ; this laboratory; unpublished results based on model compound studies indicate primarily para position attack. ;
R E C E I V E D April 13, 1972.
In Polymerization Reactions and New Polymers; Platzer, N.; Advances in Chemistry; American Chemical Society: Washington, DC, 1973.