Synthesis and Properties of Branched Epoxy Resins - American

14 Synthesis and Properties of Branched Epoxy Resins JON

F. GEIBEL

Downloaded by UNIV LAVAL on May 5, 2016 | http://pubs.acs.org Publication Date: April 7, 1982 | doi: 10.1021/bk-1982-0184.ch014

Western Electric Co., Inc., Engineering Research Center, Princeton, NJ 08540

Epoxy resins, ubiquitous in the electronics industry, are used in a wide variety of applications in the manufacture of electronic components, including insulation materials, c i r c u i t board substrates, and component coatings and encapsulants. Thus, the cured epoxy resin is a highly functional material whose final chemical, physical, and electrical properties dictate the ultimate u t i l i t y of that material. Most coating applications mandate control over the viscosity of the epoxy resin(s) during the coating and/or curing processes. Linear epoxy resins span a large range of viscosities; however, only the upper range of commercially available resins (e.g. EEW ≥ 500 g/eq.) is suitable for powder coating applications. An important consideration in many protective coatings is solvent resistance. It is known that decreasing the molecular weight between cross-links w i l l decrease the solvent absorption of that thermoset (1, 2). Therefore, the lower molecular weight pre-polymers ( i . e . , lower EEW epoxy resins) w i l l provide the optimum solvent resistance. These solvent resistant coatings are not accessible with higher molecular weight solid epoxy resins. To solve this problem, a higher functionality epoxy resin is typically blended with the linear epoxy resin. This class of resins is the epoxy cresol/phenol novolacs. These materials are solids, with a variety of functionalities commercially available. Novolac resins possess low melt viscosities. This impacts on two areas: 1) When blended with a high molecular weight resin, the viscosity of the mixture is lowered. The high molecular weight resin was originally used to maintain a viscosity commensurate with processing constraints. 2) Mixing two materials with significantly different viscosities is non-trivial. Extrusion is an industrial method for blending epoxy resins. Attempting to extrude materials with widely different viscosities is d i f f i c u l t and often yields an inhomogeneous extrudate. A direct consequence of a poor extrusion is degraded solvent resistance. 0097-6156/82/0184-0185 $ 0 5 . 0 0 / 0 ©

1982 A m e r i c a n Chemical Society

Feit and Wilkins; Polymer Materials for Electronic Applications ACS Symposium Series; American Chemical Society: Washington, DC, 1982.

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Therefore, to e l i m i n a t e the above stated p r o p e r t i e s of mixtures of high molecular weight l i n e a r epoxy r e s i n s and low molecular weight epoxy c r e s o l novolac r e s i n s , a new method for s y n t h e s i z i n g a c l a s s of r e s i n s possessing the wanted p r o p e r t i e s of high molecular weight and high c r o s s - l i n k density i s presented.


Synthesis of Branched

Epoxy Resins

The advancement process f o r s y n t h e s i z i n g s o l i d epoxy r e s i n s from the monomers proceeds v i a a fusion r e a c t i o n of the d i g l y c i d y l ether of bisphenol A and bisphenol A (3). The advancement r e a c t i o n i s shown i n Figure 1. The r e a c t i o n i s c a r r i e d out with a c a l c u l a t e d excess of epoxy monomer so that: 1. A l l the phenol i s consumed; thus, the bisphenol A i s the l i m i t i n g reagent. 2. The product i s t h e o r e t i c a l l y terminated by an epoxide. Therefore, the product molecule, no matter what the molecular weight, i s capable of r e a c t i n g with curing agents i n e x a c t l y the same manner as does the epoxy monomer. Since both s t a r t i n g compounds are d i f u n c t i o n a l , t h i s polymerization t h e o r e t i c a l l y y i e l d s only l i n e a r polymers. Thus, h i g h l y f u n c t i o n a l c u r i n g agents must be used to form three-dimensional c r o s s - l i n k e d networks. A d d i t i o n a l l y , the s t a r t i n g reactants are not 100% pure ( i . e . , they c o n t a i n non-reactive end group i m p u r i t i e s ) . The advancement process consumes r e a c t i v e moieties and w i l l increase the r e l a t i v e r a t i o of "dead ends" to " r e a c t i v e " epoxides. This i s most c r i t i c a l when advancing to high molecular weights, where the m a j o r i t y of epoxides i s consumed ( 4 ) . As p r e v i o u s l y stated, to increase the c r o s s - l i n k d e n s i t y , m u l t i f u n c t i o n a l r e s i n s are mixed with these high molecular weight l i n e a r r e s i n s . An a l t e r n a t i v e to that approach i s to add a m u l t i f u n c t i o n a l r e s i n to the advancement process, thus s y n t h e s i z i n g branched high molecular weight epoxy r e s i n s . Figure 2 o u t l i n e s such a s y n t h e t i c scheme. C a l c u l a t i o n s f o r a branched advancement synthesis are defined to permit development of w e l l - c h a r a c t e r i z e d f u n c t i o n a l i t y i n the product molecules. In t h i s study, the d i f u n c t i o n a l epoxy r e s i n monomer used i s the d i g l y c i d y l ether of bisphenol A, Epon 828, and the m u l t i f u n c t i o n a l epoxy phenol novolac r e s i n used i s DEN 438. Let: X - Weight % Y = Weight % Z • Weight %

Epon 828 BPA DEN 438

(EEW = 190 g/eq) (PEW = 114 g/eq) (EEW - 183.5 g/eq)

Conservation of epoxides d i c t a t e s that f o r a branched advancement to an EEW = 1000 g/eq. the f o l l o w i n g equation i s valid:


Feit and Wilkins; Polymer Materials for Electronic Applications ACS Symposium Series; American Chemical Society: Washington, DC, 1982. Figure 1.

HO

Linear advancement reaction.

+

OH


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POLYMER


14.

GEIBEL

Branched

Epoxy

189

Resins

Xg + Zg . Yg 190 g/eq 183.5 g/eq 114 g / e q

lQOg 1000 g/eq Equivalents of epoxides remaining a f t e r advancement

Equivalents of epoxides before advancement

Equivalents of epoxides consumed by advancement

A d d i t i o n a l l y , c o n s e r v a t i o n o f mass d i c t a t e s w e i g h t s o f t h e r e a c t a n t s must e q u a l 100%:


X • Y + Z

(1)

t h e sum o f t h e

(2)

100

T h i s l e a v e s us w i t h 2 e q u a t i o n s and 3 unknowns. T h e r e f o r e , we d e f i n e a p a r a m e t e r , n, s u c h t h a t a t h i r d e q u a t i o n a l l o w s a u n i q u e s o l u t i o n t o X, Y, and Z. T h u s , n i s d e f i n e d as the r a t i o o f moles o f b r a n c h p o i n t s t o moles o f epoxy r e s i n . I n s p e c t i o n o f t h e f i r s t few members o f an i d e a l i z e d homologous s e r i e s shows some o b v i o u s t r e n d s . Table

I.

I d e a l i z e d Homologous

Branch C o n c e n t r a t i o n

S e r i e s o f Branched

Structure

Epoxy

EEW

0

Resins

MW

1000

2000

1

1000

3000

2

1000

4000

o-

The m o l e c u l a r

weight o f the r e s i n MW

i sclearly

g i v e n bv:

= 2000 + lOOOn


(3)

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Thus, f o r 100 g of r e s i n , the number of moles of r e s i n i s given by: , . moles of r e s i n =


c

100 g . , . 2 v 7—:— (2000 + lOOOn) g/mole

/,x (4)

nn

M f t A

DEN 438 has a s t a t i s t i c a l f u n c t i o n a l i t y of 3.6 epoxides/molecule ( 5 ) . Thus, i n c o r p o r a t i o n of 1 molecule of DEN 438 i n t o 1 molecule of advanced r e s i n gives s t a t i s t i c a l l y 1.6 branches i n that molecule of r e s i n (3.6 epoxides are present. Two are consumed to form the l i n e a r c o n t i n u a t i o n of the r e s i n . The d i f f e r e n c e , 1.6 epoxides, i s the number of branches generated.). The t i t r a t e d EEW of DEN 438 i s 183.5 g/eq. Thus, the molecular weight i s 3.6 times greater (660.60 g/mole of DEN 438). Thus, knowing that 1 mole of DEN 438 gives 1.6 branches, one gets a "branch equivalent weight" (BEW). BEW

=

: mole of DEN 438 1.6 moles of branches BEW - 412.9 g/mole of branches.

(5) (6)

Thus, f o r a given composition with Z grams of DEN 438, the t o t a l number of moles of branches i s given by: moles of branches = .. 412.9 0

n

, 8—— — g/mole of branches Z

(7)

S u b s t i t u t i n g (4) and (7) i n t o the d e f i n i t i o n of n:

10

A l 2 . 9 + lOOOn)

(8)

°/(2000

Solving f o r Z: m Z

41.29 n (2 • n)

(

^

Thus, merely by s p e c i f y i n g n, and using equations (1), ( 2 ) , and (9) a unique s o l u t i o n to X, Y, and Z i s obtained. Results and D i s c u s s i o n An homologous s e r i e s of advancement r e a c t i o n s was synthesized using standard r e a c t i o n conditions on a 300 gram s c a l e . The branch concentration was increased from zero to 0.677 branches/molecule. V i s c o s i t y and gel permeation (GPC) data were obtained. Table II summarizes the r e s u l t s .


}

14.

GEIBEL

Branched

Epoxy

Resins

191

Table I I . Branched Epoxy Resins: GPC and Melt V i s c o s i t y v s . Branch Concentration n

EEW


0 0.098 0.184 0.260 0.327 0.441 0.534 0.677

1015 972 971 1030 980 976 972 1021

^ (cp @ 175C) 2954 2918 3643 4050 4738 5920 6449 9839

Mn 3242 4274 4817 5324 5615 6499 7248 9700

1601 1846 1804 1914 1911 1973 1984 2126

The t h e o r e t i c a l EEW was 1000 g/eq f o r a l lof these r e a c t i o n s . A l l r e a c t i o n s were + 30 g/eq (+3%) of the c a l c u l a t e d equivalent weight. The weight average and number average molecular weights increase monotonically with i n c r e a s i n g branch c o n c e n t r a t i o n . The melt v i s c o s i t i e s a l s o increase with i n c r e a s i n g branch c o n c e n t r a t i o n . Figure 3 shows the melt v i s c o s i t y at 175°C versus branch c o n c e n t r a t i o n . The melt v i s c o s i t y increases by greater than a f a c t o r o f three f o r t h i s homologous s e r i e s of r e s i n s . At branch concentrations greater than 0.5 branches/molecule there i s a d e v i a t i o n from the l i n e a r l y i n c r e a s i n g v i s c o s i t y seen at lower branch c o n c e n t r a t i o n s . Figure 4 d i s p l a y s versus branch c o n c e n t r a t i o n . At branch concentrations g r e a t e r than 0.5, M increases more r a p i d l y than at lower branch concentrations. Figure 5 p l o t s l o g (melt v i s c o s i t y ) versus log(M ) The l i n e a r i t y of t h i s p l o t i n d i c a t e that the s i z e of these epoxy r e s i n s i s below the c r i t i c a l molecular weight f o r chain-chain entanglements. The slope o f t h i s p l o t i s 1.4 and i s c o n s i s t e n t with no chain entanglements. An homologous s e r i e s of cured coatings of branched epoxy r e s i n s was tested f o r the k i n e t i c s of swelling with methyl e t h y l ketone. The s e r i e s of epoxy r e s i n s was synthesized with constant EEW and i n c r e a s i n g branch content (EEW = 1000 g/eq and n - 0, 0.25 and 0.50, r e s p e c t i v e l y ) . The syntheses were c a r r i e d out on a 3.5 kg s c a l e . Samples were cured with a s t o i c h i o m e t r i c amount of methylene d i a n i l i n e at 200°C f o r 30 minutes. Increasing branch content decreases the rate of solvent absorption d r a m a t i c a l l y . The increased number of c r o s s - l i n k s i n the cured samples o f the h i g h l y branched epoxy r e s i n s r e s u l t s i n decreased chain m o b i l i t y which i s responsible f o r the decreased solvent uptake. Figure 6 shows the weight uptake o f methyl e t h y l ketone per unit area versus square root of time o f immersion i n the neat solvent. w

w

#


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Branched

Epoxy

Resins


GEIBEL


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194


GEIBEL

Branched

Epoxy

195

Resins


14.

I

2 Time « v

Figure 6.

3

(minute ) l/t

MEK absorption vs. square root of time. Key: A, n = 0.00; B, n = 0.25; and C,n — 0.50.


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Conclusions A c o n c i s e s y n t h e s i s o f b r a n c h e d epoxy r e s i n s i s presented. S t o i c h i o m e t r i c c a l c u l a t i o n s are d i s c u s s e d which t r e a t t h e s y n t h e s i s i n an i d e a l i z e d s t a t i s t i c a l m o d e l . The c a l c u l a t i o n s c a n be a d a p t e d t o any w e l l c h a r a c t e r i z e d r e a c t a n t s .


An h o m o l o g o u s s e r i e s o f epoxy r e s i n s w i t h c o n s t a n t e p o x i d e e q u i v a l e n t w e i g h t and i n c r e a s i n g b r a n c h c o n c e n t r a t i o n d i s p l a y e d i n c r e a s e d m e l t v i s c o s i t y and w e i g h t a v e r a g e m o l e c u l a r w e i g h t . The r a n g e o f m o l e c u l a r w e i g h t s i n v e s t i g a t e d i n t h i s s t u d y was shown t o be b e l o w t h a t r e q u i r e d f o r c h a i n - c h a i n e n t a n g l e m e n t s . Powder c o a t i n g s were p r e p a r e d by e x t r u d i n g s t o i c h i o m e t r i c q u a n t i t i e s o f m e t h y l e n e d i a n i i i n e w i t h epoxy r e s i n s v a r y i n g only i n branch c o n c e n t r a t i o n . More h i g h l y b r a n c h e d r e s i n s r e s u l t i n a more t i g h t l y c r o s s - l i n k e d t h e r m o s e t network. Solvent absorption data i n d i c a t e decreased absorption with i n c r e a s i n g branch c o n c e n t r a t i o n . Experimental Advancement r e a c t i o n s were c a r r i e d o u t on a 300 gran^ scale, unless otherwise s p e c i f i e d , using commercially supplied Epon 828, BPA and DEN 438. A l l r e s i n s were u s e d as r e c e i v e d , w i t h no f u r t h e r p u r i f i c a t i o n . T r i p h e n y l p h o s p h i n e was u s e d as r e c e i v e d from P o l y s c i e n c e s ( l o t 2 - 2 4 0 1 ) . Advancement r e a c t i o n s were p e r f o r m e d u s i n g e l e c t r i c heating mantles. Temperatures of the r e s i n , mantle/beaker i n t e r f a c e , and m a n t l e i n t e r i o r were r e c o r d e d v i a thermocouples. R e a c t i o n m i x t u r e s were n o t p r o t e c t e d f r o m a t m o s p h e r i c oxygen. The advancement r e a c t i o n was i n i t i a t e d a t 120°C u s i n g 0.1% ( w e i g h t / w e i g h t ) t r i p h e n y l p h o s p h i n e . R e a c t i o n m i x t u r e s e x o t h e r m e d t o 1 7 5 ° - 185°C and were a l l o w e d t o c o o l t o 175°C. A l l r e a c t i o n s were t h e r m a l l y q u e n c h e d by p o u r i n g o u t on aluminum f o i l e x a c t l y 30 m i n u t e s a f t e r t h e peak o f t h e e x o t h e r m . The d i r e c t t i t r a t i o n o f t h e e p o x i d e e q u i v a l e n t w e i g h t (EEW) was a c c o m p l i s h e d by t h e method o f J a y ( ] ) • M e l t v i s c o s i t y m e a s u r e m e n t s were d e t e r m i n e d a t 175°C u s i n g a Haake RV-3 R o t o v i s c o m e t e r e q u i p p e d w i t h h i g h t e m p e r a t u r e r a n g e c o n e - p l a t e v i s c o s i t y s e n s o r s y s t e m (PK-401W). Gel permeation c h r o m a t o g r a p h y was p e r f o r m e d on a W a t e r s A s s o c i a t e s HPLC u s i n g / ^ - s t y r a g e l c o l u m n s ( 1 0 , 1 0 , 1 0 , 500, 500, 100, 100 A) in series. The f l o w r a t e was 2.0 m l / m i n . Samples were d i s s o l v e d i n a s p e c t r a l g r a d e THF and f i l t e r e d p r i o r t o c h r o m a t o g r a p h y t h r o u g h M i l l i p o r e 0.5 yu f i l t e r s (FHLP 0 1 3 0 0 ) . A l l c a l c u l a t i o n s were b a s e d on the o u t p u t o f a d i f f e r e n t i a l refractomer detector. 5

4

3

Powder c o a t i n g s o f b r a n c h e d e p o x y r e s i n s were p r e p a r e d e x t r u d i n g s t o i c h i o m e t r i c amounts o f t h e e p o x y r e s i n and m e t h y l e n e d i a n i i i n e (1 e q u i v a l e n t o f e p o x i d e p e r 1 N-H


by

14.

GEiBEL

Branched

Epoxy

Resins

197

e q u i v a l e n t ) i n a Buss PR-46 s i n g l e s c r e w e x t r u d e r . The e x t r u d a t e was p u l v e r i z e d i n a Bantam M i c r o p u l h a m m e r m i l l . Samples f o r s o l v e n t a b s o r p t i o n ( 2 ) were p r e p a r e d by e l e c t r o s t a t i c a l l y c o a t i n g c o p p e r f o i l and c u r i n g f o r t h e r e q u i s i t e schedule* The sample w e i g h t i s d e t e r m i n e d a c c u r a t e l y p r i o r to t e s t i n g . The sample i s submerged i n n e a t MEK i n a c o n s t a n t temperature b a t h a t 23+0.5°C. The sample i s removed a f t e r t h e a p p r o p r i a t e i m m e r s i o n t i m e , b l o t t e d d r y , and w e i g h e d p r e c i s e l y 45 s e c o n d s a f t e r r e m o v a l f r o m t h e s o l v e n t . The a b s o r p t i o n i s c a l c u l a t e d i n 8/cm^ a c c o r d i n g t o the f o l l o w i n g formula: m


Absorption

(

m g

Wt - Wt /cm ) = — — - — Area K

(10)

where Wt2 i s t h e w e i g h t a f t e r a b s o r p t i o n , Wt^ i s t h e w e i g h t p r i o r t o a b s o r p t i o n , and A r e a i s t h e s u r f a c e a r e a o f t h e sample. The a b s o r p t i o n v a l u e s r e p o r t e d a r e t h e a v e r a g e o f f o u r samples.

Literature Cited 1. 2. 3. 4. 5. 6. 7.

Nielsen, L. E. Macromol. Sci. - Revs. Macromol. Chem. 1969, C3(1), 69. Romanchick, W. Α., Geibel, Jon F . , Second Chemical Congress of the North American Continent, Las Vegas, 1930, ORPL-118. Batzer, H.; Zahir, S. A. J . Appl. Poly. Sci. 1975, 19, 585. Ravindranath, K.; Ghandi, K. S. J . Appl. Poly. Sci. 1979, 24, 1115. Dow Chemical Company, Production Description - DEN Epoxy Novolac Resins, form No. 170 - 143B (1967). Nielsen, L. E. "Mechanical Properties of Polymers", Reinhold, London, 1962, p. 58. Jay, R. R., Analytical Chemistry 1964, 35, 197.

RECEIVED

November

6,

1981.


Synthesis and Properties of Branched Epoxy Resins - American

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