CN102010686A - Double-solidification system fast-flowing underfill and preparation method thereof - Google Patents

Double-solidification system fast-flowing underfill and preparation method thereof Download PDF

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CN102010686A
CN102010686A CN201010297440XA CN201010297440A CN102010686A CN 102010686 A CN102010686 A CN 102010686A CN 201010297440X A CN201010297440X A CN 201010297440XA CN 201010297440 A CN201010297440 A CN 201010297440A CN 102010686 A CN102010686 A CN 102010686A
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epoxy resin
underfill
dual cure
cure systems
fast
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CN102010686B (en
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王红娟
王建斌
陈田安
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Yantai Darbond Technology Co Ltd
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Yantai Darbond Electronic Materials Co Ltd
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Abstract

The invention discloses a double-solidification system fast-flowing underfill and a preparation method thereof. The underfill comprises the following raw materials in parts by weight: 30-80% of epoxy resin, 10-50% of epoxy acrylate, 5-30% of acrylate, 2-20% of polyol, 1-20% of silane coupling agent, 0.3-4% of cationic initiator, 0.1-3% of radical initiator and 0.1-0.5% of carbon black; and the preparation method comprises the following steps of: weighing the epoxy resin and the cationic initiator in the proportion, putting in a reaction kettle and stirring into a uniform solution; weighing the epoxy acrylate, the acrylate, the polyol, the silane coupling agent, the radical initiator and the carbon black in the proportion, putting in the reaction kettle in sequence, mixing and stirring to obtain the finished product of the double-solidification system fast-flowing underfill.

Description

A kind of dual cure systems is mobile underfill and preparation method thereof fast
Technical field
The present invention relates to a kind of dual cure systems mobile underfill and preparation method thereof fast, be applicable to that encapsulation such as chip size packages (CSP), BGA Package (BGA) with the bottom filling, belong to the sizing agent field.
Background technology
Along with the fast development of electronic industry, closely-related with it Electronic Packaging technology is also more and more advanced.The main development trend intelligent, in light weight, that volume is little, speed is fast, function is strong, good reliability etc. becomes electronic product.For the development that adapts to this trend has produced flip-chip technology.The main advantage of flip-chip comprises can reduce and save the space, also has interconnection vias shorter and inductance is lower, high I/O density, do over again and the autoregistration ability in addition.Concerning radiating management, the performance of flip-chip is also very outstanding.And underfill is high-density flip-chip BGA, and CSP reaches one of crucial electronic material required in the SIP microelectronics Packaging; its main effect is protection high-density soldered ball node and chip; and BGA, processibility, reliability and the life-time service of CSP and SIP device have been guaranteed.
The underfill of cationic system has lot of advantages, and, curing back smell low as shrinking percentage is little etc.But also there are some defectives simultaneously,, may cause not solidified phenomenon of part glue because the consistency of glue and some soldering flux is not good enough.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, a kind of radical cation dual cure systems underfill and preparation method thereof that flows fast is provided, do not solidify, the purpose of characteristics such as reach good stability, can keep in repair to avoid running into some soldering flux.
The technical scheme that the present invention solves the problems of the technologies described above is as follows: the mobile fast underfill of a kind of radical cation dual cure systems, form by each raw material of following weight percent: Resins, epoxy 30~80%, acrylic acid epoxy resin 10~50%, acrylate 5~30%, polyvalent alcohol 2~20%, silane coupling agent 1~20%, cationic initiator 0.3~4%, radical initiator 0.1~3%, carbon black 0.1~0.5%.
The invention has the beneficial effects as follows: the mobile fast underfill of dual cure systems of the present invention, shrinking percentage is low, has effectively guaranteed the reliability of encapsulation components and parts; It is little to solidify the back smell, has complied with the trend of environmental protection; Velocity of flow is fast, adapts to the requirement of high density packing; In warm fast setting, meet high efficiency beat in the modern production; Stability in storage is good, can keep in repair, and is applied widely.
On the basis of technique scheme, the present invention can also do following improvement.
Further, described Resins, epoxy is a kind of or any several mixture in cycloaliphatic epoxy resin, bisphenol A type epoxy resin, bisphenol f type epoxy resin and the phenol aldehyde type epoxy resin.
Adopt the beneficial effect of above-mentioned further scheme to be, select dissimilar Resins, epoxy to cooperate, can be so that curing speed, cohesive strength etc. reach a trim point, excellent combination property.
Further, described aliphatic epoxy resin is 3,4-epoxycyclohexyl methyl-3,4-epoxycyclohexyl manthanoate and two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid ester; Described 3,4-epoxycyclohexyl methyl-3, the structural formula of 4-epoxycyclohexyl manthanoate is:
Figure BSA00000290376200021
The structural formula of described two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid esters is:
Figure BSA00000290376200022
Further, the structural formula of described bisphenol A type epoxy resin is represented by following general formula I:
Figure BSA00000290376200031
Wherein, n=0~19.
Further, the structural formula of described bisphenol f type epoxy resin is represented by following general formula I I:
Figure BSA00000290376200032
Wherein, n=0~1
Further, the structural formula of described phenol aldehyde type epoxy resin is represented by following general formula I II:
Figure BSA00000290376200033
Wherein, n=1~3.
Further, described acrylic acid epoxy resin is that an end of molecular chain is two keys, and the other end is an epoxide group, i.e. the cationically polymerizable resin of free redical polymerization again, and its structural formula is represented by following general formula I V:
Adopt the beneficial effect of above-mentioned further scheme to be, acrylic acid epoxy resin is positively charged ion, free radical two individual system bonded bridges, makes the mutual supplement with each other's advantages of two individual system, obtains a kind of have fast, the middle temperature fast setting of velocity of flow, filling glue that reliability is high.
Further, described acrylate is a kind of or any several mixture in butyl acrylate, Isooctyl acrylate monomer, the lauryl methacrylate(LMA).
Further, described polyvalent alcohol is polyester polyol, polyether glycol, polycaprolactone polyol, 1, a kind of or any several mixture in the 4-butyleneglycol.
Adopt the beneficial effect of above-mentioned further scheme to be, the curing speed that the adding of polyalcohols promptly can regulation system, toughness and any surface finish planeness that can regulate cured article again.
Further, described silane coupling agent is a kind of or any several mixture in β-(3, the 4-epoxycyclohexyl) ethyl trimethoxy silane, γ-glycidoxypropyltrimewasxysilane, γ-Qiu Jibingjisanjiayangjiguiwan, the γ-An Bingjisanyiyangjiguiwan.
Adopt the beneficial effect of above-mentioned further scheme to be, silane coupling agent helps improving fills the wettability of glue to base material, improves liquidity.
Further, described cationic initiator is a hexafluoro antimonate.
Further, described radical initiator is a kind of or any several mixture in benzoyl peroxide, Diisopropyl azodicarboxylate, di-tert-butyl peroxide, the peroxide-2-ethyl hexanoic acid tert-butyl.
Another technical scheme that the present invention solves the problems of the technologies described above is as follows: a kind of radical cation dual cure systems is the preparation method of mobile underfill fast, comprise by following weight percent and take by weighing Resins, epoxy 30~80%, cationic initiator 0.3~4%, it is dropped in the reactor, mixed 30 minutes at 30~35 ℃, make it dissolving and become uniform solution, and then take by weighing acrylic acid epoxy resin 10~50%, acrylate 5~30%, polyvalent alcohol 2~20%, silane coupling agent 1~20%, radical initiator 0.1~3% and carbon black 0.1~0.5%, add in the reactor successively, in 15~20 ℃ of temperature, vacuum tightness-0.08~-0.05MPa, 500~1000 rev/mins of rotating speeds, mixed 1~2 hour, and promptly got product.
Embodiment
Below principle of the present invention and feature are described, institute gives an actual example and only is used to explain the present invention, is not to be used to limit scope of the present invention.
Embodiment 1
Accurately take by weighing following various raw material, 3,4-epoxycyclohexyl methyl-3,4-epoxycyclohexyl manthanoate 40g, two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid ester 40g, hexafluoro antimonate are that U.S. King Corporation's Super XC-7231 0.5g drops in the reactor, mixed 30 minutes at 30 ℃, make it dissolving and become uniform solution, add acrylic acid epoxy resin 10g, butyl acrylate 5g, 1 then, 4-butyleneglycol 3g, β-(3, the 4-epoxycyclohexyl) ethyl trimethoxy silane 1g, benzoyl peroxide 0.3g, carbon black 0.2g.Controlled temperature is at 15 ℃, and vacuum tightness is-0.05MPa, and revolution is 500 rev/mins, and vacuum stirring was mixed 2 hours, obtained the homogeneous product.
Embodiment 2
Accurately take by weighing following various raw material, two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid ester 50g, bisphenol A type epoxy resin 20g, hexafluoro antimonate is that the K-PURE CXC-16123g of U.S. king company drops in the reactor, mixed 30 minutes at 35 ℃, making it dissolving becomes uniform solution, adds acrylic acid epoxy resin 10g, Isooctyl acrylate monomer 8g, polycaprolactone polyol 6.5g, γ-glycidoxypropyltrimewasxysilane 2g, Diisopropyl azodicarboxylate 0.3g, carbon black 0.2g then; Controlled temperature is at 15 ℃, and vacuum tightness is-0.05MPa, and revolution is 1000 rev/mins, and vacuum stirring was mixed 2 hours, obtained the homogeneous product.
Wherein, the structural formula of described bisphenol A type epoxy resin is:
Figure BSA00000290376200051
N is the mixture of 0,1,2~18,19 compounds of forming.
Embodiment 3
Accurately take by weighing following various raw material, two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid ester 30g, hexafluoro antimonate is that the K-PURE CXC-1612 1g of U.S. king company drops in the reactor, mixed 30 minutes at 30 ℃, making it dissolving becomes uniform solution, adds acrylic acid epoxy resin 15g, lauryl methacrylate(LMA) 30g, polyester polyol 20g, γ-Qiu Jibingjisanjiayangjiguiwan 3g, di-tert-butyl peroxide 0.5g, carbon black 0.5g then; Controlled temperature is at 15 ℃, and vacuum tightness is-0.07MPa, and revolution is 700 rev/mins, and vacuum stirring was mixed 2 hours, obtained the homogeneous product.
Embodiment 4
Accurately take by weighing following various raw material, 3,4-epoxycyclohexyl methyl-3,4-epoxycyclohexyl manthanoate 50g, phenol aldehyde type epoxy resin 15g, hexafluoro antimonate is that U.S. King Corporation's Super XC-72312g drops in the reactor, mixed 30 minutes at 35 ℃, making it dissolving becomes uniform solution, adds acrylic acid epoxy resin 15g, butyl acrylate 5g, polyester polyol 9.5g, γ-An Bingjisanyiyangjiguiwan 3g, peroxide-2-ethyl hexanoic acid tert-butyl 0.3g, carbon black 0.2g then; Controlled temperature is at 15 ℃, and vacuum tightness is-0.07MPa, and revolution is 1000 rev/mins, and vacuum stirring was mixed 2 hours, obtained the homogeneous product.
Wherein, the structural formula of described phenol aldehyde type epoxy resin is:
Figure BSA00000290376200061
N is 1,2 or 3 compound compositions that constitute.
Embodiment 5
Accurately take by weighing following various raw material, bisphenol A type epoxy resin 15g, bisphenol f type epoxy resin 15g, hexafluoro antimonate is that U.S. King Corporation's Super XC-7231 4g drops in the reactor, mixed 30 minutes at 30 ℃, make it dissolving and become uniform solution, add acrylic acid epoxy resin 45g, lauryl methacrylate(LMA) 10g, polycaprolactone polyol 5g, β-(3, the 4-epoxycyclohexyl) ethyl trimethoxy silane 5g, benzoyl peroxide 0.5g, carbon black 0.5g then; Controlled temperature is at 15 ℃, and vacuum tightness is-0.05MPa, and revolution is 1000 rev/mins, and vacuum stirring was mixed 2 hours, obtained the homogeneous product.
The comparative example 1
Common bottom is filled glue prescription-traditional curing mode, take by weighing resin 828EL 13.2g, resin 830LVP 39.2g, colorant 0.5g, solidifying agent fujicure fxr 1020 25g, promotor PN-H 5g, coupling agent KH5600.56g, epoxy active diluent AGE 20g toasts resin 830LVP one night down at 70-75 ℃, then resin 828EL, resin 830LVP, color mixes, 30 minutes time, 25 ℃ of temperature add solidifying agent then, promotor, three-roller mixes, 25 ℃ of temperature, mix under the cooling drying condition, cold water is controlled at 15 ℃, mixes three times, mix in the back adding reactor and expire vacuum 15 minutes, after mixing, resin and solidifying agent add coupling agent, epoxide diluent mixes, and full vacuum 30 minutes obtains sample.
Concrete experimental example
Flow the fast performance of underfill of dual cure systems by following experimental test the above embodiment of the present invention 1-5 and comparative example.
The test of experimental example 1 curing performance
The DSC cure profile, 60 ℃/minute of temperature rise rates, 130 ℃ of curing of constant temperature.
The test of experimental example 2 flowing propertys
24mm * 24mm testing plate, cover glass and slide glass are formed, and the slit is 25 microns, the velocity of flow that (simulation packaged chip) is 25 ℃.
Experimental example 3 thermal expansivity tests (CTE)
The TMA test, 10 ℃/minute of temperature rise rates, the μ m/m of unit ℃
Test according to ASTM D696
The test of experimental example 4 shearing resistances
The AL/AL shearing resistance, 130 ℃ of conditions of cure, 2 hours.
Test according to GB/T7124-1986.
Test result is shown in following table 1.
Sample that table 1 embodiment 1-5 makes and comparative example's sample common bottom are filled colloidality can the contrast test result
Figure BSA00000290376200081
Data from table 1 as can be seen, the dual cure systems of the present invention underfill that flows fast all has a clear superiority at more traditional underfills in aspect such as curing speed, velocity of flow, thermal expansivity, shearing resistances; When having higher reliability, be fit to the requirement of fast beat packaging process more.
The above only is preferred embodiment of the present invention, and is in order to restriction the present invention, within the spirit and principles in the present invention not all, any modification of being done, is equal to replacement, improvement etc., all should be included within protection scope of the present invention.

Claims (9)

1. the dual cure systems underfill that flows fast, it is characterized in that, form: Resins, epoxy 30~80%, acrylic acid epoxy resin 10~50%, acrylate 5~30%, polyvalent alcohol 2~20%, silane coupling agent 1~20%, cationic initiator 0.3~4%, radical initiator 0.1~3%, carbon black 0.1~0.5% by each raw material of following weight percent.
2. the mobile fast underfill of dual cure systems according to claim 1, it is characterized in that described Resins, epoxy is a kind of or any several mixture in cycloaliphatic epoxy resin, bisphenol A type epoxy resin, bisphenol f type epoxy resin and the phenol aldehyde type epoxy resin.
3. the mobile fast underfill of dual cure systems according to claim 2, it is characterized in that, described aliphatic epoxy resin is 3,4-epoxycyclohexyl methyl-3,4-epoxycyclohexyl manthanoate and two (7-oxabicyclo [4.1.0] 3-methyl in heptan) adipic acid ester.
4. the mobile fast underfill of dual cure systems according to claim 2 is characterized in that the structural formula of described bisphenol A type epoxy resin is represented by following general formula I:
Wherein, n=0~19
5. the mobile fast underfill of dual cure systems according to claim 2 is characterized in that the structural formula of described bisphenol f type epoxy resin is represented by following general formula I I:
Figure FSA00000290376100012
Wherein, n=0~1
6. the mobile fast underfill of dual cure systems according to claim 2 is characterized in that the structural formula of described phenol aldehyde type epoxy resin is represented by following general formula I II:
Figure FSA00000290376100021
Wherein, n=1~3
7. the mobile fast underfill of dual cure systems according to claim 1 is characterized in that, described acrylic acid epoxy resin is that an end of molecular chain is two keys, and the other end is an epoxide group, and its structural formula is represented by following general formula I V:
Figure FSA00000290376100022
8. the mobile fast underfill of dual cure systems according to claim 1 is characterized in that, described acrylate is a kind of or any several mixture in butyl acrylate, Isooctyl acrylate monomer, the lauryl methacrylate(LMA); Described polyvalent alcohol is polyester polyol, polyether glycol, polycaprolactone polyol, 1, a kind of or any several mixture in the 4-butyleneglycol; Described silane coupling agent is a kind of or any several mixture in β-(3, the 4-epoxycyclohexyl) ethyl trimethoxy silane, γ-glycidoxypropyltrimewasxysilane, γ-Qiu Jibingjisanjiayangjiguiwan, the γ-An Bingjisanyiyangjiguiwan.
9. the mobile fast underfill of dual cure systems according to claim 1 is characterized in that described cationic initiator is a hexafluoro antimonate; Described radical initiator is a kind of or any several mixture in benzoyl peroxide, Diisopropyl azodicarboxylate, di-tert-butyl peroxide, the peroxide-2-ethyl hexanoic acid tert-butyl.
A kind of dual cure systems is the preparation method of mobile underfill fast, it is characterized in that, described method comprises: take by weighing Resins, epoxy 30~80% by following weight percent, cationic initiator 0.3~4%, it is dropped in the reactor, mixed 30 minutes at 30~35 ℃, make it dissolving and become uniform solution, and then take by weighing acrylic acid epoxy resin 10~50%, acrylate 5~30%, polyvalent alcohol 2~20%, silane coupling agent 1~20%, radical initiator 0.1~3% and carbon black 0.1~0.5%, add in the reactor successively, in 15~20 ℃ of temperature, vacuum tightness-0.08~-0.05MPa, 500~1000 rev/mins of rotating speeds, mixed 1~2 hour, and promptly got product.
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