CN101671514A - Solidifiable coating with low permeability on sulfurous gas - Google Patents
Solidifiable coating with low permeability on sulfurous gas Download PDFInfo
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- CN101671514A CN101671514A CN200910178275A CN200910178275A CN101671514A CN 101671514 A CN101671514 A CN 101671514A CN 200910178275 A CN200910178275 A CN 200910178275A CN 200910178275 A CN200910178275 A CN 200910178275A CN 101671514 A CN101671514 A CN 101671514A
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Abstract
The invention provides a composition obtained from siloxane crosslinked polyolefin, the composition is almost non-permeable to sulfur compound in the gas state, such as hydrogen sulfide, and the composition endows various products, in particular to electronic subassemblies, with a protective coating. The invention also provides a method for protecting each type of product from the effect of the sulfur compound in the gas state.
Description
It is on 05 20th, 2004 that the present patent application is based on the applying date, application number is 200480024135.6 (international application no is PCT/US2004/015747), and denomination of invention is divided an application for the patent application of " hardenable coatings that sulfurous gas is had low-permeability ".
Technical field
The present invention relates to the polymer composition that contains polyisobutene that can be used as coating in general, comprises two-component network and segmented copolymer.More specifically, the present invention relates to comprise two-component network and segmented copolymer by making a plurality of polyisobutene polymer chains and the silicone compounds keyed jointing that has at least two SiH parts synthesize the various novel compositions that contain polyisobutene that can be used as coating.Specifically, make polyfunctional poly iso-butylene (polyisobutene of preferred allyl capped) synthesize two-component network with multifunctional linear polysiloxanes (for example end capped polydimethylsiloxane of two telechelic line style SiH-) keyed jointing by means of the hydrosilylation effect, this two-component network can be applied on the electron device.Equally, make the polyisobutene of difunctionality allyl capped and the end capped linear polysiloxanes of difunctionality SiH-(for example polydimethylsiloxane) termination can synthesize segmented copolymer by the hydrosilylation effect.Other polymer networks that comprise polyisobutene also can be by means of the hydrosilylation effect by making polyfunctional poly iso-butylene (polyisobutene of preferred two telechelic allyl capped) and be synthesized with the polyfunctional compound who contains SiH (preferred cyclosiloxane, for example hexamethyl six hydrogen cyclosiloxane) keyed jointing and can be used as coating.
Background of invention
Along with the discovery of living cationic polymerization, people can synthesize the polyisobutene (PIBs) that has controllable molecular weight and quantitatively hold functional group.Nowadays, be known that allyl capped polyisobutene can by means of hydrosilylation effect and the molecular method quantification that contains SiH part be terminated.This reaction has generated the Si-C key of hydrolysis-stable.But, up to now, the availability of the polyisobutene of quantitative end functional group and the PIBs of allyl capped have been concentrated in the preparation of star polymer and star block copolymer by the Research on ability analysis that hydrosilylation effect and silicone compounds are terminated.For example, U.S. Patent No. 5,663,245 have instructed the synthetic and sign of multi-arm star polymkeric substance, and the multi-arm star polymkeric substance comprises the polyisobutene arm that stretches out from the siloxanes core of clearly definition.Polyisobutene-block-polystyrene arm that utilization is stretched out from the siloxanes core of clearly definition can prepare star block copolymer.Rarely have at present (if any) to this building-up reactions in for example research of availability in the preparation of two-component network or segmented copolymer of network.
Polymer network of the present invention, and be that two-component network (BCNs) should be to be different from multiple traditional interpenetrating polymer networks (IPNs) specifically.People are defined as the unitary elasticity volume grid with BCN, and it comprises the sequence of the different covalent bonding of two kinds of chemical constitutions; And IPN is made of the separate network that two or more do not connect.This difference is clearly, because these polymkeric substance among the IPNs are not chemically carrying out keyed jointing, and the intermeshing network that would rather say so two kinds and separate.Most two component systems of being studied so far all relate to IPNs, only have only a few to utilize the research of BCNs.
Will be appreciated that segmented copolymer is similar to BCNs,, but exist and BCNs is crosslinked in uncrosslinked mode because they also comprise the sequence of the different covalent bonding of two kinds of chemical constitutions.Different is, segmented copolymer is the line style block of at least two kinds of polymkeric substance, for example be for the present invention polyisobutene (A-) and any difunctionality linear polysiloxanes (B-) terminate at together and form segmented copolymer (A-B-) n.It should be noted that these segmented copolymers synthetic different with " routine " segmented copolymer be polymkeric substance (A-) with (B-) before being terminated, form.But, " two-component network " that they neither above definition, crosslinked because they do not carry out, therefore and inelastic body, so dissolve in all kinds of SOLVENTS.What generally speaking BCNs required is that two kinds of crosslinked components help the physics and the chemical property of polymer network at least in theory.That is to say that the performance of two-component network will reflect the performance of each component.For example, the two-component network that contains polyisobutene and polysiloxane is extremely noticeable, polyisobutene is celebrated because of low-cost, outstanding mechanical property, extremely low gas permeability and the excellent feature of environmental protection, hydrolysis and high thermal resistance, and it is opposite, siloxanes is relatively expensive, mechanical property is relatively poor, but splendid aspect high gas permeability, low surface energy and consistency (bi-compatibility).
Summary of the invention
The invention provides a kind of at least two kinds of polymer compositions that chemically different component covalent bondings forms together, described composition can be used as coating.The present invention also provides a kind of clearly demarcated two-component network or segmented copolymer of structure that can be used as coating, and it contains for example polydimethylsiloxane of polyfunctional poly iso-butylene and linear polysiloxanes.The present invention further provides a kind of polymer composition, it has elastomeric properties thereby is insoluble to solvent.The invention provides in addition and a kind ofly by the hydrosilylation effect polyisobutene of two sense allyl capped and the end capped polydimethylsiloxane of multifunctional SiH-are terminated to synthesize the method for above-mentioned two-component network.The present invention provides a kind of again and by the hydrosilylation effect polyisobutene of two sense allyl capped and the end capped polydimethylsiloxane of two sense SiH-has been terminated to synthesize the method for above-mentioned segmented copolymer.The present invention provides also that a kind of being terminated synthesizes the method for above-mentioned polyisobutene network by hydrosilylation effect polyisobutene (or polyolefine of other allyl capped) that makes two telechelic allyl capped and the compound (for example hexamethyl six hydrogen cyclosiloxane) that contains SiH-, and adopts resulting composition as coating.At least one or a plurality of aforementioned purpose with and be superior to the advantage of known polymer network of prior art and segmented copolymer, will reach by the present invention as described below and realize, and it is more clear and obvious to be become by the following description.On the whole, the invention provides a kind of composition, the polyisobutene that said composition comprises a plurality of multifunctional allyl capped is bonded to a plurality of products that have the hydrosilylation reactions of at least two SiH multifunctional silicone compounds partly and obtain.The present invention also provides a kind of two-component network, its polyisobutene that comprises a plurality of multifunctional allyl capped is connected to a plurality of products that have the hydrosilylation reactions of at least two SiH two telechelic linear polysiloxanes partly and obtain, and the chemistry of this two-component network and physicals are determined jointly by polyisobutene and polysiloxane.The present invention further provides a kind of segmented copolymer, its polyisobutene that comprises a plurality of two telechelic allyl capped is connected to the hydrosilylation reactions of a plurality of two telechelic linear polysiloxanes that have at the most two SiH parts and the product that obtains, and the chemistry of this segmented copolymer and physicals are determined jointly by polyisobutene and polysiloxane.Further, the invention provides a kind of polymer network, its polyisobutene that comprises a plurality of multifunctional allyl capped is bonded to a plurality of products that have the hydrosilylation reactions of at least two SiH multifunctional silicone compounds partly and obtain.More other purposes of the present invention and aspect can be finished by synthesizing the polymer network method for compositions, this method comprises polyisobutene and a plurality of silicone compounds keyed jointing that has at least two SiH parts that makes a plurality of multifunctional allyl capped by the hydrosilylation effect, and described polymer network can be used as coating.
The invention provides a kind of coating that comprises polymer composition, this polymer composition comprises the reaction product of polyolefine and siloxanes or polysiloxane, wherein said coating has low spread coefficient to hydrogen sulfide under 50 ℃, perhaps under 50 ℃ thiomethyl alcohol is had low spread coefficient or the two is all had low spread coefficient.
The present invention includes:
1. coating that comprises polymer composition, this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) siloxanes
Pass at 50 ℃ of following hydrogen sulfide thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram hydrogen sulfide/square metre film/sky.
2. 1 coating, wherein said rate of diffusion is lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
3. 1 coating, wherein said rate of diffusion is lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
4. coating that comprises polymer composition, this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) siloxanes,
Pass at 50 ℃ of following thiomethyl alcohol gases thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram thiomethyl alcohol/square metre film/sky.
5. 4 coating composition, wherein said rate of diffusion is lower than about 0.0005 gram thiomethyl alcohol/square metre film/sky.
6. 1 coating composition, wherein said polyolefine is a polyisobutene.
7. 1 coating composition, wherein said polyolefine is a polypropylene.
8. 1 coating composition, wherein said polyolefine is a polymethylpentene.
9. 6 coating composition, wherein said rate of diffusion is lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
10. 6 coating composition, wherein said rate of diffusion is lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
11. the coated article of a coating, this coating comprises polymer composition, and this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) siloxanes
Pass at 50 ℃ of following hydrogen sulfide thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram hydrogen sulfide/square metre film/sky.
12. the goods of item 10, wherein said rate of diffusion are lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
13. the goods of item 10, wherein said rate of diffusion are lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
14. comprise the coated article of polymer composition, this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) siloxanes,
Pass at 50 ℃ of following thiomethyl alcohol gases thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram thiomethyl alcohol/square metre film/sky.
15. the goods that comprise composition of item 14, wherein said rate of diffusion are lower than about 0.0005 gram thiomethyl alcohol/square metre film/sky.
16. the goods that comprise composition of item 10, wherein said polyolefine is a polyisobutene.
17. the goods that comprise composition of item 10, wherein said polyolefine is a polypropylene.
18. the goods that comprise composition of item 10, wherein said polyolefine is a polymethylpentene.
19. the goods that comprise composition of item 16, wherein said rate of diffusion are lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
20. the goods that comprise composition of item 16, wherein said rate of diffusion are lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
21. a method of protecting goods not to be subjected to the hydrogen sulfide effect, this method comprises:
A) prepare coating composition by the polymer composition of the reaction product that comprises following material:
1) telechelic polyolefin and
2) siloxanes
Pass at 50 ℃ of following hydrogen sulfide thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram hydrogen sulfide/square metre film/sky,
With
B) described coating composition is coated on the described goods.
22. the method for item 21, wherein said polyolefine is a polyisobutene.
23. a method of protecting goods not to be subjected to the thiomethyl alcohol effect, this method comprises:
A) prepare coating composition by the polymer composition of the reaction product that comprises following material:
1) telechelic polyolefin and
2) siloxanes
Pass at 50 ℃ of following thiomethyl alcohol gases thus that to comprise thickness be that about 10 rate of diffusion to the described composition film of about 30 mils are lower than about 0.0010 gram thiomethyl alcohol/square metre film/sky,
With
B) described coating composition is coated on the described goods.
24. the method for item 23, wherein said polyolefine is a polyisobutene.
Detailed Description Of The Invention
The present invention at first relates to the synthetic of polymer composition, and this polymer composition comprises two-component network and segmented copolymer, comprises the polyfunctional poly iso-butylene and has one or more SiH polyfunctional compound partly.More specifically, the present invention has explored for example siloxanes of the molecule that how to utilize known hydrosilylation reactions to come the polyisobutene of termination allyl capped and contain SiH part, thereby provides a class to contain polyisobutene or other polyolefinic useful novel polymerizable compositions.Should understand, for the object of the invention, " polymer composition " is meant sequence those compositions of polyisobutene and polysiloxane for example that comprise two kinds of chemically different covalent bondings, and this polymer composition comprises two-component network, segmented copolymer and other network of relation as herein described.
The two-component network that contains the polyisobutene that clearly defines can be terminated with the end capped linear polysiloxanes of two sense SiH that clearly defines by the polyisobutene that makes multifunctional allyl capped by means of the hydrosilylation effect and be synthesized.These BCNs of the present invention have elastomeric properties and are insoluble to solvent, and they are considered to the important branch of elastomer rubber industry.
Equally, the segmented copolymer that contains clearly the polyisobutene of definition and siloxanes can be terminated and is synthesized by means of polyisobutene and the two sense SiHs end capped linear polysiloxanes of hydrosilylation effect by making two sense allyl capped.If use PIB and PDMS, then described as scheme hereinafter, this reaction process will produce many blocks PIB/PDMS multipolymer.Also can figure out further, if the amount of polyisobutene overwhelms the amount of the molecule that contains the SiH part fully, just synthesize the polyisobutene network that makes new advances in this new composition.These polyisobutene networks comprise the polyisobutene and the silicone compounds that contains SiH of the allyl capped of multifunctional and preferred two telechelics.More preferably, be terminated and synthesize the polyisobutene network by means of polyisobutene and line style or cycloalkyl hydroperoxide siloxanes or the hydrogen silane of hydrosilylation effect by making two telechelic allyl capped.This line style or cycloalkyl hydroperoxide siloxanes or hydrogen silane are well-known in the art.
In fact, the clear and definite polyisobutene network of structure the cyclosiloxane compound that contains SiH (also being hexamethyl six hydrogen cyclosiloxane) by making the known two telechelic polyisobutene of number-average molecular weight (Mn) and suitable functionality being terminated to synthesize obtains, it should be noted that most with two telechelic PIBs to carry out hydrosilylation reactions.
Should be noted that two telechelic PIBs and silicone components are keyed jointings.Therefore, if silicone components has enough molecular weight and size, network just can form two-component network so.The cyclosiloxane component can be different from lower molecular weight annular siloxane (normally volatile), and if silicone components have enough molecular weight and size, only so just can form can swelling rather than be dissolved in the network-like structure of solvent.For synthetic this polymer composition, at first how far synthesize the polyisobutene of chela allyl capped according to methods known in the art.The PIBs of this allyl capped can make by the following method: make iso-butylene carry out living polymerization to any practical length (therefore almost being all molecular weight that need), then making end-functionalization quantitatively is the olefinic end group.By using 2-chloro-2,4,4-trimethylpentane/TiC14 initiator system is as electron pair donor(EPD), and in the presence of N,N-dimethylacetamide, the reaction of initiating activity isobutene polymerisation can obtain the end capped polyisobutene of chlorine.Being described in more detail of this process is set out in " the carbonization stabilization (Electron Pair Donors in Carbocationic Polymerization; III.Carbonation Stabilization by External Electron Pair Donors in IsobutylenePolymerization) of the electron pair donor(EPD) III. exoelectron in the carbon cation polymerization to bringing for body " in isobutene polymerisation, people such as Kaszas, J.Macromol.Sci., Chem., A26 is among the 1099-1114 (1989).After polymerization is finished, make it chilling on the spot, so that the PIBs of allyl capped to be provided, thereby can realize the allylation of active polyisobutene with excessive allyl trimethyl silane.Being described in more detail of this process is set out in " the electrophilic substitution II. of silicoorganic compound makes the tetrachloro polyisobutylene alkylate and the end capped polyisobutene of synthesis of allyl (Electrophilic Substitution ofOrganosilicon Compounds II.; Synthesis of Allyl-terminated Polyisobutylenes byQuantitative Alkylation of tert-Chloro-Polyisobutylenes withAllyltrimethylsilane) quantitatively with allyl trimethyl silane ", people such as Wilczek, J.Polym, Sci.:Polym.Chem.25 is among the 3255-3265 (1987).Characterize the PIBs of the allyl capped of gained then by means of H-NMR spectrum, gel permeation chromatography (GPC) and dsc (DSC).
The present composition more completely is described in the special here U.S. Patent No. of introducing as a reference 6,005,051.
The preparation of siloxane polymer can separate with the preparation of polyisobutene to be carried out.For example, the end capped polydimethylsiloxane of two sense SiH can be synthesized in the presence of corresponding chain terminator tetramethyl disiloxane in the acid catalysis balanced reaction by cyclic tetramer D4.Can characterize polysiloxane with H-NMR spectrum and DSC then.If expect a kind of cyclosiloxane, six hydrogen pregnancy basic rings, six siloxanes for example, then it can prepare by the hydrolysis of dimethyl dichlorosilane (DMCS), this is that this area is known altogether and more specifically is described in U.S. Patent No. 3, in 484,468, document disclosure is introduced as a reference at this.The terminology used here siloxanes comprises monomer or polymeric siloxanes kind, and it comprises one or more active parts that can carry out condensation reaction with the olefinic end of two telechelic polyolefins.This often means that oxyalkylene segment will have one or more, the preferably silicon of two or more hydrogen bonding atoms, for example silyl hydride of following general formula or hydrogen siloxane:
M
aM
H bD
cD
H dT
eT
H fQ
g
Wherein each siloxanes formation unit M, D, T and Q are defined as follows:
M＝R
1R
2R
3SiO
1/2；
M
H＝HR
4R
5SiO
1/2；
D＝R
6R
7SiO
2/2；
D
H＝HR
8SiO
2/2；
T＝R
9SiO
3/2；
T
H=HSiO
3/2With
Q=SiO
4/2Wherein
R
1, R
2, R
3, R
4, R
5, R
6, R
7, R
8And R
9Be selected from the univalence hydrocarbyl of one to 60 carbon atom and the unit price organic group of one to 60 carbon atom independently of one another, wherein subscript a, b, c, d, e, f and g are 0 or positive integer, and the b+d+f that satisfies condition 〉=1, preferred b+d+f 〉=2, more preferably b+d+f 〉=3, and b+d+f 〉=4 most preferably.The unit price organic group of one to 60 carbon atom of word means carbon carbochain wherein by heteroatoms any organic group at interval, and heteroatoms is selected from oxygen, sulphur, nitrogen and phosphorus.Term siloxanes used herein is to include the very wide in range term of scope and comprise functionalized and reactive siloxanes.
Because two telechelic polyolefins that use in the coating of the present invention possess reactivity, form the oxyethane end group so they can react, epoxide groups just, and can with aforementioned hydrogen siloxane M for example
aM
H bD
cD
H dT
eT
H fQ
gCarry out polymerization or crosslinked.
Similarly, the olefinic end group can oxidized formation carboxylic end group.Then they can with the material that contains silanol M for example
aM
OH bD
cD
OH dT
eT
OH fQ
gCarry out condensation reaction, wherein standard construction is defined as follows:
M＝R
1R
2R
3SiO
1/2；
M
OH＝HOR
4R
5SiO
1/2；
D＝R
6R
7SiO
2/2；
D
OH＝HOR
8SiO
2/2；
T＝R
9SiO
3/2；
T
OH=HOSiO
3/2With
Q＝SiO
4/2；
R wherein
1, R
2, R
3, R
4, R
5, R
6, R
7, R
8And R
9Be selected from the univalence hydrocarbyl of hydroxyl, one to 60 carbon atom and the unit price organic group of one to 60 carbon atom independently of one another, wherein subscript a, b, c, d, e, f and g are 0 or positive integer, and the b+d+f that satisfies condition 〉=1, preferred b+d+f 〉=2, more preferably b+d+f 〉=3, and b+d+f 〉=4 most preferably.The unit price organic group of one to 60 carbon atom is meant that wherein the carbon carbochain is by heteroatoms any organic group at interval, and heteroatoms is selected from oxygen, sulphur, nitrogen and phosphorus.
Under the hydrosilylation reactions condition,, two telechelic polyolefins, preferred polyisobutene and suitably crosslinked hydrogen siloxane can prepare coating of the present invention by being reacted.The hydrosilylation reactions precious metal catalyst, the preferred platinum of precious metal, this class catalyzer discloses many useful prescriptions.The many class noble metal catalysts that are used for this hydrosilylation reactions are known, and this class catalyzer can be used for reaction of the present invention.When the needs optical transparence, preferred catalyzer is the catalyzer that dissolves in reaction mixture.As precious metal, the applicant is defined as precious metal with Ru, Rh, Pd, Os, Ir and Pt, equally also comprises Ni, because known its has hydrogenation activity.Catalyzer is preferably platinic compound, and the described formula (PtCl of the optional United States Patent (USP) freely 3,159,601 of platinic compound (introducing as a reference at this)
2Alkene), H (PtCl
3Alkene) those compounds or H
2PtCl
6Alkene in above-mentioned two formulas almost can be the alkene of any kind, but is preferably the alkene with 2 to 8 carbon atoms, cycloolefin or the vinylbenzene with 5 to 7 carbon atoms.The concrete alkene that can be used for following formula is various isomer, octene, cyclopentenes, tetrahydrobenzene, suberene of ethene, propylene, butylene or the like.
The platiniferous material that can be used for the present composition in addition is to be described in United States Patent (USP) 3,159, the muriatic cyclopropane complex compound of platinum in 662, and the document is introduced herein as a reference.
The platiniferous material can also be that this composition is selected from alcohol, ester, aldehyde and its mixture by Platinic chloride and the complex compound that forms up to the composition of 2 moles per gram platinum, and as the United States Patent (USP) of introducing as a reference at this 3,220,972 is described.
The preferred catalyzer that uses with the liquid infusion moulding compound is described in the United States Patent (USP) 3,715,334,3,775,452 and 3,814,730 of Karstedt.Other background technologies relevant with prior art can be referring to " transition metal hydrosilylation homogeneous catalyst (the HomogeneousCatalysis of Hydrosilation by Transition Metals) " of J.L.Spier, the organometallic chemistry progress (
Advances In Organometallic Chemistry), the 17th volume, the 407th to 447 page, F.G.A.Stone and R.West edit, and Academic Press press publishes (New York, 1979).Those skilled in the art are easy to determine the significant quantity of platinum catalyst.Usually, the significant quantity that is used for hydrosilylation be the organopolysiloxane composition total amount about 0.1 to 50ppm, and can be that therebetween all are divided sections.
Employed two telechelic polyolefins of coating of the present invention can also react and form epoxidised olefinic end group, and these epoxidation two telechelic alkene form the cross-linked polymer that can be used as coating of the present invention with the hydrogen siloxane reaction under acid catalyzed condition.
In order to make composition of the present invention obtain high tensile, need in composition, add filler.The example of available many fillers is the silicon-dioxide handled of titanium dioxide, lithopone, zinc oxide, zirconium silicate, aerosil, ferric oxide, diatomite, lime carbonate, pyrogenic silica, silazane, precipitated silica, glass fibre, magnesium oxide, chromic oxide, zirconium white, aluminum oxide, α quartz, calcined clay, asbestos, carbon, graphite, cork, cotton, synthon or the like.
The present composition should with preferred filler be through surface-treated pyrogenic silica or through surface-treated precipitated silica.A kind of method of surface-treated is that pyrogenic silica or precipitated silica are exposed in the ring-type organopolysiloxane under heat and pressure effect.The method of processing filler in addition is the method that in the presence of amine compound silicon-dioxide is exposed in siloxanes or the silane.
The method of particularly preferred surface treatment silica filler is used methyl-monosilane silazane surface treatment agent.System of forging or precipitated silica filler that methyl-monosilane or silazane are surface-treated have the mobile of being easy to performance, nor can increase the low viscosity of uncured liquid precursor silicone composition.After the curing, the silicon-dioxide that silazane is handled is given the solidified elastomerics with improved tear strength.The silazane treatment process is disclosed in United States Patent (USP) 3,635, in 743 and 3,847,848, it is introduced as a reference herein.
The consumption of filler for the cross-linked polymer of per 100 weight part gained or network polymer normally about 5 to about 70 parts, preferred 15 to 50 parts of fillers.Preferred filler is pyrogenic silica or the pyrogenic silica of silazane processing and the mixture of the precipitated silica that silazane is handled that silazane is handled.Back one mixture is particularly preferred, and the pyrogenic silica that it is contained and the weight ratio of precipitated silica are about 25/1 to about 1/1, preferred about 10/1 to about 5/1.
The organopolysiloxane fluid that can add hydroxyl is to prolong the working life of crosslinkable organopolysiloxane composition.If the precipitated silica filler that exists silazane to handle in the composition then can add organopolysiloxane fluid or the resin of precipitated silica filler with hydroxyl, thereby obtain long working life and release property.The organopolysiloxane fluidic viscosity of suitable hydroxyl 25 ℃ down for about 5 to about 100 centipoises, be preferably about 20 to about 50 centipoises.These fluids can be represented by the formula:
R
j(OH)
kSiO
(4-j-k)/2
Wherein R is the univalence hydrocarbyl with one to 40 carbon atom, and j is 0 to about 3, preferred 0.5 to about 2.0, and k is 0.005 to about 2, and j and k sum are about 0.8 to about 3.0.It mainly is that terminal hydroxy group replaces that hydroxyl on organopolysiloxane fluid or the resin replaces.
If wish to form cured compositions, then in the presence of precious metal hydrosilylation catalysts and any desirable inhibitor be that PIB is mixed with each other with siloxane prepolymer and is in the same place, so composition is cured with two components.According to the difference of selected inhibitor, composition can be cured under the effect of heat.
In case form desirable PIB and siloxane prepolymer, just the clearly siloxanes of definition of the SiH functional group that can the PIB precursor of allyl capped is bonded to contain desired amt by means of the hydrosilylation effect.In this case, (30wt% PIB), and if necessary, can add 1-ethynyl-1-hexalin (Aldrich) to postpone or to suppress hydrosilylation polyisobutene can be dissolved in toluene.Have now found that, adopt inhibitor can reduce cure shrinkage significantly.Inhibitor also can produce controlled restraining effect to the reaction between allyl group part and the hydrogen silyl part, and this is as United States Patent (USP) 5,506,289,5,922,795,5,928,564,5,948,339,6,002,039,6,015,853 and 6,034,199 instruct, at this these are all introduced as a reference.The H that adds 500ppm then
2PtCl
6Catalyst solution, and with pouring the Teflon mould into after the solution mixing, build and place it in the baking oven, place down at about 60 ℃ and placed about 24 hours down at about 90 ℃ then in about 48 hours.From baking oven, take out this network sample afterwards.
In order to confirm the efficient of hydrosilylation reactions, the content of extractable matter (sol-fraction) is measured by after fixing.With the network samples weighing, and at room temperature extraction (just be immersed in the toluene, changed a time toluene every about 8 hours) about 48 made its deswelling with a series of mixture of toluene/methanol then to about 72 hours.The concentration of mixture of toluene/methanol can just change 10% every 12 to 24 hours, was about 90 to 10 from toluene to the ratio of methyl alcohol, finished when reaching 100% methyl alcohol.From solvent, take out the network sample then and in about 3 day time, made it in about 60 ℃ vacuum oven, be dried to constant weight.By the network sample before extraction and the weight difference after the extraction and draw the content of colloidal sol.
The present composition can be used as coating to make the barrier of impermeable steam or gas, and this barrier is impervious to S-contained substance.Composition of the present invention thus provides a kind of method of making coated article, wherein said coated article has tolerance to some corrosive gases or vapor action, corrosive gases or steam is sulfurous gas for example, such as hydrogen sulfide, thiomethyl alcohol, sulfurous gas, sulphur trioxide.This coating process or method can make the laminated product that comprises coating of the present invention and substrate, and described substrate is the goods that hope is protected, for example electron device, circuit card or chip.
Because coating of the present invention especially has tolerance or pressuretightness to sulfurous gas, so they are specially adapted to protect the electronic package in the automobile, wherein used silver-colored former tool before this is reactive and tarnish or be corroded in the electronic circuit of electronic package.
This root of pressuretightness can have several different implications according to the difference of purposes.Pressuretightness used herein is meant under 50 ℃ or the higher temperature (the steam umber in per 1,000,000 parts or 1,000,000 parts several parts at 50ppm, ppm) S-contained substance for example exposes two days later in hydrogen sulfide or the thiomethyl alcohol, does not find measurable corrosion or corrosion phenomenon.
Will be appreciated that aforementioned process synthesizes the many component polymer compositions that contain polyisobutene.But, other alkene, for example methylpentene, propylene, what also can both carry out polymerization and generate allyl group or olefinic end group.These materials also can be undertaken crosslinked by the hydrosilylation effect, thus make with by those similar polymerization compositions of polyisobutene deutero-.Make following examples in order to prove the present invention to implement.Following embodiment only is used to explain the present invention, and should not think limitation of the scope of the invention.Scope of the present invention is decided by invention required for protection in the claim.
Embodiment
The method of manufacturing test film (membrane) or film (film)
With the siloxanes is the coating (not containing solvent) of base-material:
1. with clean glass surface of cleaning of releasing agent spraying.
2. become or drip the coating of the shape that is in line at the glass top-pour with transfer pipet.
3. even up paint line with drawing bar, be set desired thickness in the 10-20 mil.
4. this glass was placed 15 minutes in 150 ℃ baking oven.
5. from baking oven, take out glass then and make it be cooled to room temperature.
6. peel off down cured coating carefully from glass, and be cut to 5 " x5 " squared magnitude.
With PIB the coating (with ISOPAR C as solvent, boiling point～100 ℃) of base-material
Step 1,2,3 is that the coating of base-material is described identical with above siloxanes:
4. glass was placed 1 hour in 100 ℃ baking oven.
5. from baking oven, take out glass, and make it be cooled to room temperature.
Peel off down cured coating and be cut to 5 from glass carefully " x5 "
Permeability test method:
The film that will test is cut into the size that meets permeation unit.This unit has one and has wherein introduced test gas (challenge the gas) (H in the nitrogen
2S or thiomethyl alcohol) lower chamber and a upper chamber that is used to take a sample.When test gas when unit bottom infiltrates into the top and passes film, will be taken away by tail gas, and deliver to the quantitative analysis detector.This unit has entrance and exit so that can be to being subjected to examination and gas sampled to carry out dashing continuously sweeping under normal pressure.
The testing permeability process:
The film that will test is cut into the size of the lower chamber that can cover 2-part permeation unit.Lower chamber has the entrance and exit passage, so that test gas can unhinderedly flow through chamber, and can not produce back pressure.Test gas is 50ppmH
2The mixture that S or thiomethyl alcohol form in nitrogen.
The one side of lower chamber has groove.Be placed with a "O in the groove.Because upper chamber places on the lower chamber, thereby the film that covers lower chamber and be stacked and placed on "O has formed sealing.Upper chamber is fixing in position with it by pressure assembly.
Upper chamber also has the entrance and exit passage.Nitrogen is with inswept this passage of the speed of 45 cm per minute.As test gas (H
2S or thiomethyl alcohol) it will be delivered to detector towards sweeping stream by nitrogen when this film is passed in infiltration.
If analyze H
2S then will send into especially at low levels H towards the scavenging body
2S detects and the analyzer (the Jerome-X631-0101 Gold Film Hydrogen Sulfide Analyzer that ArizonaInstrument company makes) of design.
If analyze thiomethyl alcohol, then will send into gas injection apparatus towards the scavenging body, in this device, be introduced into the gas chromatograph that comprises PID that is used for quantitative measurment.
There are several measurement liquid or gas to pass the ASTM method of barrier infiltration, but do not have a kind of method to be appropriate to this application especially.The available reference method is ASTM F739.
The liquid that comes self-circulation to bathe is pumped through described unitary passage so that it is used for cooling or heats this unit.
Test conditions
Cell temperature: 50 ℃
Test gas concentration: 50ppm vol
Overall flow rate: 45 cm per minute
Silicone film-hydrogen sulfide diffusivity
Unit #1 14 ± 2 mil thickness
Test gas 50ppm H
2S
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
Beginning
0 0.00 0.0000
2 0.43 0.0085
38 1.60 0.0315
99 1.70 0.0335
841 1.40 0.0276
901 1.70 0.0335
962 1.30 0.0256
1022 1.20 0.0237
1088 1.50 0.0296
1156 1.50 0.0296
1277 1.70 0.0335
1337 1.80 0.0355
1440 1.60 0.0315
Silicone film-hydrogen sulfide diffusivity (continuing)
Unit #2 14 ± 2 mil thickness
Test gas 50ppm H
2S
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
0 0.00 0.0000
5 3.90 0.0769
68 3.70 0.0729
119 3.80 0.0749
871 3.70 0.0729
931 3.30 0.0650
1110 3.20 0.0631
1176 2.60 0.0531
1237 3.60 0.0710
1298 3.60 0.0710
1470 3.60 0.0710
Silicone film-thiomethyl alcohol diffusivity
Unit #1 14 ± 2 mil thickness
Test gas 50ppm CH
3SH
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
Beginning
0 0.00 0.0000
1 0.00 0.0000
2 0.02 0.0006
4 0.06 0.0017
8 0.76 0.0210
16 1.30 0.0360
63 1.41 0.0390
124 1.37 0.0379
140 1.53 0.0423
184 1.31 0.0362
199 1.42 0.0393
244 1.33 0.0368
259 1.41 0.0390
Silicone film-thiomethyl alcohol diffusivity (continuing)
Unit #2 14 ± 2 mil thickness
Test gas 50ppm CH
3SH
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
0 0.00 0.0000
4 0.06 0.0017
12 2.23 0.0617
34 2.65 0.0733
49 2.45 0.0678
94 2.60 0.0719
154 2.52 0.0697
214 2.51 0.0694
229 2.49 0.0689
Polyolefine (polyisobutene) silicone film-hydrogen sulfide diffusivity
Unit #1 16 ± 2 mil thickness
Test gas 50ppm H
2S
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
0 0.000 0.0000
60 0.001 0.0000
210 0.000 0.0000
1800 0.000 0.0000
1980 0.002 0.0000
2460 0.003 0.0001
2580 0.003 0.0001
2820 0.004 0.0001
3090 0.005 0.0001
3180 0.006 0.0001
4620 0.013 0.0003
5580 0.014 0.0003
5760 0.014 0.0003
Polyolefine (polyisobutene) silicone film-hydrogen sulfide diffusivity
Unit #2 16 ± 2 mil thickness
Test gas 50ppm H
2S
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
0 0.000 0.0000
30 0.000 0.0000
180 0.000 0.0000
1500 0.000 0.0000
2010 0.003 0.0001
2490 0.004 0.0001
2610 0.004 0.0001
2880 0.007 0.0001
3120 0.008 0.0002
3210 0.009 0.0002
4650 0.015 0.0003
5610 0.016 0.0003
5760 0.016 0.0003
Polyolefine (polyisobutene) silicone film-thiomethyl alcohol diffusivity
Unit #1 15 ± 2 mil thickness
Test gas 50ppm CH
3SH
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2My god)
0 0.00 0.0000
60 0.00 0.0000
210 0.00 0.0000
1800 0.00 0.0000
1980 0.00 0.0000
2460 0.00 0.0000
2580 0.00 0.0000
2820 0.00 0.0000
3090 0.00 0.0000
3180 0.00 0.0000
4620 0.00 0.0000
5580 0.00 0.0000
5760 0.00 0.0000
Polyolefine (polyisobutene) silicone film-thiomethyl alcohol diffusivity
Unit #2 15 ± 2 mil thickness
Test gas 50ppm CH
3SH
50 ℃ of temperature
The residence time (minute) amount (ppm) amount (g/m
2-day)
0 0.00 0.0000
30 0.00 0.0000
180 0.00 0.0000
1500 0.00 0.0000
2010 0.00 0.0000
2490 0.00 0.0000
2610 0.00 0.0000
2880 0.00 0.0000
3120 0.00 0.0000
3210 0.00 0.0000
4650 0.00 0.0000
5610 0.00 0.0000
5760 0.00 0.0000
These results show that thickness is that about 10 mils to the barrier film of about 30 mils or the hydrogen sulfide penetration number or the rate of diffusion of film is about 0.0003 gram hydrogen sulfide/square metre film/sky.These results show that also film has stronger resistivity to the conveying of thiomethyl alcohol, do not have thiomethyl alcohol to pass barrier film basically in four day test duration (96 hours).50 ℃ of useful rate of permeation of following hydrogen sulfide is about 0.0010 gram or hydrogen sulfide/square metre film/sky still less, preferred rate of permeation is about 0.0007 gram or hydrogen sulfide still less/square metre film/sky, more preferably rate of permeation is about 0.0005 gram or hydrogen sulfide still less/square metre film/sky, and most preferably rate of permeation is about 0.0003 gram or hydrogen sulfide still less/square metre film/sky.50 ℃ of useful rate of permeation of following thiomethyl alcohol is about 0.0010 gram or thiomethyl alcohol/square metre film/sky still less, preferred rate of permeation is about 0.0007 gram or thiomethyl alcohol still less/square metre film/sky, more preferably rate of permeation is about 0.0005 gram or thiomethyl alcohol still less/square metre film/sky, and most preferably rate of permeation is about 0.0003 gram or thiomethyl alcohol still less/square metre film/sky.These rate of permeation can be used separately or be used in combination to define preferred operating parameters.
Claims (10)
1. coating, it comprises polymer composition, and this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) to pass thickness at 50 ℃ of hydrogen sulfide thus be that about 10 rate of diffusion to the film that comprises described composition of about 30 mils are lower than about 0.0010 gram hydrogen sulfide/square metre film/sky to siloxanes.
2. the coating of claim 1, wherein said rate of diffusion are lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
3. the coating of claim 1, wherein said rate of diffusion are lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
4. coating, it comprises polymer composition, and this polymer composition contains the reaction product of following material:
A) telechelic polyolefin and
B) siloxanes,
Passing thickness at 50 ℃ of thiomethyl alcohol gases thus is that about 10 rate of diffusion to the film that comprises described composition of about 30 mils are lower than about 0.0010 gram thiomethyl alcohol/square metre film/sky.
5. the coating of claim 4, wherein said rate of diffusion are lower than about 0.0005 gram thiomethyl alcohol/square metre film/sky.
6. the coating of claim 1, wherein said polyolefine is a polyisobutene.
7. the coating of claim 1, wherein said polyolefine is a polypropylene.
8. the coating of claim 1, wherein said polyolefine is a polymethylpentene.
9. the coating of claim 6, wherein said rate of diffusion are lower than about 0.0005 gram hydrogen sulfide/square metre film/sky.
10. the coating of claim 6, wherein said rate of diffusion are lower than about 0.0003 gram hydrogen sulfide/square metre film/sky.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910178275A CN101671514A (en) | 2004-05-20 | 2004-05-20 | Solidifiable coating with low permeability on sulfurous gas |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910178275A CN101671514A (en) | 2004-05-20 | 2004-05-20 | Solidifiable coating with low permeability on sulfurous gas |
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|---|---|---|---|
| CNB2004800241356A Division CN100564415C (en) | 2004-05-20 | 2004-05-20 | The hardenable coatings that sulfurous gas is had low-permeability |
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|---|---|
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113330620A (en) * | 2019-01-23 | 2021-08-31 | 大日本印刷株式会社 | Exterior material for all-solid-state battery, method for producing same, and all-solid-state battery |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113330620A (en) * | 2019-01-23 | 2021-08-31 | 大日本印刷株式会社 | Exterior material for all-solid-state battery, method for producing same, and all-solid-state battery |
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