CN109666153A - A kind of hydridization dynamic aggregation compositions and its application - Google Patents

A kind of hydridization dynamic aggregation compositions and its application Download PDF

Info

Publication number
CN109666153A
CN109666153A CN201710966091.8A CN201710966091A CN109666153A CN 109666153 A CN109666153 A CN 109666153A CN 201710966091 A CN201710966091 A CN 201710966091A CN 109666153 A CN109666153 A CN 109666153A
Authority
CN
China
Prior art keywords
cross
dynamic
group
linking
hydrogen bond
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201710966091.8A
Other languages
Chinese (zh)
Inventor
不公告发明人
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xiamen iron cloth Mstar Technology Ltd.
Original Assignee
Weng Qiumei
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Weng Qiumei filed Critical Weng Qiumei
Priority to CN201710966091.8A priority Critical patent/CN109666153A/en
Publication of CN109666153A publication Critical patent/CN109666153A/en
Pending legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F232/00—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system
    • C08F232/08—Copolymers of cyclic compounds containing no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic ring system having condensed rings
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F138/00—Homopolymers of compounds having one or more carbon-to-carbon triple bonds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
    • C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
    • C08F220/10—Esters
    • C08F220/12—Esters of monohydric alcohols or phenols
    • C08F220/14—Methyl esters, e.g. methyl (meth)acrylate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30—Low-molecular-weight compounds
    • C08G18/32—Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3225—Polyamines
    • C08G18/3228—Polyamines acyclic
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/48—Polyethers
    • C08G18/4825—Polyethers containing two hydroxy groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/62—Polymers of compounds having carbon-to-carbon double bonds
    • C08G18/6287—Polymers of sulfur containing compounds having carbon-to-carbon double bonds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666—Compounds of group C08G18/48 or C08G18/52
    • C08G18/667—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
    • C08G18/6681—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38
    • C08G18/6685—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38 with compounds of group C08G18/3225 or polyamines of C08G18/38
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/73—Polyisocyanates or polyisothiocyanates acyclic
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7614—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68—Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/682—Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens
    • C08G63/6822—Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens derived from hydroxy carboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/91—Polymers modified by chemical after-treatment
    • C08G63/912—Polymers modified by chemical after-treatment derived from hydroxycarboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/075—Macromolecular gels
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/08—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/32—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof from compositions containing microballoons, e.g. syntactic foams
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L91/00—Compositions of oils, fats or waxes; Compositions of derivatives thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2201/00—Foams characterised by the foaming process
    • C08J2201/02—Foams characterised by the foaming process characterised by mechanical pre- or post-treatments
    • C08J2201/034—Post-expanding of foam beads or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2333/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2333/04—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters
    • C08J2333/14—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers esters of esters containing halogen, nitrogen, sulfur, or oxygen atoms in addition to the carboxy oxygen
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2349/00—Characterised by the use of homopolymers or copolymers of compounds having one or more carbon-to-carbon triple bonds; Derivatives of such polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2361/00—Characterised by the use of condensation polymers of aldehydes or ketones; Derivatives of such polymers
    • C08J2361/20—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen
    • C08J2361/22—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds
    • C08J2361/24—Condensation polymers of aldehydes or ketones with only compounds containing hydrogen attached to nitrogen of aldehydes with acyclic or carbocyclic compounds with urea or thiourea
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00—Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/04—Polyesters derived from hydroxy carboxylic acids, e.g. lactones
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04—Polyurethanes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2375/00—Characterised by the use of polyureas or polyurethanes; Derivatives of such polymers
    • C08J2375/04—Polyurethanes
    • C08J2375/08—Polyurethanes from polyethers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2391/00—Characterised by the use of oils, fats or waxes; Derivatives thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2445/00—Characterised by the use of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Derivatives of such polymers
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Abstract

The invention discloses a kind of hydridization dynamic aggregation compositions, include at least two component of A, B.Wherein component A is the dynamic aggregation object comprising at least one cross-linked network and simultaneously containing the unsaturated carbon-carbon double bond and supermolecule hydrogen bond action that olefin cross metathesis metathesis reaction can occur；Component B is the catalyst or its compound of the dynamic covalent bond generation exchange reaction in catalyst component A.The composition has merged dynamic covalant character and supermolecule dynamic characteristic；On the one hand dynamic covalent bond assigns material structure stability and mechanical strength under the conditions of uncatalyzed reaction, dynamic reversibility is on the other hand embodied under catalytic reaction condition, and hydrogen bond then assigns material supermolecule dynamic reversibility and stimulating responsive；Its collective effect makes the composition have the characteristics such as self-repairability, recuperability, repeatable processability, can be widely applied to self-repairability material, toughness material, thermal insulation material, shape-memory material, energy storage device material, toy, toy filler etc..

Description

A kind of hydridization dynamic aggregation compositions and its application
Technical field
The present invention relates to intelligent polymer fields, and in particular to a kind of hydridization dynamic aggregation comprising at least two component of A, B Compositions and its application.
Background technique
Crosslinking is that polymer formation three-dimensional net structure is equivalent to reach raising polymer material stability and mechanical property The universal method of fruit.Crosslinking can be (covalent) crosslinking of chemistry either physics (non-covalent/supermolecule) crosslinking.Chemical crosslinking by In the stability and mechanical property etc. that are particularly helpful to promotion polymer material, therefore occupy biggish ratio in crosslinked polymer Example.But when only with chemical crosslinking, if crosslink density is lower, i.e., the chain between crosslinking points is longer or crosslinking points official Energy degree is lower, then often cross-linked polymer is softer, lacks dimensional stability, and mechanical property is bad；And if crosslink density Higher, i.e., the chain between crosslinking points is shorter or crosslinking points degree of functionality is higher, then it is hard and crisp to often lead to cross-linked polymer, easy fragmentation Failure；And general chemical crosslinking lacks dynamic, is chemically crosslinked once being formed, and crosslinking will be unable to change in itself, not only gather The performance for closing object material is immobilized, and is difficult to recycle.
Therefore, it is necessary to develop a kind of novel cross-linked polymer, so that system can either with good stability and power Performance is learned, and there can be excellent dynamic and reusable, to solve problems of the prior art.
Summary of the invention
For above-mentioned background, in order to make polymer obtain good stability and mechanical property, but also with dynamic and can Reusing, the present invention provides a kind of hydridization dynamic aggregation compositions.For this purpose, we introduce dynamic altogether in the polymer Valence link and supermolecule hydrogen bond, with dynamic covalent cross-linking and supermolecule crosslinking replace traditional chemical covalent crosslinking and form hydridization and hand over Networking network.Dynamic covalent cross-linking can maintain the structure and mechanical property of polymer, and supermolecule hydrogen bond crosslinks can be mentioned further High crosslink density enhances its stability and mechanical property；Meanwhile supermolecule hydrogen bond provides dynamic, and dynamic covalent bond is one Being broken under fixed condition and re-forming compensates for the dynamic that chemical crosslinking lacks, and polymer is made to have self-repairability and can return Receive re-workability.
The present invention is achieved by following technical solution:
A kind of hydridization dynamic aggregation compositions comprising at least two component of A, B, which is characterized in that the wherein hydridization Dynamic aggregation compositions component A is comprising at least one cross-linked network and at the same time containing olefin cross metathesis subdivision can occur It solves the unsaturated carbon-carbon double bond of reaction and the hydridization dynamic aggregation object of the hydrogen bond group of supermolecule hydrogen bond action can be formed；Wherein institute The hydridization dynamic aggregation compositions component B stated is the unsaturation in the catalysis hydridization dynamic aggregation compositions component A Catalyst, catalyst composites or the catalyst and catalyst composites of carbon-carbon double bond generation olefin cross metathesis metathesis reaction Mixture；Wherein, when the hydrogen bond group for forming supermolecule hydrogen bond action is only side group hydrogen bond group, contain At least one of structure shown in following formula:
Wherein,Indicate the connection with polymer chain, R is substituent group, and G is end group；Between G,With R it Between, can be cyclic or not cyclic between G and R；Wherein, X respectively stands alone as any one of oxygen atom, sulphur atom, nitrogen-atoms, Y Respectively stand alone as any one of oxygen atom, sulphur atom；Wherein, a is the number for the R being connected with X atom；When X be oxygen atom or When sulphur atom, a 0, R is not present；When X is nitrogen-atoms, a 1, R is respectively individually present.
In one embodiment of the invention, wherein only one in the hydridization dynamic aggregation compositions component A A cross-linked network is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the friendship of dynamic covalent cross-linking simultaneously Connection degree reaches its gel point or more, and the degree of cross linking of supermolecule crosslinking is in its gel point above and below.
In one embodiment of the invention, wherein only one in the hydridization dynamic aggregation compositions component A A cross-linked network is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the friendship of dynamic covalent cross-linking simultaneously Connection degree is in its gel point hereinafter, the degree of cross linking of supermolecule crosslinking is more than its gel point.
In one embodiment of the invention, wherein only one in the hydridization dynamic aggregation compositions component A A cross-linked network is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the friendship of dynamic covalent cross-linking simultaneously Connection degree in its gel point hereinafter, supermolecule crosslinking the degree of cross linking in its gel point hereinafter, but the sum of the two degree of cross linking in gel point More than.
In one embodiment of the invention, wherein containing two in the hydridization dynamic aggregation compositions component A A network；Dynamic covalent cross-linking is contained only in 1st network, the degree of cross linking is more than its gel point；Supermolecule friendship is contained only in 2nd network Connection, the degree of cross linking is more than its gel point.
In one embodiment of the invention, wherein containing two in the hydridization dynamic aggregation compositions component A A network；Covalent cross-linking containing dynamic and supermolecule crosslinking in 1st network, in the cross-linked network simultaneously containing dynamic covalent cross-linking and Supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking is more than its gel point, and the degree of cross linking of supermolecule crosslinking is in its gel Point above and below；Supermolecule crosslinking is contained only in 2nd network, the degree of cross linking is more than its gel point.
In one embodiment of the invention, wherein containing one in the hydridization dynamic aggregation compositions component A A network, wherein the supermolecule degree of cross linking is in its gel point supermolecule below only containing dynamic covalent cross-linking more than gel point Polymer is dispersed in dynamic covalent cross-linking network.
In one embodiment of the invention, wherein containing one in the hydridization dynamic aggregation compositions component A A network is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the degree of cross linking of dynamic covalent cross-linking simultaneously Reach its gel point or more, the degree of cross linking of supermolecule crosslinking is in its gel point above and below；The supermolecule degree of cross linking is in its gel Point supermolecule polymer below is dispersed in dynamic covalent cross-linking network.
In one embodiment of the invention, wherein containing one in the hydridization dynamic aggregation compositions component A A network, wherein only containing dynamic covalent cross-linking more than gel point, supermolecule of the supermolecule degree of cross linking more than its gel point Polymer is dispersed in dynamic covalent cross-linking network with graininess.
In one embodiment of the invention, wherein containing one in the hydridization dynamic aggregation compositions component A A network is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the degree of cross linking of dynamic covalent cross-linking simultaneously Reach its gel point or more, the degree of cross linking of supermolecule crosslinking is in its gel point above and below；The supermolecule degree of cross linking is in its gel Or more supermolecule polymer be dispersed in dynamic covalent cross-linking network with graininess.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is not higher than 25 DEG C.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is not higher than 0 DEG C.
In one embodiment of the invention, wherein the hydridization dynamic aggregation compositions component A all glass Glass transition temperature is no greater than 25 DEG C.
In one embodiment of the invention, wherein the hydridization dynamic aggregation compositions component A all glass Glass transition temperature is no greater than 0 DEG C.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is higher than 25 DEG C and is lower than 40 DEG C.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is not less than 40 DEG C.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is not less than 100 DEG C.
In one embodiment of the invention, wherein the hydridization dynamic aggregation compositions component A all glass Glass transition temperature is all not less than 40 DEG C.
In one embodiment of the invention, wherein the hydridization dynamic aggregation compositions component A all glass Glass transition temperature is all not less than 100 DEG C.
In one embodiment of the invention, wherein at least the one of the hydridization dynamic aggregation compositions component A A glass transition temperature is not higher than 25 DEG C, and at least one glass transition temperature is not less than 100 DEG C.
In one embodiment of the invention, contain in the cross-linked network skeletal chain of the hydridization dynamic aggregation object At least one unsaturated carbon-carbon double bond shown in following formula that olefin cross metathesis metathesis reaction occurs:
Wherein,Indicate the connection with polymer chain or any other suitable group or atom.
In one embodiment of the invention, wherein can be formed in the hydridization dynamic aggregation compositions component A When the hydrogen bond group of supermolecule hydrogen bond action is only side group hydrogen bond group, wherein it is former that R, G are each independently selected from hydrogen atom, halogen Son, C1-20Alkyl, C1-20Miscellaneous alkyl, substituted C1-20Alkyl or substituted miscellaneous alkyl.
In one embodiment of the invention, wherein can be formed in the hydridization dynamic aggregation compositions component A When the hydrogen bond group of supermolecule hydrogen bond action is only side group hydrogen bond group, wherein R, G be each independently selected from hydrogen atom, fluorine atom, Chlorine atom, bromine atom, iodine atom, methyl, ethyl, n-propyl, isopropyl, butyl, amyl, hexyl, heptyl, octyl, nonyl, the last of the ten Heavenly stems Base, undecyl, dodecyl, tridecyl, myristyl, pentadecyl, cetyl, heptadecyl, octadecyl, ten Nine alkyl, eicosyl, allyl, acrylic, vinyl, phenyl, aminomethyl phenyl, butyl phenyl, benzyl, methoxycarbonyl, Ethoxy carbonyl, phenyloxycarbonyl, benzyloxycarbonyl, methyl mercapto carbonyl, ethylmercapto group carbonyl, thiophenyl carbonyl, benzylthio carbonyl, B aminocarbonyl, benzylaminocarbonyl, methoxyl group thiocarbonyl, ethyoxyl thiocarbonyl, phenoxythiocarbonyl, benzyloxy are thio Carbonyl, methyl mercapto thiocarbonyl, ethylmercapto group thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, substituted C1-20Alkane Base, substituted C1-20Alkenyl, substituted aryl, substituted aryl, substituted C1-20Rouge miscellaneous alkyl, replaces substituted heteroaryl Heteroaryl alkyl, substituted C1-20Alkoxy carbonyl, substituted aryloxycarbonyl, substituted C1-20Alkyl sulfenyl carbonyl replaces Artyl sulfo carbonyl, substituted C1-20Alkoxy carbonyl, substituted aryloxy thiocarbonyl, substituted C1-20Alkyl Alkylthio carbonyl, substituted artyl sulfo thiocarbonyl.
In one embodiment of the invention, wherein also containing amino, hydroxyl, carboxylic in the hydridization dynamic aggregation object At least one of base, amide groups, thioamides base, pyrrolidone-base, imidazole radicals, pyrazolyl, nitrogen oxazolyl and its derivative base As side group hydrogen bond group.
In one embodiment of the invention, wherein in the hydridization dynamic aggregation object simultaneously containing at least one kind Contain the hydrogen bond group of hydrogen bond donor and hydrogen bond receptor as main chain backbone hydrogen bond group, side chain skeleton hydrogen bond group, terminal hydrogen Key group or in which any two, three kinds of combination, wherein containing the hydrogen bond base of hydrogen bond donor and hydrogen bond receptor while described At least one secondary amino group is preferably comprised in group；
Wherein, when containing the hydrogen bond group of hydrogen bond donor and hydrogen bond receptor when described while and being located at main chain and/or side chain, At least one of its further preferably following constituent:
Wherein,Indicate the connection with polymer chain；
Wherein, when containing the hydrogen bond group of hydrogen bond donor and hydrogen bond receptor when described while and being located at end group, more preferably Contain at least one of following constituent:
Wherein,Indicate the connection with polymer chain, L is end group；It can be cyclic or not cyclic with L；Z is respectively only It is vertical to be selected from oxygen atom or sulphur atom.
In one embodiment of the invention, wherein the hydridization dynamic aggregation object, which contains at least one, is no more than four The hydrogen bond group of tooth.
In one embodiment of the invention, wherein the hydridization dynamic aggregation object contains two or more institute The hydrogen bond group stated.
In one embodiment of the invention, wherein at least a kind of hydrogen bond group is located at institute in the hydrogen bond group The side group or side chain or side group and side chain for the hydridization dynamic aggregation object stated.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that main chain is carbon-chain structure or carbon heterochain The polymer segment of structure.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that main chain is the poly- of element heterochain structure Polymer segments.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that glass transition temperature is not higher than 25 DEG C polymer segment.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that glass transition temperature is not higher than 0 DEG C polymer segment.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that glass transition temperature is higher than 25 DEG C And the polymer segment lower than 40 DEG C.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that glass transition temperature is not less than 40 DEG C polymer segment.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of key and the polymer segment of hydrogen bond group, hydrogen bond group and hydrogen bond group are not less than for glass transition temperature 100 DEG C of polymer segment.
In one embodiment of the invention, wherein for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalently At least one of polymer segment of key and hydrogen bond group, hydrogen bond group and hydrogen bond group is that glass transition temperature is not higher than 25 DEG C polymer segment, and at least one be not less than 100 DEG C of polymer segment for glass transition temperature.
In one embodiment of the invention, component B is to have without catalytic activity but under ultraviolet irradiation under normal conditions There is the catalyst of catalytic activity.
In one embodiment of the invention, the hydridization dynamic aggregation compositions have following any character: Ordinary solid, elastomer, gel, foam.
In one embodiment of the invention, the recipe ingredient for constituting the hydridization dynamic aggregation compositions further includes It is any below or appoint it is several can additive or usable object: other polymers, auxiliary agent, filler, sweller.Wherein, described Other polymers preferably are selected from following any or appoint several: natural polymer, synthetic macromolecular compound；Described helps Agent preferably is selected from following any or appoints several: catalyst, initiator, antioxidant, light stabilizer, heat stabilizer, dispersing agent, cream Agent, fire retardant, toughener, coupling agent, solvent, lubricant, release agent, plasticizer, thickener, thixotropic agent, levelling agent, coloring Agent, fluorescent whitening agent, delustering agent, antistatic agent, dehydrating agent, biocide mildewcide, foaming agent, blowing promotor, nucleating agent, rheology Agent；The filler preferably is selected from following any or appoints several: inorganic non-metallic filler, metal packing, organic filler；Described Sweller preferably is selected from following any or appoints several: water, organic solvent, ionic liquid, oligomer, plasticizer.
In one embodiment of the invention, the hydridization dynamic aggregation compositions are applied to following material or system Product: self-repairability coating, self-repairability plate, self-repairability sealing material, self-repairability block glue, self-repairability conducting resinl, Toughness material, tough elastomer material, thermal insulation material, shape-memory material, energy storage device material, toy, toy filler.
Compared with prior art, the invention has the following advantages:
(1) a kind of hydridization dynamic aggregation compositions of the invention include simultaneously dynamic covalent cross-linking and hydrogen bond crosslinks.Its In, on the one hand dynamic covalent cross-linking is the necessary condition for maintaining polymer architecture, on the other hand specific as polymerization linking point Under conditions of embody dynamic, assign material self-repairability and can re-workability；On the one hand supermolecule hydrogen bond crosslinks are used for dynamic State covalent cross-linking carries out crosslinking supplement, enhances its stability and mechanical property, on the other hand for providing based on its dynamic Specific performance assigns the good toughness of material, self-repairability and reusing.Dynamic covalent cross-linking and supermolecule hydrogen bond are handed over Connection combines, so that the material based on such hydridization dynamic aggregation compositions is not only had excellent performance, and can reuse, It can satisfy the ecological requirements growing to new material, this cannot achieve in existing polymeric system.
(2) the dynamic covalent bond in a kind of hydridization dynamic aggregation compositions of the invention is to be based on that olefin cross can occur The characteristics of unsaturated carbon-carbon double bond of transposition metathesis reaction, the reaction, is the crosslink density of polymer network before and after reacting not Become, this characteristic can make the topological structure of polymer network remain unchanged, and material property is made to keep stablizing.Moreover, of the invention Selectable catalyst be also it is diversified, reasonably select the adjustable dynamic covalent bond of different catalyst and embody dynamic With temperature, the pH value of self-repairability etc., achieve the purpose that performance of control.Also, since unsaturated carbon-carbon double bond has centainly Special reaction activity, polymer material and product after molding still remain that further progress is modified or functionalization can Can, expand application range.In addition, the chemical raw material containing unsaturated carbon-carbon double bond is easy to get, it is suitble to industrialized production.
(3) a kind of network structure of hydridization dynamic aggregation compositions of the invention can be diversified.Wherein, institute The supermolecule crosslinking stated both can form cross-linked network in the same network together with dynamic covalent cross-linking, can also independent shape At dynamic crosslinking network, it can also be individually formed the particle of dynamic crosslinking, can also be dispersed in noncrosslinking polymer form In dynamic covalent cross-linking network.In different polymer architectures, the supermolecule hydrogen bond can play its dynamic, special It is not strain-responsive.Also, different structure respectively has feature again, can give full play to respective advantage.For example, when supermolecule is handed over When connection is respectively formed interpenetrating or Semi-IPN two networks with dynamic covalent cross-linking, comprehensive effectiveness can be preferably played；For another example, When two networks all contain supermolecule crosslinking, collaboration or orthogonal dynamic can be provided using the supermolecule crosslinking in two networks State property.In addition, hydrogen bond group of the invention is usually urethane bond, urea bond derivative etc., excellent effect and can be very It is conveniently synthesized, is suitble to industrialized production.
(4) a kind of hydridization dynamic aggregation compositions of the invention have good Modulatory character.Pass through control raw material The parameters such as molecular structure, molecular weight can be prepared with different appearance features, the dynamic aggregation object that performance is adjustable, widely used； By controlling position, type and the number of hydrogen bond group, dynamic reversibility dynamic aggregation object of different strengths and weaknesses can be prepared；Pass through The ratio for controlling both dynamic covalent cross-linking and supermolecule hydrogen bond crosslinks ingredient, can prepare mechanical strength, self-repairability, shape The multifarious hydridization dynamic aggregation compositions such as shape memory.
(5) method and approach of preparation hydridization dynamic aggregation compositions provided by the invention are varied, are preparing Other additives can also be added in journey according to actual needs to be modified hydridization dynamic aggregation compositions material, extend material The application performance of material.
With reference to following embodiments explanation, embodiment and the appended claims, these and other features of the invention with And advantage will become obvious.
Specific embodiment
The present invention relates to a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B, wherein component A is packet Containing at least one cross-linked network and at the same time containing can occur olefin cross metathesis metathesis reaction unsaturated carbon-carbon double bond and The hydridization dynamic aggregation object of the hydrogen bond group of supermolecule hydrogen bond action can be formed；Component B is the unsaturated carbon carbon in catalyst component A The catalyst and/or its compound of double bond generation olefin cross metathesis metathesis reaction.
In order to illustrate simplicity the term is indicated using conjunction "and/or" in the description of the invention It may include the option selected from the conjunction "and/or" foregoing description, or described option after conjunction "and/or", Or it is simultaneously selected from described these three situations of option before and after conjunction "and/or".
In the following, first the polymers compositions A in the present invention is described in detail.
Heretofore described " polymerization " reaction/action be chain propagation process/effect, namely by intermolecular reaction/ Effect (including covalent chemical reaction and supermolecule hydrogen bond action) formation straight chain, branching, ring, two-dimensional/three-dimensional cluster, three-dimensional are unlimited The polymer of network structure.
Term " crosslinking " reaction/action used in the present invention, refer to intermolecular and/or intramolecular by covalent bond and/ Or supermolecule hydrogen bond action forms the process with three-dimensional unlimited reticular pattern product.In cross-linking process, polymer chain is generally first Constantly increase in two-dimensional/three-dimensional direction, gradually form cluster (can be two dimension or three-dimensional), developing deeply is three-dimensional infinite net Network.Therefore, crosslinking can be considered as a kind of special shape of polymerization.In cross-linking process, just reach a three-dimensional infinite network When the degree of cross linking, referred to as gel point, also referred to as percolation threshold.The cross-linking products (contained, similarly hereinafter) more than gel point, have Three-dimensional infinite network structure, cross-linked network constitute an entirety and across entire polymer architectures；In gel point friendship below Co-product, is only lax interchain link structure, and not formed three-dimensional infinite network structure, and is not belonging to across entire polymerization The cross-linked network that can constitute an entirety of object structure.Unless stated otherwise, the present invention in cross-linked structure be gel point with On three-dimensional infinite network structure, non-crosslinking structure includes the line style that the degree of cross linking is zero and non-linearity structure and gel point or less Two-dimensional/three-dimensional cluster structure.
In the present invention, " skeleton " refers to structure on the chain length direction of polymer chain.It is described for cross-linked polymer " main chain ", refer to any segment being present in cross-linked network skeleton.It is described for the polymer of non-crosslinking structure " main chain " refers to the most chain of chain link if not otherwise indicated.Wherein, " side chain " refers to same main polymer chain phase Connect and be distributed in the chain structure of main chain side；Wherein, " branch "/" bifurcated chain " can be side chain and be also possible to other The chain structure come out from any chain bifurcated.Wherein, " side group " refers to that any chain of same polymer is connected and is distributed in The chemical group of chain side.Wherein, " end group " refers to that any chain of same polymer is connected and is located at the change of chain end Learn group.If not otherwise indicated, side group refers in particular to group of the molecular weight no more than 1000Da for being connected to polymer chain skeleton side And subunit group therein.When the molecular weight of side chain, branch, bifurcated chain is no more than 1000Da, itself and group thereon are regarded For side group.For the sake of simplicity, if not otherwise indicated, side chain, branch and bifurcated chain are collectively referred to as side chain.Above-mentioned " side chain ", " side Base " can have multilevel structure namely side chain/side group that can continue with side chain/side group, side chain/side group side chain/side group It can continue have side chain/side group.In the present invention, if not otherwise indicated, for hyperbranched and dendroid chain and its relevant link Structure, the polymer segment of outermost can be considered as side chain, and rest part can be considered as main chain.
Heretofore described " dynamic covalent cross-linking network " is referred to when supermolecular mechanism is all disconnected in covalent cross-linking network It opens when only remaining common covalent bond and dynamic covalent bond, still with the polymer network of the above structure of gel point；And when dynamic is total When valence link also all disconnects, original crosslinked polymer network dissociation resolves into following any or appoints several secondary units: monomer gathers Close object chain segment, polymer cluster, polymer beads more than gel point etc..
Heretofore described " supermolecule cross-linked network " refers to all disconnecting only when the dynamic covalent bond in cross-linked network When remaining common covalent bond and supermolecule hydrogen bond, still with the polymer network of the above structure of gel point；And work as supermolecule hydrogen bond When also all disconnecting, following any or several secondary units: monomer, polymer are resolved into original crosslinked polymer network dissociation Chain segment, polymer cluster, polymer beads more than gel point etc..
Heretofore described " common covalent bond ", what is referred to is traditional covalent in addition to dynamic covalent bond Key, under typical temperature (is generally not more than 100 DEG C) and (generally less than 1 day) is more difficult in the usual time is broken comprising But it is not limited only to common carbon-carbon bond, carbon-oxygen bond, carbon-hydrogen link, carbon-nitrogen bond, carbon-sulfide linkage, nitrogen-hydrogen bond, nitrogen-oxygen key, hydrogen-oxygen Key, nitrogen-nitrogen key etc..
Heretofore described " dynamic covalent bond ", refers to the unsaturated carbon carbon that olefin cross metathesis metathesis reaction can occur Double bond.Wherein, " the olefin cross metathesis metathesis reaction " refers to the unsaturated carbon carbon by metal olefin complex catalysis Carbon skeleton rearrangement reaction between double bond.Wherein, described " rearrangement reaction " refers to, new carbon-carbon double bond generates in elsewhere and with old Carbon-carbon double bond dissociate, to generate the exchange of chain and the variation of polymer local topology.For the purpose of the present invention, exist In this rearrangement process, due to the particularity of reaction, the crosslink density of polymer network is basically unchanged.Wherein, described " can occur " Refer to, in the presence of a suitable catalyst, when temperature condition, pressure condition, olefin cross metathesis metathesis reaction can be with It carries out.
Heretofore described " supermolecular mechanism " only refers to supermolecule hydrogen bond action, referred to as " hydrogen bond action " or " hydrogen Key ".
In embodiments of the present invention, cross-linked network included in hydridization dynamic aggregation object component A at least one, Either single one network, there can also be the multiple networks being mutually blended, there can also be multiple networks of interpenetrating, it can also be with Exist simultaneously blending and interpenetrating, etc.；It can using any appropriate crosslinking topological structure, chemical structure, reactive mode and A combination thereof etc..Wherein, when the cross-linked network quantity included in the hydridization dynamic aggregation object component A is two or more, these Network can be identical or different；Can be subnetwork only and include dynamic covalent cross-linking and subnetwork only includes that supermolecule is handed over The combination of connection, or part only include dynamic covalent cross-linking and part while being crosslinked comprising dynamic covalent cross-linking and supermolecule Combination, or the group that part is only crosslinked comprising dynamic covalent cross-linking and supermolecule comprising supermolecule crosslinking and part simultaneously It all simultaneously include dynamic covalent cross-linking and supermolecule crosslinking in conjunction or each network, but the present invention is not limited only to this.By It is crosslinked simultaneously comprising dynamic covalent cross-linking and supermolecule in the cross-linked network of hydridization dynamic aggregation object component A of the present invention, therefore, The polymer network is known as " hybrid cross-linked network ".
(the first network structure) in a preferred embodiment of the present invention, the hydridization dynamic aggregation object component Only one cross-linked network in A is crosslinked in the cross-linked network simultaneously containing dynamic covalent cross-linking and supermolecule, wherein dynamic is altogether The degree of cross linking of valence crosslinking reaches its gel point or more, and the degree of cross linking of supermolecule crosslinking is in its gel point above and below.The network Structure structure is simple, can keep balanced structure by dynamic covalent cross-linking, supermolecule crosslinking provides dynamic；In specific item Under part, dynamic covalent cross-linking also can provide covalent dynamic.
In another preferred embodiment of the invention (second of network structure), the hydridization dynamic aggregation object Only one cross-linked network in component A is crosslinked in the cross-linked network simultaneously containing dynamic covalent cross-linking and supermolecule, wherein dynamic The degree of cross linking of state covalent cross-linking is in its gel point hereinafter, the degree of cross linking of supermolecule crosslinking is more than its gel point.The network structure With good dynamic, it is based particularly on the strain-responsive of supermolecule crosslinking；Dynamic covalent cross-linking does not keep flat directly Weigh structure, but under given conditions, dynamic covalent cross-linking also can provide the work that additional covalent dynamic plays regulation performance With.
In another preferred embodiment of the invention (the third network structure), the hydridization dynamic aggregation object Only one cross-linked network in component A is crosslinked in the cross-linked network simultaneously containing dynamic covalent cross-linking and supermolecule, wherein dynamic The degree of cross linking of state covalent cross-linking in its gel point hereinafter, supermolecule crosslinking the degree of cross linking in its gel point hereinafter, but the two be crosslinked The sum of degree is more than gel point.Dynamic covalent cross-linking and the degree of cross linking of supermolecule crosslinking are lower in the network structure, network knot The whole degree of cross linking of structure is not high, and dynamic covalent cross-linking and supermolecule crosslinking extremely close the effect for providing balanced structure regulation performance It is important.
In another preferred embodiment of the present invention (the 4th kind of network structure), the hydridization dynamic aggregation object group Divide in A containing there are two networks；Dynamic covalent cross-linking is contained only in 1st network, the degree of cross linking is more than its gel point；In 2nd network Supermolecule crosslinking is contained only, the degree of cross linking is more than its gel point.In the network structure, the 2nd network has good dynamic, the 1 network provides balanced structure, by the interpenetrating of two networks or the combinations such as Semi-IPN, can preferably play comprehensive effect Energy；Under given conditions, dynamic covalent cross-linking also can provide additional covalent dynamic and play the role of regulation performance.
In another preferred embodiment of the present invention (the 5th kind of network structure), the hydridization dynamic aggregation object group Divide in A containing there are two networks；Covalent cross-linking containing dynamic and supermolecule are crosslinked in 1st network, simultaneously containing dynamic in the cross-linked network State covalent cross-linking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking is more than its gel point, the friendship of supermolecule crosslinking Connection degree is in its gel point above and below；Supermolecule crosslinking is contained only in 2nd network, the degree of cross linking is more than its gel point.The net In network structure, by combinations such as the interpenetrating of two networks, comprehensive effectiveness can be preferably played；And two can be used Supermolecule crosslinking in network provides collaboration or orthogonal dynamic.
In another preferred embodiment of the present invention (the 6th kind of network structure), the hydridization dynamic aggregation object group Contain a network in point A, wherein only containing dynamic covalent cross-linking more than gel point, the supermolecule degree of cross linking its gel point with Under supermolecule polymer be dispersed in dynamic covalent cross-linking network.In the network structure, dynamic covalent cross-linking can keep flat Weigh structure, and under given conditions, dynamic covalent cross-linking also can provide covalent dynamic；Supermolecule polymer dispersed therein Dynamic, especially strain-responsive are provided.
In another preferred embodiment of the present invention (the 7th kind of network structure), the hydridization dynamic aggregation object group Divide and contain a network in A, is crosslinked simultaneously containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein dynamic is covalent The degree of cross linking of crosslinking reaches its gel point or more, and the degree of cross linking of supermolecule crosslinking is in its gel point above and below；Supermolecule is handed over Connection degree is dispersed in dynamic covalent cross-linking network in its gel point supermolecule polymer below.In the network structure, dynamic is altogether Valence crosslinking can keep balanced structure, and under given conditions, dynamic covalent cross-linking also can provide covalent dynamic；Supermolecule is handed over Connection provides dynamic, and supermolecule polymer dispersed therein provides supplement dynamic, especially strain-responsive.
In another preferred embodiment of the present invention (the 8th kind of network structure), the hydridization dynamic aggregation object group Contain a network in point A, wherein only containing dynamic covalent cross-linking more than gel point, the supermolecule degree of cross linking its gel point with On supermolecule polymer be dispersed in dynamic covalent cross-linking network with graininess.In the network structure, dynamic covalent cross-linking Balanced structure can be kept, under given conditions, dynamic covalent cross-linking also can provide covalent dynamic；Supermolecule polymer Grain provides filling and dynamic, and local viscosity and intensity can be obtained in strain-responsive and is increased.
In another preferred embodiment of the present invention (the 9th kind of network structure), the hydridization dynamic aggregation object group Divide and contain a network in A, is crosslinked simultaneously containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein dynamic is covalent The degree of cross linking of crosslinking reaches its gel point or more, and the degree of cross linking of supermolecule crosslinking is in its gel point above and below；Supermolecule is handed over Supermolecule polymer of the connection degree more than its gel point is dispersed in dynamic covalent cross-linking network with graininess.The network structure In, dynamic covalent cross-linking can keep balanced structure, and under given conditions, dynamic covalent cross-linking also can provide covalent dynamic Property；Supermolecule crosslinking provides dynamic, and supermolecule polymer particle provides filling and supplement dynamic, and can in strain-responsive Increased with obtaining viscosity and the intensity of part.
In the present invention, there can also be other diversified embodiments.Those skilled in the art can be according to this The logic and train of thought of invention, are rationally and effectively realized.
In embodiments of the present invention, the hydridization dynamic aggregation compositions component A can not have vitrifying Transition temperature can have one or more glass transition temperature.Wherein, a kind of preferred embodiment is described Hydridization dynamic aggregation compositions component A at least one glass transition temperature be not higher than 25 DEG C, more preferably not above 0 DEG C, more preferably glass transition temperature all when there are multiple glass transition temperatures is not higher than 25 DEG C, most preferably all glass Change temperature and be not higher than 0 DEG C, helps to embody dynamic and self-repairability of the supermolecule hydrogen bond when room temperature and low temperature use, just In materials or products such as acquisition adhesive, elastomer, gels；Another preferred embodiment is the hydridization dynamic aggregation At least one glass transition temperature of compositions component A is higher than 25 DEG C but lower than 40 DEG C, and it is more steady to help to obtain size Fixed and moving state property is moderate, the higher elastomer of temperature sensitivity, foam and ordinary solid etc.；Another preferred embodiment is At least one glass transition temperature of the hydridization dynamic aggregation compositions component A is not less than 40 DEG C, more preferably not Lower than 100 DEG C, more preferably glass transition temperature all when there are multiple glass transition temperatures is not less than 40 DEG C, most preferably when depositing In multiple glass transition temperatures, all glass transition temperatures are not less than 100 DEG C, facilitate embody material at high temperature dimensional stability, The characteristics such as the hardness under shape memory, low temperature and room temperature, the readily available gel with property, foam, ordinary solid Equal materials or product；Another preferred embodiment is at least one of the hydridization dynamic aggregation compositions component A Glass transition temperature is not higher than 25 DEG C, and in addition at least one glass transition temperature is not less than 100 DEG C, can take into account low temperature And high-temperature behavior.
In embodiments of the present invention, alkene can occur containing at least one in hydridization dynamic aggregation compositions component A The unsaturated carbon-carbon double bond of hydrocarbon cross metathesis metathesis reaction, polymerization linking point or crosslinking link as dynamic aggregation object Point exists as polymerization linking point and crosslinking linking point simultaneously.In addition, the present invention be not excluded for carbon-carbon double bond as side group, End group and the group of other positions exist.In the present invention, unless making the unsaturated carbon carbon using specific method Irreproducibility dissociation occurs for double bond, and otherwise degradability variation will not occur for covalent cross-linking network and covalent polymer chain.It is preferred that can The unsaturated carbon-carbon double bond that olefin cross metathesis metathesis reaction occurs exists only on the chain backbone of cross-linked network.
In embodiments of the present invention, the unsaturated carbon-carbon double bond that olefin cross metathesis metathesis reaction occurs Type be not particularly limited, at least one small reaction work of steric hindrance shown in following formula is contained preferably in cross-linked network skeletal chain The high structure of property:
Wherein,Indicate the connection with polymer chain or any other suitable group/atom (including hydrogen atom). It is such when what is hereinafter occurred againAbove-mentioned definition and range are all continued to use, such as without special case, no longer progress repeated explanation.
In the present invention, the hydrogen bond group for forming supermolecule hydrogen bond action includes being present in polymer chain skeleton Go up the hydrogen bond group (calling " skeleton hydrogen bond group " in the following text) of (including on main chain/side chain/branch/bifurcated chain backbone) and in polymerization The hydrogen bond base of hydrogen bond group (calling " side group hydrogen bond group " in the following text) and polymer chain and other compound ends in object chain side group Group's (calling " end group hydrogen bond group " in the following text).The skeleton hydrogen bond group refers to that at least one atom in the group directly participates in The building polymer chain skeleton, including main polymer chain, side chain, branch, bifurcated chain skeleton；The side group hydrogen bond base Group, refers to all atoms on the group in side group；The end group hydrogen bond group refers to all atoms on the group On end group.
In embodiments of the present invention, the hydrogen bond group can be with skeleton hydrogen bond group, side group hydrogen bond group, end The combination of any one or more of the forms such as base hydrogen bond group is present in the hydridization dynamic aggregation compositions.Due to Part hydrogen bond, which does not have directionality and selectivity, can form hydrogen bond under specific circumstances between the hydrogen bond group of different location Effect, can form between each other between the hydrogen bond group of identical or different position in identical or different polymer molecule Hydrogen bond action, can also be with the other compositions in polymer as contained by optional other polymers molecule, filler, small molecule etc. Hydrogen bond group between form hydrogen bond action.As an example, the hydrogen bond action in the present invention includes but is not limited to such as: the side chain And/or the hydrogen bond group in side group forms interchain hydrogen bond crosslinking between different molecular；Hydrogen bond base in the side chain and/or side group Interchain hydrogen bond crosslinking is formed in group and the main chain backbone between hydrogen bond group；Hydrogen bond in the part side chain and/or side group Chain inner ring is independently formed with hydrogen bond between group；It is independently formed between hydrogen bond group in the main chain backbone of part with hydrogen bond Chain inner ring；Hydrogen bond group collective effect in the part side chain and/or side group forms chain inner ring etc. with hydrogen bond.It may be noted that It is to be not excluded for part in the present invention to be formed by intrachain hydrogen bond effect neither formation inter-chain action, does not also form chain inner ring, only shape The effects of at grafting is included but are not limited to.
In the preferred embodiment of the present invention, only contain side in the hydridization dynamic aggregation compositions component A Base hydrogen bond group；In another preferred embodiment of the invention, contained only in the hydridization dynamic aggregation compositions component A There is main chain backbone hydrogen bond group；In another preferred embodiment of the invention, the hydridization dynamic aggregation compositions group Divide and only contains side chain skeleton hydrogen bond group in A；In another preferred embodiment of the invention, the hydridization dynamic aggregation object Only contain side chain end group hydrogen bond group in composition component A；In another preferred embodiment of the invention, the hydridization is dynamic Only contain main chain end group hydrogen bond group in state polymer composition components A；In another preferred embodiment of the invention, institute It states and only contains pendant hydrogen key group and side chain skeleton hydrogen bond group in hydridization dynamic aggregation compositions component A；Of the invention In another preferred embodiment, pendant hydrogen key group and main chain are only contained in the hydridization dynamic aggregation compositions component A Skeleton hydrogen bond group；In another preferred embodiment of the invention, in the hydridization dynamic aggregation compositions component A only Contain side group hydrogen bond group and main chain end group hydrogen bond group；In another preferred embodiment of the invention, the hydridization is dynamic Only contain pendant hydrogen key group and side chain end group hydrogen bond group in state polymer composition components A；It is excellent in another kind of the invention It selects in embodiment, side chain end group hydrogen bond group and main chain backbone is only contained in the hydridization dynamic aggregation compositions component A Hydrogen bond group；In another preferred embodiment of the invention, only contain in the hydridization dynamic aggregation compositions component A Side chain end group hydrogen bond group and main chain end group hydrogen bond group；In another preferred embodiment of the invention, the hydridization is dynamic Only contain main chain end group hydrogen bond group and main chain backbone hydrogen bond group in state polymer composition components A；Of the invention another In kind preferred embodiment, pendant hydrogen key group, side chain terminal hydrogen are only contained in the hydridization dynamic aggregation compositions component A Key group and main chain backbone hydrogen bond group；In another preferred embodiment of the invention, the hydridization dynamic aggregation object group Only contain pendant hydrogen key group, side chain end group hydrogen bond group and main chain end group hydrogen bond group in polymer component A；Of the invention another In a kind of preferred embodiment, pendant hydrogen key group, side chain end group are only contained in the hydridization dynamic aggregation compositions component A Hydrogen bond group and side chain skeleton hydrogen bond group；In another preferred embodiment of the invention, the dynamic aggregation object combination Only contain pendant hydrogen key group, side chain skeleton hydrogen bond group and main chain end group hydrogen bond group in object component A；Of the invention another In kind preferred embodiment, pendant hydrogen key group, side chain skeleton hydrogen are only contained in the hydridization dynamic aggregation compositions component A Key group, side chain end group hydrogen bond group and main chain backbone hydrogen bond group；It is described in another preferred embodiment of the invention Only contain pendant hydrogen key group, side chain skeleton hydrogen bond group, side chain end group hydrogen bond base in hydridization dynamic aggregation compositions component A Group and main chain end group hydrogen bond group；In another preferred embodiment of the invention, the hydridization dynamic aggregation compositions In component A containing side group hydrogen bond group, side chain end group hydrogen bond group, side chain skeleton hydrogen bond group, main chain end group hydrogen bond group and Main chain backbone hydrogen bond group.But the present invention is not limited only to this.
In embodiments of the present invention, since the general quantity of main chain backbone hydrogen bond group is than relatively limited and not easy to control, And the side chain/side group hydrogen bond group can before polymerized/cross-linked, later or in the process generate, before or after generate Quantity can be than relatively freely controlling, and side chain/side group hydrogen bond freedom degree is higher is more prone to produce dynamic, therefore, It is preferred that side chain and/or side group hydrogen bond group.The link structure of side chain/between side group hydrogen bond group and chain backbone, length and its this The structure of body includes that substituent group and side group etc. can carry out diversified adjusting, so that it is steady to control HYDROGEN BOND INTENSITY, steric hindrance, heat Qualitative, glass transition temperature etc., and then regulate and control dynamic property, assign the different ultra-tough of polymer, selfreparing, strain-responsive The performances such as property, shape memory.
In embodiments of the present invention, the hydrogen bond action in the supermolecular mechanism by hydrogen bond group donor (H, Namely hydrogen atom) and receptor (Q, that is, receive the electronegative atom of hydrogen atom) interaction formed, can be times The meaning number of teeth.Wherein, the number of teeth refers to being formed by hydrogen bond quantity, each H ... Q group by the donor and receptor of hydrogen bond group It is combined into a tooth.In following formula, the bonding situation of the schematically illustrate tooth of difference, two teeth and three tooth hydrogen bonds.
The bonding situation of one tooth, two teeth and three tooth hydrogen bonds can concrete example it is as follows:
In embodiments of the present invention, the number of teeth of hydrogen bond is not limited.The number of teeth of hydrogen bond is more, and synergistic effect is got over Greatly, the intensity of hydrogen bond is bigger.If the number of teeth for being formed by hydrogen bond is more, intensity is big, then the dynamic of hydrogen bond action is just It is weak, it can be used as structural hydrogen bond and play promotion dynamic aggregation object holding balanced structure and improve mechanical property (modulus and intensity) Effect.If the number of teeth of formed hydrogen bond is few, intensity is low, and the dynamic of hydrogen bond action is with regard to strong.It is a kind of preferred in the present invention Embodiment for select be no more than four teeth hydrogen bond dynamic is provided；Another preferred embodiment is to select two kinds or two Kind or more hydrogen bond group form the different hydrogen bond of dynamic, multi-level dynamic is provided.
In embodiments of the present invention, when the hydrogen bond group is only side group hydrogen bond group, containing following logical At least one of structure shown in formula (4), (5):
Wherein,Indicate the connection with polymer chain, R is substituent group, and G is end group；Between G,With R it Between, can be cyclic or not cyclic between G and R.
Wherein, X respectively stands alone as any one of oxygen atom, sulphur atom, nitrogen-atoms, and it is former that Y respectively stands alone as oxygen atom, sulphur Any one of son.
Wherein, a is the number for the R being connected with X atom.
When X is oxygen atom or sulphur atom, a 0, R is not present.
When X is nitrogen-atoms, a 1, R is respectively individually present.
R, the structure of G is not particularly limited, and respectively independent includes but is not limited to linear chain structure, the branched structure containing side group Or cyclic structure.Wherein, cyclic structure is not particularly limited, and can be selected from aliphatic ring, aromatic ring, saccharide ring, condensed ring, preferably Aliphatic ring.
R, the structure of G is respectively independently preferably linear chain structure.
R can contain hetero atom, can also be free of hetero atom；G can contain hetero atom, can also be free of hetero atom.
R, the carbon atom number of G is not particularly limited, and respectively independent is preferably 1~20, respective independent more preferably 1~ 10。
R, G is each independently selected from hydrogen atom, halogen atom, C1-20Alkyl, C1-20Miscellaneous alkyl, substituted C1-20Alkyl takes The miscellaneous alkyl in generation.Wherein, the substitution atom in R, G or substituent group are not particularly limited, and are each independently selected from halogen atom, alkyl Substituent group contains heteroatomic substituent group.
R, G is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Unsaturated aliphatic hydrocarbyl moiety, aryl, virtue Alkyl, C1-20Miscellaneous alkyl, C1-20Alkyl oxygroup acyl group, C1-20Alkylthio acyl group and its any substituted form.
R, G is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Alkenyl, aryl, aryl, C1-20 Rouge miscellaneous alkyl, heteroaryl, heteroaryl alkyl, C1-20Alkoxyacyl, aryloxy acyl group, C1-20Alkyl sulfenyl acyl group, artyl sulfo Acyl group and its any substituted form.
R, G is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Alkenyl, aryl, aryl, C1-20 Rouge miscellaneous alkyl, heteroaryl, heteroaryl alkyl, C1-20Alkoxy carbonyl, aryloxycarbonyl, C1-20Alkyl sulfenyl carbonyl, artyl sulfo Carbonyl, C1-20Alkoxy carbonyl, aryloxy thiocarbonyl, C1-20Alkyl sulfenyl thiocarbonyl, artyl sulfo thiocarbonyl And its any substituted form.
Specifically, R, G be each independently selected from including but not limited to hydrogen atom, fluorine atom, chlorine atom, bromine atom, iodine atom, Methyl, ethyl, n-propyl, isopropyl, butyl, amyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, Tridecyl, myristyl, pentadecyl, cetyl, heptadecyl, octadecyl, nonadecyl, eicosyl, allyl Base, acrylic, vinyl, phenyl, aminomethyl phenyl, butyl phenyl, benzyl, methoxycarbonyl, ethoxy carbonyl, phenoxy group carbonyl Base, benzyloxycarbonyl, methyl mercapto carbonyl, ethylmercapto group carbonyl, thiophenyl carbonyl, benzylthio carbonyl, B aminocarbonyl, benzyl amino carbonyl Base, methoxyl group thiocarbonyl, ethyoxyl thiocarbonyl, phenoxythiocarbonyl, benzyloxy thiocarbonyl, the thio carbonyl of methyl mercapto Base, ethylmercapto group thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, substituted C1-20Alkyl, substituted C1-20Alkenyl, Substituted aryl, substituted aryl, substituted C1-20Rouge miscellaneous alkyl, substituted heteroaryl, substituted heteroaryl alkyl, replace C1-20Alkoxy carbonyl, substituted aryloxycarbonyl, substituted C1-20Alkyl sulfenyl carbonyl, takes substituted artyl sulfo carbonyl The C in generation1-20Alkoxy carbonyl, substituted aryloxy thiocarbonyl, substituted C1-20Alkyl sulfenyl thiocarbonyl replaces Artyl sulfo thiocarbonyl.Wherein, butyl includes but is not limited to normal-butyl, tert-butyl.Octyl include but is not limited to n-octyl, 2- ethylhexyl.Wherein, atom or substituent group is replaced to be selected from halogen atom, hydrocarbyl substituent, contain heteroatomic substituent group.
R, G further respectively it is independent be preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, Amyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, myristyl, pentadecyl, ten Six alkyl, heptadecyl, octadecyl, nonadecyl, eicosyl, allyl, benzyl, trityl, phenyl, benzyl, first Base benzyl, nitrobenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio, acetyl group, benzoyl, 2- pyridyl group carbonyl Base, methoxycarbonyl, ethoxy carbonyl, t-butyloxycarbonyl, phenyloxycarbonyl, benzyloxycarbonyl, methyl mercapto carbonyl, second sulphur Base carbonyl, tert. butyl-sulphenyl carbonyl, thiophenyl carbonyl, benzylthio carbonyl, ethylenebis dithiocarbamate carbonyl, phenyl first thiocarbonyl, methoxy Base thiocarbonyl, ethyoxyl thiocarbonyl, tert-butyl oxygroup thiocarbonyl, phenoxythiocarbonyl, benzyloxy thiocarbonyl, first Alkylthio carbonyl, ethylmercapto group thiocarbonyl, tert. butyl-sulphenyl thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, C1-10It halohydrocarbyl, trifluoroacetyl group, halogenophenyl, halogeno-benzyl, nitrobenzophenone, nitrobenzyl and its any is substituted Form.Wherein, replace atom or substituent group is preferably fluorine atom, alkoxy, nitro.
R, G respectively independent more preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, benzyl, three Benzyl, phenyl, benzyl, methylbenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio, 2- pyridylcarbonyl, tertiary fourth Base Epoxide carbonyl, phenyloxycarbonyl, benzyloxycarbonyl, tert-butyl oxygroup thiocarbonyl, phenoxythiocarbonyl, benzyloxy are thio Carbonyl, tert. butyl-sulphenyl thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, trifluoroacetyl group.
R, G respectively independently be more preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, benzyl, Trityl, phenyl, benzyl, methylbenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio.
R, G is respectively independently most preferably hydrogen atom, methyl, ethyl, n-propyl, normal-butyl.
Heretofore described hetero atom is not particularly limited, including but not limited to oxygen atom, sulphur atom, nitrogen-atoms, phosphorus Atom, silicon atom, fluorine atom, chlorine atom, bromine atom, iodine atom, boron atom etc..Wherein, heteroatomic quantity can be one, It may be two or more.Hetero atom, which can be used as, replaces atom to exist, can also be independently as divalent linker In the presence of illustrate such as-O- (oxygroup or ehter bond) ,-S- (sulfenyl or thioether bond).
There is good compatibility with formula (4), the hydrogen bond group of (5) structure and catalytic component B, preferably by isocyanide The reaction that acid esters compound is participated in obtains, and conveniently performs the derivatization, and obtains structure and performance abundant.Such reaction Raw material sources are abundant, and synthesis is simple, and operation is easy, and are suitble to large-scale industrial production.
As an example, side group hydrogen bond group as described below can be enumerated, but the present invention is not limited only to this:
Wherein, m, n, x are the quantity of recurring group, can be fixed value, are also possible to average value.M, n value range is 0 Be more than or equal to 1 integer, preferably no greater than 20, more preferably no higher than 10；X value range is the integer more than or equal to 1.
Other optional side group hydrogen bond groups can be selected from including but are not limited to amino, hydroxyl, carboxyl, amide groups, thio Amide groups, pyrrolidone-base, imidazole radicals, pyrazolyl, nitrogen oxazolyl and its derivative base.
In embodiments of the present invention, main chain and/or side chain skeleton hydrogen bond group can be any appropriate hydrogen bond base Hydrogen bond donor and hydrogen bond receptor are preferably contained simultaneously in group, contain at least one secondary amino group preferably wherein, further preferably following knot At least one of composition point:
Wherein,Indicate the connection with polymer chain.
As an example, the hydrogen bond group on main chain and/or side chain skeleton as described below can be enumerated, but the present invention not only limits In this:
In embodiments of the present invention, end group hydrogen bond group can be any appropriate hydrogen bond group, preferably contain simultaneously There are hydrogen bond donor and hydrogen bond receptor, contain at least one secondary amino group preferably wherein, in further preferably following constituent extremely Few one kind:
Wherein,Indicate the connection with polymer chain, L is end group；It can be cyclic or not cyclic with L.
Wherein, Z is each independently selected from oxygen atom or sulphur atom.
The structure of L is not particularly limited, respectively it is independent include but is not limited to linear chain structure, the branched structure containing side group or Cyclic structure.Wherein, cyclic structure is not particularly limited, and can be selected from aliphatic ring, aromatic ring, saccharide ring, condensed ring, preferably rouge Fat race ring.
The structure of L is respectively independently preferably linear chain structure.
L can contain hetero atom, can also be free of hetero atom.
The carbon atom number of L is not particularly limited, and respectively independent is preferably 1~20, and respective independent more preferably 1~10.
L is each independently selected from hydrogen atom, halogen atom, C1-20Alkyl, C1-20Miscellaneous alkyl, substituted C1-20Alkyl or substitution Miscellaneous alkyl.Wherein, the substitution atom in L or substituent group are not particularly limited, and are each independently selected from halogen atom, alkyl replaces Base contains heteroatomic substituent group.
L is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Unsaturated aliphatic hydrocarbyl moiety, aryl, aromatic hydrocarbons Base, C1-20Miscellaneous alkyl, C1-20Alkyl oxygroup acyl group, C1-20Alkylthio acyl group and its any substituted form.
L is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Alkenyl, aryl, aryl, C1-20Rouge Miscellaneous alkyl, heteroaryl, heteroaryl alkyl, C1-20Alkoxyacyl, aryloxy acyl group, C1-20Alkyl sulfenyl acyl group, artyl sulfo acyl Base and its any substituted form.
L is respectively independently more preferably hydrogen atom, halogen atom, C1-20Alkyl, C1-20Alkenyl, aryl, aryl, C1-20Rouge Miscellaneous alkyl, heteroaryl, heteroaryl alkyl, C1-20Alkoxy carbonyl, aryloxycarbonyl, C1-20Alkyl sulfenyl carbonyl, artyl sulfo carbonyl Base, C1-20Alkoxy carbonyl, aryloxy thiocarbonyl, C1-20Alkyl sulfenyl thiocarbonyl, artyl sulfo thiocarbonyl and Its any substituted form.
Specifically, L is each independently selected from including but not limited to hydrogen atom, fluorine atom, chlorine atom, bromine atom, iodine atom, first Base, ethyl, n-propyl, isopropyl, butyl, amyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, ten Trialkyl, myristyl, pentadecyl, cetyl, heptadecyl, octadecyl, nonadecyl, eicosyl, allyl, Acrylic, vinyl, phenyl, aminomethyl phenyl, butyl phenyl, benzyl, methoxycarbonyl, ethoxy carbonyl, phenyloxycarbonyl, benzyl Epoxide carbonyl, methyl mercapto carbonyl, ethylmercapto group carbonyl, thiophenyl carbonyl, benzylthio carbonyl, B aminocarbonyl, benzylaminocarbonyl, first Oxygroup thiocarbonyl, ethyoxyl thiocarbonyl, phenoxythiocarbonyl, benzyloxy thiocarbonyl, methyl mercapto thiocarbonyl, second sulphur Base thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, substituted C1-20Alkyl, substituted C1-20Alkenyl, replace Aryl, substituted aryl, substituted C1-20Rouge miscellaneous alkyl, substituted heteroaryl, substituted heteroaryl alkyl, substituted C1-20Alkane Epoxide carbonyl, substituted aryloxycarbonyl, substituted C1-20Alkyl sulfenyl carbonyl, substituted artyl sulfo carbonyl, replace C1-20Alkoxy carbonyl, substituted aryloxy thiocarbonyl, substituted C1-20Alkyl sulfenyl thiocarbonyl, substituted virtue Base alkylthio carbonyl.Wherein, butyl includes but is not limited to normal-butyl, tert-butyl.Octyl includes but is not limited to n-octyl, 2- second Base hexyl.Wherein, atom or substituent group is replaced to be selected from halogen atom, hydrocarbyl substituent, contain heteroatomic substituent group.
It is preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, penta that L is further respectively independent Base, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, myristyl, pentadecyl, 16 Alkyl, heptadecyl, octadecyl, nonadecyl, eicosyl, allyl, benzyl, trityl, phenyl, benzyl, methyl Benzyl, nitrobenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio, acetyl group, benzoyl, 2- pyridylcarbonyl, Methoxycarbonyl, ethoxy carbonyl, t-butyloxycarbonyl, phenyloxycarbonyl, benzyloxycarbonyl, methyl mercapto carbonyl, ethylmercapto group Carbonyl, tert. butyl-sulphenyl carbonyl, thiophenyl carbonyl, benzylthio carbonyl, ethylenebis dithiocarbamate carbonyl, phenyl first thiocarbonyl, methoxyl group Thiocarbonyl, ethyoxyl thiocarbonyl, tert-butyl oxygroup thiocarbonyl, phenoxythiocarbonyl, benzyloxy thiocarbonyl, first sulphur Base thiocarbonyl, ethylmercapto group thiocarbonyl, tert. butyl-sulphenyl thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, C1-10It halohydrocarbyl, trifluoroacetyl group, halogenophenyl, halogeno-benzyl, nitrobenzophenone, nitrobenzyl and its any is substituted Form.Wherein, replace atom or substituent group is preferably fluorine atom, alkoxy, nitro.
L respectively independent more preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, benzyl, triphen Methyl, phenyl, benzyl, methylbenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio, 2- pyridylcarbonyl, tert-butyl Epoxide carbonyl, phenyloxycarbonyl, benzyloxycarbonyl, tert-butyl oxygroup thiocarbonyl, phenoxythiocarbonyl, the thio carbonyl of benzyloxy Base, tert. butyl-sulphenyl thiocarbonyl, phenylthiothiocarbonyl carbonyl, benzylthio thiocarbonyl, trifluoroacetyl group.
L is respectively independently more preferably hydrogen atom, methyl, ethyl, n-propyl, isopropyl, normal-butyl, tert-butyl, benzyl, three Benzyl, phenyl, benzyl, methylbenzyl, tert. butyl-sulphenyl, benzyl sulfenyl, 2- pyridinylthio.
L is respectively independently most preferably hydrogen atom, methyl, ethyl, n-propyl, normal-butyl.
As an example, end group hydrogen bond group as described below can be enumerated, but the present invention is not limited only to this:
Wherein, m, n, x are the quantity of recurring group, can be fixed value, are also possible to average value.M, n value range is 0 With the integer for being more than or equal to 1；X value range is the integer more than or equal to 1.
In embodiments of the present invention, contain other while property is also an option that in the hydridization dynamic aggregation object component May participate in the other components to form hydrogen bond action containing hydrogen bond group, including but not limited to small molecule, polymer, inorganic material, Metal material, hydrogen bond group contained therein can be any appropriate group, as an example, including but not limited to general formula (4)- (9) hydrogen bond group and amino, hydroxyl, imidazole radicals, pyrazolyl, nitrogen oxazolyl and its derivative base described in.Such other components Between can also form hydrogen bond.In the present invention, the content of other such hydrogen bond groups is not particularly limited, preferably shorter than hydrogen bond The 50mol% of group total content, more preferably less than 20mol%, even more preferably below 5mol%.
In embodiments of the present invention, the hydrogen bond group of hydrogen bond action is formed either mutual between different hydrogen bond groups Apotype combination is also possible to combining between hydrogen bond group of the same race from complementary type, makees as long as being capable of forming suitable hydrogen bond between group With.The combination of some hydrogen bond groups can be exemplified below, but the present invention is not limited only to this:
In the present invention, the supermolecule hydrogen bond action, which can be, carries out the friendship of dynamic supermolecule in hydridization dynamic aggregation object It is generated during connection/polymerization；It is also possible to carry out after pre-generated supermolecule hydrogen bond action dynamic supermolecule crosslinking/poly- again It closes；Supermolecule can also be generated during hydridization dynamic aggregation object subsequent forming after dynamic supermolecule crosslinking/polymerization is formed Hydrogen bond action, but the present invention is not limited only to this.
The unsaturated carbon that olefin cross metathesis metathesis reaction occurs of reversible dynamic crosslinking is used to form in the present invention Carbon double bond group can be the polymer precursor for having contained unsaturated carbon-carbon double bond from selection, can also be without unsaturation It generates or introduces on the basis of the polymer precursor of carbon-carbon double bond.The generation or introducing of unsaturated carbon-carbon double bond, can be covalent Before crosslinking, later or in the process carry out.But the reaction condition of the reaction due to generating carbon-carbon double bond is typically more harsh, because This is it is preferable to use the polymer precursor containing carbon-carbon double bond or using the polymer precursor without containing carbon-carbon double bond and contains carbon The reagent of carbon double bond reacts, and achievees the purpose that introduce carbon-carbon double bond.
Wherein, contained the polymer precursor of unsaturated carbon-carbon double bond, as an example, including but not limited to butadiene rubber, 1,2- butadiene rubber, isoprene rubber, polynorbornene, neoprene, butadiene-styrene rubber, nitrile rubber, polychlorobutadiene, bromination Polybutadiene, Ethylene-Propylene-Diene rubber (EPDM), acrylonitrile-butadiene-styrene copolymer (ABS), styrene-fourth two Alkene rubber (SBR), Styrene-Butadiene-Styrene Block Copolymer (SBS), styrene-isoprene-phenylethene block are total Polymers (SIS), unsaturated polyester (UP), unsaturated polyether and its copolymer etc..
Wherein, the group containing carbon-carbon double bond or introducing for segment can use any appropriate reaction, including but not only Be limited to Types Below: isocyanates and amino, hydroxyl, sulfydryl, carboxyl, epoxy group are reacted, carboxylic acid, carboxylic acid halides, acid anhydrides, active ester It is reacted with amino, hydroxyl, sulfydryl, free radical acrylate reaction, acrylamide radical reaction, double bond radical reaction, Epoxy group and amino, hydroxyl, sulfydryl react, phenol-formaldehyde reaction, nitrine-alkynes click-reaction, tetrazine-norbornene reaction, silicon hydroxyl Base condensation reaction；Preferred isocyanate and amino, hydroxyl, sulfydryl react, carboxylic acid halides, acid anhydrides and amino, hydroxyl, sulfydryl it is anti- It answers, free radical acrylate reaction, acrylamide radical reaction, double bond radical reaction, epoxy and amino, hydroxyl, sulfydryl Reaction.As an example, the available small organic agents containing carbon-carbon double bond include but is not limited to following lifted: Isosorbide-5-Nitrae-butylene Glycol, 1,5- di-p oxyphenyl -1,4- pentadiene -3- ketone, single ricinoleic acid glyceride, maleic acid, fumaric acid, transmethyl fourth Enedioic acid (mesaconic acid), cis-methyl-butene diacid (citraconic acid), chloro maleic acid, 2- methylene-succinic acid (clothing health Acid), 4,4'- stilbenedicarboxylicacid acid, 1,5- di-p oxyphenyl -1,4- pentadiene -3- ketone, fumaryl chloride, 1,4- phenylene two Acryloyl chloride, citraconic anhydride, maleic anhydride, dimethyl fumarate, monomethyl ester, diethyl fumarate, citraconic acid diformazan Bromo- 2- butylene of ester, Isosorbide-5-Nitrae-dichloro-2-butene, Isosorbide-5-Nitrae-two etc. can also be selected double containing carbon carbon on the chain backbone of end group functional The oligomer of key.
Wherein, the generation of carbon-carbon double bond can use any appropriate method, include but are not limited to following chemical reaction Type: hydrogen halides reaction is lost in alcohol dehydration reaction, halogenated hydrocarbons, dihalo hydrocarbon loses halogen reaction, Hofmann elimination reaction, amine oxide Hot tearing reaction, ester hot tearing reaction, xanthate hot tearing reaction, Wittig reaction and Wittig-Horner reaction, alkene it is acyclic Metathesis polymerization reacts (ADMET), cyclenes ring-opening polymerization etc..Wherein, preferable reaction temperature is not higher than 200 DEG C of reaction.
The generation or introducing of the hydrogen bond group of supermolecular mechanism are used to form in the present invention, can dynamic covalent cross-linking it Before, carry out later or in the process.It is preferred that carrying out before dynamic covalent cross-linking or in the process, more preferably covalently handed in dynamic It is carried out before connection.Because must will be generally added by way of swelling in relation to reagent if being carried out after dynamic covalent cross-linking, Complex process and effect is poor.
In embodiments of the present invention, the generation or introducing of hydrogen bond group can use any appropriate reaction, including but Be not limited only to Types Below: isocyanates and amino, hydroxyl, sulfydryl, carboxyl react, free radical acrylate reaction, double bond Radical reaction, double bond cyclization, epoxy and amino, hydroxyl, sulfydryl react, nitrine-alkynes click-reaction, and sulfydryl-double bond/ Alkynes click-reaction, the reaction of urea-amine, amidation process, tetrazine-norbornene reaction, active ester and amino, hydroxyl, sulfydryl Reaction, silicone hydroxyl condensation reaction；Preferred isocyanate and amino, hydroxyl, sulfydryl react, the reaction of urea-amine, amidation Reaction, active ester and amino, hydroxyl, sulfydryl react.In any one network structure, hydrogen bond group can have one or its Above reaction type, reaction means and the structure.
In embodiments of the present invention, for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalent bond and hydrogen bond The ingredient of group, hydrogen bond group and hydrogen bond group can be small molecule and/or polymer segment.The wherein polymer chain Section, including but are not limited to main chain is carbon-chain structure, carbon heterochain structure, carbon chain structure, element chain structure, element heterochain knot The polymer segment of the miscellaneous element chain structure of structure, carbon.The carbon-chain structure is the structure that main chain backbone contains only carbon atom；It is described Carbon heterochain structure be main chain backbone contain simultaneously carbon atom and it is any or appoint several heteroatomic structures, wherein the miscellaneous original Son includes but are not limited to sulphur, oxygen, nitrogen；The carbon chain structure be main chain backbone contain simultaneously carbon atom and it is any or Appoint the structure of several Elements Atoms, wherein Elements Atom includes but are not limited to silicon, boron, aluminium；Based on the element chain structure Chain backbone is only containing the structure of Elements Atom；The element heterochain structure is main chain backbone simultaneously and only containing at least one miscellaneous The structure of atom and at least one Elements Atom；The miscellaneous element chain structure of the carbon is main chain backbone while including carbon atom, miscellaneous The structure of atom and Elements Atom.In an embodiment of the invention, it is carbon that the preferably described polymer segment, which is main chain, The polymer segment of chain structure and carbon heterochain structure, because of its structure-rich, has excellent performance.As an example, preferred carbochain and carbon Heterochain polymer segment is included but are not limited to such as acrylic polymer, saturation of olefins quasi polymer, ethylenic unsaturation hydro carbons Polymer, polystyrenic polymer, halogen-containing olefin polymer, polyacrylonitrile quasi polymer, polyvinyl alcohol Type of Collective Object, poly- (2- oxazoline) quasi polymer, polyether-based polymers, polyester polymer, Biopolvester quasi polymer, polycarbonate are birdsed of the same feather flock together Close object, polyurethane polymer, polyureas quasi polymer, polyamide polymers, polyamine quasi polymer, liquid crystal quasi polymer, ring Homopolymer, copolymer, modifier, the derivative etc. of oxygen quasi polymer, polysulfide ether polymer etc..In another reality of the invention It applies in mode, preferably the polymer segment is element heterochain structure, by way of example, such as all kinds of poly-organosilicon polymer.Make For citing, preferred polymer segment includes but are not limited to acrylic polymer, saturation of olefins quasi polymer, unsaturation Olefin polymer, halogen-containing olefin polymer, poly- (2- oxazoline) quasi polymer, polyether-based polymers, polyester Type of Collective Object, Biopolvester quasi polymer, polyurethane polymer, polyureas quasi polymer, polysulfide ether polymer, silicone-based polymers Deng homopolymer, copolymer, modifier, derivative etc..Specifically, currently preferred polymer segment includes but are not limited to Polymethyl acrylate, polyethyl acrylate, butyl polyacrylate, polyethylene, polypropylene, polyisobutene, polybutadiene, polycyclic are pungent Alkene, polynorbornene, polyisoprene, polyvinyl chloride, poly- (2- oxazoline), polyethylene glycol, polypropylene glycol, polycaprolactone, poly- β- Homopolymer, copolymer, modifier, the derivative of butyric ester, polyurethane, polyureas, polythiaether, polyorganosiloxane etc. Deng.
In yet another embodiment of the present invention, it is preferably described for connect dynamic covalent bond and dynamic covalent bond, The glass transition temperature of the polymer segment of dynamic covalent bond and hydrogen bond group, hydrogen bond group and hydrogen bond group is not higher than 25 DEG C, more preferably no higher than 0 DEG C, it is presented as flexibility at room temperature before the reaction, it is convenient to carry out adding for subsequent products at normal temperature Work preparation facilitates and obtains flexible and viscosity product, is also convenient for adjusting by increasing crosslink density or using other additives The hardness of material matrix is conducive to embody the dynamic of supermolecule hydrogen bond as matrix.In another embodiment party of the invention In formula, preferably the glass transition temperature of the polymer segment is higher than 25 DEG C but lower than 40 DEG C, and it is quick to be conducive to introducing temperature The characteristics such as perceptual, moderate elasticity and dynamic.In yet another embodiment of the present invention, the preferably described polymer segment Glass transition temperature be not less than 40 DEG C, more desirably not less than 100 DEG C, be conducive to introduce shape memory, Temperature Size steady The characteristics such as qualitative, low temperature and room temperature hardness.In yet another embodiment of the present invention, in the preferably described polymer segment extremely A kind of few polymer segment that 25 DEG C are not higher than for glass transition temperature, and at least one is not less than for glass transition temperature 100 DEG C of polymer segment, convenient for obtaining the various characteristics under low temperature and high temperature simultaneously.
In embodiments of the present invention, for connecting dynamic covalent bond and dynamic covalent bond, dynamic covalent bond and hydrogen bond Group, the small molecule of hydrogen bond group and hydrogen bond group and/or polymer segment and/or dynamic aggregation object can have any conjunction Suitable topological structure includes but are not limited to linear chain structure, branched structure (including but not limited to starlike, H-type, dendroid, comb It is shape, hyperbranched), cyclic structure (including but not limited to monocycle, polycyclic, bridged ring, grommet, torus), two-dimensional/three-dimensional cluster structure and Its two kinds or several combination；Wherein, the linear chain structure of synthesis and control structure, the branched structure of structure-rich are preferably facilitated With can be with the two-dimensional/three-dimensional cluster structure of local enhancement, more preferable linear chain structure and branched structure.In the present invention, or even not It excludes to carry out the reaction such as further polymerized/cross-linked and connection using the polymer beads of crosslinking.
Selected above-mentioned each quasi polymer and its segment in the present invention, i.e., have hydrogen bond base containing dynamic covalent bond simultaneously again The polymer and its segment of group, the polymer for not only not contained dynamic covalent bond but also not contained hydrogen bond group and its segment only contain Polymer and its segment and only polymerization containing hydrogen bond group without dynamic covalent bond of the dynamic covalent bond without hydrogen bond group Object and its segment can directly select the raw material of commercialization, can also voluntarily polymerize.Polymerization is according to selected polymer Type includes but is not limited to polycondensation, addition polymerization and ring-opening polymerisation；Wherein, addition polymerization includes but is not limited to free radical polymerization, activity freedom Base polymerization, anionic polymerisation, cationic polymerization, coordination polymerization etc..Wherein, polymerization process can carry out in a solvent, can also be with It is solvent-free bulk polymerization.Specifically, as an example, the available polymerization of the present invention includes but is not limited to: styrene Class, the heat of (methyl) acrylic ester monomer cause general radical polymerization, phenylethylene, (methyl) acrylic ester monomer Light lnduced Free Radicals polymerization, the Iniferter free radical polymerization of vinyl chloride monomer, phenylethylene, (methyl) acrylic acid The atom transfer radical polymerization (ATRP) of esters monomer, phenylethylene, (methyl) esters of acrylic acid, acrylonitrile monomer are reversible Addition-fracture transferring free-radical polymerization (RAFT), nitroxide-mediated stable free-radical polymerization (NMP), ethylene, propylene coordination polymerization, benzene second The anionic polymerisation of vinyl monomer, lactone ring opening polymerization, lactams ring-opening polymerisation, epoxy addition polymerization, binary acid and dihydric alcohol Between polycondensation, the polycondensation between binary acid and diamine, between binary mercaptan and binary alkene/alkynes click-reaction polymerization, two Click-reaction polymerization between first nitrine and binary alkynes, the ring-opening polymerisation of 2- oxazoline derivative, polyurethane/polyurea reaction etc..? In specific implementation process, raw materials of compound can utilize above-mentioned any polymerisation process, appoint by the way that this field is general A kind of suitable polymerization technique is implemented, to obtain hydridization dynamic aggregation object of the invention.
It can be addition-crosslinked or condensation cross-linking for the mechanism of crosslinking of polymer.Wherein, it is addition-crosslinked refer to pass through addition Form and the cross-linking polymerization carried out, usually by the addition reaction containing multi-functional strand by intermolecular functional group And cross-linking products are formed, it is generated without by-product.Condensation cross-linking refers to the cross-linking reaction carried out by condensed forms, usually By forming cross-linking products by intermolecular functional group's condensation reaction containing multi-functional strand, there is by-product generation.
In embodiments of the present invention, crosslinking can be using any appropriate physics and chemical crosslinking technique.Physics is handed over Connection technique includes but is not limited to heat initiation crosslinking, photo-initiated crosslinking, radiation-induced crosslinking, plasma causes crosslinking, microwave draws Hair crosslinking etc.；Chemical crosslinking technique includes but is not limited to peroxide crosslinking, nucleopilic reagent substitution crosslinking, isocyanates reaction friendship Connection, epoxy reaction crosslinking, acrylate reactions crosslinking etc..Cross-linking process can be carried out in the form of ontology, solution, lotion etc..When Using bulk form, solid end product is conveniently directly obtained；When using solution form, gel is conveniently directly obtained；When using cream Liquid mode facilitates and obtains particle dispersing but with tack.It should be pointed out that any crosslinking must assure that the carbon carbon Double bond complete is incompletely dissociated the disintegration that can lead to covalent cross-linking network.
Initiator needed for above-mentioned polymerization, cross-linking method and polymerization, cross-linking process, catalyst, crosslinking agent, other Auxiliary agent and reaction condition etc. are all open known routine techniques (such as Pan Zuren chief editor, " polymer chemistry (enhanced editions) "), Those skilled in that art, which can according to need, to be reasonably selected and combines.
It is illustrated below for the embodiment of the part preparation method of network structure of the invention.
For example, the first network structure of the invention can be prepared by following methods: will be easy containing that olefin cross can occur The unsaturated carbon-carbon double bond group of position metathesis reaction (is denoted as V in following structural formulam) double carboxylic monomers and have skeleton hydrogen Key group (is denoted as R in following structural formulaH, RHMeet structure described in general formula (4) comprising at least one) double carboxylic monomers and With side group hydrogen bond group RHPolyhydroxy based cross-linker, the first network structure in the present invention can be formed with polymerized/cross-linked.It is logical The formula rate of control monomer and crosslinking agent is crossed, the content and ratio of dynamic covalent bond and hydrogen bond group in adjustable network, The covalent cross-linking in network is set to reach covalent gel point or more.
For another example, the first network structure of the invention can also be realized by Raolical polymerizable: end is had side group Hydrogen bond group RHAcrylate and with the unsaturated carbon-carbon double bond group V that olefin cross metathesis metathesis reaction can occurm's The first network structure of double methacrylate by the Raolical polymerizable of alkene, in the available present invention.Pass through control The dosage of monoolefine, the formula rate of diolefin and the monoolefine without hydrogen bond group selectively used, adjustable net The content and ratio of dynamic covalent bond and hydrogen bond group, make the covalent cross-linking in network reach covalent gel point or more in network.
For another example, the first network structure of the invention can also be by first carrying out acyclic diene hydrocarbon of the part containing hydrogen bond group Metathesis polymerization reaction, then it is crosslinked to obtain the first network structure in the present invention.Hydrogen bond is contained or not contain by control The formula rate of the acyclic diene hydrocarbon of group and the dosage of crosslinking agent, dynamic covalent bond and hydrogen bond group in adjustable network Content and ratio, so that the covalent cross-linking in network is reached covalent gel point or more.
The embodiment of other network structures in the present invention is similar, and those skilled in the art can be according to this hair Bright understanding selects suitable preparation means, reaches ideal purpose.
Hydridization dynamic aggregation compositions component A of the invention, except network structure can have and only one polymeric web Outside network, other network structures can the Multi net voting structure based on two or its above network.In addition to common blending dispersion, more Preferably the interpenetrating networks for tangling and being formed are intertwined by two or more polymer networks.Interpenetrating net polymer knot Structure due between network component collaboration and/or orthogonal effect so that its performance is substantially better than single network polymer of its component, generate ratio The mechanical properties such as the higher toughness of single network, in the case where being based particularly on mentality of designing introducing hydrogen bond crosslinks of the invention.
In the present invention, two classes can be classified as according to polymers compositions crosslinking situation in composition interpenetrating networks, it is Semi-IPN With full interpenetrating.Only a kind of component is covalent cross-linking in Semi-IPN, and another component is worn in the form of non-covalent strand It inserts and becomes entangled in covalent cross-linking component.Between ignore network if supermolecule crosslinking that may be present, of the invention the 6th kind Network structure and the 7th kind of network structure can be considered semi-intercrossing network, the 4th kind of network structure of the invention and the 5th kind of network Structure can be considered full interpenetrating networks.
Traditional interpenetrating net polymer preparation method generally includes one-step method interpenetrating and two-step method interpenetrating.One-step method i.e. one All the components are added secondary property, then carry out polymerized/cross-linked, prepare target network.Two-step method first prepares the 1st network polymerization And then object is immersed in the monomer/pre-polymer solution to form the 2nd network, then it is miscellaneous to obtain target for initiation polymerized/cross-linked Change network.The preparation of hydridization dynamic aggregation object in the present invention can also use one-step method interpenetrating and two-step method interpenetrating, specific In the case of must also using three steps and its more than method.
It is illustrated below for the embodiment of the part preparation method of interpenetrating net polymer of the invention.With It is lower to lift only as an example, it not limits the scope of the invention, is lifted the present invention is not limited to following.
For example, the dynamic aggregation object of the hybrid cross-linked network is by two nets in the 4th kind of network structure of the invention Network is constituted.Firstly, preparing one kind, there is no hydrogen bond groups, but olefin cross metathesis subdivision can occur for presence on polymer chain skeleton Solve the polymer dynamic co-crosslinking network of the unsaturated carbon-carbon double bond group of reaction.Then, gained dynamic covalent networks are swollen, It is uniformly mixed with the monomer of supermolecule cross-linked network or prepolymer, crosslinking agent etc., supermolecule crosslinking is carried out, to obtain full interpenetrating Network polymer namely Supramolecular Network disperse through in dynamic covalent cross-linking.Alternatively, by the list of dynamic covalent cross-linking network Body or prepolymer, crosslinking agent are uniformly mixed with the monomer of supermolecule cross-linked network or prepolymer, crosslinking agent etc., while carrying out dynamic Covalent cross-linking and supermolecule are crosslinked to arrive the 4th kind of network structure of the invention.
For another example, in the 7th kind of network structure of the invention, firstly, reasonably selecting preceding method preparation simultaneously containing dynamic The hybrid cross-linked network with the first network structure of covalent cross-linking and supermolecule crosslinking.It then, will be resulting hybrid cross-linked Network is sufficiently blended to arrive semi-interpenetrating network polymer with supermolecule polymer.Alternatively, will have the first network structure Monomer or prepolymer, the crosslinking agent of hybrid cross-linked network are uniformly mixed with supermolecule polymer, Mobile state covalent cross-linking of going forward side by side, i.e., Obtain the 7th kind of network structure of the invention.
In the following, in the present invention hydridization dynamic aggregation compositions component B catalyst or its compound carry out specifically It is bright.
In embodiments of the present invention, the olefin cross metathesis metathesis reaction based on ruthenium, molybdenum, tungsten, titanium, It is carried out under the catalysis of the metallic catalysts such as palladium, nickel, includes but are not limited to such as document " Recent Advances in High Oxidation State Mo and W Imido Alkylidene Chemistry ", RichardR.Schrock, Chem.Rev.2009,109,3211-3226, document " Ruthenium-Based Heterocyclic Carbene- Coordinated Olefin Metathesis Catalysts ", Georgios C.Vougioukalakis and Robert H.Grubbs, Chem.Rev.2010,110,1746-1787, document " Olefin Metathesis in Aqueous Media ", Jasmine Tomasek and J ü rgen Schatz, Green Chemistry, 2013,15,2317-2338, text Offer " Remote Control Grubbs Catalysts That Modulate Ring-Opening Metathesis Polymerizations ", Aaron J.Teator and Christopher W.Bielawski, 2017,55,2949- 2960, book " Olefin Metathesis:Theory and Practice " 2014 John Wiley &Sons, Inc., patent Catalyst is suitable for the invention disclosed in CN201210067234.9.Selected catalyst both can be used alone, It can also be used cooperatively with two or more；It can be directly dispersing in hydridization dynamic aggregation compositions component A and use, It can be used in the form of the compound containing catalyst, such as, but not limited to by either physically or chemically coating or loading on It is used on organic and inorganic, polymer support, and (such as suitable temperature, pressure) has under the conditions of selfreparing with other The component of low-viscosity high-fluidity is coated in microcapsules or microtubular together and uses；It can also be the nonactive shape of catalyst Formula can be converted to active catalyst under the appropriate environmental stimuli such as such as heat, soda acid, illumination, free radical.When selected Catalyst be used alone when need to in each analog assistant filler existing for hydridization dynamic aggregation compositions component A and selectivity Existing all kinds of groups are compatible.Reasonably selecting catalyst carrier can be enhanced catalyst or its compound in hydridization dynamic aggregation object Dispersibility in composition component A, reduces the partial size of catalytic clusters, thus improve catalytic efficiency, reduce catalyst amount and Reduce cost.Reasonably selecting covering material can also avoid catalyst from inactivating in composition preparation process or in the course of work.
The example of available catalyst of the invention or its inactive form includes but is not limited to following lifted:
Wherein, PCy3ForMes isPh is phenyl, and Et is ethyl, and i-Pr is isopropyl Base, t-Bu are tert-butyl, and PEG is polyethylene glycol.
Wherein, component B is preferably based on the catalyst of ruthenium, molybdenum, tungsten, and more preferable catalytic efficiency is higher and unwise to empty gas and water The ruthenium catalyst of sense, the catalyst being especially commercialized such as a Grubbs generation, two generations, three generations's catalyst, Hoveyda- A Grubbs generation, two generation catalyst, (Zhan Shi catalyst is to urge disclosed in patent CN201210067234.9 to Zhan Shi catalyst Agent) etc..The another kind of component B preferably has catalysis without catalytic activity but under ultraviolet irradiation under normal conditions in the present invention Active catalyst, it includes but are not limited to catalyst 64-66 etc. as an example.
It is important to note that should be noted its compatibility between component A Zhong Ge functional group when selecting catalyst Problem need to select suitable catalyst to avoid its failure.For example, causing since amino can form chelate with partial catalyst Catalyst failure, therefore when containing amino in polymer, the catalyst based on Mo need to be used, or boryl lewis acid is added and keeps away Exempt from this effect, improves catalytic efficiency；For another example, when in component A there are when itrile group, should be avoided using Grubbs generation catalyst, And select other catalyst.
In embodiments of the present invention, the preparation method of the compound containing catalyst is not particularly limited, and is used Method commonly known in the art.
As an example, a kind of preferred embodiment that the compound containing catalyst is prepared in the present invention is by catalyst packet It overlays in organic carrier.Available organic carrier is not particularly limited, and may be selected from but not limited to paraffin, poly- second as an example Glycol etc., it is known disclosed technological means that catalyst, which is coated on the method in organic carrier, and the present invention selects common system Preparation Method.For example, preferred the preparation method comprises the following steps: by selected catalysis by one kind of organic carrier coated catalysts of paraffin Agent, paraffin and surfactant are sufficiently blended under paraffin molten condition, and blend is poured into the stirring of certain revolving speed and temperature Higher than in the water of paraffin melting point；After stirring reaches stable state to blending liquid, ice water, which is added, makes water temperature be rapidly cooled to paraffin Below fusing point；Stop stirring, filtering obtains the catalyst composites of paraffin cladding.
Another preferred embodiment that the compound containing catalyst is prepared in the present invention is by selected catalyst Through physical absorption or chemical reaction load in organic or inorganic carrier.Available carrier is not particularly limited, as Example may be selected from but not limited to polystyrene resin beads, magnetic nano-particle, silica gel particle, molecular sieve, other mesoporous materials Deng being known disclosed technological means by method of the catalyst load on inorganic carrier, for example, Zhu Yinghuai etc. exists 《Magnetic Nanoparticle Supported Second Generation Hoveyda-Grubbs Catalyst For Metathesis of Unsaturated Fatty Acid Esters ", Adv.Synth.Catal.2009,351, It is disclosed in 2650-2656 and loads bis- generation of Hoveyda-Grubbs catalyst on magnetic nano-particle simultaneously by chemical means Method applied to olefin metathesis reaction；For another example, Yang H. etc. is in " Hoveyda-Grubbs Catalyst Confined in the Nanocages of SBA-1:Enhanced Recyclability for Olefin Metathesis》, It is disclosed in Chem.Commun.2010,46,8659-8661 by Catalyst Adsorption in molecular sieve and applied to olefin metathesis Method.The present invention selects common preparation method.
Another preferred embodiment that the compound containing catalyst is prepared in the present invention is by catalyst and other choosings Auxiliary agent existing for selecting property is coated on using polymer as in the microcapsules of shell.Wherein, as the polymer of microcapsules outer wall without spy Other limitation as an example but is not limited to following lifted: natural polymer such as Arabic gum, sodium alginate, agar etc., semi-synthetic Macromolecule such as cellulose derivative, synthesis macromolecule for example polyolefin, polyester, polyethers, polyurethane, polyureas, poly(urea formaldehyde), polyamide, Polyvinyl alcohol, polysiloxanes etc..It is known disclosed skill that catalyst, which is coated on by the method in the microcapsules of shell of polymer, Art means, for example, S.H.Cho etc. is at " Polydimethylsiloxane-Based Self-Healing Materials " The method for preparing polyurethane microcapsule is disclosed in Adv.Mater.2006,18,997-1000；For another example, E.N.Brown etc. exists 《In situ poly(urea-formaldehyde)Microencapsulation of Dicyclopentadiene》 The method of preparation ureaformaldehyde microcapsules is disclosed in J.Microencapsulation 2003,20,719-730.The present invention selects logical Normal preparation method.
In the following, being deposited to hybrid mode, existence form, other alternatives of hydridization dynamic aggregation compositions in the present invention Ingredient etc. be described in detail.
In embodiments of the present invention, hydridization can be moved with any appropriate material hybrid mode known in the art State polymer composition components A (or each material in component A) and component B (or each material in component B) is by being mixed with Hydridization dynamic aggregation compositions can be interval, semicontinuous or continuous processing form mixing；Similarly, it also may be selected Intermittently, semicontinuous or continuous processing form forms hydridization dynamic aggregation compositions.The hybrid mode of use include but Be not limited only to solution be stirred, melt be stirred, mediate, mixing, mill, melting extrusion, ball milling etc., wherein it is preferred that solution It is stirred, melts and be stirred and melting extrusion.Energy in material mixed process provides form and includes but are not limited to Heating, illumination, radiation, microwave, ultrasound.The molding mode of use includes but are not limited to extrusion molding, is injection moulded, is molded into Type, tape casting, calendering formation, cast molding.
In embodiments of the present invention, it is stirred using solution and melting is stirred, mainly in a manner of following two Carry out: (1) being directly stirred reaction mass in the reactor or heating melting after be stirred reaction, such mode is general Reaction mass be liquid or lower melting-point solid or reaction mass is more difficult find cosolvent in the case where use；(2) will Reaction mass is dissolved in respective solvent or is stirred mixing in common solvent in the reactor, and such mode is general It is used in the case where reaction mass is higher fusing point or solid of not definite melting point.Mixing temperature is not particularly limited, and leads to Often at 0-200 DEG C, preferably 25-120 DEG C, more preferable 25-80 DEG C, mixing time is not particularly limited, and is preferably controlled in 1 point Clock is 10-120 minutes more preferable to 12 hours.The product obtained after mixing is poured into suitable mold, suitable Under the conditions of temperature, preferably at 0-150 DEG C, under the conditions of more preferable 25-80 DEG C of temperature, place the regular hour, preferably 0-48 hours Polymer samples can be obtained, this can remove solvent as needed in the process.
Used solvent in above-mentioned preparation method, it has to be possible to while dissolve reaction mass respectively, and dissolve There is the solvent of two class compounds to allow for dissolving each other, reaction mass is not precipitated in the mixed solvent, and solvent used includes but not Be only limitted to it is following any or appoint several solvents mixed solvents: deionized water, methanol, ethyl alcohol, acetonitrile, acetone, butanone, benzene, Toluene, dimethylbenzene, chlorobenzene, ethyl acetate, ether, methyl tertiary butyl ether(MTBE), tetrahydrofuran (THF), chloroform, methylene chloride, 1,2- Dichloroethanes, 1,1,2,2- tetrachloroethanes, dimethyl sulfoxide (DMSO), dimethylformamide (DMF), dimethyl acetamide, N- Methyl pyrrolidone, isopropyl acetate, n-butyl acetate, trichloro ethylene, mesitylene, dioxanes, trishydroxymethylaminomethane (Tris) buffer, citrate buffer solution, acetic acid buffer solution, phosphate buffer solution, borate buffer solution etc.；It is preferred that deionization Water, ethyl alcohol, toluene, chloroform, methylene chloride, 1,2- dichloroethanes, DMF, phosphate buffer solution.
In embodiments of the present invention, the specific of hydridization dynamic aggregation compositions material is mixed with using melting extrusion A certain amount of reaction mass, is usually added in extruder and carries out extrusion blending reaction by preparation method, and extrusion temperature does not have Especially limitation, usually 0-280 DEG C, preferably 25-150 DEG C, more preferable 50-100 DEG C.Reaction product can be cut out after direct tape casting At suitable dimension, sample preparation either is carried out using injection molding machine or moulding press.Injection temperature is not particularly limited, usually 0-280 DEG C, preferably 25-150 DEG C, more preferable 50-100 DEG C；Molding temperature is not particularly limited, usually 0-280 DEG C, preferably 25-150 DEG C, more preferable 50-100 DEG C, clamp time is not particularly limited, usually 0.5-60min, preferably 1-10min.Batten is placed in In suitable mold, at 25-150 DEG C, under the conditions of preferably 50-80 DEG C of temperature, 0-24h is placed, final composition sample is obtained.
In embodiments of the present invention, in the hydridization dynamic aggregation compositions, the quality of component A account for component A, The range of the ratio of B quality sum is 90-99.99%, and the range that the quality of component B accounts for the ratio of component A, B quality sum is 0.01-10% can also contain other components in composition.
In the present invention, the form of the hydridization dynamic aggregation compositions can be ordinary solid, elastomer, coagulate Glue, foam etc..Wherein, the dissolvable small-molecular-weight component content contained in ordinary solid, elastomer and foamed material is generally not Higher than 10wt%, and the small-molecular-weight component content contained in gel is generally not less than 50wt%.Ordinary solid mechanical property is good, Mechanics of elastic bodies moderate performance but has the unexistent flexibility of ordinary solid, preparation method is also most easy, therefore more preferably. Foam is since light and hardness and bendable folding endurance are adjustable, and purposes is wide, therefore also more preferably.In embodiment party of the invention In formula, sweller can be introduced in hydridization dynamic aggregation compositions, prepare hydridization dynamic aggregation compositions gel.Gel Product flexibility and bendable folding endurance are all good, and can have certain toughness by structure and formula adjustment, because there are molten Swollen dose, the unexistent beneficial constituent of material of many other forms can be incorporated, there is special purposes.Wherein, described Sweller can include but is not limited to organic solvent, ionic liquid, oligomer, plasticizer, water.
A kind of hydridization dynamic aggregation compositions gel provided by the present invention, including organic solvent gel, ionic liquid Gel, oligomer swell gel, plasticizer swell gel, hydrogel.Wherein, preferred ion liquid gel and plasticising solvent swell are solidifying Glue.In the presence of hydridization dynamic aggregation compositions are with different existence forms, especially with the shape of hydrogel and ionic gel It is needed in the presence of formula using adaptable component B.
A kind of preferred preparation method of hydridization dynamic aggregation compositions ionic liquid gel of the invention includes but unlimited In following steps: each raw material for preparing hydridization dynamic aggregation compositions component A, B and other raw materials are added to ionic liquid In body, making the sum of prepared mass fraction of hydridization dynamic aggregation compositions component A, B is 0.5~70%, by described Appropriate means are polymerize, are coupled, are crosslinked or other kinds of chemical reaction, after reaction, that is, a kind of hydridization dynamic are made Polymer composition ionic liquid gel.Another hydridization dynamic aggregation compositions ionic liquid gel of the invention it is preferred Preparation method includes but is not limited to following steps: by described hydridization dynamic aggregation compositions component A, B and and other originals Material is swollen in ionic liquid or solvent containing ionic liquid, makes the quality of hydridization dynamic aggregation compositions component A, B The sum of score is 0.5~70%, one kind is made in the solvent for sufficiently removing extra ionic liquid after swelling and selectively using Hydridization dynamic aggregation compositions ionic liquid gel.When selecting ionic liquid and when catalytic component B, should be avoided positive and negative from Son causes catalyst or its complex components B to decompose inactivation.As an example, the group of preferred ionic liquid and catalytic component B Conjunction includes but is not limited to: 1- butyl -2,3- methylimidazole/tetrafluoroborate ion/catalyst 33,1- butyl -3- methyl miaow Azoles bis trifluoromethyl/fluorine-containing sulfimide ion/catalyst 35,1- butyl -3- methylimidazole/hexafluorophosphoricacid acid ions/catalysis Agent 36 etc..
A kind of preferred preparation method of hydridization dynamic aggregation compositions oligomer swell gel of the invention includes but not It is limited to following steps: each raw material for preparing hydridization dynamic aggregation compositions component A, B and other raw materials and oligomer is total to It is mixed, make the mass fraction 0.5~70% of prepared hydridization dynamic aggregation compositions component A, B, passes through the suitable hand A kind of hydridization dynamic aggregation object is made after reaction in Duan Jinhang polymerization, coupling, crosslinking or other kinds of chemical reaction Composition oligomer swell gel.The preferred system of another hydridization dynamic aggregation compositions oligomer swell gel of the invention Preparation Method includes but is not limited to following steps: hydridization dynamic aggregation compositions component A, B and other raw materials is molten It is swollen in the solvent containing oligomer, make the sum of mass fraction of hydridization dynamic aggregation compositions component A, B be 0.5~ 70%, solvent sufficiently is removed after swelling, that is, a kind of hydridization dynamic aggregation compositions oligomer swell gel is made.
A kind of preferred preparation method of hydridization dynamic aggregation compositions plasticizer swell gel of the invention includes but not It is limited to following steps: each raw material for preparing hydridization dynamic aggregation compositions component A, B and other raw materials is added to plasticising In agent, making the sum of prepared mass fraction of hydridization dynamic aggregation compositions component A, B is 0.5~70%, by described Appropriate means are polymerize, are coupled, are crosslinked or other kinds of chemical reaction, after reaction, that is, a kind of hydridization dynamic are made The gel of polymer composition plasticising solvent swell.Another hydridization dynamic aggregation compositions plasticizer swell gel of the invention Preferred preparation method include but is not limited to following steps: by hydridization dynamic aggregation compositions component A, B and its He swells in the solvent containing plasticizer raw material, make hydridization dynamic aggregation compositions component A, B mass fraction it Be 0.5~70%, sufficiently swelling after remove solvent, that is, a kind of hydridization dynamic aggregation compositions plasticizer swell gel is made.
A kind of preferred preparation method of hydridization dynamic aggregation compositions hydrogel of the invention is including but not limited to as follows Step: each raw material for preparing hydridization dynamic aggregation compositions component A, B and other raw materials are added to the water, and are made prepared The sum of the mass fraction of hydridization dynamic aggregation compositions component A, B be 0.5~70%, gathered by the appropriate means It closes, be coupled, a kind of dynamic aggregation object hydrogel is made after reaction in crosslinking or other kinds of chemical reaction.The present invention The preferred preparation method of another hydridization dynamic aggregation compositions hydrogel include but is not limited to following steps: will be described Hydridization dynamic aggregation compositions component A, B and other raw materials are sufficiently swollen in water, make the hydridization dynamic aggregation object group The sum of mass fraction of polymer component A, B is 0.5~70%, removes extra water, that is, a kind of hydridization dynamic aggregation object group is made Close object hydrogel.When dynamic aggregation object, which swells in water, forms hydrogel, it should select insensitive to water and have in water molten enough The component B of Xie Du, as an example, the catalyst that can be used for hydrogel includes but is not limited to such as catalyst 25-32.
In embodiments of the present invention, hydridization dynamic aggregation compositions can be prepared into foamed material.Wherein, foam packet Include flexible foam or semi-flexible, semi-rigid, micropore or rigid foam.
In embodiments of the present invention, the structure of hydridization dynamic aggregation compositions foamed material be related to open-celled structure, Three kinds of hole-closing structure, half-open semi-closure structure etc..It in open-celled structure, is interconnected between abscess and abscess, or connection completely, one-dimensional Or three-dimensional can be transferred through gas or liquid, abscess diameter is 0.01 to 3mm etc..Hole-closing structure has individual blisters structure, internal There is wall film to separate between abscess and abscess, the overwhelming majority is not interconnected, and abscess diameter is 0.01 to 3mm etc..Contained Abscess is existing to be interconnected again that have mutual disconnected structure be then half open-celled structure.
In embodiments of the present invention, foaming method is usual way, can be divided according to the difference of foaming agent used For physical blowing method and chemical blowing process two major classes.Foam can have water or it is anhydrous under the conditions of prepare, mechanical can send out Bubble or on-mechanical foaming.Wherein, in order to avoid in foaming process component B inactivate at high temperature, preferably entire foaming process temperature Degree is not higher than 110 DEG C of foaming method.Further, the non-reacted hair of auxiliary known in the art can be used in the preparation of foam Infusion.
A kind of preparation method of preferred hydridization dynamic aggregation compositions foam of the present invention, includes the following steps: making When standby single network dynamic aggregation object foam, two component reaction materials are first prepared.Reaction mass one includes to generate hydridization dynamic to gather All small molecule monomers of polymer composition component A, chain extender, crosslinking agent etc. and component B and the auxiliary agent needed for other；Instead Answering material two includes foaming agent, foam stabiliser, the catalyst for being catalyzed foaming and/or polymerization crosslinking reaction and other institutes The auxiliary agent needed.Then two component reaction materials are mixed according to a certain percentage, is stirred, and carry out temperature control as needed, obtained To the single network polymer of foaming.By the hydridization dynamic aggregation of this preparation method preparation hydridization dynamic aggregation compositions foam Object is preferably based on the polymer of polyurethane, polyureas.
The preparation method of another preferred hydridization dynamic aggregation compositions foam of the invention is freeze-drying, including Following steps: the hydridization dynamic aggregation compositions for swelling in volatile solvent are freezed, then close under vacuum condition Solvent is escaped in a manner of distillation.During solvent evolution and after evolution, composition can maintain the shape before freezing, Thus the foamed material of porous spongy is obtained.
In hydridization dynamic aggregation compositions foam preparation processes of the invention, when in foam contain multiple polymer networks When, multiple networks can generate simultaneously, can also be separately generated.
Hydridization dynamic aggregation compositions foamed material provided by the present invention further relates to: by welding, gluing, cutting, The hydridization dynamic aggregation compositions foamed material is transformed into any by matching plane, perforation, coining, lamination and hot forming Need shape, such as pipe, stick, sheath, container, ball, piece, volume and band；By lamination, bonding, fusion and other interconnection technique, By skill in the hydridization dynamic aggregation compositions foamed material and sheet material, film, foam, fabric, stiffener and this field Other materials known to art personnel are combined into complicated interlayer structure together；The hydridization dynamic aggregation compositions foam material Expect the purposes in washer or sealing；The hydridization dynamic aggregation compositions foamed material is in packaging material or in a reservoir Purposes.About hydridization dynamic aggregation compositions of the invention, foamable hydridization dynamic aggregation compositions are such a Type allows to become them by other forming techniques known to extrusion, injection molding, compression moulding or those of skill in the art Shape.
Foamed material provided by the present invention is different from common foamed material, three-dimensional prepared by common foamed material Once being formed, structure cannot change structure again, repair difficulty, not can be recycled after damaged, and foamed material provided by the present invention, Although the polymer network of crosslinking, can also be repaired after being ruptured under certain condition, or pass through plastotype or recycling again Regeneration is done him and is used, and there are hydrogen bond actions and dynamic covalent bond while reason is in network structure.It is provided by the present invention Foamed material solves the problems, such as plastotype again, controllable reparation and the reclaiming of regular-type foam material.
Hydridization dynamic aggregation compositions material of the invention during the preparation process, in the range for not interfering the object of the invention It is interior, it can also according to circumstances select to be added or used to other polymers, auxiliary agent, filler, sweller and come collectively as hydridization dynamic The recipe ingredient of polymer composition can improve material processing performance, improve product quality and yield, and reduce product cost Or assign certain distinctive application performance of product, but these additives it is not necessary to.
Wherein, the other polymers can play in system as additive and improve material property, assign material Material new capability improves materials'use and economic benefit, has the function that material comprehensively utilizes.Addible other polymers, It can be selected from natural polymer, synthetic macromolecular compound.The present invention is to the character of added polymer and is had Some molecular weight can be oligomer or high polymer according to the difference of molecular weight without limitation, according to the difference of polymeric species, Can be homopolymer or copolymer, in the specific use process should be according to the performance of target material and the need of actual fabrication process It wants and is selected.
When the other polymers are selected from natural polymer, it can be selected from following any or appoint several days Right high-molecular compound: natural rubber, chitosan, chitin, native protein, polysaccharide etc..
When the other polymers are selected from synthetic macromolecular compound, it can be selected from following any or appoint several: Polytrifluorochloroethylene, haloflex, chliorinated polyvinyl chloride, polyvinyl chloride, Vingon, low density polyethylene (LDPE), middle density Polyethylene, high density polyethylene (HDPE), ultra-high molecular weight polyethylene, melamine formaldehyde resin, polyamide, polyacrylic acid, polypropylene Acid esters, polyacrylamide, polyacrylonitrile, polybenzimidazoles, polyethylene terephthalate, polybutylene terephthalate Ester, polycarbonate, polyethylene glycol, polyester, polyether sulfone, polyarylsulfone (PAS), polyether-ether-ketone, tetrafluoroethylene-perfluoro propane copolymer, polyamides Imines, polyacrylate, polyacrylonitrile, polyphenylene oxide, polypropylene, polyphenylene sulfide, polyphenylsulfone, polystyrene, high-impact polyphenyl second Alkene, polysulfones, polytetrafluoroethylene (PTFE), polyurethane, polyureas, polyvinyl acetate, ethylene-propylene copolymer, ethane-acetic acid ethyenyl ester are total Polymers, AAS acrylonitrile acryloid styrene, acrylonitrile-butadiene-styrene copolymer, vinyl chloride-acetate Ester copolymer, polyvinylpyrrolidone, epoxy resin, phenolic resin, Lauxite, unsaturated polyester (UP), polyisoprene, gather it is suitable Butadiene, styrene-butadiene copolymer, hycar, poly- (the chloro- 1,3- butadiene of 2-), isobutene-are different Pentadiene copolymer, ethylene-propylene-Isosorbide-5-Nitrae-hexadiene copolymer, ethylene-propylene-dicyclopentadiene copolymer, ethylene-propylene- Ethylidene norbornene copolymer, dimethyl silicone polymer, Polymethyl methacrylate, polymethylphenylsiloxane, poly- methyl Vinyl benzene radical siloxane, poly- methyl ethylene trifluoropropyl siloxane, vinylidene-chlorotrifluoroethylene, inclined fluorine second Alkene-hexafluoropropylene copolymer, vinylidene-tetrafluoraoethylene-hexafluoropropylene copolymer, tetrafluoroethylene propylene copolymer, polycyclic oxygen Chloropropane, epichlorohydrin ethylene oxide copoymer, epoxychloropropane-ethylene oxide-propylene oxide copolymer etc..
Wherein, the type of other polymers does not limit, mainly depending on required material property；Other used are poly- The dosage for closing object is not particularly limited, generally 1-50wt%.
Wherein, the auxiliary agent may include but be not limited to the combination of following one or more, such as additive synthesis, including catalysis Agent, initiator；Stabilizing additive, including antioxidant, light stabilizer, heat stabilizer, dispersing agent, emulsifier, fire retardant；Improve The auxiliary agent of mechanical property, including toughener, coupling agent；Improve the auxiliary agent of processing performance, including solvent, lubricant, release agent, increasing Mould agent, thickener, thixotropic agent, levelling agent；Change the auxiliary agent of coloured light, including colorant, fluorescent whitening agent, delustering agent；Other are helped Agent, including antistatic agent, biocide mildewcide, foaming agent, foam stabiliser, nucleating agent, rheological agent etc..
Catalyst in the auxiliary agent can reduce reaction activity by changing reaction path to accelerate to react The reaction rate of object during the reaction.It includes but are not limited to following any or appoints several catalyst: 1. polyurethane closes At with catalyst: amines catalyst, such as triethylamine, triethylenediamine, bis- (dimethylaminoethyl) ethers, 2- (2- dimethylamino- Ethyoxyl) ethyl alcohol, trimethyl hydroxyethylammonium propane diamine, N, bis- (dimethylamine propyl) isopropanolamines of N-, N- (dimethylamino-propyl) two Isopropanolamine, N, N, N '-trimethyl-N '-ethoxy diamine ethylether, tetramethyl dipropylenetriamine, N, N- dimethyleyelohexane Amine, N, N, N ', N '-tetramethyl Alkylenediamine, N, N, N ', N ', N '-five methyl diethylentriamine, N, N- dimethyl ethanol Amine, N-ethylmorpholine, 2,4,6- (dimethylamino methyl) phenol, trimethyl-N-2- hydroxypropyl caproic acid, N, N- dimethyl benzylamine, N, N- dimethyl cetylamine etc.；Organometallic catalysts, such as stannous octoate, dibutyltin dilaurate, dioctyl tin two Laurate, zinc Isoocatanoate, isooctyl acid lead, potassium oleate, zinc naphthenate, cobalt naphthenate, ferric acetyl acetonade, phenylmercuric acetate, propionic acid Benzene mercury, bismuth naphthenate, sodium methoxide, potassium octanoate, potassium oleate, calcium carbonate etc.；2. polyolefin catalyst for synthesizing: such as Ziegler- Natta catalyst, π-allyl nickel, alkyl lithium catalyst, metallocene catalyst, aluminium diethyl monochloride, titanium tetrachloride, tri-chlorination Titanium, boron trifluoride etherate, magnesia, dimethylamine, stannous chloride, triethylamine, tetraphenylboron sodium, antimony oxide, sesquialter Ethylmercury chloride aluminium, vanadium oxytrichloride, triisobutyl aluminium, nickel naphthenate, naphthenic acid rare earth etc.；3. CuAAC catalysts: by monovalence Copper compound and amine ligand share concerted catalysis；Monovalence copper compound can be selected from Cu (I) salt, as CuCl, CuBr, CuI, CuCN, CuOAc etc.；Also selected from Cu (I) complex compound, such as [Cu (CH3CN)4]PF6、[Cu(CH3CN)4]OTf、CuBr(PPh3)3Deng；Amine Ligand can be selected from three [(1- benzyl -1H-1,2,3- triazole-4-yl) methyl] amine (TBTA), three [(1- tert-butyl -1H-1,2,3- Triazole-4-yl) methyl] amine (TTTA), three (2- benzimidazole methyl) amine (TBIA), hydration bathophenanthroline disulfonic acid sodium etc.；④ Thiol-ene catalysts: photochemical catalyst, such as dimethoxybenzoin, 2- hydroxy-2-methyl phenylacetone, 2,2- dimethoxy Base -2- phenyl acetophenone etc.；Nucleopilic reagent catalyst, such as ethylenediamine, triethanolamine, triethylamine, pyridine, 4- dimethylamino pyrrole Pyridine, imidazoles, diisopropyl ethyl amine etc..Catalyst amount used is not particularly limited, generally 0.01-0.5wt%.
Initiator in the auxiliary agent can cause monomer molecule to activate in polymerization process and generate free Base improves reaction rate, and reaction is promoted to carry out, and includes but are not limited to following any or appoints several initiators: 1. free radical Polymerization initiator: organic peroxide, such as lauroyl peroxide, benzoyl peroxide (BPO), dicetyl peroxydicarbonate diisopropyl Bis- (4- tert-butylcyclohexyl) esters of ester, di-cyclohexylperoxy di-carbonate, dicetyl peroxydicarbonate, tert-butyl hydroperoxide benzoic acid Ester, tert-butyl hydroperoxide pivalate, di-tert-butyl peroxide, di-isopropylbenzene hydroperoxide；Azo-compound, such as azo two Isobutyronitrile (AIBN), azobisisoheptonitrile；Inorganic peroxide, such as ammonium persulfate, potassium peroxydisulfate；2. living polymerization causes Agent: such as 2,2,6,6- tetramethyl -1- oxygroup piperidines, 1- chloro-1-phenyl ethane/stannous chloride/bis- pyridines ternary system；3. from Son polymerization initiator: such as butyl lithium, sodium/naphthalene system, boron trifluoride/aqueous systems, tin tetrachloride/alkyl halide system；4. matching Position polymerization initiator: such as titanium tetrachloride/triethyl aluminum system, two zirconium cyclopentadienyl of dichloro/methylaluminoxane system；5. ring-opening polymerisation With initiator: such as sodium methoxide, potassium methoxide, ethylenediamine, hexamethylene diisocyanate, stannous octoate.Wherein, the preferred mistake of initiator Aoxidize lauroyl, benzoyl peroxide, azodiisobutyronitrile, potassium peroxydisulfate.Initiator amount used is not particularly limited, and one As be 0.1-1wt%.
Antioxidant in the auxiliary agent can delay the oxidation process of polymer samples, guarantee that material can be suitable It is processed and is prolonged its service life sharply, include but are not limited to following any or appoint several antioxidant: Hinered phenols, Such as 2,6 di tert butyl 4 methyl phenol, 1,1,3- tri- (- 4 hydroxyl -5- tert-butyl-phenyl of 2- methyl) butane, four [β-(3,5- Di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, 2,2 '-di-2-ethylhexylphosphine oxides (4- methyl-6-tert-butylphenol)；Sulfur-bearing by Hinder phenols, such as 4,4 '-thiobis-[3 methy 6 tert butyl phenol], 2,2 '-thiobis-[4- methyl-6-tert-butylphenol]； Triazine system hindered phenol, such as 1,3,5- bis- [β-(3,5- di-tert-butyl-hydroxy phenyl) propionyl]-perhydro-s-triazines；Trimerization isocyanide Acid esters Hinered phenols, such as three (3,5- di-tert-butyl-4-hydroxyl benzyl)-triisocyanates；Amine, such as N, N '-two (betanaphthyl) P-phenylenediamine, N, N '-diphenyl-para-phenylene diamine, N- phenyl-N '-cyclohexyl p-phenylenediamine；Sulfur-bearing class, such as thiodipropionic acid dilauryl Osmanthus ester, 2-mercaptobenzimidazole, 2-mercaptobenzothiazole；Phosphorous acid esters, such as triphenyl phosphite, three nonyl benzene of phosphorous acid Ester, three [2.4- di-tert-butyl-phenyl] phosphite esters etc.；Wherein, the preferred tea polyphenols of antioxidant (TP), butylated hydroxy anisole (BHA), dibutyl hydroxy toluene (BHT), tert-butyl hydroquinone (TBHQ), three [2.4- di-tert-butyl-phenyl] phosphite esters (irgasfos 168), four [β-(3,5- di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol esters (antioxidant 1010).Used Antioxidant dosage is not particularly limited, generally 0.01-1wt%.
Light stabilizer in the auxiliary agent can prevent polymer samples from light aging occurs, prolong its service life, It includes but are not limited to following any or appoints several light stabilizers: photomask agent, such as carbon black, titanium dioxide, zinc oxide, sulfurous Sour calcium；Ultraviolet absorbing agent, such as ESCALOL 567,2-hydroxy-4-n-octoxybenzophenone, 2- (2- hydroxyl Base -3,5- di-tert-butyl-phenyl) -5- chlorobenzotriazole, 2- (2- hydroxy-5-methyl base phenyl) benzotriazole, (the 2- hydroxyl of 2,4,6- tri- Base -4- n-butoxyphenyl) -1,3,5- s-triazine, 2- cyano -3,3- diphenylacrylate 2- ethylhexyl；Pioneer's type is ultraviolet Light absorbers, such as the p- tert-butyl phenyl ester of salicylic acid, double acid double phenol A ester；UV quenchers, such as bis- (3,5- bis- tertiary fourths Base -4- benzylphosphonic acid mono ethyl ester), 2,2 '-thiobis (4- spy's octyl phenol oxygroup) nickel；Hindered amine light stabilizer, such as the last of the ten Heavenly stems two Bis- (2,2,6,6- tetramethyl piperidine) esters of acid, benzoic acid (2,2,6,6- tetramethyl piperidine) ester, three (1,2,2,6,6- pentamethyl piperazines Piperidinyl) phosphite ester；Other light stabilizers, such as 3,5- di-tert-butyl-4-hydroxybenzoic acid (2,4- di-tert-butyl) ester, alkyl Phosphoamide, N, N '-zinc dibutyl dithiocaarbamate, N, positive fourth positive group aminodithioformic acid nickel of N '-two etc.；Its In, bis- (2,2,6, the 6- tetramethyl piperidine) esters (light stabilizer 770) of the preferred carbon black of light stabilizer, decanedioic acid.Light used is stablized Agent dosage is not particularly limited, generally 0.01-0.5wt%.
Heat stabilizer in the auxiliary agent enables to polymer samples in processing or use process not due to heated Chemical change occurs, or delays these variations to achieve the purpose that prolong the service life comprising but it is not limited only to following A kind of or several heat stabilizers: lead salts, such as lead sulfate tribasic, dibasic lead phosphite, dibasic lead stearate, disalt Base phthalic acid lead, tribasic Malaysia lead plumbate, slag lead silicate, lead stearate, lead salicylate, dibasic phthalic acid Lead, basic lead carbonate, silica gel are co-precipitated lead silicate；Metal soap: such as cadmium stearate, barium stearate, calcium stearate, stearic acid Lead, zinc stearate；Organo-tin compound class, such as di-n-butyltin dilaurate, Bis(lauroyloxy)dioctyltin, maleic acid two (just) butyl tin, double single-ethylhexyl maleate dioctyltins, dimercapto 2-ethyl hexyl ethanoate dioctyltin, capital tin C-102, two mercaptos Guanidine-acetic acid isooctyl stannous methide, two mercaptan stannous methides and its compound；Antimony stabilizer, such as mercaptan antimonic salt, mercaptoacetate Mercaptans type, mercapto-carboxylic ester antimony, carboxylate antimony；Epoxy compound species, such as epoxidized oil, epoxy aliphatic ester, epoxy resin；It is sub- Phosphoric acid ester, such as three aromatic ester of phosphorous acid, three alkyl ester of phosphorous acid, three aralkyl ester of phosphorous acid, alkane virtue mixed ester, aggretion type phosphorous acid Ester；Polyalcohols, such as pentaerythrite, xylitol, mannitol, D-sorbite, trimethylolpropane；Composite thermal stabilizer, such as altogether Precipitate metallic soap, liquid metal soap compound stabilizer, organotin compound stabilizer etc.；Wherein, the preferred barium stearate of heat stabilizer, Calcium stearate, di-n-butyltin dilaurate, maleic acid two (just) butyl tin.Heat stabilizer dosage used does not limit especially It is fixed, generally 0.1-0.5wt%.
Dispersing agent in the auxiliary agent enables to solid flocculation group in mixed with polymers liquid to be separated into tiny particle And be suspended in liquid, those are poorly soluble the solid and liquid particles in liquid for uniform dispersion, while can also prevent particle Sedimentation and cohesion form stable suspension comprising but be not limited only to following any or appoint several dispersing agents: anionic, Such as alkylsurfuric acid ester sodium salt, sodium alkyl benzene sulfonate, petroleum sodium sulfonate；Cationic；It is non-ionic, such as aliphatic alcohol polyethenoxy Ether, sorbitol anhydride fatty acid polyoxyethylene ether；Inorganic type, such as silicate, condensed phosphate；Polymer electrolyte, such as starch, bright Glue, water-soluble glue, lecithin, carboxymethyl cellulose, hydroxyethyl cellulose, sodium alginate, lignosulfonates, polyvinyl alcohol Deng.Wherein, the preferred neopelex of dispersing agent, naphthalene system methylene sulfonate (dispersing agent N), aliphatic alcohol polyethenoxy Ether, dispersant dosage used are not particularly limited, generally 0.3-0.8wt%.
Emulsifier in the auxiliary agent can improve in the mixed with polymers liquid comprising auxiliary agent between various composition phases Surface tension is allowed to form uniform and stable dispersion or emulsion comprising but be not limited only to following any or appoint several Kind emulsifier: anionic, such as higher fatty acid salt, alkylsulfonate, alkylbenzene sulfonate, Negel, succinic acid Sulfonated ester, petroleum sulfonate, aliphatic alcohol sulfate, castor oil salt, sulphation butyl ricinoleate salt, phosphate ester salt, Fatty acyl-peptide condensation product；Cationic, such as alkylammonium salt, alkyl quaternary ammonium salts, Fixanol；Amphoteric ion type, such as carboxylate Type, sulfonic acid ester type, sulfuric acid ester type, phosphate type；It is non-ionic, such as fatty alcohol polyoxyethylene ether, alkyl phenol polyoxyethylene ether, rouge Fat acid polyoxyethylene ester, polypropylene oxide-ethylene oxide adduct, fatty acid glyceride, pentaerythritol fatty ester, sorbierite And sorbitan fatty acid ester, sucrose fatty ester, hydramine fatty acid amide etc..Wherein, preferably neopelex, lose Water Span, triethanolamine stearate (Emulphor FM), emulsifier used are not particularly limited, generally For 1-5wt%.
Fire retardant in the auxiliary agent can increase the flame resistance of material comprising but be not limited only to following any Or appoint several fire retardants: phosphorus system, such as red phosphorus, tricresyl phosphate, triphenyl phosphate, tricresyl phosphate, tricresyl phosphate hexichol Ester；Halogen phosphoric acid ester, such as three (2,3- dibromopropyl) phosphates, tricresyl phosphate (2,3- dichloro the third) ester；Organohalogen compounds are such as high Chlorinty chlorinated paraffin, 1,1,2,2- tetrabromoethane, deca-BDE, penta decane of perchloro- ring；Inorganic fire retardants, such as three oxidations two Antimony, aluminium hydroxide, magnesium hydroxide, zinc borate；Reactive flame retardant, such as chlorendic anhydride, bis- (2,3- dibromopropyl) anti-butylene two Acid esters, tetrabromobisphenol A, tetrabromophthalic anhydride etc.；Wherein, the preferred deca-BDE of fire retardant, triphenyl phosphate, tricresyl phosphate Toluene ester, phosphate toluene diphenyl ester, antimony oxide.Amount of flame-retardant agent used is not particularly limited, generally 1-20wt%.
Toughener in the auxiliary agent can reduce polymer samples brittleness, increase toughness, and it is strong to improve material carrying Degree comprising but be not limited only to following any or appoint several toughener: methyl methacrylate-butadiene-styrene copolymerization Resin, chlorinated polyethylene resin, ethylene-vinyl acetate copolymer resin and its modifier, acrylonitrile-butadiene-benzene second Alkene copolymer, acrylonitrile-butadiene copolymer, the third glue of second, ethylene-propylene diene copolymer, cis-butadiene cement, butadiene-styrene rubber, styrene-butadiene-benzene Ethylene block copolymer etc.；Wherein, preferred the third glue of second of toughener, acrylonitrile-butadiene-styrene copolymer (ABS), benzene second Alkene-butadiene-styrene block copolymer (SBS), Methyl Methacrylate-Butadiene-Styrene Copolymer resin (MBS), Chlorinated polyethylene resin (CPE).Toughener dosage used is not particularly limited, generally 5-10wt%.
Coupling agent in the auxiliary agent can improve the interface characteristics of polymer samples and inorganic filler or reinforcing material Can, the viscosity of material melt is reduced in plastic processes, improves the dispersion degree of filler to improve processing performance, and then make to make Product obtain good surface quality and machinery, heat and electrical property comprising but be not limited only to following any or appoint several couplings Agent: chromium of organic acid complex compound, silane coupling agent, titanate coupling agent, sulfonyl azide coupling agent, aluminate coupling agent etc.；Wherein, The preferred gamma-aminopropyl-triethoxy-silane of coupling agent (Silane coupling agent KH550), γ-(the third oxygen of 2,3- epoxy) propyl trimethoxy Base silane (silane coupling agent KH560).Coupling agent dosage used is not particularly limited, generally 0.5-2wt%.
Solvent in the auxiliary agent, adjustable viscosity are convenient for technological operation, make in product preparation process or in preparing With.Its include but are not limited to it is following any or appoint it is several: hydro carbons (such as hexamethylene, heptane), halogenated hydrocarbon (such as methylene chloride, Chloroform, tetrachloromethane), aromatic hydrocarbons (such as toluene, dimethylbenzene), ketone (such as acetone, methyl ethyl ketone), ethers (such as ether, tetrahydro furan Mutter, dioxane), esters (such as ethyl acetate, butyl acetate), glycol ether-ether (such as ethylene glycol ether acetate, propylene glycol list first Ether acetate), dimethylformamide (DMF), N-Methyl pyrrolidone (NMP) etc..Solvent usage used is not particularly limited, Generally 1-200wt%.
Lubricant in the auxiliary agent can be improved the lubricity of polymer samples, reduce friction, reduce Interface Adhesion Performance comprising but be not limited only to following any or appoint several lubricants: saturated hydrocarbons and halogenated hydrocarbon, such as solid paraffin, micro- Spar wax, atoleine, low molecular weight polyethylene, oxidized polyethylene wax；Fatty acid, such as stearic acid, hydroxy stearic acid；Fat Esters of gallic acid, such as fatty acid low-carbon-ester, polyol esters of fatty acids, native paraffin, ester type waxes and saponified wax；Aliphatic amide type is such as hard Acyl amine or stearic amide, oleamide or oleamide, erucyl amide, N, N '-ethylene bis stearamide；Fatty alcohol and polynary Alcohols, such as stearyl alcohol, cetanol, pentaerythrite；Metal soap, as lead stearate, calcium stearate, barium stearate, magnesium stearate, Zinc stearate etc.；Wherein, the preferred solid paraffin of lubricant, atoleine, stearic acid, low molecular weight polyethylene.Lubrication used Agent dosage is not particularly limited, generally 0.5-1wt%.
Release agent in the auxiliary agent, it can make polymer samples be easy to demould, and surface is smooth, clean comprising but It is not limited only to following any or appoints several release agents: paraffin hydrocarbon, soaps, dimethicone, ethyl silicon oil, aminomethyl phenyl silicon Oil, castor oil, used oil, mineral oil, molybdenum disulfide, polyethylene glycol, vinyl chloride resin, polystyrene, silicon rubber, polyvinyl alcohol Deng；Wherein, the preferred dimethicone of release agent, polyethylene glycol.Release agent dosage used is not particularly limited, generally 0.5- 2wt%.
Plasticizer in the auxiliary agent can increase the plasticity of polymer samples, so that the hardness of polymer, mould Amount, softening temperature and brittle temperature decline, elongation, flexibility and flexibility improve comprising but be not limited only to following any Kind appoints several plasticizer: Phthalates: dibutyl phthalate, dioctyl phthalate, phthalic acid two Different monooctyl ester, dibutyl phthalate (DHP), diisooctyl phthalate, diisononyl phthalate, phthalic acid fourth benzyl Bis- (13) esters of ester, butyl phthalate butyl glycolate, dicyclohexyl phthalate, phthalic acid, terephthaldehyde Sour two (2- ethyl) own esters；Phosphoric acid ester, such as tricresyl phosphate, phosphoric acid (hexichol -2- ethyl) own ester；Fatty acid ester, such as The own ester of adipic acid two (2- ethyl), decanedioic acid two (2- ethyl) own ester；Epoxy compound species, such as epoxy glycerite esters, epoxy rouge Fatty acid monoester class, epoxy tetrahydrophthalic acid esters, epoxidized soybean oil, the own ester of epoxystearic acid (2- ethyl), epoxy soybean Oleic acid 2- ethylhexyl, the own ester of 4,5- epoxy tetrahydrophthalic acid two (2- ethyl), Chinese littleleaf box methyl acetylricinolate, binary Alcohol lipid, such as the sour glycol ester of C5~9, the sour Triethylene Glycol of C5~9；Class containing chlorine such as afforests paraffin class, chlorinated fatty acid Ester；Polyesters, such as ethanedioic acid 1,2-PD system polyester, decanedioic acid 1,2-PD polyester；Phenyl alkylsulfonate, trimellitic acid Ester, citrate, pentaerythrite and pentaerythritol fatty acid ester etc.；Wherein, plasticizer pref-erable dioctyl phthalate (DOP), neighbour Dibatyl phithalate (DBP), diisooctyl phthalate (DIOP), diisononyl phthalate (DINP), adjacent benzene two Formic acid diisodecyl ester (DIDP), tricresyl phosphate (TCP).Plasticizer consumption used is not particularly limited, generally 5- 20wt%.
Thickener in the auxiliary agent, can assign the good thixotropy of mixed with polymers liquid and consistency appropriate, and one As used during production of the invention and semi-finished product store comprising but be not limited only to following any or appoint several thickenings Agent: lower-molecular substance, such as fatty acid salt, fatty alcohol polyoxyethylene ether sulfate, alkyldimethylamine oxide, fatty acid monoethanol Amide, fatty diglycollic amide, fatty acid Isopropamide, anhydro sorbitol tricarboxylic ester, glycerol trioleate, coconut monoethanolamide Propyl betaine, 2- alkyl-N- carboxymethyl-N- hydroxyethyl imidazole quinoline, titanate coupling agent；Polymer substance, such as bentonite, manually Hectorite, fine particle silica, colloidal aluminum, plant polyose class, microbial polysaccharide class, animal protein, cellulose family, starch, Seaweed acids, poly-methyl acrylate, methacrylic acid copolymer, cis-butenedioic anhydride copolymer, crotonic acid-copolymers, polyacrylamide, Polyvinyl pyrrolidone, polyvinyl alcohol, polyethers, polyvinyl methyl ether urethane polymer etc.；Wherein, the preferred hydroxy ethyl fiber of thickener Element, coconut oil diethanol amide, acrylic acid-methacrylic acid copolymer.Thickener dosage used is not particularly limited, generally For 0.1-1.5wt%.
Thixotropic agent in the auxiliary agent is added in polymeric system, increases the thixotropy of polymeric system.Including but not It is only limitted to following any or appoints several: gas-phase silica, rilanit special, bentonite, silicic acid anhydride, silica derivative, urea Derivative etc..Thixotropic agent dosage used is not particularly limited, generally 0.5-2wt%.
Levelling agent in the auxiliary agent can guarantee the flat and smooth uniform of polymer coating film, improve film coated surface matter Amount improves dicoration comprising but be not limited only to following any or appoint several levelling agents: dimethyl silicone polymer, poly- methyl Phenyl siloxane, cellulose acetate butyrate, polyacrylate, organic siliconresin etc.；Wherein, the preferred poly dimethyl of levelling agent Siloxanes, polyacrylate.Levelling agent dosage used is not particularly limited, generally 0.5-1.5wt%.
Colorant in the auxiliary agent can make polymeric articles show required color, increase surface color and polish, It includes but are not limited to following any or appoints several colorants: inorganic pigment, such as titanium white, chrome yellow, cadmium red, iron oxide red, molybdenum chromium Red, ultramarine, chrome green, carbon black；Organic pigment, such as lithol red BK directions, lake red C, red, good base R is red, phthalocyanine is red, Yong Guyang The bright red R of red HF3C, the plastics and not red BR of Crow, forever solid orange HL, Fast Yellow G, vapour bar plastics Huang R, permanent yellow 3G, permanent yellow H2G, Phthalocyanine blue B, dark green, plastics purple RL, nigrosine；Organic dyestuff, such as thioindigo red, vat yellow 4GF, indanthrene blue RSN, slag rose Rare essence, Oil Yellow etc.；Wherein, the selection of colorant does not need to be particularly limited to depending on color sample demand.Coloring used Agent dosage is not particularly limited, generally 0.3-0.8wt%.
Fluorescent whitening agent in the auxiliary agent can make contaminated substance obtain the sparkling effect of similar fluorite, It includes but are not limited to following any or appoints several fluorescent whitening agents: Stilbene-based, coumarin type, pyrazoline type, benzo Oxygen nitrogen type, phthalimide type etc.；Wherein, the preferred stilbene biphenyl sodium disulfonate (fluorescent whitening agent of fluorescent whitening agent CBS), bis- (5 methyl -2- benzoxazolyl) talan (fluorescent whitening agent KSN) of 4,4-, 2,2- (4,4 '-diphenylethyllene) Double benzoxazoles (fluorescent whitening agent OB -1).Fluorescent whitening agent dosage used is not particularly limited, generally 0.002- 0.03wt%.
Delustering agent in the auxiliary agent when incident light being enabled to reach polymer surfaces, occurs diffusing reflection, generates low The matt and delustring appearance of gloss comprising but be not limited only to following any or appoint several delustering agents: sedimentation barium sulfate, dioxy SiClx, aqueous gypsum powder, talcum powder, titanium dioxide, poly- methyl carbamide resin etc.；Wherein, the preferred silica of delustering agent.Used disappears Photo etching dosage is not particularly limited, generally 2-5wt%.
The deleterious charge assembled in polymer samples can be guided or be eliminated, make it by the antistatic agent in the auxiliary agent Production and life are not brought inconvenience or are endangered comprising but be not limited only to following any or appoint several antistatic agents: yin from Subtype antistatic agent, such as alkylsulfonate, to Sodium Nonylphenoxypropane Sulfonate, alkyl phosphate diethanolamine salt, alkyl phenol Polyoxyethylene groups ether sulfonic acid triethanolamine, to nonyl diphenyl ether potassium sulfonate, alkyl polyoxyethylene base ether sulfonic acid triethanolamine, phosphoric acid Ester derivant, phosphate, phosphoric acid polyethylene oxide alkyl ethers alcohol ester, alkyl bis- [two (2- ethylol amine)] phosphates, phosphate Derivative, fatty amine sulfonate, butyrate sodium sulfonate；Cationic antistatic agent, such as aliphatic ammonium salt hydrochlorate, lauryl trimethyl Ammonium chloride, dodecyl trimethylamine bromide, N, N- cetyl-ethyl morpholine ethyl-sulfate salt, stearamide propyl (2- hydroxyl second Base) dimethylammonium nitrate, alkyl hydroxyethyl dimethylammonium perchlorate, 2- alkyl -3,3- dihydroxy ethyl imidazoline perchlorate, 2- Heptadecyl -3- ethoxy -4- carboxymethyl imidazoline, N, bis- (α-ethoxy)-N-3 (dodecyloxy -2- hydroxypropyl) first of N- Ammonium Methylsulfate salt；Amphoteric ion type antistatic agent, such as alkyl dicarboxyl methyl ammonium second inner salt, lauryl betaine, N, N, N- tri- Alkylammonium acetyl (N '-alkyl) amine second inner salt, bis- polyethylene oxide base-N- ethylphosphonic acid sodium of N- lauryl-N, N-, alkyl two Salt hydroxide, -3 ethoxy -3- acetic acid alkali imidazoline quaternary amine alkali of 2- alkyl, N- alkyl amino acid in (polyoxyethylene) ammonium second Salt；Non-ionic antistatic agent, such as fatty alcohol ethylene oxide adduct, fatty acid ethylene oxide addition product, alkyl phenol epoxy second The polyethylene oxide of alkane addition product, tricresyl phosphate polyoxyethylene groups ether-ether, fatty acid monoglyceride, sorbitan mono-laurate Addition product；Polymer Antistatic Agent, ethylene oxide propylene oxide addition product, polyethylene glycol-terephthalic acid (TPA) such as ethylenediamine Ester -3,5- dibenzoate sodium sulfonate copolymers, polyene propionamide N- quaternary ammonium salt substituent, poly- 4- vinyl -1- acetonyl pyrrole Pyridine phosphoric acid-is to butyl phenyl ester salt etc.；Wherein, the preferred lauryl trimethyl ammonium chloride of antistatic agent, octadecyldimethyl hydroxyl second Base quaternary ammonium nitrate (antistatic agent SN), alkyl phosphate diethanolamine salt (antistatic agent P).Antistatic agent dosage used does not have It is particularly limited to, generally 0.3-3wt%.
Dehydrating agent in the auxiliary agent, can moisture in removing system comprising but be not limited only to it is following any or Appoint several: oxazolidine compound (such as 3- Ethyl-2-Methyl -2- (3- methyl butyl) -1,3- oxazolidine), different to Methyl benzenesulfonyl Cyanate, triethyl orthoformate, vinyl silanes, calcium oxide etc..Dehydrating agent dosage used is not particularly limited, generally 0.1-2wt%.
Biocide mildewcide in the auxiliary agent can inhibit the growth of bacterium, and the appearance for keeping product clean and tidy extends and uses Service life；Or protection user, the health for promoting user, such as reduce tinea pedis.It includes organic matter and inorganic matter, including but It is not limited only to following any or appoints several: isothiazolinone derivatives, such as 5-Chloro-2-methyl-4-isothiazolin-3-one, 2- Methyl -4- isothiazoline -3- ketone, N- normal-butyl -1,2- benzisothiazole-3-ketone, octylisothiazolinone, 2,4,4- tri- Chlorine-2-hydroxyl-diphenyl ether, 2- (4- thiazolyl) benzimidazole, copper 8-quinolinolate or bis- (8-hydroxyquinoline base) copper；It is organic Tin compound, such as tributyl-tin fumarate, tributyltin acetate, bis- (tributyl tin) sulfide, bis- (tributyl tin) tin oxide； N, N- dimethyl-N '-phenyl (fluorine dichloromethyl is thio) sulfonamide；Inorganic compound or compound, such as nano silver, nano-silica Change titanium, nano silica, nano zine oxide, superfine cupper powder, inorganic antiseptic YY-Z50, XT inorganic antiseptic, composite antibacterial Agent KHFS-ZN.Biocide mildewcide dosage used is not particularly limited, generally 0.5-2wt%.
Foaming agent in the auxiliary agent can make polymer samples foaming pore-forming, to obtain light polymeric material Material comprising but be not limited only to it is following any or appoint several foaming agents: physical blowing agent, as carbon dioxide, nitrogen, argon gas, Methane, ethane, propane, butane, iso-butane, pentane, neopentane, hexane, isopentane, heptane, isoheptane, acetone, benzene, toluene, Methyl ether, ether, petroleum ether, chloromethanes, methylene chloride, dichloroethylene, dicholorodifluoromethane, trifluorochloromethane, hydrochlorofluorocarbons- 22, hydrochlorofluorocarbons -142b, hydrofluorocarbons -134a, hydrofluorocarbons -152a, chlorofluorocarbons -11, chlorofluorocarbons -12, chlorine fluorine Hydrocarbon -114；Inorganic foaming agent, such as sodium bicarbonate, ammonium carbonate, ammonium hydrogen carbonate, carbonate ammonia natrium, azido compound, hydroboron Deng；Organic foaming agent, such as N, N '-dinitrosopentamethlyene tetramine, N, N '-dimethyl-N, N '-dinitroso paraphenylene terephthalamide Amine, azodicarbonamide, barium azo-biscarbonate, two diisopropyl carbonate of azo, azodicarbonamide potassium formate, two isobutyl of azo Nitrile, 4,4 '-oxobenzenesulfonyl hydrazide, 3,3 '-disulfonyl hydrazide diphenyl sulphone (DPS)s, 1,3- benzene Erhuang hydrazides, benzene sulfonyl hydrazide, three diazanyls three Piperazine, p-toluene sulfonylsemicarbazide, biphenyl -4,4 '-disulfonyl nitrine, diazo aminobenzene；Physical microballoon/granule foaming agent, such as The expandable microballoon of the companies such as Akzo Nobel production.Wherein, the preferably environmentally friendly carbon dioxide of foaming agent, nitrogen, argon Gas and sodium bicarbonate, ammonium carbonate, azodicarbonamide (blowing agent AC), N, five methine tetramine (foaming agent of N '-dinitro H), N, N '-dimethyl-N, N '-dinitrosoterephthalamine (foaming agent NTA), physical microballoon foaming agent.Hair used Infusion dosage is not particularly limited, generally 0.1-30wt%.
Blowing promotor in the auxiliary agent comprising but be not limited only to foamed promoter, frothing inhibitor, foam and stablize Agent etc..The foamed promoter comprising but be not limited only to it is following any or appoint it is several: urea, stearic acid, lauric acid, Salicylic acid, tribasic lead sulfate, dibasic lead phosphite, lead stearate, cadmium stearate, zinc stearate, zinc oxide, ZB- 530,KZ-110,MS-1；The frothing inhibitor comprising but be not limited only to following any or appoint several: maleic acid, richness Horse acid, stearyl chloride, phthalyl chloride, maleic anhydride, phthalate anhydride, hydroquinone, naphthalenediol, aliphatic amine, amide, Oxime, isocyanates, mercaptan, thiophenol, thiocarbamide, sulfide, sulfone, cyclohexanone, acetylacetone,2,4-pentanedione, hexacholorocyclopentadiene, dibutyl Malaysia Sour tin etc.；The foam stabiliser comprising but be not limited only to it is following any or appoint it is several:: silicone oil, sulfonated aliphatic alcohol, Alpha-sulfonated fatty acid, NaLS, dodecyldimethylamine oxide, alkylolamides, polyethylene glycol oxide, alkylaryl are poly- Ethylene oxide alcohol, tridecyl ether, Polyoxyethylene sorbitan glycerol monolaurate, siloxanes-ethylene oxide are embedding Section copolymer etc..Blowing promotor dosage used is not particularly limited, generally 0.05-10wt%.
Nucleating agent in the auxiliary agent can accelerate crystalline rate, increase knot by the crystallization behavior of change polymer Brilliant density and promote fine grain size, reach and shorten material molding cycle, improves the product transparency, lustrous surface, tension The purpose of the physical mechanical properties such as intensity, rigidity, heat distortion temperature, creep resistance comprising but be not limited only to following any Or appoint several nucleating agents: benzoic acid, adipic acid, sodium benzoate, talcum powder, p-phenolsulfonic acid's sodium, silica, two benzal sorbs Sugar alcohol and its derivative, EP rubbers, ethylene propylene diene rubber etc.；Wherein, the preferred silica of nucleating agent, benzylidene sorbitol (DBS), ethylene propylene diene rubber.Nucleating agent dosage used is not particularly limited, generally 0.1-1wt%.
Rheological agent in the auxiliary agent can guarantee that polymer has good brushability and appropriate during film Coating thickness, the sedimentation of solid particle, can be improved its redispersibility comprising but be not limited only to following when preventing storage A kind of or several rheological agents: inorganic, such as barium sulfate, zinc oxide, alkaline earth oxide, calcium carbonate, lithium chloride, sulfuric acid Sodium, magnesium silicate, fumed silica, waterglass, colloidal silicon dioxide；Organo-metallic compound, as aluminum stearate, aluminium alkoxide, Titanium chelate, aluminium chelate compound；Organic, such as organobentonite, rilanit special/amide waxe, isocyanate derivates, acrylic acid Lotion, acrylic copolymer, polyethylene wax, cellulose esters etc.；Wherein, the preferred organobentonite of rheological agent, polyethylene wax, hydrophobic Modified alkaline swellable emulsions (HASE), alkali-swellable emulsions (ASE).Rheological agent dosage used is not particularly limited, and one As be 0.1-1wt%.
The filler primarily serves following effect in polymer samples: 1. reducing the shrinking percentage of molded article, mentions Dimensional stability, surface smoothness, flatness and the zero diopter of high product or without photosensitiveness etc.；2. adjusting the viscosity of material；③ Meet different performance requirement, such as improves material impact intensity and compressive strength, hardness, rigidity and modulus, improve wearability, improve Heat distortion temperature improves electric conductivity and thermal conductivity etc.；4. improving the coloring effect of pigment；5. assigning photostability and chemically-resistant being rotten Corrosion；6. playing compatibilization, cost can be reduced, improves product competitiveness in the market.
The filler, selected from following any or appoint several fillers: inorganic non-metallic filler, organic is filled out at metal packing Material.
The inorganic non-metallic filler includes but are not limited to following any or appoints several: calcium carbonate, clay, sulphur It is sour barium, calcium sulfate and calcium sulfite, talcum powder, white carbon black, quartz, mica powder, clay, asbestos, asbestos fibre, orthoclase, white Chalk, lime stone, blanc fixe, gypsum, graphite, carbon black, graphene, graphene oxide, fullerene, carbon nanotube, molybdenum disulfide, Slag, flue dust, wood powder and shell powder, diatomite, red mud, wollastonite, silica-alumina carbon black, aluminium hydroxide, magnesium hydroxide, flyash, Oil shale powder, swelling perlite powder, aluminum nitride powder, boron nitride powder, vermiculite, iron cement, white clay, alkali mud, boron mud, glass microballoon, tree Rouge microballon, glass powder, cement, glass fibre, carbon fiber, quartz fibre, charcoal core boron fibre, titanium diboride fiber, calcium titanate are fine Dimension, silicon carbide fibre, ceramic fibre, whisker etc..In an embodiment of the invention, preferably conductive inorganic non- Metal packing includes but are not limited to graphite, carbon black, graphene, carbon nanotube, carbon fiber, facilitates and obtains electric conductivity and/or tool There is the composite material of electric heating function.In yet another embodiment of the present invention, preferably have and make in infrared and/or near infrared light With the lower non-metallic fillers with heating function, graphene, graphene oxide, carbon nanotube are included but are not limited to, is conveniently obtained Obtain the composite material heated using infrared and/or near infrared light.Good heating property, the especially fever of remote control property Performance help to obtain the performances such as controllable shape memory, selfreparing.In yet another embodiment of the present invention, preferably have There is the inorganic non-metallic filler of thermal conductivity, includes but are not limited to graphite, graphene, carbon nanotube, aluminium nitride, boron nitride, carbon SiClx facilitates the composite material for obtaining thermally conductive function.
The metal packing, including metallic compound include but are not limited to following any or appoint several: metal powder End, fiber comprising but it is not limited only to copper, silver, nickel, iron, gold etc. and its powder, the fiber of alloy；Nano-metal particle, packet Include but be not limited only to nanogold particle, nano-Ag particles, nanoparticle palladium, nano iron particles, nano cobalt granule, nano nickel Grain, nanometer Fe3O4Particle, nanometer γ-Fe2O3Particle, nanometer MgFe2O4Particle, nanometer MnFe2O4Particle, nano Co Fe2O4? Grain, nano Co Pt3Particle, nanometer Fe Pt particle, nanometer Fe Pd particle, ferronickel bimetallic magnetic nanoparticle and other red Outside, near-infrared, ultraviolet, the nano-metal particle that can be generated heat under at least one effect of electromagnetism etc.；Liquid metal comprising but not It is only limitted to mercury, gallium, gallium indium liquid alloy, gallium indium tin liquid alloy, other gallium base liquid metal alloys；Metallo-organic compound point Son, crystal and other in infrared, near-infrared, ultraviolet, the substance that can be generated heat under at least one effect of electromagnetism etc..In the present invention An embodiment in, can preferably carry out electromagnetism and/or near-infrared heating filler, include but are not limited to nanogold, Nano silver, Technique of Nano Pd, nanometer Fe3O4, to carry out remote sensing heating.In yet another embodiment of the present invention, preferably liquid is golden Belong to filler, the flexibility and ductility of substrate can be kept while enhancing the thermally conductive of flexible parent metal, electric conductivity.In the present invention Another embodiment in, preferably in infrared, near-infrared, ultraviolet, the organic gold that can generate heat under at least one effect of electromagnetism Belong to compound molecule, crystal, on the one hand facilitates compound, another side raising induction is generated heat efficiency and promote heating effect.
The organic filler includes but are not limited to following any or appoints several: 1. natural organic filler, such as natural Rubber, cotton, velveteen, fiber crops, jute, flax, asbestos, cellulose, cellulose acetate, lignin, starch, wood powder etc.；2. synthesizing Resin extender, such as AAS acrylonitrile acryloid styrene, acrylonitrile-butadiene-styrene copolymer, acetate fiber Element, polytrifluorochloroethylene, haloflex, chliorinated polyvinyl chloride, epoxy resin, ethylene-propylene copolymer, ethylene-acetate second Enoate copolymer, high density polyethylene (HDPE), high impact polystyrene, low density polyethylene (LDPE), medium density polyethylene, melamine-first Urea formaldehyde, polyamide, polyacrylic acid, polyacrylamide, polyacrylonitrile, polyarylsulfone (PAS), polybenzimidazoles, poly terephthalic acid fourth two Alcohol ester, polycarbonate, dimethyl silicone polymer, polyethylene glycol, polyester, polysulfones, polyether sulfone, polyethylene terephthalate, Phenolic resin, tetrafluoroethylene-perfluoro propane copolymer, polyimides, polymethyl acrylate, polymethacrylonitrile, poly- methyl-prop E pioic acid methyl ester, polypropylene, polyphenylene sulfide, polyphenylsulfone, polystyrene, polytetrafluoroethylene (PTFE), polyurethane, polyvinyl alcohol, gathers polyphenylene oxide Vinyl acetate, polyvinyl butyral, polyvinyl chloride, vinyl chloride vinyl acetate copolymer, Vingon, polyethylene Alcohol formal, polyvinylpyrrolidone, Lauxite, ultra-high molecular weight polyethylene, unsaturated polyester (UP), polyether-ether-ketone etc.；3. closing At gum filler, as isoprene rubber, butadiene rubber, butadiene-styrene rubber, nitrile rubber, neoprene, butyl rubber, EP rubbers, Silicon rubber, fluorubber, lactoprene, polyurethane rubber, epichlorohydrin rubber, thermoplastic elastomer (TPE) etc.；4. synthetic fibers are filled out Material, such as viscose fiber, copper ammonia fiber, diethyl ester fiber, triethyl fiber, Fypro, polycarbonate, polyvinyl alcohol Fiber, polyester fiber, polyurethane fiber, polyacrylonitrile fibre, vinylon, polyvinyl chloride fibre, polyolefin are fine Dimension, fluorofibre, polytetrafluoroethylene fibre, aromatic polyamide fibre, aramid fiber or aramid fiber etc.；5. foamed polymer Composition granule and expandable polymer beads.
Wherein, wire feeding does not limit, mainly depending on required material property.Amount of filler used is without spy It does not limit, generally 1-30wt%.
Wherein, the sweller may include but be not limited to water, organic solvent, ionic liquid, oligomer, plasticizer.Its In, oligomer can also be considered as plasticizer.
Organic solvent in the sweller is selected from as an example and includes but is not limited to any of the following or appoint several Kind: hydro carbons (such as hexamethylene, heptane), halogenated hydrocarbon (such as methylene chloride, chloroform, tetrachloromethane), aromatic hydrocarbons (such as toluene, dimethylbenzene), Ketone (such as acetone, methyl ethyl ketone), ethers (such as ether, tetrahydrofuran, dioxane), esters (such as ethyl acetate, acetic acid fourth Ester), glycol ether-ether (such as ethylene glycol ether acetate, propylene glycol monomethyl ether acetate), dimethylformamide (DMF), N- methyl Pyrrolidones (NMP) etc..
Ionic liquid in the sweller is generally made of organic cation and inorganic anion, as an example, sun It includes but is not limited to that alkyl quaternary ammonium ion, alkyl quaternary are seen imidazol ion, the N- alkyl that ion, 1,3- dialkyl group replace that ion, which is selected from, Substituted pyridinium ion etc.；Anion be selected from include but is not limited to for halide ion, tetrafluoroborate ion, hexafluoro-phosphate radical from Son also has CF3SO3 -、(CF3SO2)2N-、C3F7COO-、C4F9SO3 -、CF3COO-、(CF3SO2)3C-、(C2F5SO2)3C-、 (C2F5SO2)2N-、SbF6 -、AsF6 -Deng.In ionic liquid used in the present invention, the preferred glyoxaline cation of cation, anion It is preferred that hexafluorophosphoricacid acid ions and tetrafluoroborate ion.
Oligomer in the sweller is selected from as an example and includes but is not limited to any of the following or appoint several: Polyethylene glycol oligomer, polyvinyl alcohol oligomer, polyvinyl acetate ester oligomer, polyacrylic acid N-butyl oligomer, liquid stone Wax etc..
Plasticizer in the sweller is selected from as an example and includes but is not limited to any of the following or appoint several: Phthalates: dibutyl phthalate (DBP), dioctyl phthalate (DOP), diisooctyl phthalate (DIOP), dibutyl phthalate (DHP), diisooctyl phthalate (DIDP), diisononyl phthalate (DINP), neighbour Phthalic acid butyl benzyl, butyl phthalate butyl glycolate, dicyclohexyl phthalate, phthalic acid are bis- (13) Ester, terephthalic acid (TPA) two (2- ethyl) own ester；Phosphoric acid ester, as tricresyl phosphate (TCP), phosphoric acid (hexichol -2- ethyl) oneself Ester；Fatty acid ester, such as the own ester of adipic acid two (2- ethyl), decanedioic acid two (2- ethyl) own ester；Epoxy compound species, such as epoxy Glyceride type, epoxy fatty acid monoester class, epoxy tetrahydrophthalic acid esters, epoxidised soybean oil, epoxystearic acid (2- second Base) own ester, epoxy soybean oleic acid 2- ethylhexyl, the own ester of 4,5- epoxy tetrahydrophthalic acid two (2- ethyl), Chinese littleleaf box acetyl Methyl ricinolcic acid, dihydric alcohol lipid, such as C5~9Sour glycol ester, C5~9Sour Triethylene Glycol；Class containing chlorine such as afforests stone Wax class, chloro fat acid esters；Polyesters, such as ethanedioic acid 1,2-PD system polyester, decanedioic acid 1,2-PD polyester；Petroleum sulphur Acid phenenyl ester, trimellitate, citrate, pentaerythrite and pentaerythritol fatty acid ester etc..Wherein, the preferred DBP, DOP of plasticizer, DIOP, DIDP, DINP, TCP, epoxidised soybean oil.Wherein, epoxidised soybean oil is that a kind of environment-friendly type plastic of function admirable increases Mould agent, epoxidation reaction preparation occurs for refined soybean oil and peroxide, in polymer product resistance to volatilization, it is not easy to migrate, Not easy to lose, this is to keeping product light, thermal stability and to prolong the service life be highly beneficial.Epoxidised soybean oil toxicity pole It is small, it is allowed for the packaging material of food and medicine by many countries, is that the unique of Food and Drug Adminstration of the US's approval can For the epoxy plasticiser of packaging material for food, therefore it is more highly preferred to.
In the preparation process of hydridization dynamic aggregation compositions, to hydridization dynamic aggregation compositions each component raw material Dosage is not particularly limited, and those skilled in the art can carry out according to practical preparation situation and objective cross physical performance Adjustment.
A kind of hydridization dynamic aggregation compositions provided by the present invention have dynamic covalent bond and supermolecule hydrogen simultaneously Key, performance are adjustable on a large scale.By suitable component selection and formula design, self-repair function can be introduced polymer material, So that material internal can be repaired independently after generating damage, help to obtain that the service life is longer, more reliable performance and more economical Material, plug, sealing ring, part, adhesive, film, coating, fiber, tubing, plate, type with self-repairability is made Material etc. can be applied to electronic device, military aerospace equipment, functional paint and coating, biological medicine, bio-medical material, energy The fields such as source, building, bionical every field, has broad application prospects.In electronic correlation field, microelectronics polymer device With adhesive in use, as heat and mechanics fatigue generate microcrack caused by performance forfeiture be long-term existence the problem of, will Self-repair function introduces these materials, can greatly improve the reliability and service life of microelectronic product；Using material from Repairing performance, as the plug of the charger interface of mobile phone, tablet computer, notebook, camera etc., data line interface etc., The aperture generated in connector swapping process carries out repairing reach the purpose of waterproof.It is additionally aided as self-repair material To the material with bionical effect, also have wide practical use in biologic medical field, available more durable human body closes Section or Osteological gel.The material of exploitation specific use is also contributed to as self-repair material, it such as under certain condition can be with Restore the material of interface performance, conduction and the performances such as thermally conductive, or can as battery/electrode of super capacitor binder, diaphragm To reduce the damaged service life for increasing electrode material of electrode.The presence of supermolecule hydrogen bond can further enhance polymerization in the present invention The toughness of object can be prepared into as the splendid film of performance, fiber, tubing, plate, profile.In addition, utilizing its dynamic reversible Property, the self-repairability polymer material of shape memory can be prepared, can also being applied to preparation, there is visco-elastic magic to turn Change the toy of effect.
Hydridization dynamic aggregation compositions of the present invention are described further below with reference to some specific embodiments. Specific embodiment is that present invention be described in more detail, non-limiting protection scope of the present invention.
Embodiment 1
Prepare a kind of hydridization dynamic aggregation compositions plasticizer swell gel based on polynorbornene, oversubscription therein Son effect is based on side cyanuric acid group.
Cyanuric acid and the chloro- 1- hexene of 6- are kept into molar ratio 4:1, are dissolved in anhydrous dimethyl sulphoxide, is catalyzed in potassium carbonate Under be stirred to react at 80 DEG C 15 hours, obtain the olefinic monomer 1a of hydrogen bonds group.Toluene is added in compound 1a, will be reacted Container is cooled to 5 DEG C, and cyclopentadiene is added dropwise in low temperature, keeps compound 1a and cyclopentadiene molar ratio is 10:13.It is added dropwise After be warming up to reflux temperature and continue to be stirred to react, obtain the norbornene derivative 1b of hydrogen bonds group.
The norbornene derivative 1b of 30 molar equivalent hydrogen bonds groups, 65 molar equivalent norbornene and 5 moles are worked as Amount 2,5- norbornadiene reacts in methylene chloride under the catalysis of Grubbs bis- generations catalyst, obtains the random crosslinking of three Copolymer.
By the above-mentioned copolymer of 100 mass parts, 220 mass parts uniformly mix naphthenic oil, 80 mass parts of carbon black, 0.5 mass parts Catalyst 12 is sufficiently mixed, and is placed in mold, and dynamic aggregation object plasticizer swell gel of the invention is obtained after molding.
The product has good intensity, toughness, self-repairability, and resilience is good, and set resistant is small, can carry out larger The stretching of range can be used for preparing conveyer belt, components etc..
Embodiment 2
A kind of hydridization dynamic aggregation compositions hydrogel based on polyacetylene is prepared, supermolecular mechanism therein is based on side Imidazoline ketone group, side amide groups and framework amide base.
Under nitrogen protection, sodium hydrate aqueous solution is dissolved in phenylethynyl benzoic acid by a certain amount of (naoh concentration is 10M), keeping the molar ratio of monomer and sodium hydroxide is 2:3.In 30 DEG C of addition catalyst [Rh (cod)2]BF4Aqueous solution, adjust The concentration of whole monomer and catalyst is respectively 0.5M and 0.0025M.After 3 hours, resulting polymers are deposited in ethyl alcohol, it is dry After be again dissolved in water, centrifugation after being acidified with hydrochloric acid obtains poly- [(4- carboxyl phenyl) acetylene].
Under the conditions of anhydrous and oxygen-free, a certain amount of resulting polymer is dissolved in DMF, under the conditions of -60 DEG C, carboxyl 0.4 is added and rubs 1- (2- the amino-ethyl) -2- imidazolone of your equivalent and the crosslinking agent 2,2'- (ethylene dioxy) of 0.05 molar equivalent of carboxyl are double (ethamine) is to slowly warm up to room temperature under stirring, removes solvent and drying, obtains the hydridization dynamic aggregation compositions based on polyacetylene Component A.
Obtained component A is swollen in containing the sodium hydrate aqueous solution with remaining carboxyl equimolar equivalent, and component A is added The catalyst 26 of quality 0.5% obtains hydridization dynamic aggregation compositions hydrogel of the invention.The hydridization dynamic aggregation object group Closing object hydrogel has good self-repairability, can be used for preparing the toy with magic effect.
Embodiment 3
Prepare a kind of hydridization dynamic aggregation compositions ordinary solid based on unsaturated polyester (UP), supermolecular mechanism therein Based on side imidazoline ketone group, side amide groups and framework amide base.
2- chlorine cyclohexanone is dissolved in methylene chloride, metachloroperbenzoic acid is added, keeps 2- chlorine cyclohexanone and m-chloro peroxide The molar ratio of benzoic acid is 10:12, and reaction obtains the chloro- 6-caprolactone 3a of α-.Under anhydrous condition, by 1 molar equivalent α-chloro- ε-oneself Lactone is dissolved in toluene, and 1.3 molar equivalents 1 are added, and 5- diazabicyclo [4.3.0] nonyl- 5- alkene reacts 16 hours at 80 DEG C, After crude product to be used to water and salt acid extraction respectively, the mixture of compound 3b, 3c are obtained.The mixture is further with methylene chloride For washing lotion silica gel post separation.
It is under anhydrous condition, 120 molar equivalent 6-caprolactones, 100 molar equivalent compound 3a and 30 molar equivalent 3c are molten In toluene, in 1 molar equivalent initiator 2,2- dibutyl -2- tin -1,3- cyclic heptane dioxide reacts under causing in 20 DEG C, obtains side Base contains the random copolymer based on unsaturated polyester (UP) of chlorine atom.
The polymer that resulting side group contains chlorine atom is dissolved in dimethylformamide (DMF), is added and 2 moles of chlorine atom Chlorine atom side group is converted azido by the sodium azide of equivalent.It is again polymer, the 2- propargyl-N- of azido by side group Butyl carbamate and 1, the pungent diine of 7- are dissolved in tetrahydrofuran, and keeping the molar ratio of three is 10:8:1, in cuprous iodide and Under the catalysis of pyridine, hydridization dynamic aggregation compositions component A of the invention is obtained in 35 DEG C of reactions.
Under the conditions of anhydrous and oxygen-free, by 5 mass parts Grubbs generation catalyst 1,100 mass parts paraffin and in paraffin molten It is sufficiently blended under state.Surfactant ethylene maleic acid anhydride copolymer and n-octyl alcohol are added to the water, and keep water temperature about 80 ℃.Aqueous solution with 900rpm revolving speed stirring in the case where, blend is poured into and stir to be blended liquid reach stable state Afterwards, ice water is added cools down water temperature rapidly.Stop stirring, filtering obtains the catalyst composites component B of paraffin cladding.
At room temperature, 5 mass parts urine is added into the aqueous solution of 250 mass parts ethylene maleic acid anhydride copolymers containing 0.5wt% Element, 0.5 mass parts ammonium chloride and 0.5 mass parts resorcinol, and pH value is modulated 3.5 by the way that sodium hydroxide or hydrochloric acid is added. Solution is stirred with the speed of 800rpm, and a small amount of n-heptanol defoaming is added.Solution into stirring is slowly added to 60 matter of chlorobenzene Part is measured, after emulsion-stabilizing, formalin is added, and keeping the molar ratio ratio for obtaining urea formadehyde is 1:1.8.By lotion with 1 DEG C of speed per minute is warming up to 55 DEG C, and keeps the temperature 4 hours.Later, it is kept stirring but stops heating.Room is cooled to lotion Wen Hou, washing, obtains the ureaformaldehyde microcapsules containing chlorobenzene solution.
100 content of component A are swollen in into DMF, and the micro- glue of ureaformaldehyde of 5 mass parts obtained component B and 10 mass parts is added Capsule removes solvent after being sufficiently blended, obtains hydridization dynamic aggregation compositions of the invention.In the present embodiment, when being generated in material When crackle, the generation or diffusion of crackle will lure the microcapsules rupture containing solvent into.It is poly- around the solvent infiltration crackle of outflow Polymer segments simultaneously dissolve the paraffin particles near crackle containing catalyst, can carry out selfreparing to crackle at room temperature.
Embodiment 4
Prepare a kind of hydridization dynamic aggregation compositions ionic liquid gel based on polyacrylate, supermolecule therein Effect is based on side urea groups.
Acrylic acid 2- amino-ethyl ester and 4- biphenyl isocyanates are reacted in methylene chloride, keep amino and different The molar ratio of cyanate is 1:1, obtains the acrylate monomer 4a containing urea groups.Isocyanates ethyl acrylate and n-propylamine are existed It is reacted in methylene chloride, keeping the molar ratio of amino and isocyanates is 1:1, obtains the acrylate monomer containing urea groups 4b.By the hydroxy-end capped polybutadiene oligomer of 2 molar equivalent acrylic acid and 1 molar equivalent both ends, (average molecular weight is about 1000) it is reacted under the catalysis of bicyclic ethyl carbodiimide (DCC) and 4-dimethylaminopyridine (DMAP), obtains compound 4c.
By 30 molar equivalent methyl methacrylates, 10 molar equivalent monomer 4a, 20 molar equivalent monomer 4b, 5 moles are worked as Crosslinking agent 4c is measured, 1 molar equivalent photoinitiator 2- hydroxy-2-methyl -1- phenyl -1- acetone is in ionic liquid 1- butyl -3- first It is sufficiently mixed in base limidazolium hexafluorophosphate, and the quality of ionic liquid is the 50% of mixture total weight.Illumination in the UV lamp After reaction 4 hours, the ionic liquid gel of hydridization dynamic aggregation compositions component A is obtained.By gained ionic liquid gel and Component B catalyst 36 is sufficiently mixed to arrive corresponding hydridization dynamic aggregation compositions according to mass ratio 100:1.
The embodiment preparation can selfreparing ionic liquid gel not only have good conductivity and mechanical strength, and And can stablize in very wide temperature range and electrochemical window, it can be made into a kind of ideal electrolyte.
Embodiment 5
A kind of hydridization dynamic aggregation compositions foam based on polyurethane is prepared, supermolecular mechanism therein is based on side sulphur For carbamate groups, side carbamateyl and backbone amino formic acid ester group.
Pure and mild third cysteine of a certain amount of 5- cyclo-octene -1,2- bis- is mixed, the ratio of both control molal quantity is about 1:2, using DCC and DMAP as catalyst, methylene chloride is solvent, obtains the Cyclooctene derivative monomer 5a of hydrogen bonds group.It will The ratio of the mixing of a certain amount of monomer 5a, 5- cyclo-octene -1,2- bis- pure and mild cyclo-octene, both control molal quantity is about 5:1:4, with Grubbs bis- generations catalyst is catalyst, and using methylene chloride as solvent, reaction obtains the polymer based on polycyclic octene.
Under the conditions of anhydrous and oxygen-free, by bis- generation of 5 mass parts Grubbs catalyst 2,100 mass parts paraffin and in paraffin molten It is sufficiently blended under state.Surfactant ethylene maleic acid anhydride copolymer and n-octyl alcohol are added to the water, and keep water temperature about 80 ℃.Aqueous solution with 900rpm revolving speed stirring in the case where, blend is poured into and stir to be blended liquid reach stable state Afterwards, ice water is added cools down water temperature rapidly.Stop stirring, filtering obtains the catalyst composites component B of paraffin cladding.
Above-mentioned side group is contained to the polycyclic octene and ethyl isocyanate, 2,4- hexamethylene diisocyanate (HDI) of hydroxyl It is 10:8:1 mixing according to hydroxyl, ethyl isocyanate, HDI molar ratio, mixture is denoted as 100 mass parts.Add 50 mass parts Montmorillonite, 0.2 mass parts organic silicone oil, the expandable polymer microballoon of 1.5 mass parts, 0.1 mass parts DBTDL, 0.1 mass parts three The catalyst composites component B of ethylene diamine, 5 mass parts paraffin cladding, is uniformly mixed, and solidifies 30 minutes at room temperature. Later in 80 DEG C of resolidifications 4 hours to get arriving hydridization dynamic aggregation compositions foamed material of the invention.
In the present embodiment, crackled foamed product is kept the temperature 6 hours in 50 DEG C, is released after the paraffin particles dissolution at slight crack Catalyst is released, selfreparing can be carried out to the slight crack in product.
Embodiment 6
A kind of hydridization dynamic aggregation compositions flexible foam based on polyurethane is prepared, supermolecular mechanism therein is based on Side carbamateyl.
Under nitrogen protection, by 10 molar equivalent ethylene glycol monoallyl ethers (average molecular weight about 500) and 1 molar equivalent Potassium methoxide is blended, and the epoxy prapanol of 70 molar equivalents is slowly added dropwise at 95 DEG C, and obtaining end group is the alkene that hydroxyl has branched structure Hydrocarbon monomer 6a.It under nitrogen protection, is olefinic monomer 6a and and hydroxyl molar equivalent of the hydroxyl with branched structure by end group Ethyl isocyanate reacts in methylene chloride under the catalysis of DBTDL, obtains olefinic monomer 6b.
Olefinic monomer 6b is sufficiently blended with 3- sulfydryl -1,2-PD equimolar equivalent, 1wt% photoinitiator 2 is added, 2- dimethoxy -2- phenyl acetophenone, illumination 30 minutes under 300W ultraviolet lamp are obtained with cladodification pendant polyether group and cladodification side The glycol of base end amido-containing acid ester base.
X=direct key,
By the above-mentioned diol compound with hydrogen bond group of 30 molar equivalents, 20 molar equivalent polyether Glycols (molecular weight About 2000), 50 molar equivalent Isosorbide-5-Nitraes-butylene glycol, 98 molar equivalent toluene di-isocyanate(TDI)s are blended, and are calculated as 100 mass parts, then 1 mass of water-soluble organic silicone oil, 2 mass parts water, 0.2 mass parts DBTDL, 0.1 mass parts triethylenediamine and 1 matter is added Part component B catalyst 65 is measured, is uniformly mixed and quickly stirring solidifies 15 minutes, to bubble is generated then at 60 DEG C at room temperature Solidify 2 hours to get hydridization dynamic aggregation compositions foamed product of the invention is arrived.
Foam obtained in the present embodiment has good flexibility, and slight crack can be repaired under ultraviolet lighting, has longer Service life.
Embodiment 7
Prepare a kind of hydridization dynamic aggregation compositions ordinary solid based on unsaturated polyester (UP), supermolecular mechanism therein Based on side carbamateyl and backbone amino formic acid ester group.
By anti-form-1,4- cyclohexyl dicarboxylic acid, maleic acid and polyethylene glycol diepoxide for example methyl ether are according to molar ratio 4:1:5 Mixing, is prepared a kind of polymer containing pendant hydroxyl group.By resulting polymers, ethyl isocyanate and 4,4- diisocyanate two Cyclohexyl-methane is sufficiently blended by pendant hydroxyl group, unitary isocyanates, binary isocyanates molar ratio 30:28:1, in urging for DBTDL Under change, hydridization dynamic aggregation compositions component A of the invention is obtained.
By 100 mass parts obtained component A, 5 parts by mass of cellulose are nanocrystalline and 0.3 mass parts of catalyst 12 is sufficiently mixed, Obtain corresponding hydridization dynamic aggregation compositions.The resulting dynamic aggregation compositions of the present embodiment have good toughness And elasticity, it can be according to the product for needing to be pressed into different shape size, sample that is damaged or no longer needing may be recovered, and be made New product uses.
Embodiment 8
A kind of hydridization dynamic aggregation compositions hydrogel based on polyvinyl alcohol is prepared, supermolecular mechanism therein is based on Side urea groups.
The ethyl isocyanate of glycine and equimolar equivalent is dissolved in methylene chloride, reaction obtains the chemical combination that one end is carboxyl Object 8a.By 1 molar equivalent polyvinyl alcohol (average molecular weight is about 10000, alcoholysis degree be about 99%), 10 molar equivalent compounds 8a is dissolved in tetrahydrofuran, under the catalysis of DCC and DMAP, obtains the dynamic aggregation object containing side urea bond.By above-mentioned polyvinyl alcohol It is prepared into aqueous solution respectively with butylene dialdehyde and mixes in proportion, makes the molar ratio 4:3 of modified polyvinylalcohol Yu butylene dialdehyde. With between second acid for adjusting pH value to 2.0 to 4.0, reaction temperature is room temperature, and the reaction time is 30 minutes, is obtained based on polyvinyl alcohol Hydridization dynamic aggregation compositions component A.
The sufficiently swelling mixing in water by 100 mass parts obtained component A and 1 mass parts of catalyst 29, obtains corresponding miscellaneous Change dynamic aggregation compositions hydrogel.The obtained hydrogel of the embodiment can be used as packaging material, when occurring damaged, often Selfreparing can be carried out under temperature.
Embodiment 9
Prepare a kind of hydridization dynamic aggregation compositions ionic liquid gel based on polyethers, supermolecular mechanism base therein In side benzimidazolyl and backbone amino formic acid ester group.
1H- benzimidazole -5- the acyl chlorides of the pure and mild equimolar equivalent of 1,4- pentadiene -3- is anti-under the catalysis of triethylamine It answers, obtains double olefin monomer compound 9a.By the allyl isocyanate of 2 molar equivalents and 1 molar equivalent one end hydroxy-end capped one The polyethylene glycol (average molecular weight is about 500Da) of end alkenyl sealing end sufficiently reacts under the catalysis of DBTDL, obtains both ends alkenyl Polyethylene glycol containing a carbamate base on sealing end and skeleton.
Ionic liquid 1- is dissolved in by double olefin monomer compound 9a, the polyethylene glycol of diene sealing end and according to molar ratio 1:4 Butyl -3- methylimidazole bis trifluoromethyl sulfimide salt ([bmim] NTf2) keeps the sum of material quality and ionic liquid Mass ratio is 1:1.And it is denoted as 100 mass parts.The catalyst 35 for adding ionic liquid quality 0.5%, it is sufficiently mixed in 50 DEG C After closing 24 hours, hydridization dynamic aggregation compositions ionic liquid gel of the invention can be obtained.
Prepared ionic liquid gel stability is good in the present embodiment, can be applied to dye solar cell, brake, The fields such as supercapacitor, artificial-muscle and electrochromic device.In the present embodiment, carried out in surface of polymer material with blade It after delineation, places it in 50 DEG C of vacuum drying ovens after placing 6 hours, scratch disappears, and sample is able to carry out selfreparing.
Embodiment 10
A kind of hydridization dynamic aggregation compositions elastomer based on polybutadiene and polyacrylate is prepared, it is therein super Molecular action is based on side thiocarbamate base.
Under the conditions of anhydrous and oxygen-free, by the isocyanates ethyl acrylate of ethyl mercaptan and equimolar equivalent under triethylamine catalysis It is reacted in methylene chloride, obtains the acrylate monomer 10a containing thio carbamate groups.
By polybutadiene (average molecular weight is about that 20000, x:y is about 90:10), 3- sulfydryl -1- propyl alcohol, photoinitiator benzene Even acyl dimethyl ketal (BDK) is reacted in tetrahydrofuran, keep in polybutadiene side alkenyl and 3- sulfydryl -1- propyl alcohol and The molar ratio of BDK is 30:30:1, obtains modified polybutadiene 10b.Under the conditions of anhydrous and oxygen-free, by a certain amount of modified polybutadiene 10b is dissolved in anhydrous pyridine, and excessive 2- bromine isobutyl acylbromide is slowly added dropwise under 0 DEG C of stirring, then is warming up to room temperature reaction 24 hours, obtains The modified polybutadiene 10c brominated to side group.
Under the conditions of anhydrous and oxygen-free, keeps side group bromine atom in modified polybutadiene 10c and contain thio carbamate groups Acrylate monomer 10a molar ratio be 1:30, under the catalysis of cuprous bromide and pentamethyl-diethylenetriamine (PMDTA), It is reacted in toluene in 80 DEG C, obtains the polybutadiene graft containing thiocarbamate base in graft polypropylene acid esters side group Acrylate.By above-mentioned 100 mass parts of polymer, 20 mass parts calcium carbonate, 0.3 mass parts of catalyst 15,0.2 mass parts antioxygen Agent 754 demoulds to arrive hydridization dynamic aggregation compositions of the invention after abundant blending is placed on and shapes in mold.
In the present embodiment, by the product sample vertically to mediating after cutting, 6 hours are stood at 50 DEG C in the case of no external force It carries out Mechanics Performance Testing again afterwards, measures 96% before tensile strength is, 90% be broken before rate elongation is.The product is resistance to Mill property is good, can be used for preparing coating, the sealing element etc. with self-repair function.
Embodiment 11
A kind of hydridization dynamic aggregation compositions plasticizer swell gel based on polychlorobutadiene and polyvinyl chloride is prepared, Supermolecular mechanism therein is based on side urea groups.
Branching type polyvinyl chloride (average molecular weight about 50000) and 4- (2- pyrrolidinyl) benzenethiol are dissolved in hexamethylene and existed 60 DEG C are reacted 12 hours, and keeping the molar ratio of side group chlorine atom and 4- (2- pyrrolidinyl) benzenethiol is about 3:2, are obtained containing side The polyvinyl chloride of secondary amino group.By in side group containing parahelium polyvinyl chloride and methyl isocyanate react in methylene chloride, keep The molar ratio of secondary amino group and methyl isocyanate is about 1:1, obtains side group containing the polyvinyl chloride for replacing urea groups.
The commercially available cross-linking type neoprene of 100 mass parts is swollen in into toluene, is added polyvinyl chloride obtained by 100 mass parts, 70 Mass parts epoxidized soybean oil, 50 mass parts tricresyl phosphates, 0.5 mass parts of catalyst 10 are removed solvent after mixing, are obtained Hydridization dynamic aggregation compositions plasticizer swell gel of the invention.The material has good toughness, can be used as having certainly Plate, tubing, film, sealing material of repair function etc..
Embodiment 12
A kind of hydridization dynamic aggregation compositions ionic liquid gel based on nitrile rubber and polyacrylonitrile is prepared, wherein Supermolecular mechanism be based on side carbamateyl and side urea groups.
By acrylonitrile (average molecular weight about 10000) 1 molar equivalent, 3 molar equivalent of 2- azido second ammonia, 2,5- dehydrations- 20 molar equivalent of 1- nitrine -1- deoxy-D-glucose alcohol, 100 molar equivalent of zinc chloride are dissolved in dimethylformamide, surpass at room temperature 125 DEG C are warming up to after enabling each component be sufficiently mixed within sound 5 minutes to be stirred to react, and obtain the modified polypropene of side group hydroxyl and amino Nitrile.By resulting modified polyacrylonitrile and with the ethyl isocyanate of the sum of contained hydroxyl amino equimolar equivalent in dimethyl sulfoxide Middle reaction obtains the modified polyacrylonitrile of side group amido-containing acid ester and urea bond.
By the commercially available crosslinking butadiene nitrile rubber of 100 mass parts and swell in 200 mass parts 1- butyl -2,3- methylimidazoles four Borofluoride and suitable solvent dimethylformamide, the resulting side group amido-containing acid ester of 100 mass parts of addition and urea bond The carbon nanotube of modified polyacrylonitrile, 0.5 mass parts of catalyst 33 and gross mass 4%, removes solvent again, obtains after being sufficiently mixed To corresponding hydridization dynamic aggregation compositions ionic liquid gel.The ionic liquid gel stability of embodiment preparation is good, It can be used as the use of selfreparing toughness material, and there is good heating effect under near infrared light.
Embodiment 13
Prepare a kind of hydridization dynamic aggregation compositions foam based on polyvinyl alcohol and polyethyleneimine, oversubscription therein Son effect is based on side carbamateyl and end urea groups.
The isophorone diisocyanate of equimolar equivalent and n-propylamine are dissolved in DMF, are added after complete reaction certain The branched polyethylene imine (average molecular weight is about 20000) of amount, and keep in polyethyleneimine segment middle-end amino and solution Isocyanate group be 1:1, obtain end group be urea groups modified branched polyethylene imines.
By 1 molar equivalent polyvinyl alcohol, (99%) average degree of polymerization about 2000, alcoholysis degree are higher than, 100 molar equivalent urea It is dissolved in water with 100 molar equivalent methanol, is stirred 20 minutes, the modified polyvinylalcohol that part side group is carbamate groups is obtained. Above-mentioned polyvinyl alcohol is prepared into aqueous solution with butylene dialdehyde respectively and is mixed in proportion, modified polyvinylalcohol and butylene dialdehyde are made Mass ratio is 100:1.With between second acid for adjusting pH value to 2.0 to 4.0, reaction temperature is room temperature, and the reaction time is 30 minutes, is obtained To the polyvinyl alcohol containing triple carbon-carbon bonds.
The resulting polyvinyl alcohol of 100 mass parts is swollen in into Isosorbide-5-Nitrae-dioxane solvent, is added that 50 mass parts are resulting to be changed Property branched polyethylene imine and 3 mass parts of catalyst 32 be sufficiently blended.Blend is placed in mold at -80 DEG C and has been freezed Entirely, aspiration pump is opened at -50 DEG C, maintains dry air pressure less than 50 μ atm24 hours, is done in 20 DEG C of vacuum ovens It is dry, whole solvents are extracted, hydridization dynamic aggregation compositions foamed material of the invention is obtained.
The foamed material has good toughness and self-repairability, due to percent opening height, is alternatively arranged as filtering material or load Body uses.
Embodiment 14
A kind of hydridization dynamic aggregation compositions ordinary solid based on polyether polyurethane is prepared, supermolecule therein is made With based on side carbamateyl, side amide groups, Amino End Group formic acid ester group, backbone amino formic acid ester group and framework amide base.
By 1 molar equivalent ethylene glycol, 100 molar equivalent ethylene oxide, 50 molar equivalents (S)-(oxiranylmethyl) ammonia Base t-butyl formate, 50 molar equivalent 3- [(acetparaminosalol) phenoxy group] -1,2 epoxy prapane hybrid reaction preparation both ends are Pendant hydroxyl groups contain the polyethers of carbamate groups and amide groups.10 molar equivalent urea are instilled into 100 molar equivalent 4,4- bis- Isocyanates dicyclohexyl methyl hydride after abundant blending and stirring 24 hours, is cooled to 35 DEG C, adds 40 molar equivalent institutes in 70 DEG C Polyethers, 40 molar equivalent Isosorbide-5-Nitraes-butylene glycol, 10 molar equivalent ethanol amines and the 1 molar equivalent DBTDL obtained, sufficiently reaction are obtained Crosslinked polyethers type polyurethane.
Under nitrogen protection, 5 molar equivalent pentaerythrites and 2 molar equivalent potassium methoxides are blended, are slowly added dropwise at 95 DEG C The epoxy prapanol of 300 molar equivalents, it is the polyethers of hydroxyl that obtaining, which has dissaving structure end group,.By gained polyethers with it is excessive different Ethyl cyanate reacts under the catalysis of DBTDL, and after complete reaction, it is carbamate that obtaining, which has dissaving structure end group, Polyethers.The hydroxy-end capped polyethylene glycol in both ends is reacted under the catalysis of DBTDL with excessive ethyl isocyanate, to fully reacting Afterwards, it is the polyethers of carbamate that obtaining, which has linear structure end group,.
Crosslinked polyethers type polyurethane obtained by 100 mass parts is swollen in into methylene chloride, the resulting modification of 100 mass parts is added The resulting polyethers with linear structure of hyperbranched polyether, 50 mass parts, 10 mass parts graphenes and 5 mass parts of catalyst 31, It is sufficiently blended after removing solvent and obtains hydridization dynamic aggregation compositions of the invention.This hydridization dynamic aggregation compositions embodies Apparent dynamic characteristic can apply to use on textile or in foams, or can be used as functional coating, it may also be used for Prepare the film with hot sensing function.
Embodiment 15
It is commonly solid to prepare a kind of hydridization dynamic aggregation compositions based on ethylene-butylene random copolymer and polyethylene Body, supermolecular mechanism therein are based on triazoline diketone-ene adducts side group and side urea groups pyrimidine ketone group.
Under anhydrous condition, the toluene of reactor volume 14% is added in reactor and 1 atmospheric pressure of maintenance by ethylene full of 2L And the butadiene toluene solution (9wt%) of volume 0.95%.It is added in 40 DEG C and contains scandium catalyst, AliBu3[Ph3C][B (C6F5)4] 20 milliliters of catalyst solution, meanwhile, the butadiene first of reactor volume 6% is instilled with 6 milliliters of speed per minute Benzole soln (9wt%).After butadiene solution is all added dropwise, 20 milliliters of acidified methanols are rapidly added, and product is sunk in ethanol It forms sediment, obtains ethylene-butylene random copolymer.By gained copolymer and a certain amount of 4- methyl-triazolidine -3,5- diketone and 4, 4'- (di-2-ethylhexylphosphine oxide (4,1- phenylene)) bis- (3H- pyrazoles -3,5 (4H)-diketone) is dissolved in tetrahydrofuran, keeps double bond and 4- first Mole of base-triazolidine -3,5- diketone, 4,4'- (di-2-ethylhexylphosphine oxide (4,1- phenylene)) bis- (3H- pyrazoles -3,5 (4H)-diketone) Than sufficiently being reacted after stirring, obtaining crosslinking modified ethylene-butadiene random copolymerization that side group contains hydrogen bond group for 10:3:1 Object.
Low-density cladodification polyethylene (average molecular weight is about 20000) is dissolved by heating in dimethylbenzene, 100 moles is added and works as The initiator cumyl peroxide for being dissolved in dimethylbenzene, constant temperature is added after solution temperature rises to 130 DEG C in the maleic anhydride of amount Reaction obtained Research of Grafting Malaic Anhydride Onto Polyethylene after 1 to 3 hour.Under inert gas protection, UPy derivative 15a and gained are gathered Vinyl Graft maleic anhydride is dissolved in dimethylbenzene, and keeping the molar ratio of compound 15a and maleic anhydride side group is 1:1, and stirring is lower to be added Enter catalyst paratoluenesulfonic acid sodium salt, is stirred to react in 105 DEG C.By water in the dichloromethane solution of products therefrom and trifluoroacetic acid Solution, obtains the modified poly ethylene containing UPy side group hydrogen bond group.
By the resulting ethene improved-butadiene random copolymer of 100 mass parts, the resulting modified poly ethylene of 50 mass parts, 5 The odium stearate of mass parts of catalyst 5,30 mass parts, the sodium bicarbonate of 8 mass parts and 0.2 mass parts vaseline oil are sufficiently total Mixed, extrusion molding obtains corresponding foamed product, and sufficiently solidification at room temperature, obtains hydridization dynamic aggregation object group of the invention Close object foam.The foam has certain intensity and compressibility, and can be stretched in a certain range, can be used for thermal insulation separation Heat.
Embodiment 16
A kind of hydridization dynamic aggregation compositions ordinary solid based on butadiene rubber and polyethylene glycol is prepared, it is therein super Molecular action is based on end cytimidine base and end guanyl-.
Cytimidine is reacted under the catalysis of triethylamine with the polyethylene glycol that both ends are succinimidyl succinate base, is obtained It is the polyethylene glycol of cytimidine base to both ends.Guanine is existed with both ends for the polyethylene glycol of succinimidyl succinate base It is reacted under the catalysis of triethylamine, obtains the polyethylene glycol that both ends are guanyl-.
100 mass parts of cross-linking type butadiene rubber are swollen in into methylene chloride, resulting each 50 matter of two kinds of polyethylene glycol is added Part and 1 mass parts of catalyst 3 are measured, it is sufficiently miscible rear except solvent, obtain hydridization dynamic aggregation compositions of the invention.By the group It closes object and is prepared into film, show more excellent comprehensive performance, there is certain tensile strength and good tear resistance, And it can largely be stretched.After thin polymer film is cut, section part is placed in 50 DEG C of mold and is bonded 6 hours Later, the crackle of section part disappears, and sample forms a film again, has self-repair function.Such hydridization dynamic aggregation compositions can It applied to preparing function film, or can be used as automobile and the pad pasting of furniture uses, also can be used as stretch wrappers progress It uses, and can be recycled and reuse.
Embodiment 17
Prepare the hydridization dynamic aggregation compositions bubble of a kind of styrene-based-butadiene random copolymer and polyisobutene Foam, supermolecular mechanism therein are based on Amino End Group formic acid esters-urea groups.
After 2, the 4- toluene di-isocyanate(TDI) of the amino-terminated polyisobutene in one end and equimolar equivalent is sufficiently reacted, Equimolar eq. ethanol is added, the reaction was continued under the catalysis of TDBDL, obtains the poly- isobutyl of modification that end hydrogen bond group is contained in one end Alkene.
By resulting 40 mass parts of modification polyisobutene containing end hydrogen bond group, 25 mass parts of polystyrene, poly-vinegar acid 8 mass parts of vinyl acetate, 100 mass parts of line style styrene butadiene random copolymer, 1 mass parts of 2,3- succinimide mercaptans and AIBN0.2 mass parts are melted and are sufficiently mixed at 110-120 DEG C, and after being down to 60 DEG C, heat preservation 1 hour to temperature, 1 mass parts are added Catalyst 15 is simultaneously sufficiently mixed.Mold is filled this blend into, is placed in pressure reaction still, supersaturated carbon dioxide is passed through, is heated To 90 DEG C, pressure control is depressured after 7-14MPa, 4 hours with the speed of 1MPa per second, and product is cooling in ice water rapidly, Hydridization dynamic aggregation compositions foamed product of the invention is obtained after demoulding.The foamed product has good self-repairability, It can be used as light heat-insulating material.
Embodiment 18
It prepares a kind of based on the combination of the hydridization dynamic aggregation object of vinylacetate-vinylalcohol random copolymer and polycaprolactone Object ordinary solid, supermolecular mechanism therein are based on side urea groups, diamides base naphthyridines end group and urea groups pyrimidone end group.
The ethyl isocyanate of glycine and equimolar equivalent is dissolved in methylene chloride, reaction obtains the chemical combination that one end is carboxyl Object 18a.By 10 molar equivalent 4,4'- stilbenedicarboxylicacid acids, 1 molar equivalent polyvinyl acetate-polyvinyl alcohol random copolymerization Object (average molecular weight is about 10000, alcoholysis degree be about 60%), 20 molar equivalent compound 18a be dissolved in tetrahydrofuran, in DCC Under the catalysis of DMAP, the vinylacetate-vinylalcohol random copolymer containing side urea bond is obtained.
Using methylene chloride as solvent, it will be reacted by the polycaprolactone of end group of acid chloride group with ammonium hydroxide, obtain two end groups For the polycaprolactone of amide groups.With lead acetate, bis- diphenylphosphine -9, the 9- xanthphos of 4,5- and potassium carbonate for catalyst, By 10 molar equivalents 2, chloro- 1, the 8- naphthyridines of 7- bis- reacts in chloroform with 9 molar equivalent 2- ethyl hexanoyl ammonia, obtains one end and 2- The connected naphthyridines intermediate of ethyl hexanoyl amino.It is the poly- of amide groups by the resulting naphthyridines intermediate of 2 molar equivalents and two end groups Caprolactone reacts under the catalysis of lead acetate, bis- diphenylphosphine -9, the 9- xanthphos of 4,5- and potassium carbonate, obtains both ends and contains There is the polycaprolactone of 2,7- amide groups -1,8- naphthyridines end group.In anhydrous conditions, by 1 molar equivalent compound 18b and 1 mole Equivalent 2,6- diisopropyl phenylisocyanate are dissolved in tetrahydrofuran, react 16 hours at room temperature, obtain the UPy that one end is alkenyl Derivative 18c.By gained UPy derivative 18c respectively with the mercaptoethanol of equimolar equivalent BDK and ultraviolet light collective effect Lower reaction, converts hydroxyl for alkenyl.It is acyl by UPy derivative and 1 molar equivalent, two end group that 2 molar equivalent one end are hydroxyl The polycaprolactone of chloro reacts under the catalysis of triethylamine, obtains the polycaprolactone that UPy derivative base is contained at both ends.
2,7- amide is contained at vinylacetate-vinylalcohol random copolymer, 20 mass parts both ends obtained by 100 mass parts The polycaprolactone of base -1,8- naphthyridines end group, 30 mass parts both ends contain the polycaprolactone of UPy derivative base, the catalysis of 0.5 mass parts Agent 8 is sufficiently mixed, and obtains dynamic aggregation compositions of the invention.In the present embodiment, by the product sample vertically to after cutting It mediates, carries out Mechanics Performance Testing again after standing 6 hours at 50 DEG C in the case of no external force, measure before tensile strength is 82%, 78% be broken before rate elongation is.The product can be used for preparing coating, the adhesive etc. with self-repair function.
Embodiment 19
It is common to prepare a kind of hydridization dynamic aggregation compositions based on dimethyl silicone polymer and poly-β-hybroxybutyric acid Solid, supermolecular mechanism therein are based on side imidazoline ketone group and skeleton urea groups.
By the high molecular weight poly-β-hybroxybutyric acid of 1 molar equivalent, (300000) PHB, average molecular weight are about dissolved in dichloromethane Alkane instills the mixed solution for containing 1000 molar equivalent p-methyl benzenesulfonic acid and 10000 molar equivalent 1,4-butanediol.It is anti-at room temperature It answers, with methanol extraction and rinses product, obtaining the low molecular weight poly-β-hybroxybutyric acid that both ends are hydroxyl, (average molecular weight is about 3000).By UPy derivative 18c that one end is alkenyl respectively with the thioacetic acid of equimolar equivalent in the common of BDK and ultraviolet light The lower reaction of effect, converts carboxyl for alkenyl.By the PHB and 2 molar equivalent carboxyls envelope that the resulting both ends of 1 molar equivalent are hydroxyl The UPy derivative at end reacts under the catalysis of DCC and DMAP, obtains the PHB that two end groups are UPy derivative.
Under nitrogen protection, amination dimethyl siloxane 19a is added in urea, keeps the molar ratio of urea and side amino It is down to room temperature, obtains the ketone group of imidazoline containing side and side ammonia after being to slowly warm up to 160 DEG C, heat preservation about 1 hour under stirring for 9:10 The modified dimethyl polysiloxane 19b of base.1 molar equivalent 1,5- di-p oxyphenyl -1,4- pentadiene -3- ketone and 2 moles are worked as Amount 1,5- naphthalene diisocyanate is dissolved in methylene chloride, reacts under the catalysis of stannous octoate, obtains a kind of containing unsaturated bond Diisocyanate.
Under nitrogen protection, 100 mass parts molecular sieve SBA-1 and 2 mass parts of catalyst 5 are dispersed in toluene, at room temperature Stirring 6 hours is filtered and is eluted with n-hexane, obtains the molecular sieve for being loaded with catalyst after dry.
A certain amount of modified dimethyl polysiloxane 19b is blended with a certain amount of resulting unsaturated diisocyanate, is kept The molar ratio of side amino and isocyanate group is 1:1.02 in dimethyl silicone polymer, and it is sufficiently anti-in 60 DEG C to be calculated as 100 mass parts It answers.After complete reaction, adding the resulting both ends of 100 mass parts is UPy derivative PHB and the molecule for being loaded with catalyst Sieve removes solvent after being sufficiently blended, obtains hydridization dynamic aggregation compositions of the invention.
The product shows good viscoplasticity, while also showing excellent hydrolytic resistance, and catalyst carrier is also Has the function of enhancing.When its surface occurs damaged, by heating the healing that breakage can be achieved to form again, realize The selfreparing and recycling of material can be used for preparing the charger interface, number of mobile phone, tablet computer, notebook, camera etc. According to the plug of line interface etc., the aperture generated in connector swapping process carries out repairing reach the purpose of waterproof.
Embodiment 20
A kind of hydridization dynamic aggregation compositions ordinary solid for being based on butadiene-styrene rubber and poly- (methyl) acrylate is prepared, Supermolecular mechanism therein is based on side urea groups.
Acrylic acid 2- amino-ethyl ester and 4- biphenyl isocyanates are reacted in methylene chloride, keep amino and different The molar ratio of cyanate is 1:1, obtains the acrylate monomer 20a containing urea groups.By isocyanates ethyl acrylate and n-propylamine It is reacted in methylene chloride, keeping the molar ratio of amino and isocyanates is 1:1, obtains the acrylate monomer containing urea groups 20b.Isocyanates ethyl acrylate and nafoxidine are reacted in methylene chloride, keep rubbing for isocyanates and amino You obtain the acrylate monomer 20c of the derivative containing urea bond than being 1:1.
1 molar equivalent photoinitiator 2- hydroxy-2-methyl -1- phenyl -1- acetone, 10 molar equivalent 20a, 30 moles are worked as Amount 20b, 10 molar equivalent 20c, 10 molar equivalent n-BMAs are sufficiently blended and polymerize under light illumination, obtain containing not Poly- (methyl) acrylate of the modification of ipsilateral urea groups.
Modified poly- (methyl) acrylate obtained by 50 mass parts is broken into particle, is had with suitable catalyst 7 and swelling The toluene solution of 100 mass parts cross-linking type butadiene-styrene rubber is sufficiently blended, except obtaining hydridization dynamic aggregation object of the invention after solvent Composition.In the present embodiment, composition sample can be made to sealant or recuperability elastic component is carried out using can embody Good toughness and elasticity out, and can be according to the product for needing to be pressed into different shape size, breakage or the sample no longer needed Product may be recovered, and new product is made and uses.
Embodiment 21
A kind of hydridization dynamic aggregation compositions oligomer swell gel based on polynorbornene and polyethers is prepared, wherein Supermolecular mechanism be based on side carbamateyl and side amide groups.
Using 1 molar equivalent ethyl alcohol as initiator, by 100 molar equivalent ethylene oxide, 50 molar equivalents (S)-(ethylene oxide Methyl) t-butyl carbamate, the preparation of 50 molar equivalent 3- [(acetparaminosalol) phenoxy group] -1,2 epoxy prapane hybrid reaction Side group contains the polyethers of carbamate groups and amide groups.
By the catalysis of polyethers obtained by 50 mass parts, 100 mass parts alkyl-blocked polyethylene glycol oligomer and 1 mass parts The mass parts cross-linking type polynorbornene of agent 5 and 100 is sufficiently blended, and obtains hydridization dynamic aggregation compositions oligomer of the invention Swell gel.
The composition oligomer swell gel sample not only embodies very excellent tensile toughness, also have it is good can Plasticity and resilience；Product of different shapes, after pressing its surface, recess energy can be prepared into according to die size It is enough to reply rapidly, it when its surface occurs damaged, can be formed again by heating, realize and recycle.It can be made into each Class sealing element or other rubber accessories.
Embodiment 22
Prepare a kind of hydridization dynamic aggregation compositions ordinary solid based on polyurethane and polysiloxanes, oversubscription therein Son effect is based on side urea groups, side diamino triazine and side thymine base.
Using chloroplatinic acid as catalyst, by hydrogen containing siloxane and 2- vinyl -4,6- diamino-1,3,5-triazines and 1- (4- vinyl benzene methyl) thymidine reacts 3 hours at 90 DEG C in cyclohexanone, control hydrogen containing siloxane in silicon hydrogen with Compound 2- vinyl -4,6- diaminostilbene, 3,5- triazine, the molar ratio of 1- (4- vinyl benzene methyl) thymidine are 2:1: 1, obtain the polysiloxanes containing side hydrogen bond group.
With 1 molar equivalent 4,4'- azo bis- (4- cyano amylalcohols) is that initiator draws using 4- amylene-1-ol as chain-transferring agent 15 molar equivalent 20b and the polymerization of 15 molar equivalent n-butyl acrylates are sent out, the hydroxy-end capped polyacrylate in both ends is obtained.It will Polyacrylate obtained by 100 molar equivalents, 110 molar equivalent toluene di-isocyanate(TDI)s, 5 molar equivalent 9- alkenyl -12- hydroxyls ten Eight sour glyceryl esters are sufficiently blended, and sufficiently react under the catalysis of DBTDL, obtain the polyurethane based on polyacrylate.
By 2 molar equivalents and 1 molar equivalent 2,4-TDI is dissolved in hexamethylene with-two butanol of Isosorbide-5-Nitrae and reacts 24 hours at 80 DEG C, Obtain isocyanate-terminated prepolymer.Prepolymer obtained by 3 mass parts and bis- generation of 1 mass parts Grubbs catalyst 2 are dissolved in The chlorobenzene of 32 mass parts, and add in the water of 28.8 mass parts, it is stirred 30 minutes with the speed of 1000rpm in 70 DEG C.By 1 mass The glycol chain extender of part is slowly added in lotion, is maintained temperature revolving speed to continue stirring 2 hours, is obtained using polyurethane as microcapsules The catalytic component B of shell.
Polyurethane obtained by 100 mass parts, 10 content of component B, 30 mass parts are contained to the polysiloxanes of side hydrogen bond group And 15 mass parts polyvinylpyrrolidone microballoon be sufficiently blended, obtain the dynamic aggregation compositions of hydridization of the present invention.The reality Applying composition obtained in example can be made into the sealing element with self-repair function, while have certain moisture absorption moisture-proof function.
Embodiment 23
It is common to prepare a kind of hydridization dynamic aggregation compositions based on poly- limonene carbonic ester and poly-β-hybroxybutyric acid Solid, supermolecular mechanism therein are based on side carbamateyl and side urea groups pyrimidine ketone group.
Under the conditions of 90 DEG C of anhydrous no air, limonene oxide and catalyst 23a are dissolved in toluene, keep limonene oxide Molar ratio with catalyst is 100:1, and 10bar carbon dioxide is passed through into reaction vessel, and reaction obtains poly- limonene carbonic ester 23b.A certain amount of resulting poly- limonene carbonic ester 23b is dissolved in chloroform, excessive 2 mercapto ethanol, the positive fourth of 3- mercaptopropionic acid is added Ester and azo-bis-isobutyl cyanide, keeping 2 mercapto ethanol, 3- mercaptopropionic acid N-butyl, the molar ratio of initiator is 3:7:3, at 60 DEG C Lower reaction obtains the poly- limonene carbonic ester that part side group is hydroxyl.It is the poly- limonene carbonic acid of hydroxyl by resulting part side group Ester, one end are the UPy derivative (see embodiment 19) of carboxyl, fumaric acid blending, keep side hydroxyl in poly- limonene carbonic ester Base, one end are the UPy derivative of carboxyl, fumaric molar ratio is 5:4:1, and the pyrimidine of urea groups containing side is obtained after fully reacting The cross-linking modified poly- limonene carbonic ester of ketone.
6- amino -1- hexanol and methylchloroformate are reacted in methylene chloride, using anhydrous sodium bicarbonate as catalyst, control The molal quantity ratio of amino and methylchloroformate processed is 10:11, obtains compound 23c.By poly-β-hybroxybutyric acid (mean molecule Amount about 20000) and maleic anhydride be dissolved in chlorobenzene, make the initial mass volumetric concentration 3% of maleic anhydride.It was added at 130 DEG C Benzoyl Oxide makes the initial concentration 0.2% of benzoyl peroxide, is kept for thermotonus 6 hours, obtains Poly-β-hydroxybutyric acid Ester grafted maleic anhydride.Under inert gas protection, poly-β-hybroxybutyric acid grafted maleic anhydride and compound 23c are dissolved in two Toluene, keeps maleic anhydride side group and the molar ratio of compound segment 23c is 1:2.1.Catalyst is added with stirring to toluene sulphur Sour sodium is stirred to react in 105 DEG C, obtains the modification poly-β-hybroxybutyric acid in side group containing urethane bond.
At room temperature, 5 mass parts urine is added into the aqueous solution of 250 mass parts ethylene maleic acid anhydride copolymers containing 0.5wt% Element, 0.5 mass parts ammonium chloride and 0.5 mass parts resorcinol, and pH value is modulated 3.5 by the way that sodium hydroxide or hydrochloric acid is added. Solution is stirred with the speed of 800rpm, and a small amount of n-heptanol defoaming is added.Solution into stirring is slowly added to containing 5wt% Formalin is added after emulsion-stabilizing in 60 mass parts of chlorobenzene of catalyst 4, and keeps obtaining the molar ratio of urea formadehyde Than for 1:1.8.Lotion is warming up to 55 DEG C with 1 DEG C of speed per minute, and keeps the temperature 4 hours.Later, it is kept stirring but stops adding Heat.After lotion is cooled to room temperature, washing obtains the ureaformaldehyde microcapsules containing catalyst and chlorobenzene solution.
The resulting cross-linking modified poly- limonene carbonic ester of 100 mass parts is swollen in into dimethylbenzene, and 50 mass parts are added The polyester tiny balloon of modification poly-β-hybroxybutyric acid, 50 mass parts containing urethane bond, 20 mass parts contain catalysis The ureaformaldehyde microcapsules of agent 4 and chlorobenzene remove solvent, obtain hydridization dynamic aggregation compositions of the invention after being sufficiently mixed.
The resulting polymer composition sample surfaces of the embodiment are smooth, have certain intensity and rigidity.It is crushed It is placed on after placing 8h in 100 DEG C of molds, sample can compression moulding again.
Embodiment 24
A kind of hydridization dynamic aggregation compositions hydrogel based on polyvinylpyrrolidone and starch is prepared, it is therein super Molecular action is based on side carbamateyl.
1 molar equivalent 1,3-diamino-2-propanol 0.1mol, 3 molar equivalent anhydrous sodium bicarbonates are dissolved in methylene chloride, 2.2 molar equivalent methylchloroformates are instilled at room temperature.After being stirred to react two hours, compound 24a is obtained.
By polyvinylpyrrolidone (average molecular weight about 14000, average degree of polymerization be about 100) and etc. quality hydroxide Potassium dissolves in deionized water, reacts 48 hours under conditions of 150 DEG C.To after the reaction was completed, remove unreacted hydroxide Potassium, with salt acid for adjusting pH to 2-3, after carboxylic acid reaction one hour, then the bag filter for being 3500Da with interception is different in pH The dialysis of acid solution (pH=3, pH=4, pH=5) He Shuizhong gradient, freeze-drying obtain the polyvinylpyrrolidone of solid powder part open loop 24b.It is integrated through characteristic peak in nucleus magnetic hydrogen spectrum, calculating open loop rate is about 25%.
By the polyvinylpyrrolidone 24b of the part open loop containing 25 molar equivalent side carboxyls, 10 molar equivalent 1- (2- hydroxyls Ethyl) -2- imidazolone, 10 molar equivalent 4- hydroxy methylimidazoles and 5 molar equivalents Isosorbide-5-Nitrae-butylene glycol be dissolved in tetrahydrofuran, Under the catalysis of DCC and DMAP, the crosslinked polyvinylpyrrolidone that side group contains hydrogen bond group is obtained.
1 molar equivalent 1,4- butylene glycol and 2 molar equivalent isophorone diisocyanate is anti-under the catalysis of TDBDL It answers, obtains the diisocyanate containing unsaturated bond.100 mass parts of gained polyvinylpyrrolidone are swollen in into DMSO (DMSO In contain sodium nitrate, concentration 50mmol/L), the starch (the ratio between branched chain type straight chain type be about 3:7) of 80 mass parts is added, and A certain amount of ethyl isocyanate and gained diisocyanate keep hydroxyl and ethyl isocyanate in starch, diisocyanate to rub You sufficiently react under the catalysis of TDBDL than being about 40:8:1, obtain hydridization dynamic aggregation compositions component A of the invention. 100 mass parts obtained component A are swollen in into water, 1 mass parts of catalyst 27 is added to get corresponding hydrogel is arrived.
After hydrogel sample obtained by the present embodiment is cut, section is gently contacted, stand at room temperature 12 hours it is laggard Row rheometer test, the elasticity modulus and loss modulus of selfreparing sample restore to not cutting 90% or more of sample, with other Sterilization anti-inflammatory component combines, and can be used as medical dressing.
Embodiment 25
It is general to prepare a kind of hydridization dynamic aggregation compositions based on polyisoprene, unsaturated polyester (UP) and polyacrylate Logical solid, supermolecular mechanism therein are based on side imidazoline ketone group, side urea groups and side thiocarbamate base.
1 molar equivalent 1- (2- amino-ethyl) -2- imidazolone and 1 molar equivalent isocyanates ethyl acrylate are dissolved in Methylene chloride reacts 6 hours at room temperature, obtains acrylic ester monomer 25a.By 150 molar equivalent n-butyl acrylates and 50 Molar equivalent monomer 25a is sufficiently blended, and using 1 molar equivalent azo-bis-isobutyl cyanide as initiator, reacts, is contained at 85 DEG C Polymer of the side hydrogen bond group based on polyacrylate.
4,4'- stilbenedicarboxylicacid acids and 2- (t-butoxycarbonyl-amino) ethyl mercaptan are mixed according to molar ratio 1:1.1, then The photoinitiator benzoin dimethylether (DMPA) of 0.2wt% is added, the ultraviolet radioactive 4h in UV crosslinking instrument obtains side group and has The dicarboxylic acid compound of carbamate groups.
It takes the commercially available cross-linking type polyisoprene of 50 mass parts and the resulting polyacrylate of 300 mass parts is swollen or dissolution Or it is scattered in methylene chloride.By gained with the dicarboxylic acid compound of hydrogen bond group, 1,6-HD, 1,4- butylene glycol and Trimethylolpropane is mixed according to molar ratio 100:30:20:40, is taken 50 mass parts, is added to containing polyisoprene and polypropylene The methylene chloride of acid esters is sufficiently reacted, and product is blended with 1 mass parts of catalyst 5, is obtained using DCC and DMAP as catalyst Hydridization dynamic aggregation compositions of the invention.The resulting composition of the embodiment can be used as adhesive, block glue.
The above description is only an embodiment of the present invention, is not intended to limit the scope of the invention, all to utilize this hair Equivalent structure or equivalent flow shift made by bright description is applied directly or indirectly in other relevant technology necks Domain is included within the scope of the present invention.

Claims (11)

1. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B, which is characterized in that wherein the hydridization is dynamic State polymer composition components A is comprising at least one cross-linked network and at the same time containing olefin cross metathesis double decomposition can occur The hydridization dynamic aggregation object of the unsaturated carbon-carbon double bond of reaction and the hydrogen bond group that supermolecule hydrogen bond action can be formed；It is wherein described Hydridization dynamic aggregation compositions component B be unsaturated carbon in the catalysis hydridization dynamic aggregation compositions component A Catalyst, catalyst composites or the catalyst and catalyst composites of olefin cross metathesis metathesis reaction occur for carbon double bond Mixture；Wherein, when the hydrogen bond group for forming supermolecule hydrogen bond action is only side group hydrogen bond group, under containing At least one of structure shown in formula:
Wherein,Indicate the connection with polymer chain, R is substituent group, and G is end group；Between G,Between R, G and R Between it is cyclic or not cyclic；
Wherein, X respectively stands alone as any one of oxygen atom, sulphur atom, nitrogen-atoms, and Y respectively stands alone as oxygen atom, in sulphur atom It is any；
Wherein, a is the number for the R being connected with X atom；When X is oxygen atom or sulphur atom, a 0, R is not present；When X is that nitrogen is former The period of the day from 11 p.m. to 1 a.m, a 1, R is respectively individually present.
2. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In wherein the hydridization dynamic aggregation compositions component A has one of network structure as described below:
Only one cross-linked network in the hydridization dynamic aggregation compositions component A, simultaneously containing dynamic in the cross-linked network State covalent cross-linking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking reaches its gel point or more, supermolecule crosslinking The degree of cross linking is in its gel point above and below；
Only one cross-linked network in the hydridization dynamic aggregation compositions component A, simultaneously containing dynamic in the cross-linked network State covalent cross-linking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking is in its gel point hereinafter, the friendship of supermolecule crosslinking Connection degree is more than its gel point；
Only one cross-linked network in the hydridization dynamic aggregation compositions component A, simultaneously containing dynamic in the cross-linked network State covalent cross-linking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking is in its gel point hereinafter, the friendship of supermolecule crosslinking Connection degree in its gel point hereinafter, but the sum of the two degree of cross linking more than gel point；
Containing there are two networks in the hydridization dynamic aggregation compositions component A；Dynamic covalent cross-linking is contained only in 1st network, Its degree of cross linking is more than its gel point；Supermolecule crosslinking is contained only in 2nd network, the degree of cross linking is more than its gel point；
Containing there are two networks in the hydridization dynamic aggregation compositions component A；Covalent cross-linking containing dynamic and super in 1st network Molecule cross-link is crosslinked containing dynamic covalent cross-linking and supermolecule in the cross-linked network, wherein the crosslinking of dynamic covalent cross-linking simultaneously Degree is more than its gel point, and the degree of cross linking of supermolecule crosslinking is in its gel point above and below；Supermolecule friendship is contained only in 2nd network Connection, the degree of cross linking is more than its gel point；
Contain a network in the hydridization dynamic aggregation compositions component A, wherein only containing dynamic more than gel point Covalent cross-linking, the supermolecule degree of cross linking are dispersed in dynamic covalent cross-linking network in its gel point supermolecule polymer below；
Contain a network in the hydridization dynamic aggregation compositions component A, contains dynamic simultaneously altogether in the cross-linked network Valence crosslinking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking reaches its gel point or more, the crosslinking of supermolecule crosslinking Degree is in its gel point above and below；The supermolecule degree of cross linking is dispersed in dynamic covalently in its gel point supermolecule polymer below In cross-linked network；
Contain a network in the hydridization dynamic aggregation compositions component A, wherein only containing dynamic more than gel point Covalent cross-linking, supermolecule polymer of the supermolecule degree of cross linking more than its gel point are dispersed in dynamic covalent cross-linking with graininess In network；
Contain a network in the hydridization dynamic aggregation compositions component A, contains dynamic simultaneously altogether in the cross-linked network Valence crosslinking and supermolecule crosslinking, wherein the degree of cross linking of dynamic covalent cross-linking reaches its gel point or more, the crosslinking of supermolecule crosslinking Degree is in its gel point above and below；Supermolecule polymer of the supermolecule degree of cross linking more than its gel point is dispersed with graininess In dynamic covalent cross-linking network.
3. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In shown in following formula alkene friendship occurring containing at least one in the cross-linked network skeletal chain of the hydridization dynamic aggregation object Pitch the unsaturated carbon-carbon double bond of transposition metathesis reaction:
Wherein,Indicate the connection with polymer chain or any other suitable group or atom.
4. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In wherein can be formed in the hydrogen bond group of supermolecule hydrogen bond action in the hydridization dynamic aggregation compositions component A, R choosing From hydrogen atom, halogen atom, C1-20Alkyl, C1-20Miscellaneous alkyl, substituted C1-20Alkyl or substituted miscellaneous alkyl.
5. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In wherein also containing amino, hydroxyl, carboxyl, amide groups, thioamides base, pyrrolidones in the hydridization dynamic aggregation object At least one of base, imidazole radicals, pyrazolyl, nitrogen oxazolyl and its derivative base are used as side group hydrogen bond group.
6. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In wherein containing at least a kind of hydrogen bond base containing hydrogen bond donor and hydrogen bond receptor simultaneously in the hydridization dynamic aggregation object Group as main chain backbone hydrogen bond group, side chain skeleton hydrogen bond group, end group hydrogen bond group or in which any two, three kinds of group It closes.
7. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 1, feature exist In wherein at least a kind of hydrogen bond group is located at the side group or side chain of the hydridization dynamic aggregation object in the hydrogen bond group Or side group and side chain.
8. a kind of hydridization dynamic aggregation comprising at least two component of A, B described in any claim in -7 according to claim 1 Compositions, which is characterized in that the hydridization dynamic aggregation compositions have following any character: ordinary solid, elasticity Body, gel, foam.
9. a kind of hydridization dynamic aggregation comprising at least two component of A, B described in any claim in -7 according to claim 1 Compositions, which is characterized in that constitute the hydridization dynamic aggregation compositions recipe ingredient further include it is following any or Appoint it is several can additive or usable object: other polymers, auxiliary agent, filler, sweller.
10. a kind of hydridization dynamic aggregation compositions comprising at least two component of A, B according to claim 9, feature It is, wherein the other polymers are selected from following any or appoint several: natural polymer, synthesis macromolecule Compound；The auxiliary agent is selected from following any or appoints several: catalyst, initiator, antioxidant, light stabilizer, heat are steady Determine agent, dispersing agent, emulsifier, fire retardant, toughener, coupling agent, solvent, lubricant, release agent, plasticizer, thickener, thixotroping Agent, colorant, fluorescent whitening agent, delustering agent, antistatic agent, dehydrating agent, biocide mildewcide, foaming agent, helps foaming at levelling agent Agent, nucleating agent, rheological agent；The filler is selected from following any or appoints several: inorganic non-metallic filler, has metal packing Machine filler；The sweller is selected from following any or appoints several: water, organic solvent, ionic liquid, oligomer, plasticizer.
11. a kind of hydridization dynamic comprising at least two component of A, B described in any claim in -7,10 according to claim 1 Polymer composition, which is characterized in that the hydridization dynamic aggregation compositions are applied to following material or product: selfreparing Property coating, self-repairability plate, self-repairability sealing material, self-repairability block glue, self-repairability conducting resinl, toughness material, Tough elastomer material, thermal insulation material, shape-memory material, energy storage device material, toy, toy filler.
CN201710966091.8A 2017-10-17 2017-10-17 A kind of hydridization dynamic aggregation compositions and its application Pending CN109666153A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710966091.8A CN109666153A (en) 2017-10-17 2017-10-17 A kind of hydridization dynamic aggregation compositions and its application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710966091.8A CN109666153A (en) 2017-10-17 2017-10-17 A kind of hydridization dynamic aggregation compositions and its application

Publications (1)

Publication Number Publication Date
CN109666153A true CN109666153A (en) 2019-04-23

Family

ID=66140446

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710966091.8A Pending CN109666153A (en) 2017-10-17 2017-10-17 A kind of hydridization dynamic aggregation compositions and its application

Country Status (1)

Country Link
CN (1) CN109666153A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111948383A (en) * 2019-05-23 2020-11-17 裴广华 Sucrose-containing biological product stabilizer for ELISA kit
CN113045283A (en) * 2021-03-24 2021-06-29 交通运输部公路科学研究所 Intelligent trigger type concrete micro-crack self-repairing microcapsule and preparation method thereof
CN113698802A (en) * 2021-08-24 2021-11-26 成都新柯力化工科技有限公司 Graphene hybridized organic-inorganic anticorrosive paint and preparation method thereof
CN113801469A (en) * 2020-06-16 2021-12-17 香港城市大学深圳研究院 Graphene oxide-based nanocomposite and preparation method thereof
WO2023176106A1 (en) * 2022-03-18 2023-09-21 株式会社ブリヂストン Rubber composition

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4080398A (en) * 1974-03-15 1978-03-21 Entreprise De Recherches Et D'activites Petrolieres (Erap) Process for preparing catalysts for use in olefins conversion reactions
CN102317357A (en) * 2008-12-19 2012-01-11 3M创新有限公司 Shape-memory polymer
CN105646872A (en) * 2016-02-26 2016-06-08 翁秋梅 Dynamic polymer material
CN105860017A (en) * 2016-04-12 2016-08-17 江南大学 Bio-based photosensitive polyurethane resin, and self-repairing coating made of resin

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4080398A (en) * 1974-03-15 1978-03-21 Entreprise De Recherches Et D'activites Petrolieres (Erap) Process for preparing catalysts for use in olefins conversion reactions
CN102317357A (en) * 2008-12-19 2012-01-11 3M创新有限公司 Shape-memory polymer
CN105646872A (en) * 2016-02-26 2016-06-08 翁秋梅 Dynamic polymer material
CN105860017A (en) * 2016-04-12 2016-08-17 江南大学 Bio-based photosensitive polyurethane resin, and self-repairing coating made of resin

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
NEAL JAMES A. ET AL: "Enhancing mechanical performance of a covalent self-healing material by sacrificial nocovalent bonds", 《JOURNAL OF THE AMERICAN CHEMICAL SOCIETY》 *
XINGYUAN ZHANG ET AL: "An Injectable Interpenetrating Polymer Network Hydrogel with Tunable Mechanical Properties and Self-Healing Abilities", 《MACROMOLECULAR CHEMISTRY AND PHYSICS》 *
ZOU WEIKE ET AL: "Dynamic covalent polymer networks: from old chemistry to modern day innovations", 《ADVANCED MATERIALS》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111948383A (en) * 2019-05-23 2020-11-17 裴广华 Sucrose-containing biological product stabilizer for ELISA kit
CN111948383B (en) * 2019-05-23 2023-10-13 合肥善本生物科技有限公司 Sucrose-containing biological product stabilizer for ELISA kit
CN113801469A (en) * 2020-06-16 2021-12-17 香港城市大学深圳研究院 Graphene oxide-based nanocomposite and preparation method thereof
CN113801469B (en) * 2020-06-16 2023-08-18 香港城市大学深圳研究院 Graphene oxide based nanocomposite and preparation method thereof
CN113045283A (en) * 2021-03-24 2021-06-29 交通运输部公路科学研究所 Intelligent trigger type concrete micro-crack self-repairing microcapsule and preparation method thereof
CN113698802A (en) * 2021-08-24 2021-11-26 成都新柯力化工科技有限公司 Graphene hybridized organic-inorganic anticorrosive paint and preparation method thereof
WO2023176106A1 (en) * 2022-03-18 2023-09-21 株式会社ブリヂストン Rubber composition

Similar Documents

Publication Publication Date Title
CN109666178A (en) A kind of hydridization dynamic aggregation compositions and its application
CN107805308B (en) Dynamic polymer with hybrid cross-linked network and application thereof
CN109666153A (en) A kind of hydridization dynamic aggregation compositions and its application
CN109206625A (en) A kind of physics split-phase supermolecule dynamic aggregation object and its application
CN107556433A (en) A kind of dynamic aggregation thing elastomer and its application with hybrid cross-linked network
CN109666168A (en) A kind of self-repairability solid-state hydridization dynamic aggregation object and its application
CN107698748A (en) A kind of dynamic aggregation thing of hybrid cross-linked network and its application
CN108341951B (en) Dynamic polymer with hybrid cross-linked structure and application thereof
CN109666167B (en) Hybrid dynamic polymer composition
CN107815055A (en) A kind of dynamic aggregation thing thermoplastic elastomer (TPE) and its application
CN109422835A (en) A kind of dynamic aggregation object containing combination supermolecular mechanism
CN109207110B (en) Hybrid cross-linked dynamic polymer
CN107815056A (en) A kind of dynamic aggregation thing thermoplastic elastomer (TPE) and its application
CN109206825A (en) A kind of assembly energy-absorbing method based on physics split-phase supermolecule dynamic aggregation object
CN109206570A (en) A kind of compliant physical split-phase supermolecule dynamic aggregation object and its application
CN109206576A (en) A kind of hybrid cross-linked dynamic aggregation object
CN109666093A (en) A kind of dynamic aggregation object with hybrid cross-linked network structure
CN109666121B (en) Hybrid dynamic cross-linked polymer and application thereof
CN109666160B (en) Dynamic polymer with hybrid cross-linked network
CN109666159A (en) A kind of method of energy-absorbing and application thereof
CN109423148A (en) A kind of energy-absorbing method based on dynamic aggregation object
CN109666156A (en) A kind of energy-absorbing method based on hydridization dynamic aggregation compositions
CN109206627A (en) A kind of hybrid cross-linked dynamic aggregation object
CN109206550B (en) Hybrid supermolecule dynamic polymer
CN109422836A (en) A kind of dynamic crosslinking polymer containing combination supermolecular mechanism

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20220120

Address after: Room 3179, Xuanye building, Pioneer Park, torch hi tech Zone, Xiamen, Fujian, 361000

Applicant after: Xiamen iron cloth Mstar Technology Ltd.

Address before: 363000 room D, 15th floor, Huayuan Building, Yan'an North Road, dongputou street, Xiangcheng District, Zhangzhou City, Fujian Province

Applicant before: Weng Qiumei

CB02 Change of applicant information
CB02 Change of applicant information

Address after: 361000 chuangkehui-219, Chuangye building, No. 11-1, torch East Road, entrepreneurship Park, Xiamen Torch High tech Zone, Xiamen, Fujian

Applicant after: Xiamen Tiance Material Technology Co.,Ltd.

Address before: Room 3179, Xuanye building, Pioneer Park, torch hi tech Zone, Xiamen, Fujian, 361000

Applicant before: Xiamen iron cloth Mstar Technology Ltd.

RJ01 Rejection of invention patent application after publication

Application publication date: 20190423