CN1278286A - Modified condensation polymer - Google Patents

Modified condensation polymer Download PDF

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Publication number
CN1278286A
CN1278286A CN98810633A CN98810633A CN1278286A CN 1278286 A CN1278286 A CN 1278286A CN 98810633 A CN98810633 A CN 98810633A CN 98810633 A CN98810633 A CN 98810633A CN 1278286 A CN1278286 A CN 1278286A
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polymkeric substance
reactor
mixture
latex
glycol
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D·L·默累
A·S·琼斯
S·S·维尔斯
小D·W·卡里科
W·R·达尼尔
D·C·维布斯特
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Eastman Chemical Co
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Eastman Chemical Co
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    • 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
    • C08F2/00—Processes of polymerisation
    • C08F2/12—Polymerisation in non-solvents
    • C08F2/16—Aqueous medium
    • C08F2/22—Emulsion polymerisation
    • 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
    • C08G18/08—Processes
    • C08G18/0838—Manufacture of polymers in the presence of non-reactive compounds
    • C08G18/0842—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents
    • C08G18/0861—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers
    • C08G18/0871—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being organic
    • C08G18/0876—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being organic the dispersing or dispersed phase being a polyol
    • 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
    • C08G18/6216—Polymers of alpha-beta ethylenically unsaturated carboxylic acids or of derivatives thereof
    • C08G18/622—Polymers of esters of alpha-beta ethylenically unsaturated carboxylic acids
    • C08G18/6237—Polymers of esters containing glycidyl groups of alpha-beta ethylenically unsaturated carboxylic acids; reaction products thereof
    • 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
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04—Polyurethanes
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00—Inks
    • C09D11/02—Printing inks
    • C09D11/03—Printing inks characterised by features other than the chemical nature of the binder
    • C09D11/033—Printing inks characterised by features other than the chemical nature of the binder characterised by the solvent
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00—Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/20—Diluents or solvents

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Dispersion Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)

Abstract

The invention pertains to methods for preparing modified condensation polymers wherein the steps include: (a) preparing a polymer colloid system comprising a first polymer dispersed in a liquid continuous phase; (b)introducing the polymer colloid system into a condensation reaction medium prior to or during the condensation reaction, wherein the condensation reaction medium comprises (1) a diacid, di-isocyanate, dialkyl carbonate, diaryl carbonate, dihalo carbonate or a mixture thereof, wherein the condensation reaction medium optionally comprises a diol component; and polymerizing the diol component and component (1), thereby forming a modified condensation polymer.

Description

Modified condensation polymer
Related application
The U.S. Provisional Application sequence number 60/057 that the present invention requires 1997-08-28 to submit to, 714 and the right of priority of the U.S. Provisional Application sequence number 60/058,008 submitted to of 1997-08-28, at this with 60/057, the full content of 714 and 60/058,008 these 2 pieces of applications is incorporated this paper into as a reference.
Invention field
The present invention relates to diol latex compositions and prepare the method for this kind diol latex compositions.This diol latex compositions preferably prepares with the main component of glycol as external phase.
The method that the invention still further relates to polycondensate and prepare this polycondensate.This polycondensate is to adopt the polymeric colloid system that preferably comprises diol component to prepare.In preferred embodiments, the polymeric colloid system is this diol latex compositions.Polycondensate according to the inventive method preparation is a multi-phase material.
Background of invention
Speak of the of the present invention the 1st main embodiment, latex polymer, the specific characteristic that has because of its feeding system, and be applied in the various products.Latex polymer because of its person's character determines, has the viscosity that is lower than its solution counterpart.This lower viscosity makes it in use can be with higher polymer concentration feed, and can not run into the such or such problem that interrelates with high viscosity fluid.Unique viscosity behavior of latex polymer derives from the inhomogeneity of this system.Latex polymer is to be dispersed in rather than to be dissolved in this fact in the low viscosity continuum, has weakened the influence of latex polymer to dielectric viscosity.Therefore, the external phase of latex or solvent are the main ingredients that influences system viscosity.
With regard to the typical case, the external phase of most of commercial latex is water.The benefit of doing like this is that the toxicity that glassware for drinking water has is little and not flammable.When with external phase during as the feed system of polymkeric substance, water is a kind of good selection.Yet in some occasion, water may be harmful to base material, perhaps will inevitably change the drying property of latex.
In external phase, can use the solvent beyond dewatering.For example, the known small amounts of diol solvent that adds.JP 04335002 discloses adding alcohol and has produced low temperature ethylene base ester emulsion as frostproofer.The consumption of disclosed diol solvent is lower than 50wt%.JP 63186703 discloses membrane-forming agent and the softening agent of the highest 10wt% that adds solid ingredient, influences the film forming character of finished emulsion.JP 06184217 discloses and added polyvalent alcohol and water-soluble inorganic salt in suspension polymerization of VC, produces the vinyl chloride-base polymer with good powder flowbility.EP 255137 discloses the water-soluble alcohol that uses 100/0～50/50-water/pure content ratio, to produce the high-polymerization degree polyvinyl ester.
US 3,779, and 969 have described the application of propylene glycol or the glycol ether of the 10～50wt% that accounts for emulsion.The purpose that adds ethylene glycol is to improve the wettability of emulsion.
US 4,458, and 050 has described the method for making polymeric dispersions in diol chain extender.This patent relates to the production of the low viscosity polymer used of preparation urethane.Should in diol solvent, reach stable composition by the unexposed latex that makes of ' 050 patent.This patent also discloses employing number of polymers stablizer and has prepared this dispersed polymeres.
JP 60040182 and JP 64001786 disclose the composition that waterproof-grease proofing fabric treating is used.Said composition is intended to prepare fluoropolymer emulsion in the diol solvent mixture.This kind fluoropolymer is not a purpose of the present invention.
US 4,810,763 be disclosed in carry out in the organic medium suspension polymerization with the preparation pressure sensitive adhesive.The concrete purpose of composition described in these ' 763 patents is to produce the macrobead dispersion.This patent is unexposed to generate the composition that granularity is lower than the granularity latex of 1000nm.The also unexposed letex polymerization of this patent.
US 4,885, and 350 and the open dispersion polymerizations of vinyl monomer in hydrophilic organic liquid of US 5,061,766.For producing dispersed polymeres, the number of polymers dispersion stabilizer is used in suggestion.
Before the present invention, still do not know to have the people in the external phase of latex polymer, to use and account for 40% of external phase, more preferably 60wt% or higher glycol.So the glycol consumption of level can give latex composition some advantage, the improvement of consistency for example and between the specific base material, and the improvement of latex drying property perhaps can be used in the present invention's the 2nd main embodiment (preparation of polycondensate/the 1st polymeric matrix).
About the present invention's the 2nd main embodiment, knownly can in forcing machine, carry out the purpose that blend reaches this polycondensate modification by polycondensate and another kind of polymkeric substance.For example, for improving the impact property of polyester, in twin screw extruder, the elastomerics of lower glass transition temperatures (Tg) is joined in the polyester usually.Japan Kokai JP 02155944 has described a kind of mixed ingredients of mo(u)lded item, the physical blending thing that comprises saturated polyester and styrene polymer, this styrene polymer contain the glycidyl amido grafting olefin polymer of the olefin polymer of 1～100phr (umbers of per hundred parts of resins) glycidyl methacrylate graft.Japan Kokai JP02016145, JP 02024346, JP 01123854, JP 01153249 and JP 01163254 is all disclosed is aromatic polyester and the blend of passing through between the resin of graft emulsion copolymerization.The size of disperse phase is the key that obtains advantageous property.This is a kind of energy-intensive process, causes polymer physics performance decrease, particularly molecular weight sometimes, and it also requires the blend step, and this will need to use more resource and more time.
United States Patent (USP) 5,652,306,4,180,494 and 5,409,967 disclose the composition that is used to improve the aromatic polyester shock-resistance, relate to the blend of vinylformic acid or polyhutadiene/acrylic rubber powder and polyethylene terephthalate (PET).The acrylic rubber particle is by typical core/shell letex polymerization, latex enforcement spraying drying is reclaimed make then.The program that reclaims this latex is summarized in United States Patent (USP) 3,895, in 703.
Elastomerics and plastics extrude blend, labour intensity is big and time-consuming.Generally with polyhutadiene or poly-(butyl acrylate) as the lower glass transition temperatures polymkeric substance, realize impact-resistant modified to polyester.The low Tg elastomerics of this class is difficult to operation, so require to use the 2nd monomer, is typically " core " that will hang down the Tg polymkeric substance as " shell " with poly-(methyl methacrylate) and wraps up so that make and hang down the Tg polymkeric substance and can operate.Core-shell polymer joins in the polyester in forcing machine then through separation, drying.
Need a kind of method of producing blend polymer at present in comparatively economic mode.If can be in not only can use with a kind of method core-shell and non-core-shell base polymer the two but also can use the two one of produce blend polymer, that also will be desirable.This kind needs are solved by the present invention, and the present invention can adopt polymerization reactor to obtain this kind blend, and wherein the physicals of polycondensate is kept or improves.
Summary of the invention
The present invention the 1st main aspect relates to a kind of diol latex compositions, comprises:
(a) contain the latex polymer particles of the residue of ethylene linkage unsaturated monomer, wherein the granularity of latex polymer particles is lower than 1000nm;
(b) tensio-active agent; And
(c) comprise the continuous liquid phase of diol component, wherein diol component accounts for 60～100wt% of external phase.
The present invention the 2nd main aspect relates to a kind of method for preparing polycondensate/the 1st polymeric matrix, comprises the following steps;
(a) preparation polymeric colloid system, it comprises the 1st polymkeric substance that is dispersed in the continuous liquid phase; And
(b) the polymeric colloid system is incorporated in the condensation reaction medium, can before the condensation reaction or during implement, wherein the condensation reaction medium comprises (1) diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether (dihalo carbonate) or above-mentioned mixture;
Wherein continuously liquid phase, condensation reaction medium or the two comprise diol component, so just form " polycondensate/the 1st polymeric matrix ".
Detailed Description Of The Invention
The present invention by describe in detail with reference to the following preferred embodiment of the invention and comprising embodiment, will become is more readily understood.
Before disclosure and description composition of matter of the present invention and method, it is to be noted, the invention is not restricted to these concrete synthetic methods or concrete prescription, because these can change naturally.Be also pointed out that term used herein only is used for the specific embodiments purpose of description, has not intended the qualification effect.
In this paper and claim subsequently, will use many terms, and limit them and will have following implication:
Singulative " a " reaches " an " and " the " contains the plural number that object is discussed, unless spell out in addition in the context.
" optional " or " randomly " is meant that incident described later or situation can or can not take place, and refer to, described content comprises the example that described incident or situation take place, and the example that does not take place.
" latex " is defined as the dispersion of a kind of polymer beads in external phase in this article, and the preferred granularity of this polymer beads is in the scope of 10～1000nm.Polymer beads is by emulsion polymerization prepared." latex particle " is defined as this kind polymer beads that is dispersed in the external phase in this article.
" glycol " is the synonym of dibasic alcohol or dihydroxy alcohol." polyvalent alcohol " is the polyhydroxy-alcohol that contains 3 or more a plurality of oh groups.
The application in the whole text in, every when mentioning publication, whole disclosures of this publication are all incorporated this paper into as a reference, so that current state-of-the-art technology related to the present invention more fully is described.
The present invention the 1st main aspect relates to a kind of diol latex compositions, comprises:
(a) close the latex polymer particles of the residue of ethylene linkage unsaturated monomer, wherein the granularity of latex polymer particles is lower than 1000nm;
(b) tensio-active agent; And
(c) comprise the continuous liquid phase of diol component, wherein diol component accounts for 60～100wt% of external phase.
The present invention the 2nd main aspect relates to a kind of method for preparing polycondensate/the 1st polymeric matrix, comprises the following steps:
(a) preparation polymeric colloid system, it comprises the 1st polymkeric substance that is dispersed in the continuous liquid phase; And
(b) the polymeric colloid system is incorporated in the condensation reaction medium, can before the condensation reaction or during implement, wherein the condensation reaction medium comprises (1) diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether or above-mentioned mixture;
Wherein continuously liquid phase, condensation reaction medium or the two comprise diol component, so just form polycondensate/the 1st polymeric matrix.
The method that the present invention the 1st main aspect relates to a kind of diol latex compositions and prepares this kind diol latex compositions, wherein this diol latex compositions comprise by the ethylene linkage unsaturated monomer radical initiator, suitable surfactant and do not dissolve this polymkeric substance glycol external phase in the presence of carry out polymerization and the deutero-latex polymer.This diol latex compositions is by emulsion polymerization prepared, and wherein the external phase of emulsion comprises the combination of diol component or a kind or multiple glycol and other (being total to) solvents.
The present invention the 2nd main aspect relates to introduces the polymeric colloid system in polycondensation, this system preference comprises diol component as co-reactant.This diol component can be used as the co-reactant in the polycondensation, with preparation polyester, polycarbonate, urethane, perhaps is used for the polycondensation that any other uses glycol.
More particularly, the present invention the 2nd main aspect comprises, by introduce the polymeric colloid system in the polycondensation that contains glycol, captures the method and composition of polymer beads during this polycondensation.In one embodiment of the present invention, the polymeric colloid system is the diol latex compositions of the present invention the 1st aspect, and the external phase that wherein contains diol component is the glycol source of polycondensation.In another embodiment, the polymeric colloid system comprises the external phase based on water.External phase based on water can or can not contain diol component.In another embodiment, the polymeric colloid system comprises the external phase that is mainly glycol.If make this polymeric colloid system stabilization rightly, then this polymeric colloid system will keep its integrity and maintain obtain disperse phase in the polycondensate matrix.Character on polymer beads is decided, and the physical property of polycondensate can improve.The present invention includes the composition and the method that are used to produce polymkeric substance, wherein at the 2nd polymkeric substance, i.e. polycondensate, polymerization period between, introduce the 1st polymkeric substance, promptly constitute the polymkeric substance of polymeric colloid system.
So the polycondensate that is obtained comprises the polymer beads that constitutes the polymeric colloid system, wherein this polymer beads preferably is dispersed in again in this solid state condensation thing external phase.The blend polymer that this just provides a kind of physicals to improve.For example, if the diol latex polymkeric substance is low Tg rubber, and polycondensate is that polyester is as gathering (ethylene glycol terephthalate) (PET), just the polycondensate blend that is obtained can have the shock-resistant of improvement.And, do like this with regard to avoided to as prior art for obtaining the needs that low Tg rubber uses core-housing system.I. diol latex compositions
Mention above, the present invention the 1st main aspect relates to by the emulsion polymerization prepared diol latex compositions, and wherein external phase comprises diol component.This diol latex compositions can be used for various purposes, includes but not limited to, and ink composite, pigment masterbatch, coating, and as the reactant in the polycondensation.Diol latex compositions comprises latex polymer and external phase, and this external phase comprises diol component.
The diol component that can be used for the external phase of diol latex compositions includes but not limited to, any aliphatic series that contains about 2～about 10 carbon atoms or cycloaliphatic diol and composition thereof.Preferred glycol comprises ethylene glycol, 1,3-trimethylene, 1,2-propylene glycol, tripropylene glycol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, 1,7-heptanediol, 1,8-ethohexadiol, 1,9-nonanediol, neopentyl glycol, suitable-or anti--cyclohexanedimethanol, suitable-or anti--2,2,4,4-tetramethyl--1,3-cyclobutanediol, glycol ether, 2,2,4-trimethylammonium-1,3-pentanediol, 2-methyl isophthalic acid, ammediol, 2-methyl isophthalic acid, 3-pentanediol or its mixture; Preferred glycol comprises ethylene glycol, 1,2-propylene glycol, tripropylene glycol, 1,4-butyleneglycol, glycol ether, neopentyl glycol, suitable-as to reach instead-cyclohexanedimethanol and composition thereof; Further preferred glycol comprises neopentyl glycol, ethylene glycol, suitable-or anti--cyclohexanedimethanol, 1,4-butyleneglycol or its mixture.
Except diol component, external phase also can comprise a kind or multiple polyol component.The typical polyol component that can be used for external phase includes but not limited to, glycerine, TriMethylolPropane(TMP), tetramethylolmethane, 1,2,6-hexanetriol, Sorbitol Powder, 1,1,4,4-four (methylol) hexanaphthene, three (2-hydroxyethyl) isocyanuric acid ester, Dipentaerythritol and composition thereof.Except low molecular weight polyols, also can use the polyvalent alcohol (MW 400～3000) of higher molecular weight, preferably by the alkylene oxide that contains 2～3 carbon atoms such as oxyethane or propylene oxide and contain the polyol initiator of 3～6 carbon atoms such as the condensation deutero-triol of glycerine and so on.
External phase also can comprise cosolvent.This class cosolvent includes but not limited to, water, methyl alcohol, ethanol, propyl alcohol, propyl carbinol and composition thereof.The consumption of cosolvent is a benchmark in the external phase gross weight, less than 60wt%, is more preferably less than 40wt%.
" the external phase gross weight " that this paper uses in the whole text comprises the weight of diol component, polyol component and cosolvent.The weight of any tensio-active agent all is not included within the external phase gross weight.
In one embodiment, the amount that diol component exists, in the external phase gross weight is benchmark, at 60～100wt%, be preferably 65～100wt% of external phase gross weight, more preferably 75～100 total amount % of external phase gross weight, more preferably 90～100wt% of external phase gross weight also, the 100wt% of further preferred external phase gross weight.In another embodiment, contain glycol and constitute by diol component substantially mutually.
In a kind of alternate embodiment, the amount that diol component exists is a benchmark in the external phase gross weight, at 40～100wt%, be preferably 50～100wt% of external phase gross weight, more preferably 65～100wt% of external phase gross weight, 90～100wt% of further preferred external phase gross weight.In another embodiment, external phase is made of diol component substantially.This external phase gross weight comprises the weight of diol component, polyol component and cosolvent.The weight of any tensio-active agent all is not included within the external phase gross weight.In this embodiment, diol component is substantially by tripropylene glycol, 1, and 4-butyleneglycol, neopentyl glycol, cyclohexanedimethanol or its mixture are formed.
Diol latex compositions of the present invention is by emulsion polymerization prepared.Solids content in the reaction is preferably at 5～60wt%, but more preferably at 20～50wt%.The granularity of the latex polymer particles of diol latex compositions preferably is lower than 1000nm; More preferably at 20～700nm, the further scope of preferred 60～250nm.Temperature of reaction is preferably at 0～190 ℃, more preferably 60～90 ℃ scope.
Preferably in the preparation of diol latex compositions, use tensio-active agent.The kind and the consumption that are used for the tensio-active agent of letex polymerization depend on monomeric combination and polymeric reaction condition.The typical surface promoting agent that uses in letex polymerization is negatively charged ion, positively charged ion or nonionogenic tenside.Can be used for anion surfactant among the present invention comprise such as alkyl, aryl or an alkarylsulphonic acid, vitriolic or the basic metal of phosphoric acid or the tensio-active agent the ammonium salt and composition thereof.Suitable ionic surfactant pack is drawn together but is not limited to, and alkyl and alkaryl polyglycol ether are as the ethoxylated product of lauryl alcohol, oleyl alcohol and Stearyl alcohol; The alkylphenol glycol ethers includes but not limited to the ethoxylated product of octyl group or nonyl phenol.Suitable tensio-active agent can be seen in the volume I in McCutheon: " emulsifying agent and washing composition " 1996, North America version, MC publishing company, Glen Rock, NJ, 1996.Tensio-active agent can or can not have reactivity in polymerization.In one embodiment, useful tensio-active agent is the sulfates/sulfonates of nonyl phenol and chain triacontanol ethoxylate.Preferred surfactants includes but not limited to, polymerizable or not polymerisable alkyl ethoxylated sulfate, alkylphenol ethoxylated sulfate, alkylethoxylate, alkylphenol ethoxylate or its mixture.
The latex polymer of diol latex compositions can adopt any technical known traditional method preparation.The monomer that can be used to prepare latex polymer can briefly be characterized by the ethylene linkage unsaturated monomer.They include but not limited to, non-sour vinyl monomer, acids vinyl monomer and/or its mixture.Latex polymer of the present invention can right and wrong multipolymer, its mixture or derivatives thereof of acid vinyl monomer and acid mono.Latex polymer of the present invention also can be the homopolymer of ethylene linkage unsaturated monomer.
The non-sour vinyl monomer that is suitable for preparing latex polymer includes but not limited to the methacrylic ester of acetoacetyl ethyl, the acrylate of acetoacetyl ethyl, methyl acrylate, methyl methacrylate, ethyl propenoate, Jia Jibingxisuanyizhi, butyl acrylate, butyl methacrylate, isobutyl acrylate, Propenoic acid, 2-methyl, isobutyl ester, the vinylformic acid (ethyl hexyl) ester, methacrylic acid 2-(ethyl hexyl) ester, 2-ethylhexyl acrylate, isoprene, Octyl acrylate, Octyl methacrylate, Isooctyl acrylate monomer, Isooctyl methacrylate, the triacrylate of TriMethylolPropane(TMP), vinylbenzene, alpha-methyl styrene, glycidyl methacrylate, the methacryloyl carbodiimide, C 1～C 18The crotonate of alkyl, n-butyl maleate, α-or β-vinyl naphthalene, dioctyl maleate, allyl methacrylate, toxilic acid diallyl ester, propanedioic acid diallyl ester, methacrylic acid methoxy base butenyl esters, isobornyl methacrylate, the hydroxyethyl methacrylate butenyl esters, (methyl) hydroxyethyl acrylate, (methyl) vinylformic acid hydroxypropyl ester, vinyl cyanide, vinylchlorid, vinylidene chloride, vinyl acetate between to for plastic, vinyl 1, the carbonic ether of 2-ethylidene, the epoxy butylene, 3,4-dihydroxyl butylene, (methyl) hydroxyethyl acrylate, Methacrylamide, acrylamide, the butyl acrylamide, ethyl acrylamide, divinyl, vinyl ester monomers, (methyl) vinylformic acid vinyl ester, the different propylene ester of (methyl) vinylformic acid, (methyl) vinylformic acid cyclic aliphatic epoxy ester, ethyl-formamide, 4-vinyl-1,3-dioxolane-2-ketone, 2,2-dimethyl-4-vinyl-1,3-dioxolane and 3,4-diacetoxyl-1-butylene or its mixture.Suitable monomers is described in " The BrandonAssociates " the 2nd edition, 1992 Merrimack, New Hampshire, and " polymkeric substance and monomer " 1996～1997 catalogues, Polyscience company, Warrington, Pennsylvania, the U.S..
The sour vinyl monomer that can be used for preparing latex polymer includes but not limited to vinylformic acid, methacrylic acid, methylene-succinic acid, Ba Dousuan and hexanodioic acid mono-vinyl ester.
The monomer that is preferred for preparing latex polymer/(being total to) polymkeric substance is the ethylene linkage unsaturated monomer, include but not limited to acrylate, methacrylic ester, vinyl ester, vinylbenzene, styrene derivatives, vinylchlorid, vinylidene chloride, vinyl cyanide, isoprene and divinyl.In a more preferred embodiment, latex polymer comprises following monomeric (being total to) polymkeric substance: 2-ethylhexyl acrylate, vinylbenzene, butyl acrylate, butyl methacrylate, ethyl propenoate, methyl methacrylate, divinyl and isoprene.
In preferred embodiments, the molecular weight of latex polymer is pressed the weight-average molecular weight (Mw) that gel permeation chromatography (GPC) is measured, and is 1,000～1,000,000, and more preferably this weight-average molecular weight is 5000～250, and 000.In one embodiment, the second-order transition temperature of latex polymer (Tg) equals about 170 ℃.
Diol latex compositions of the present invention can be characterized by the latex of stabilization in containing diol component external phase.Stable latex, its definition is with regard to purpose of the present invention, and particles contained is the stable latex of colloidal state, that is and, latex particle is through long-time, 24h for example, preferred 48h more preferably after 1 week, still keeps being dispersed in the external phase.
Latex polymer particles is generally sphere.Latex polymer can be core shell copolymer or non-core shell copolymer.Can prepare core/shell-type polymkeric substance by adding monomer stage by stage.For example, the composition of polymerization single polymerization monomer charging can change according to unexpected mode during entire reaction, thereby generates the polymer moieties of distinct core and shell.Core/core-shell polymeric particles also can be made into leafy shape, Pericarppium arachidis hypogaeae, balanate, Rubus idaeus shape.In this kind particle, core segment can account for about 20～about 80wt% of described particle gross weight, and the shell part can account for about 80～about 20wt% of particle gross weight.
In one embodiment, in letex polymerization, use chain-transfer agent.Typical chain-transfer agent be technical known those.The chain-transfer agent that can be used for preparing in the emulsion polymerization of diol latex compositions includes but not limited to, butyl sulfhydryl, dodecyl mercaptans, thiohydracrylic acid, 3-thiohydracrylic acid 2-(ethyl hexyl) ester, the positive butyl ester of 3-thiohydracrylic acid, spicy thioalcohol, isodecyl mercaptan, octadecanethiol, mercaptoacetate, thiohydracrylic acid allyl ester, Thiovanic acid allyl ester, thiohydracrylic acid crotons ester, Thiovanic acid crotons ester, and disclosure and description are at United States Patent (USP) 5,247, those reaction chain transfer agents in 040 are incorporated it into this paper as a reference at this.Preferably, chain-transfer agent is selected from mercaptan and various haloalkane, includes but not limited to tetracol phenixin; Preferred chain-transfer agent is a 3-thiohydracrylic acid 2-(ethyl hexyl) ester.The add-on of chain-transfer agent is 0～2 part per hundred parts monomers (phm), more preferably 0～0.5phm.
Latex polymer of the present invention can be uncrosslinked or crosslinked.When crosslinked, suitable crosslinking agent comprises multifunctional unsaturated compound, includes but not limited to Vinylstyrene, allyl methacrylate, vinylformic acid allyl ester, polyfunctional acrylic ester and composition thereof.Suitable polyfunctional acrylic ester includes but not limited to, the triacrylate of the dimethacrylate of ethylene glycol, the diacrylate of ethylene glycol, TriMethylolPropane(TMP), the trimethacrylate of TriMethylolPropane(TMP), the tetraacrylate of tetramethylolmethane, and composition thereof.The consumption of may command cross-linking monomer in letex polymerization is so that change the gel fraction of latex in 20～100% scope." gel fraction " is the quantity that is insoluble in the good solvent.
Latex particle can change into functional by being incorporated into the monomer that has side chain functionalities.The functional group that can be attached in the latex particle includes but not limited to, epoxide group, acetoacetyl group, carbonate group, oh group, amine groups, isocyanate groups, amide group and composition thereof.These functional groups can be derived by various different monomers, these monomers include but not limited to, the methacrylic ester of glycidyl methacrylate, acetoacetyl ethyl, vinyl ethylidene carbonic ether, methacrylic acid hydroxyethyl ester, methacrylic acid uncle fourth aminoethyl ester, methacryloyl dimethyl amine, pseudoallyl-α, α-Er Jiajibianji isocyanic ester, acrylamide and N hydroxymethyl acrylamide.The interpolation of functional group makes this polymkeric substance further to react after latex is synthetic.This functionality can be used for providing the crosslinked ability of potential or utilizes it and polycondensate reacts, as what will discuss among the following joint II.
Can use initiator so that generate diol latex compositions in letex polymerization, initiator includes but not limited to, soluble organo-peroxide of persulphate, water or glycol and azo-type initiator.Preferred initiator includes but not limited to, hydrogen peroxide, Potassium Persulfate or ammonium, dibenzoyl peroxide, lauroyl peroxide (lauryl), peroxide di-t-butyl, 2,2 '-Diisopropyl azodicarboxylate, tertbutyl peroxide, Benzoyl Peroxide and composition thereof.The iron catalysed reactions of redox initiation system such as tertbutyl peroxide and saccharosonic acid also is useful.Preferably, do not use the initiator that can produce strong acidic by-products.Can avoid contingent side reaction between the diol component of solvent and this acid like this.The add-on of initiator can be at 0.1～2phm, more preferably 0.3～0.8phm.
Reductive agent also can be used in this letex polymerization.Appropriate reductant is that those can quicken polyreaction, for example comprises V-Brite B, sodium bisulfite, sodium formaldehyde sulphoxylate, xitix, saccharosonic acid and composition thereof.If introduce reductive agent in letex polymerization, its preferred add-on is 0.1～2phm, more preferably 0.3～0.8phm.Preferably reductive agent was joined in the reactor in for some time.
Buffer reagent also can use in the letex polymerization that contains glycol, with the pH of control reaction.Suitable reducing includes but not limited to, carbonic acid-and bicarbonate of ammonia or sodium salt.Preferably under including but not limited to the situation of acidic initiator of persulphate, employing adds buffer reagent.
Polymerizing catalyst also can use in letex polymerization.Polymerizing catalyst is that those can quicken polyreaction and can cooperate the compound that the promotion polymerization starter decomposes with above-mentioned reductive agent under reaction conditions.Appropriate catalyst includes but not limited to, transistion metal compound, for example ferrous sulfate heptahydrate, iron protochloride, copper sulfate, cupric chloride, cobaltous acetate, rose vitriol and composition thereof.
The preparation of diol latex compositions comprises that at first preparation comprises the emulsion or the solution of monomer, initiator, tensio-active agent and external phase.In one embodiment, external phase comprises the diol component of 60～100wt%.Subsequently, heat this mixture, thereby make monomer polymerization and generate latex polymer.In typical case, monomer joins in for some time in the reactor and also independent initiator feed was joined in the reactor in for some time.
Diol latex compositions can comprise stablizer, but does not require and must have stablizer.The stablizer that is suitable for diol latex compositions comprises but is not limited to anionic stabilizer, nonionic suspension stabilizer, both sexes suspension stabilizer or its mixture.Suspension stabilizer must be able to be dissolved in the external phase but be insoluble to monomer basically.If present, the content of suspension stabilizer is 3～15wt% of monomer weight; Be preferably 7～8wt% of monomer weight.
Along with the concentration of glycol in external phase near 100%, diol latex compositions will improve gradually to the wettability of hydrophobic surface, and this moment diol latex compositions volatility diminish.The volatile reduction of diol latex compositions, as disclosed among the following joint II, especially favourable when diol latex compositions is used for condensation reaction.
The polymkeric substance of the present invention's preparation can be used for thermoplastic engineering resin, elastomerics, film, sheet material and container plastic.Diol latex compositions of the present invention can be used for various coating compositions, for example building coating, maintenance finish, industrial coating, car paint, weaving coating, printing ink, tackiness agent and be used for the coating of paper, timber and plastics.Therefore, the invention still further relates to this type of coating composition that contains diol latex compositions of the present invention.Diol latex compositions of the present invention can be mixed in these coating compositions according to the mode the same with known polymer latex, and the traditional composition and/or the additive of based composition is used therewith.These coating can be transparent or pigment colorings.
Once preparation, the coating composition that contains diol latex compositions of the present invention can be applied on various surface, base material or the goods subsequently, for example paper, plastics, steel, aluminium, timber, plasterboard or galvanized sheet (feel secure or do not feel secure).The type of surface to be coated, base material or goods has determined the coating composition type that should use usually.This coating composition can adopt technical known mode to apply.For example, coating composition can adopt spraying or adopt on the general coating process paint base material.Usually, coating can realize dry by heating, but preferably makes it air-dry.
This coating composition comprises diol latex compositions of the present invention, and also can comprise water, known additives or filler on solvent, pigment (organic or inorganic) and/or the other technologies.This class additive or filler include but not limited to, levelling, rheology and flow control agent, siloxanes for example, fluorocarbon, ammonia ester or Mierocrystalline cellulose, extender, active coalescing aid such as United States Patent (USP) 5,349, described in 026 those, matting agent, pigment wetting agent and dispersion agent, and even tensio-active agent, uv-absorbing agent, ultra-violet stabilizer, tinting pigment, extender, defoamer and suds suppressor, antisettling agent, sag prevention and thickening material, anti, anti-loose colour and the anti-agent of growing dim, sterilant and mould inhibitor, inhibiter, thickening material, softening agent, reactive plasticizer, solidifying agent or coalescing agent.The object lesson of examples of such additives can be seen in " raw material index ", and whole nation paint and coating association publish, 1500 Rhode Island Avenue, and NW, the Washington D.C., DC 20005, the U.S..
Diol latex compositions of the present invention can use separately, perhaps is used with other traditional polymers.This base polymer includes but not limited to that polyester is as with the terephthalate being polymer based, polyesteramide, cellulose ester, Synolac, urethane, polycarbonate, Resins, epoxy, polymeric amide, acrylic acid or the like, vinyl polymer, styrene butadiene polymkeric substance, vinyl acetate-ethylene copolymer and composition thereof.
Diol latex compositions of the present invention also can be used as the reactant in the polycondensation.As the reactant in the polycondensation, diol latex compositions of the present invention can be used to, by this latex glycol and diacid, vulcabond and dialkyl group-, diaryl-or dihalo--carbonic ether react, the thermoplastic condensed polymer is implemented modification.Among the joint II,, this kind application of this diol latex compositions as the reactant in the polycondensation described below as one of embodiment.In addition, the present invention also can be used as a kind of feeding method easily, and latex polymer is joined among the thermoplastic condensed polymer.II. modified condensation polymer matrix
The present invention the 2nd main aspect relates to a kind of polymeric colloid system is incorporated in the reaction of preparation polycondensate, comprises the product that is trapped within the polymer beads in the polycondensate matrix thereby generate.The polymeric colloid system in this polyreaction of being incorporated into is defined as being dispersed in the polymer beads in the external phase in this article, and this particulate granularity is preferably in the scope of 0.020 μ m～1000 μ m.External phase can comprise the composition of a small amount of unreacted monomer, tensio-active agent and so on.Be suitable for the polymer beads in this kind polymeric colloid system, be called as the 1st polymkeric substance in this article, comprise by relating to the same polymer that the described identical ethylene linkage unsaturated monomer of diol latex compositions constitutes among the above-mentioned joint I, and can be according to carrying out functionalized or crosslinked with the disclosed same way as of latex polymer that is used to save I.If implement functionalizedly, preferably, functional group comprises the group that can react with diacid, vulcabond, diaryl carbonate, dialkyl carbonate, dihalo-carbonic ether or diol component.These functional groups include but not limited to epoxy, acid, hydroxyl, isocyanic ester, amine, acid amides and carbonate group or its mixture.In addition, the 1st polymkeric substance can be core-shell or non-core-shell polymer.
This polymeric colloid system can adopt various method preparations, includes but not limited to emulsion, suspension or dispersion polymerization and machinery emulsification.Usually, dispersion and suspension polymerization generate bigger granularity, typically at 1～500 mu m range; Letex polymerization then generates the particle than small grain size, typically at 10～1000nm.
In preferred embodiments, the 1st polymkeric substance is non-core-shell polymer, and the 1st polymkeric substance of this polymeric colloid system comprises 50～100%, preferred 70～100%, the more preferably residue of one of 80～100% following monomers: 2-ethylhexyl acrylate, butyl acrylate, isoprene, vinylbenzene, divinyl or vinyl cyanide.
Emulsion, suspension, dispersion and machinery emulsification polymerization are the known technologies of preparation polymeric colloid system.If select dispersion polymerization to prepare to be incorporated into the polymeric colloid system in the polycondensation for use, then can adopt to be similar to United States Patent (USP) 4,885 350 and United States Patent (USP) 5, those methods described in 061,766 are come the polymeric colloid system of prepared sizes at 1 μ m～100 mu m ranges.If the employing machinery emulsification then can adopt to be similar to United States Patent (USP) 4,177,177, United States Patent (USP) 5,358,981 and United States Patent (USP) 5,612, those methods described in 407.
No matter be incorporated into the precursor that goes in the condensation reaction and emulsion, suspension, dispersion or the machinery emulsification polymeric polymeric colloid system for preparing as preparing, solvent or external phase all can be based on water or glycol.Yet preferably, external phase is based on glycol, and like this, the glycol in the external phase of polymeric colloid system just can participate in the polycondensation.In particularly preferred embodiments, the polymeric colloid system is the diol latex compositions that saves in the above described in the I.And, the external phase of each polymeric colloid system all can be substantially by or constitute by water or glycol; Perhaps comprise these two of arbitrary proportion.
In the polymeric colloid system that comprises based on the external phase of glycol, the glycol in the external phase can with the diacid that constitutes the reaction medium that forms polycondensate, vulcabond, dialkyl group-or diaryl-or dihalo--carbonic ether or its mixture " coreaction " takes place.In this embodiment, diol component preferably accounts for 25～100wt% of external phase; Preferably account for 50～100wt% of external phase; More preferably account for 70～100wt% of external phase; Further preferably account for 90～100wt% of external phase.In preferred embodiments, external phase is made of diol component substantially.Be suitable for the diol component based on the external phase of ethylene glycol of polymeric colloid system, include but not limited to save the diol component described in the I.
Diol component can be present in the external phase, in the condensation reaction medium or in the two.Be present in the adjusting of the diol concentration in the original reaction medium, should consider in the lump together with the diol concentration in the polymeric colloid system.The polymeric colloid system can be incorporated in the polycondensation in the various different stepss of polyreaction.For example at poly-(ethylene glycol terephthalate) (PET) in the polymerization, join dimethyl terephthalate (DMT) (DMT), ethylene glycol (EG) and catalyst metal in the flask and carry out polymerization.The joining day of latex can be 1) " in advance ", promptly, add together in company with other materials at the very start, 2) after the fusion of other raw materials and forming homogeneous phase solution, 3) after the reaction in the 1st stage has taken place and has emitted methyl alcohol in DMT and EG, 4) in the time will turning off nitrogen and apply vacuum at once, 5) sometimes in final " polycondensation phase " or any moment between two parties, promptly during the transesterify.Final blend is subjected to latex to add the influence of the time in the polycondensate.Though do not wish to be limited to any mechanism, the author thinks that the granularity of the emulsion polymer in the polycondensate matrix and shape can be subjected to the influence of this joining day.Equally, particular chemical between emulsion polymer and the polycondensate interacts and also is subjected to the influence of joining day, and they thereby also have influence on final blend character.
The inventive method does not require the polymkeric substance of isolating in the polymeric colloid system.Therefore, the present invention has avoided the needs of preparation core-shell polymer or isolated the needs of polymkeric substance from emulsion.Have again, in view of during blend occurs in polycondensate preparation, so do not need the such energy-intensive of blend behind the polymer/polymer, expensive and usually cause the step of molecular weight of polycondensates reduction.
In preferred embodiments, introduced the reaction medium generation polyester of polymeric colloid system of the present invention.Term " polyester " in this article refers to the polyester unit type in any polyester portion scope that belongs to this blend, includes but not limited to homopolymerization polyester and copolyester (residue of two or more monomeric unit acid and/or glycol).Polyester of the present invention comprises sour residue and diol residue.The sour residue of polyester of the present invention is total up to 100mol%, and the diol residue of polyester of the present invention is total up to 100mol%.Know that the use of derivative, particularly acid anhydrides, ester and acyl chlorides that these acid are corresponding is encompassed in the term " sour residue " that the application mentions without exception in the whole text.Except sour residue and diol residue, this polyester also can comprise other modification residues.These modification residues include but not limited to diamines, at this moment will generate polyester/acid amides.
This polyester preferably comprises the residue of dicarboxylic acid or ester, includes but not limited to that aromatic dicarboxylic acid or ester residue preferably have 8～14 carbon atoms; Aliphatic dicarboxylic acid or ester residue preferably have 4～12 carbon atoms; Perhaps cycloaliphatic dicarboxylic acid or ester residue preferably have 8～12 carbon atoms.The acid of the acid moieties of formation polyester or the residue that the ester residue comprises following material: phthalic acid; Terephthalic acid; Naphthalene dicarboxylic acids; M-phthalic acid; Cyclohexanediacetic; Phenylbenzene-4,4 '-dicarboxylic acid; Succsinic acid; Pentanedioic acid; Hexanodioic acid; Fumaric acid; Nonane diacid; Resorcinol diacetic (resorcinoldicetic acid); Didiolic acid (dihydroxylated acid); 4,4 '-oxygen connection two (phenylformic acid); Diphenyldicarboxylic acid; 1, the 12-dodecanedicarboxylic acid; 4,4 '-sulfonyldibenzoic acid; 4,4 '-methyldiphenyl formic acid; Anti-4,4 '-the stilbene dicarboxylic acid; 1,2-, 1,3-and 1,4-cyclohexane dicarboxylic acid; And composition thereof.This polyester can be by a kind in the above-mentioned dicarboxylic acid or multiple preparation.
The example that is used to prepare the preferred dicarboxylic or derivatives thereof of this polyester is terephthalic acid or its ester and 2,6-naphthalene dicarboxylic acids or its ester, succsinic acid, m-phthalic acid, pentanedioic acid, hexanodioic acid or their ester.Other naphthalene dicarboxylic acids or its ester also can use.This comprises 1,2-, 1,3-, 1,4-, 1,5-, 1,6-, 1,7-, 1,8-, 2,3-, 2,4-, 2,5-, 2,6-, 2,7-and 2,8-naphthalene dicarboxylic acids and composition thereof.More preferably with 2, the 6-naphthalene dicarboxylic acids is as modification acid.
The diol component of polyester comprises preferred residue from following glycol: cycloaliphatic diol preferably has 6～20 carbon atoms; Or aliphatic diol, preferably have 2～20 carbon atoms.The example of this type of glycol comprises ethylene glycol, glycol ether, triglycol, neopentyl glycol, 1, the 4-butyleneglycol, 1, the 6-hexylene glycol, 1, the 4-cyclohexanedimethanol, 1, ammediol, decamethylene-glycol, 2,2,4,4-tetramethyl--1, the 3-cyclobutanediol, 3-methyl-2, the 4-pentanediol, the 2-methyl isophthalic acid, the 4-pentanediol, 2,2,4-trimethylammonium-1, the 3-pentanediol, 2-ethyl-1-1, the 3-hexylene glycol, 2,2-diethyl-1, ammediol, 1, the 3-hexylene glycol, 1, two (hydroxy ethoxy) benzene of 4-, 2, two (4-hydroxy-cyclohexyl) propane of 2-, 2,4-dihydroxyl-1,1,3,3-tetramethyl-ring butane, 2, two (the 3-hydroxy ethoxy phenyl) propane of 2-, 2, two (4-propoxyl phenyl) propane of 2-and composition thereof.Diol component more preferably is selected from ethylene glycol, 1,4-butyleneglycol, neopentyl glycol, cyclohexanedimethanol, glycol ether and composition thereof.These glycol can be used the highest about 50mol%, and more preferably the highest about 20mol% any other glycol disclosed herein carries out modification.
Preferably, polyester of the present invention is line style substantially.This polyester can adopt a small amount of a kind or multiple branching agent to carry out modification.Branching agent is defined as the molecule that has at least 3 can participate in the functional group of polyester formation reaction in this article, for example hydroxyl, carboxylic acid, carboxylicesters, based on the ester (potential trifunctional) and the acid anhydrides (two senses) of phosphorus.
The branching agent that can be used for polyester manufacture of the present invention includes but not limited to, glycerine, tetramethylolmethane, trimellitic acid 1,2-anhydride, 1,2,4,5-pyromellitic acid dianhydride, tartrate and composition thereof.If use branching agent in condensation reaction, the preferred amount ranges of branching agent is a benchmark in the polyester gross weight, is 0.1～2.0wt%, more preferably from about 0.2～1.0wt%.
The adding of a small amount of branching agent can significantly not damage the physicals of polyester, yet but can provide additional melt strength, and this extrudes operation for film is very useful.In copolyester, add the multipolymer physical deterioration that too much branching agent will make generation, for example reduce its elongation.
Can add and comprise a kind or the multiple chemical agent that contains ion monomer, to improve the melt viscosity of polyester.Can be used for the ion monomer that contains of the present invention and include but not limited to, the alkaline earth salt or derivatives thereof of sulphur m-phthalic acid (sulfisophthalic acid).The preferred weight percentage ratio that contains ion monomer is about 0.3～5.0mol%, preferred about 0.3～3.0mol%.Contain that ion monomer also can improve the melt viscosity of polyester but the elongation that significantly do not reduce film.
Homopolymerization of the present invention-or copolyester preferably prepare the about 150 ℃～about 300 ℃ reaction of temperature in the presence of polycondensation catalyst by glycol and diacid (or diester or acid anhydride), catalyzer comprises but is not limited to, titanium tetrachloride, titanium tetraisopropylate, oxalic acid manganese, weisspiessglanz, nitrilotriacetic antimony, dibutyltin diacetate, zinc chloride or its mixture.The typical amounts of catalyzer is between 10～1000ppm of reactant gross weight.The terminal stage of reaction usually high vacuum (＜10mmHg) carry out under the condition, so that generate high molecular weight polyesters.
The invention still further relates to, as described herein, the high molecular homopolymerization of the method preparation by comprising the following steps or the modification of copolyester.
(I) glycol described herein is mixed with catalyst system with diacid,
(II) in the 1st stage, at 190 ℃～220 ℃, or a little more than under the atmospheric pressure heating described reaction mixture, and
(III) in the 2nd stage, add additive, reacting by heating mixture under 220 ℃～290 ℃ temperature, the decompression of 0.05～2.00mmHg based on phosphorus.
These polyester preferably adopt one of above-mentioned catalyst system to prepare in the presence of based on the additive of phosphorus.The preferred concentration of reacting middle catalyst is about 5～about 220ppm, and most preferred concentration is about 20～about 200ppm.This reaction divides 2 stages to implement preferably by described above.
In another embodiment of the present invention, polycarbonate can be by being incorporated into the polymeric colloid system in the reaction medium to realize modification.The polycarbonate of correctability includes but not limited to, the homopolymer by the prepared in reaction between dihydric phenol and the carbonate precursor, multipolymer and composition thereof.The dihydric phenol that can be used for producing carbonic ether includes but not limited to dihydroxyphenyl propane, (2, two (4-hydroxy phenyl) propane of 2-), two (4-hydroxy phenyl) methane, 2, two (the 4-hydroxy-3-methyl phenyl) propane, 4 of 2-, two (4-hydroxyphenyl) heptane, 2 of 4-, 2-(3,5,3 ', 5 '-tetrachloro-4,4 '-the dihydroxyl phenylbenzene) propane, 2,2-(3,5,3 ', 5 '-tetrabromo-4,4 '-the dihydroxyl phenylbenzene) propane, (3,3 '-two chloro-4,4 '-the dihydroxyl phenylbenzene) methane, and composition thereof.The branching agent that can be used for preparing polycarbonate of the present invention includes but not limited to, glycerine, tetramethylolmethane, trimellitic acid 1,2-anhydride, 1,2,4, and 5-pyromellitic acid dianhydride, tartrate, and composition thereof.If use branching agent in condensation reaction, the preferred amount ranges of branching agent is a benchmark in the polyester gross weight, is 0.1～2.0wt%, more preferably from about 0.2～1.0wt%.
In another embodiment of the present invention,, can comprise urethane by introducing the thermoplastic condensed polymer that the polymeric colloid system is carried out modification.The urethane of correctability comprises the residue of a kind or multiple diol residue and one or more vulcabond (di-isocyanante or di-isocyanates).The diol residue of urethane is to come by including but not limited to following glycol to derive: 1, the 3-cyclobutanediol, 1,3-encircles pentanediol, 1, the 2-cyclohexanediol, 1, the 3-cyclohexanediol, 1, the 4-cyclohexanediol, 2-hexanaphthene-1, the 4-glycol, the 2-methyl isophthalic acid, the 4-cyclohexanediol, 2-ethyl-1, the 4-cyclohexanediol, 1,3-encircles heptanediol, 1,4-encircles heptanediol, the 2-methyl isophthalic acid, 4-encircles heptanediol, the 4-methyl isophthalic acid, 3-encircles heptanediol, 1,3-encircles ethohexadiol, 1,4-encircles ethohexadiol, 1,5-encircles ethohexadiol, the 5-methyl isophthalic acid, 4-encircles ethohexadiol, 5-ethyl-1,4-encircles ethohexadiol, 5-propyl group-1,4-encircles ethohexadiol, 5-butyl-1,4-encircles ethohexadiol, 5-hexyl-1,4-encircles ethohexadiol, 5-heptyl-1,4-encircles ethohexadiol, 5-octyl group-1,4-encircles ethohexadiol, 4,4 '-methylene-bis (hexalin), 4,4 '-methylene-bis (2 methyl cyclohexanol), 3,3 '-methylene-bis (hexalin), 4,4 '-ethylenebis (hexalin), 4,4 '-propylidene two (hexalin), 4,4 '-butylidene two (hexalin), 4,4 '-isopropylidene two (hexalin), 4,4 '-isobutylene two (hexalin), 4,4 '-the dihydroxyl dicyclohexyl, 4,4 '-carbonyl two (hexalin), 3,3 '-carbonyl two (hexalin), 4,4 '-sulphonyl two (hexalin), 4,4 '-oxygen connection two (hexalin), and composition thereof.
Urethane of the present invention can adopt any currently known methods solvent exist or not in the presence of with polyisocyanates, chain extension agent and randomly high molecular weight polyols lump together and prepare.This comprises manually or the mechanically mixing measure, comprises that curtain coating, reaction are extruded, the reaction injection molding(RIM) and related methods.Can be used for typical preparation method of the present invention and be disclosed in United States Patent (USP) 4,376, in 834 and 4,567,236, incorporate this paper into as a reference at this, its disclosure relates to various compositions and the preparation procedure that generates urethane plastic.
The mixing of reactant can be in room temperature, and promptly 20 ℃～25 ℃ temperature is implemented.The mixture that obtains preferably is heated to 40 ℃～130 ℃ temperature, more preferably 50 ℃～100 ℃; Preferably, a kind in the reactant or the multiple said temperature scope that before blending, is heated to earlier.
Catalyzer can randomly be included in the reaction mixture that is used for preparing urethane.Anyly technically be used for traditionally that catalyst for reaction all can be used for this purpose between catalysis isocyanic ester and the active hydrogen-contg compound.Appropriate catalyst is disclosed in United States Patent (USP) 4,202,957, and hurdle 5 in the row 45～67, is incorporated this paper into as a reference at this.Catalyst consumption is preferably about 0.02～2.0wt% of reactant gross weight.In the particular of single stage method, reaction is adopted by continuous mode and for example is disclosed in United States Patent (USP) 3,642, and equipment and program in 964 are carried out.
But urethane of the present invention had both comprised the thermoplasticity injection moulding, also comprised heat cured resin.It is dual functional polyisocyanates and dual functional chain extension agent that the preparation of thermoplastic resin is adopted substantially, and functionality preferably is no more than 4 polyvalent alcohol, although can use the more polyvalent alcohol of high functionality when the part by weight of use is positioned at the scope of hanging down.Those skilled in the art will recognize that this scope will change to some extent along with the consumption of the molecular weight of the character of polyvalent alcohol, polyvalent alcohol and polyvalent alcohol.Usually, the polyvalent alcohol molecular weight is high more, and the functionality that permission is used under the thermoplastic prerequisite of polyurethane product is high more not losing.
This vulcabond residue can be by including but not limited to come from following vulcabond deutero-group: methylene-bis (phenyl isocyanate), comprise 4,4 '-isomer, 2,4 '-isomer and composition thereof, between-and right-phenylene vulcabond, the chlorine phenylene vulcabond, α, the alpha, alpha-dimethyl phenylene diisocyanate, 2,4-and 2,6-tolylene diisocyanate and back 2 kinds of mixture of isomers, the tolidine vulcabond, hexamethylene diisocyanate, 1, the 5-naphthalene diisocyanate, isophorone diisocyanate and suchlike, cycloaliphatic diisocyanates, as methylene-bis (cyclohexyl isocyanate), comprise 4,4 '-isomer, 2,4 '-isomer and composition thereof and their whole geometrical isomers, comprise instead/instead, suitable/anti-, suitable/along and composition thereof, the cyclohexylidene vulcabond (1,2-, 1,3-or 1,4-), 1-methyl-2,5-cyclohexylidene vulcabond, 1-methyl-2,4-cyclohexylidene vulcabond, 1-methyl-2, the 6-cyclohexyl diisocyanate, 4,4 '-isopropylidene two (cyclohexyl isocyanate), 4,4 '-two isocyanato-dicyclohexyls and whole geometrical isomer and mixture.The various modified form that also comprise methylene-bis (phenyl isocyanate).The latter is meant that thereby those are through handling various methylene-biss (phenyl isocyanate) modified form that makes it at room temperature to remain stabilising liq.This type of product comprises those that process and a small amount of (the highest about 0.2 equivalent is whenever the amount polyisocyanates) aliphatic diol or aliphatic diol mixture react, for example is described in United States Patent (USP) 3,394,164,3,644,457,3,883,571,4,031,026,4,115,429,4,118, modification methylene-bis (phenyl isocyanate) in 411 and 4,299,347.
Modification methylene-bis (phenyl isocyanate) also comprises following those: thus be converted into corresponding carbonization imines through this vulcabond of handling a small amount of ratio, thereby the latter interacts with other vulcabond more subsequently and generates inflation-imine group and make product become at room temperature stable liquid, for example be described in United States Patent (USP) 3, in 384,653.The mixture of any above-mentioned polyisocyanates, hope also can be used.Have again, under the situation of the heat cured urethane of the present invention of preparation, introduce a small amount of (the highest 30wt%) poly methylene poly phenyl poly isocyanate in the polyisocyanate component that can in reaction, use.The latter is the mixture that comprises about 20～90wt% methylene-bis (phenyl isocyanate), and the rest part of mixture then is a functionality greater than 2.0 poly methylene poly phenyl poly isocyanate.This type of polyisocyanates and preparation method thereof is known technically; For example referring to United States Patent (USP) 2,683,730,2,950,263,3,012,008 and 3,097,191.The branching agent that can be used for preparing urethane of the present invention includes but not limited to glycerine, tetramethylolmethane, trimellitic acid 1,2-anhydride, 1,2,4,5-pyromellitic acid dianhydride, tartrate and composition thereof.If use branching agent in condensation reaction, the amount ranges of preferred branched agent is at 0.1～2.0wt% of polyester gross weight, more preferably from about 0.2～1.0wt%.
Other compositions also can randomly join in the present composition to improve the performance of this polycondensate/latex polymer matrix.For example, surface lubricant, anti-intussusception agent, stablizer, oxidation inhibitor, UV light absorber, releasing agent, metal passivator, tinting material such as black iron oxide and carbon black, nucleator, phosphoric acid ester stablizer, zeolite, filler and composition thereof and so on all can be included in wherein.All these additives and being applied in are technically known.Any of these compound only otherwise infringement the present invention reaches its purpose all can be used.
End-use by the condensation polymer composition of the present invention preparation comprises impact-modified polymkeric substance, elastomerics, the polymkeric substance that polymkeric substance that high-isolation film and coating, barrier improve and mechanical property are improved is as the improvement of tensile strength, the improvement of extension at break, the improvement of Weather-resistant and the improvement of flexural strength.Other end-uses comprise that engineering resin, coating, obstruct are with container and moulded plastic.In addition, powder coating also can be prepared by the modified condensation polymer of producing by the present invention.The polymkeric substance of producing by the present invention can be used for thermoplastic engineering resin, elastomerics, film, sheet material and container plastic.
In preferred embodiments, prepared impact-modified polyester, it comprises non-core-shell the 1st polymkeric substance that is obtained by the polymeric colloid system.In another preferred embodiment, prepared the functionalized polyester coating of hydroxyl, it comprises non-core-shell the 1st polymkeric substance that is obtained by the polymeric colloid system.
In one embodiment of the present invention, modified condensation polymer includes but not limited to impact-modified plastics, and it is to be prepared by polymeric colloid system that comprises non-core-shell polymer the 1st polymkeric substance and polycondensate.Polymeric colloid in this embodiment has the Tg less than 40 ℃, and polycondensate has the Tg greater than 40 ℃.Preferably by such polymeric colloid system preparation, the 1st polymkeric substance that it comprises comprises the residue of following compounds to these impact-modified plastics: 2-ethylhexyl acrylate, butyl acrylate, isoprene, divinyl, lauryl acrylate, vinyl cyanide, vinylidene chloride or its mixture.
In another embodiment of the present invention, modified condensation polymer includes but not limited to thermoplastic elastomer, by the polymeric colloid system preparation that comprises non-core-shell polymer the 1st polymkeric substance.Polymeric colloid in this embodiment has the Tg greater than 40 ℃; And polycondensate has the Tg less than 40 ℃, and is preferably amorphous substantially.Preferably by such polymeric colloid system preparation, the 1st polymkeric substance that it comprises comprises the residue of following compounds to this thermoplastic elastomer: vinylchlorid, vinylbenzene, alpha-methyl styrene, methyl methacrylate, vinyl naphthalene, isobornyl methacrylate or its mixture.
Elastomerics is obtaining increasingly extensive application, particularly following thermoplastic elastomer (TPE class), and it is an elastomerics under use temperature, processes (for example, injection moulding, extrusion molding) but can be used as plastics under suitable temperature.Elastomerics can prepare by the inventive method.For example, polycondensate amorphous and low Tg can be the heavy-gravity fluid, can not be used as plastics or elastomerics.Should but can be used to make elastomerics by low Tg sticky polymers, its method comprises, adds a kind of the 2nd polymkeric substance of polymeric colloid system form, and it plays a part the physical crosslinking agent and as the binding site of sticky polymers chain.So will generate a kind of blend polymer that is separated with elastomer performance.
Embodiment
Below given embodiment be intended to for those skilled in the art provide full disclosure and the explanation that how to prepare and assess desired composition of matter of the application and method, do not intend limiting its invention scope that the inventor assert.Made every effort to accurately about various numerals (as quantity, temperature etc.), but some mistake and deviation are still unavoidable.Unless point out separately, umber by weight, temperature to be ℃ being unit, otherwise in room temperature; Pressure then is in or near normal atmosphere.
Material that the result adopted and test procedure that this paper provides are as follows:
Limiting viscosity (Ih.V.) is to adopt the measured in solution of 0.50g sample in 100mL 60/40 (weight) phenol/tetrachloroethane at 25 ℃.
Molecular weight distribution adopts gel permeation chromatography (GPC) to measure.Solution is by the 4mg polymer dissolution is made in containing 10 volume % toluene, 30/70 (weight) hexafluoroisopropanol/methylene dichloride as the flow rate mark.System adopts a series of narrow molecular weight distributions polystyrene standards to demarcate.Molecular weight provides with absolute molecular weight numerical value, and it is to utilize the Mark-Houwink constant of one group of PET p-poly-phenyl ethene association to determine.
Heat deflection adopts dsc (DSC) to measure on Du Pont's instrument 2200 DSC.Crystallinity percentage also is to adopt DSC to measure.DSC adopts the scanning speed of 20 ℃/min, is heated to above its melt temperature and is quenched to rapidly that it carries out after below second-order transition temperature at sample.
Film is prepared through compression moulding by the exsiccant polymkeric substance.Drying (20mmHg) in 120 ℃ of vacuum drying ovens is spent the night and is finished.The compression moulding process of dry polymer is as follows: on the press of Pasadena hydraulic pressure company, be compression molded into the film of 6 inches X6 inches under between 2 metal sheets that have 15 mil bed courses and Tm+30～50 ℃.Pressurization rises to resulting pressure 15,000 plunger force pounds and keeps 1min in 2min gradually.After the compression moulding, film is immersed in quenching in the ice bath rapidly.The film impact test of adopting instrument to carry out " is adopted load and displacement sensor mensuration plastics high speed puncture resistance " according to ASTM method D3763 and is carried out.Test is carried out on 23 ℃, CeastFractovic trier.The film thickness scope is at 0.33～0.38mm.Film is placed on the hole of internal diameter 76mm, and simultaneously, film is subjected to 0.5 inch of diameter, with the impact of the weight of the speed of 11.1ft/s motion.If film is broken or break and be fragment, then it is decided to be brittle rupture; And if in film, produce a hole, then be recorded as ductile failure.
Transmission electron microscope art (TEM).Operating in preparation section thin section on-105 ℃ the Cryo-Ultramicrotome.Thin section is placed in the Philips CM12 TEM that operates in 80kV and observes down.The contrast sample for neutral, do not apply strained.
Optical microscopy.At-60 ℃ of preparation section thin sections, and adopt the Zeiss observation by light microscope.Example 1
Add 300g ethylene glycol and 2.33g Hitenol A-10 in the 1L jacket reactor that has condenser, nitrogen purging and agitator, this is a kind of polymerizable, polyoxyethylene alkyl phenyl ether ammonium sulfate, and DKS international corporation makes.Material is heated to 80 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of the triacrylate and the 3.60g Hitenol A-10 of 118.75g 2-ethylhexyl acrylate, 6.25g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 12.85g.Allow the material of reactor again after the balance, in reactor, add the solution of 3.0g Sodium Persulfate in 15g water.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 39min, remaining monomer mixture is fed in the reactor.When adding reactor, in reactor, add the solution of 1.50g Sodium Persulfate in 50g water with monomer.After all monomer finishes, be reflected at 80 ℃ and keep 1h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.After the drying, on screen cloth, collect the 0.815g disintegrating slag.Adopt the CEM microwave dryer to measure the solids content of latex, the result is for containing 28.1% solid.Effective diameter with dynamic light scattering determination is 181nm.Example 2
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 300g ethylene glycol and 2.3g Hitenol A-10.Material is heated to 70 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of the triacrylate and the 3.60g Hitenol A-10 of 118.75g 2-ethylhexyl acrylate, 6.25g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 12.85g.Allow the material of reactor again after the balance, in reactor, add the suspensoid of 3.0g azo diisoamyl acid in 15g ethylene glycol.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 58min, remaining monomer mixture is fed in the reactor.After all monomer finishes, be reflected at 70 ℃ and keep 1.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.After the drying, on screen cloth, collect the 0.741g disintegrating slag.Adopt the CEM microwave dryer to measure the solids content of latex, the result is for containing 27.6% solid.Effective diameter with dynamic light scattering determination is 122nm.Example 3
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 272g ethylene glycol, 0.839g sodium formaldehyde sulphoxylate and 5.04g Hitenol A-10.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of triacrylate, 35.66g ethylene glycol and the 2.88g Hitenol A-10 of 132.81g 2-ethylhexyl acrylate, 6.99g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 17.8g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.777g 90wt% tertbutyl peroxide in 15g ethylene glycol.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 58min, remaining monomer mixture is fed in the reactor.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.After the drying, on screen cloth, collect the 0.837g disintegrating slag.Adopt the CEM microwave dryer to measure the solids content of latex, the result is for containing 25.2% solid.Effective diameter with dynamic light scattering determination is 126nm.Example 4
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add, 379.25g ethylene glycol and 24.65g Disponil FES 77, this is a kind of alkyl ethoxylated sodium sulfate, (the 30% active aqueous solution) is made by Henkel Corp..Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 191.55g 2-ethylhexyl acrylate, 22.54g vinylbenzene, 11.27g allyl methacrylate, 47.89g ethylene glycol and 14.09g DisponilFES77.In the reactor of heating, add this monomer/surfactant mixture of 28.7g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.751g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.255g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.901g SFS in 28g distilled water.In reactor, add the solution of 0.501g 90wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.5% solid, is 184nm with the granularity of dynamic light scattering determination.Example 5
Add in the 1L jacket reactor that has condenser, nitrogen purging and agitator, the polymerisable polyoxyethylene alkyl phenyl ether ammonium sulfate of 396.01g ethylene glycol and 7/89g Hitenol HS-20 is made by DKS international corporation.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 112.68g 2-ethylhexyl acrylate, 112.68g vinyl acetate between to for plastic, 57.46g ethylene glycol and 4.51g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.7g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.751g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.255g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.901g SFS in 28g distilled water.In reactor, add the solution of 0.501g 90wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 23.18% solid, is 114nm with the granularity of dynamic light scattering determination.Example 6
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 396.01g ethylene glycol and 7.89g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 169.01g n-butyl acrylate, 4.507g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.7g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.751g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.255g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.901g SFS in 28g distilled water.In reactor, add the solution of 0.501g 90wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.5% solid, is 102nm with the granularity of dynamic light scattering determination.Example 7
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 396.01g ethylene glycol and 7.89g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 169.01g 2-ethylhexyl acrylate, 45.07g methyl methacrylate, 11.27g allyl methacrylate, 57.46g ethylene glycol and 4.51gHitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.7g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.71g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.255g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.901g SFS in 28g distilled water.In reactor, add the solution of 0.501g 90wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.0% solid, is 140nm with the granularity of dynamic light scattering determination.Example 8
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 267.5g ethylene glycol and 1.74g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 295.65g 2-ethylhexyl acrylate, 34.78g vinylbenzene, 17.39g allyl methacrylate, 88.70g ethylene glycol and 6.96g HitenolHS-20.In the reactor of heating, add this monomer/surfactant mixture of 44.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 1.16g 90wt% tertbutyl peroxide (t-BHP) in 9g ethylene glycol, add the solution of 0.348g sodium formaldehyde sulphoxylate (SFS) in 9g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 220min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 1.391g SFS in 22g distilled water.In reactor, add the solution of 0.773g 90wt% tertbutyl peroxide in 44g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The emulsion that obtains contains 41.78% solid, is 337nm with the granularity of dynamic light scattering determination.Example 9
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 267.5g ethylene glycol and 7.85g Hitenol HS-20, the 0.0898g 1wt% ferric ammonium sulfate aqueous solution and 0.449g 1% edta solution.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 190.82g 2-ethylhexyl acrylate, 22.45g vinylbenzene, 11.2g allyl methacrylate, 57.25g ethylene glycol and 4.49g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.8g.Allow the material of reactor again after the balance, in reactor, add the solution of 1.25g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.449gd-saccharosonic acid in 11g ethylene glycol subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 1.247g d-saccharosonic acid in 22g ethylene glycol.In reactor, add the solution of 0.773g 90wt% tertbutyl peroxide in 44g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The emulsion that obtains contains 27% solid, is 127nm with the granularity of dynamic light scattering determination.Example 10
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 424.7g 75wt% aqueous solution of propylene glycol and 7.78g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 188.9g 2-ethylhexyl acrylate, 22.22g vinylbenzene, 11.11g allyl methacrylate, 56.67g 75wt% aqueous solution of propylene glycol and 4.44g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 1.73g 90wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.95g SFS in 22g distilled water.In reactor, add the solution of 0.741g 90wt% tertbutyl peroxide in 44g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.1% solid, is 196nm with the granularity of dynamic light scattering determination.Example 11
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 50: 50 (weight ratio) propylene glycol of 424.7g: ethylene glycol mixture and 7.78g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, prepare by 188.9g 2-ethylhexyl acrylate, 22.22g vinylbenzene, 11.11g allyl methacrylate, 50: 50 (weight ratio) propylene glycol of 56.67g: monomer/surfactant mixture that ethylene glycol mixture and 4.44g Hitenol HS-20 form.In the reactor of heating, add this monomer/surfactant mixture of 28.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 1.73g tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.95g SFS in 22g distilled water.In reactor, add the solution of 0.741g 90wt% tertbutyl peroxide in 44g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.6% solid, is 332nm with the granularity of dynamic light scattering determination.Example 12
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add the 394.05g 75wt% glycol ether aqueous solution and 1.15g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 195.22g 2-ethylhexyl acrylate, 22.97g vinylbenzene, 11.48g allyl methacrylate, the 58.56g 75wt% glycol ether aqueous solution and 4.59g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.984g 90wt% tertbutyl peroxide (t-BHP) in the 11g 75wt% glycol ether aqueous solution, add the solution of 0.689g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 1.605g SFS in 28g distilled water.In reactor, add the solution of 2.297g 90wt% tertbutyl peroxide in the 56g 75wt% glycol ether aqueous solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 25.6% solid, is 302nm with the granularity of dynamic light scattering determination.Example 13
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 50: 50 weight ratio glycol ethers of 394.05g: ethylene glycol mixture and 1.15g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, prepare by 195.22g 2-ethylhexyl acrylate, 22.97g vinylbenzene, 11.48g allyl methacrylate, 50: 50 weight ratio glycol ethers of 58.56g: monomer/surfactant mixture that ethylene glycol mixture and 4.59g Hitenol HS-20 form.In the reactor of heating, add this monomer/surfactant mixture of 29.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.984g 70wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.689g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 1.608g SFS in 28g distilled water.In reactor, add the solution of 2.297g 70wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Latex granularity with dynamic light scattering determination is 497nm.Example 14
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add the 75.70g 50wt% tripropylene glycol aqueous solution and 4.49g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 190.65g 2-ethylhexyl acrylate, 22.43g vinylbenzene, 11.21g allyl methacrylate, the 376.94g 50wt% tripropylene glycol aqueous solution and 6.73g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.984g tertbutyl peroxide (t-BHP) in the 11g 50wt% tripropylene glycol aqueous solution, add the solution of 0.689g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 1.608g SFS in 28g distilled water.In reactor, add the solution of 2.297g 70wt% tertbutyl peroxide in the 56g 50wt% tripropylene glycol aqueous solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Latex granularity with dynamic light scattering determination is 144nm.Example 15
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 322.13g 75wt% aqueous glycol solution and 26.71g Disponil FES 77 tensio-active agents.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, the monomer mixture that preparation is made up of 307.69g 2-ethylhexyl acrylate, 34.19g vinylbenzene.In the reactor of heating, add this monomer mixture of 34.19g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.76g 90wt% tertbutyl peroxide (t-BHP) in 8.8g 75% glycol/water mixtures, add the solution of 0.34g sodium formaldehyde sulphoxylate (SFS) in 11g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add 1.03g SFS and the solution of 22.79g Disponil FES77 tensio-active agent in 22g distilled water.In reactor, add the solution of 0.76g 90wt% tertbutyl peroxide in 44g 75% glycol/water solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 45% solid, is 63nm with the granularity of dynamic light scattering determination.Example 16
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.38g 50wt% cyclohexanedimethanol (CHDM) aqueous solution and 5.70g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 193.73g 2-ethylhexyl acrylate, 34.19g vinylbenzene, the 58.12g 50wt%CHDM aqueous solution and 4.56g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.1g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g 90wt% tertbutyl peroxide (t-BHP) in the 11g 50wt%CHDM aqueous solution, add the solution of 0.0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.50g 90wt% tertbutyl peroxide in the 56g 50wt%CHDM aqueous solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Latex granularity with dynamic light scattering determination is 225nm.Example 17
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add solution and the 5.70g HitenolHS-20 of 395.38g 25wt% cyclohexanedimethanol (CHDM) in ethylene glycol.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of EG solution and the 4.56g Hitenol HS-20 of 193.73g 2-ethylhexyl acrylate, 34.19g vinylbenzene, 58.12g 25wt%CHDM.In the reactor of heating, add this monomer/surfactant mixture of 29.1g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g 90wt% tertbutyl peroxide (t-BHP) in the EG of 11g 25%CHDM solution, add the solution of 0.0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.51g 90wt% tertbutyl peroxide in the EG of 56g 25%CHDM solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 28% solid, is 310nm with the granularity of dynamic light scattering determination.Example 18
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.38g 60wt% neopentyl glycol (NPG) aqueous solution and 5.70g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 186.89g 2-ethylhexyl acrylate, 27.35g vinylbenzene, 6.84g allyl methacrylate, 6.84g methacrylic acid, the 58.12g 60wt%NPG aqueous solution and 4.56g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.1g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g tertbutyl peroxide (t-BHP) in the 11g 50wt%NPG aqueous solution, add the solution of 0.0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.51g90wt% tertbutyl peroxide in the 56g 60wt%NPG aqueous solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Latex granularity with dynamic light scattering determination is 691nm.Example 19
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add, 392.54g 75wt% aqueous glycol solution and 11.29g Tergitol 15-S-40, this is a kind of ethoxylate (the 70wt% aqueous solution) of secondary alcohol, is made by Union Carbide Corporation.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 203.20g 2-ethylhexyl acrylate, 22.58g vinylbenzene, the 58.64g 75wt%EG aqueous solution and 6.45g Tergitol15-S-40.In the reactor of heating, add this monomer/surfactant mixture of 28.79g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.50g 90wt% tertbutyl peroxide (t-BHP) in 11g 75wt% aqueous glycol solution, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.50g 90wt% tertbutyl peroxide in 56g 75wt% aqueous glycol solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Latex granularity with dynamic light scattering determination is 118nm.Example 20
Add in the 1L jacket reactor that has condenser, nitrogen purging and agitator, 229.91g ethylene glycol and 3.62g Hitenol HS-20 add 0.72g 1% ferrous sulfate aqueous ammonium then.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 65.02g isoprene, 62.48g vinylbenzene and 2.60g methacrylic acid.In the reactor of heating, add 14.17g vinylbenzene and 0.29g methacrylic acid.Allow the material of reactor again after the balance, in reactor, add the solution of 0.21g 70wt% tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.14g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.After waiting for styrene/methacrylic acid reaction 30min, in 150min, monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.72g SFS in 52.50g distilled water.In reactor, add the solution of 1.02g 70wt% tertbutyl peroxide in 52.5g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 18% solid, is 109nm with the granularity of dynamic light scattering determination.Example 21
Add in the 1L jacket reactor that has condenser, nitrogen purging and agitator, 338.66g 1, and the 4-butyleneglycol (1,4-BD) with the 127.56g aqueous solution and 7.90g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 191.91g 2-ethylhexyl acrylate, 22.58g vinylbenzene, 11.29g allyl methacrylate and 4.52g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 23.03g.Allow the material of reactor again after the balance, add 0.65g tertbutyl peroxide (t-BHP) at 9.03g 1 in reactor, the solution among the 4-BD adds the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add 0.65g 90wt% tertbutyl peroxide again at 45.16g 1, the solution among the 4-BD.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 28% solid, is 174.9nm with the granularity of dynamic light scattering determination.
Table I
Example External phase Monomer Tensio-active agent Initiator Reductive agent
??1 ??EG ???2-EHA，TMPTA ??Hitenol?A-10 ?NaPS ???-
??2 ??EG ???2-EHA，TMPTA ??Hitenol?A-10 ?ABVA ???-
??3 ??EG ???2-EHA，TMPTA ??Hitenol?A-10 ?t-BHP ??SFS
??4 ??EG 2-EHA, vinylbenzene, ALMA ??FES?77 ?t-BHP ??SFS
??5 ??EG ???2-EHA，Vac ??Hitenol?HS-20 ?t-BHP ??SFS
??6 ??EG Vinylbenzene, BA, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??7 ??EG ???MAA，2-EHA，ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??8 ??EG 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??9 ??EG 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??IAA
??10 ??PG/H 2O 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??11 ??PG/EG 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??12 ??DEG/H 2O 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??13 ??DEG/EG 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??14 ??TPG/H 2O 2-EHA, vinylbenzene, ALMA ??Hitenol?HS-20 ?t-BHP ??SFS
??15 ??EG/H 2O 2-EHA, vinylbenzene ??FES?77 ?t-BHP ??SFS
??16 ??CHDM/H 2O 2-EHA, vinylbenzene ??Hitenol?HS-20 ?t-BHP ??SFS
??17 ??CHDM/EG 2-EHA, vinylbenzene ??Hitenol?HS-20 ?t-BHP ??SFS
??18 ??NPG/H 2O 2-EHA, vinylbenzene, MAA ??Hitenol?HS-20 ?t-BHP ??SFS
??19 ??EG/H 2O 2-EHA, vinylbenzene ??Tergitol?15-S-40 ?t-BHP ??SFS
??20 ??EG Vinylbenzene, isoprene, MAA ??Hitenol?HS-20 ?t-BHP ??SFS
??21 ??1，4BD/H 2O 2-EHA, vinylbenzene, MAA ??Hitenol?HS-20 ?t-BHP ??SFS
Modified condensation polymer examples Example 22 (Comparative Examples)
Prepare the PET homopolymer by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97g), (1.0mol 62g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃ of stirring heating 1h, then at 210 ℃ of following 3h.Temperature is brought up to 280 ℃, stops nitrogen gas stream, vacuumizes then.Polymkeric substance stirs 1h down in vacuum (0.2～0.3 holder).The polymkeric substance cooling is also ground.After the grinding, getting partial polymer fusion compression moulding is the polymeric film that can be used for measuring physical properties.Characteristic data is stated from the table 2.Example 23
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97g), (10mol 62g) and catalyst metal, is placed in the 0.5L polymerization reactor under the nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃ of stirring heating 1h, then at 210 ℃ of following 3h.Temperature is brought up to 275 ℃ and be incubated 30min.Stop nitrogen gas stream, vacuumize (5 holder) 5min then.After this, polymerization temperature is reduced to 240 ℃, and pressure is elevated to 300 holders.The emulsion of 1mL example 1 is injected in the polymerization flask by syringe, and it is distributed in this polymer melt subsequently.Temperature is elevated to 275 ℃, is decompressed to 10 holders simultaneously.Behind the 5min, pressure is elevated to 300 holders, and adds 2mL example 1 emulsion in addition.Vacuum is increased to 0.2～0.3 holder in 45min, and stirring velocity is reduced to 50rpm from 200.Melt looks and appears as homogeneous phase but have to a certain degree opaque.Remove heating and stirring, blend is the White-opalescent solid at the 15min intercrystalline.Allow polymkeric substance cool off and grinding.After the grinding, getting partial polymer fusion compression moulding is the polymeric film that can be used for physical property test.Characteristic data is stated from the table 1.The transmission electron microscope observation of melt compression molded films shows that rubber grain has been distributed in the polyester matrix.Granularity is in 50～300nm scope.Example 24
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97g), (1.0mol 52g) and catalyst metal, is placed in the 0.5L polymerization reactor under the nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃ of stirring heating 1h, then at 210 ℃ of following 3h.Temperature is brought up to 280 ℃ and be incubated 20min.Stop nitrogen gas stream, vacuumize (5 holder) 5min then.Pressure is elevated to 300 holders.The emulsion of 10 milliliters of examples 1 is injected in the polymerization flask by syringe, and it is distributed in this polymer melt subsequently.Vacuum is increased to 0.2～0.3 holder in 60min, and stirring velocity is reduced to 50rpm from 200.Melt looks and appears as homogeneous phase but have to a certain degree opaque.Remove heating and stirring, blend is the White-opalescent solid at the 30min intercrystalline.Allow polymkeric substance cool off and grinding.After the grinding, getting partial polymer fusion compression moulding is the polymeric film that can be used for testing.Characteristic data is stated from the table 2.The transmission electron microscope observation of melt compression molded films shows that rubber grain has been distributed in the polyester matrix.Granularity is in 100～400nm scope.
Table 2: adopt the emulsion of acrylate in EG to carry out impact-modified PET performance
???????????PET 1% acrylate 3.5% acrylate
Character Polymkeric substance Film Polymkeric substance Film Polymkeric substance Film
Ih?V.(dl/g) ????0.61 ????0.58 ???0.64 ????0.60 ????0.73 ????0.67
????Tch 1 Do not have ????142 Do not have ????1334 Do not have ????135
????Tm 1 ????254 (H f＝12.82) ????257 ?(H f＝10.79) ???250 (H f＝11.56) ????251 (H f＝9.08) ????239 ?(H f＝8.40) ????238 ??(H f＝7.31)
????T g ????81 ????78 ???78 ????77 ????73 ????72
????Tch 2 ????152 ????137 ???161 ????149 ????162 ????150
????Tm 2 ????257 ?(H f＝9.89) ????257 ?(H f＝12.70) ???252 (H f＝10.20) ????251 (H f＝10.92) ????240 ?(H f＝7.97) ????240 ??(H f＝9.61)
????Tcc ????161 ????193 ???158 ????178 Do not have ????154
Film %Xtal ????NT ????7.84 ???NT ????5.6 ????NT ????2.68
????M n ??12300 ????11600 ??12800 ???11800 ??13600 ???13000
????M w ??39900 ????35900 ??40300 ???37500 ??49200 ???46400
????M z ??67000 ????59800 ??64500 ???60600 ??81000 ???76400
Film shock-resistant (ft-lbs) ????NT ????2.36 ???NT ????2.60 ????NT ????2.74
Failure mode ????- Fragility ???- Toughness ????- Toughness
NT: test case 25
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 394.63g water and 2.31g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 196.15g butyl acrylate, 23.08g vinylbenzene, 11.54g allyl methacrylate, 58.85g water and 4.62g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.4g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.77g tertbutyl peroxide (t-BHP) in 11.2 gram distilled water, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.92g SFS in 28g distilled water.In reactor, add the solution of 0.51g 90wt% tertbutyl peroxide in 56g water again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 28.5% solid, is 63nm with the granularity of dynamic light scattering determination.Example 26
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1.0mol 62.0g), the emulsion and the catalyst metal of 15.0g example 25, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, then at 210 ℃ of following 2h.Temperature is brought up to 275 ℃.Stop nitrogen gas stream, vacuumize then.Polymkeric substance (0.1～0.3 holder) under vacuum stirs 60min, stops to stir and removing heating then.Allow polymkeric substance cool off and grinding.Limiting viscosity is 0.50dl/g; Mw is 32,200g/mol; Tg is 86.0 ℃.Example 27
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.93g ethylene glycol (EG) and 7.90g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 182.88g 2-ethylhexyl acrylate, 31.61g vinylbenzene, 11.29g allyl methacrylate, 57.57g EG and 4.52g HitenolHS-20.In the reactor of heating, add this monomer/surfactant mixture of 28.79g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.50g 90% tertbutyl peroxide (t-BHP) in 11.2g EG, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.50g 90wt% tertbutyl peroxide in 56g EG again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 28.4% solid, is 120nm with the granularity of dynamic light scattering determination.Example 28
Prepare blend by follow procedure.Diphenyl carbonate (0.30mol, 64.20g), (0.30mol 68.40g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere dihydroxyphenyl propane.Mixture is at 200 ℃, slow stirring heating 0.5h under the nitrogen gas stream protection, then at 220 ℃ of following 20min, and 24 ℃ of following 30min.260 ℃ of following 30min.Temperature is brought up to 280 ℃.This moment, the emulsion of 13.4g example 27 slowly adds in 2min by 125mL pressure equalization funnel, and in nitrogen atmosphere, 280 ℃ of continuation heating down.Begin to vacuumize, in 15min, the flask internal pressure is reduced to 0.35 holder from 1 normal atmosphere.Temperature is elevated to 290 ℃ in 30min, again through 1.5h to 300 ℃, 20min again is to 320 ℃.Remove heating and stirring from the thickness melt, allow polymkeric substance cool off.Tg is 135 ℃; Limiting viscosity is 0.29dl/g.The particles dispersed (observation by light microscope) in polycarbonate substrates of the maximum 30 μ m of granularity.Example 29
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.33g ethylene glycol (EG) and 5.50g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 194.84g 2-ethylhexyl acrylate, 22.92g vinylbenzene, 11.46g allyl methacrylate, 47.89g EG and 3.44g HitenolHS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.1g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g 90wt% tertbutyl peroxide (t-BHP) in 11.2g EG, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white tone that becomes blueing, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.51g 90wt% tertbutyl peroxide in 56g EG again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 27.5% solid, is 164nm with the granularity of dynamic light scattering determination.Example 30
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (0.75mol 108g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere 1,4 cyclohexane dimethanol.Mixture is at 310 ℃, slow stirring heating 10min under the nitrogen gas stream protection, so solution becomes homogeneous phase.In 15min, add the emulsion and the 1.5mL defoamer DC-7 (Dow Corning) of 30g example 29, be reflected at reheat 45min under the nitrogen atmosphere.This moment, begin to vacuumize, so pressure is reduced to 200 holders, (in the 1min) pressure is reduced to 0.3～0.5 holder then, stirs 1h then, thereby obtains sticky polymers solution.Remove heating and allow polymkeric substance cooling, grinding then.Limiting viscosity is 0.65dl/g; Tg is 91.4 ℃ (the 2nd circulations); Tm is 274.4 ℃ (the 2nd circulations).Example 31
Prepare polymkeric substance by follow procedure.(0.5mol, 97.0g), 1, (0.75mol 67.5g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere 4-butyleneglycol dimethyl terephthalate (DMT).Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, and at 2h, temperature is elevated to 255 ℃ then, and insulation 15min.This moment, begin to vacuumize, so pressure is reduced to 200 holders, (in the 1min) pressure is reduced to 0.3～0.5 holder then, stirs 1h then, thereby obtains sticky polymers solution.Remove heating and allow polymkeric substance cooling, grinding then.Limiting viscosity is 0.94dl/g; Tg is 45.6 ℃ (the 2nd circulations); Tm is 224.0 ℃ (the 2nd circulations).Mn is 13,000; Mw is 35,400.Example 32
Prepare blend by follow procedure.(0.5mol, 97.0g), 1, (0.75mol 67.5g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere 4-butyleneglycol dimethyl terephthalate (DMT).Mixture is at 200 ℃, the slow about 15min of stirring heating under the nitrogen gas stream protection, then in 2min in reaction vessel the emulsion of adding 30mL example 29.Reaction mixture is at 200 ℃ of reheat 45min, subsequently at 210 ℃ of reheat 2h.Temperature is elevated to 255 ℃, and insulation 15min vacuumizes (200 holder) then, and (in the 1min) pressure is reduced to 0.3～0.5 holder then, stirs 1h then, thereby obtains the sticky polymers melt.Remove heating and allow polymkeric substance cooling, grinding then.Limiting viscosity is 0.58dl/g; Tg is 42.3 ℃ (the 2nd circulations); Tm is 178.8 ℃ (the 2nd circulations).Example 33
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1.0mol 62.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture 200 ℃, slowly the about 10min of stirring heating is even until mixture under the nitrogen gas stream protection.Utilize 125mL pressure equalization funnel in 20min, to add the emulsion of 56.5g example 27 then.Reaction mixture is at 200 ℃ of reheat 45min, subsequently at 210 ℃ of reheat 2h.Temperature is elevated to 280 ℃ then.Begin to vacuumize this moment, make pressure in 35min, be reduced to 0.3～0.5 holder, keep 45min in 0.3～0.5 holder then, simultaneously viscous melt is stirred from 1 normal atmosphere.Remove heating and allow polymkeric substance cooling, grinding then.At 200 ℃ of fusion compression moulding 15s, thereby obtain tough and tensile (brown) semitransparent thin film.Limiting viscosity is 0.59dl/g; Tg is 28 ℃ (the 2nd circulations).The particles dispersed (observation by light microscope) in polyester matrix of the maximum 30 μ m of granularity.Example 34
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 406.17g ethylene glycol (EG) aqueous solution and 4.58g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 206.11g vinylbenzene, 22.90g Vinylstyrene, 68.70g EG and 4.58g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 30.23g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g 90% tertbutyl peroxide (t-BHP) in 11.45g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.69g SFS in 28g distilled water.In reactor, add the solution of 0.51g 90% tertbutyl peroxide in 34.35g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.This emulsion contains 28.0% solid, is 174nm with the granularity of dynamic light scattering determination.Example 35
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1.0mol 62.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, then under 210 ℃, and 2h.Utilize 125mL pressure equalization funnel to add the emulsion of 56.5g example 34 then in 17min, reaction mixture is warming up to 280 ℃ then.Begin to vacuumize this moment, make pressure in 11min, be reduced to 0.3～0.5 holder from 1 normal atmosphere.Pressure was kept 1 hour in 0.3～0.5 holder then, simultaneously viscous melt was stirred.Remove heating and allow polymkeric substance cooling, grinding then.At 280 ℃ of fusion compression moulding 15s, thereby obtain tough and tensile film.Limiting viscosity is 0.54dl/g; Tg is 57 ℃ (the 2nd circulations); Tm is 200 ℃ (the 2nd circulations).Observation by light microscope shows that agglomeration to a certain degree, the most about 30 μ m of granularity take place particle.Example 36
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 406.17g ethylene glycol (EG) aqueous solution and 4.58g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of triacrylate, 68.70g EG and the 4.58g Hitenol HS-20 of 183.21g 2-ethylhexyl acrylate, 18.32g vinylbenzene, 27.48g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 30.23g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g 90% tertbutyl peroxide (t-BHP) in 11.45g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.69g SFS in 28g distilled water.In reactor, add the solution of 0.51g 90wt% tertbutyl peroxide in 34.35g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Example 37
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1.0mol 62.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, subsequently at 210 ℃ of following 2h.Utilize 125mL pressure equalization funnel to add the emulsion of 56.5g example 36 then in 21min, reaction mixture is warming up to 280 ℃ then.Begin to vacuumize this moment, make pressure be reduced to 0.3～0.5 holder from 1 normal atmosphere in 11min, pressure is kept 1h in 0.3～0.5 holder then, simultaneously viscous melt is stirred.Remove heating and allow polymkeric substance cooling, grinding then.At 280 ℃ of fusion compression moulding 15s, thereby obtain tough and tensile film.Limiting viscosity is 0.66dl/g; Tg is 51 ℃ (the 2nd circulations); Tm is 200 ℃ (the 2nd circulations).Observation by light microscope shows that agglomeration to a certain degree, the most about 30 μ m of granularity take place particle.Example 38
Add in the 1L jacket reactor that has condenser, nitrogen purging and agitator, 338.86g 1, and the 4-butyleneglycol (1,4-BD), 127.56g distilled water and 7.90g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 191.91g 2-ethylhexyl acrylate, 22.58g vinylbenzene, 11.29g allyl methacrylate and 4.52g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 23.03g.Allow the material of reactor again after the balance, add 0.65g 70% tertbutyl peroxide (t-BHP) at 9.03g 1 in reactor, the solution among the 4-BD adds the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add 0.65g 70wt% tertbutyl peroxide again at 45.16g 1, the solution among the 4-BD.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Granularity with latex that dynamic light scattering determination obtains is 175nm.Example 39
Prepare blend by follow procedure.(0.40mol, 77.6g), 1, (0.60mol 54.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere 4-butyleneglycol dimethyl terephthalate (DMT).Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, subsequently at 210 ℃ of following 1h.Utilize 125mL pressure equalization funnel to add the emulsion of 51.8g example 38 then in 36min, reaction mixture is warming up to 255 ℃ then.Begin to vacuumize this moment, make pressure be reduced to 0.3～0.5 holder from 1 normal atmosphere in 10min, pressure is kept 1h in 0.3～0.5 holder then, simultaneously viscous melt is stirred.Remove heating and allow polymkeric substance cooling, grinding then.At 260 ℃ of fusion compression moulding 15s, thereby obtain very tough and tensile film.Limiting viscosity is 0.58dl/g; Tg is 25 ℃ (the 2nd circulations); Tm is 220 ℃ (the 2nd circulations).Observation by light microscope shows that agglomeration to a certain degree, the most about 30 μ m of granularity take place particle.Example 40
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.38g 60wt% neopentyl glycol (NPG) aqueous solution and 5.70g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 186.89g 2-ethylhexyl acrylate, 27.35g vinylbenzene, 6.84g allyl methacrylate, 6.84g methacrylic acid, the 58.12g 60wt%NPG aqueous solution and 4.56g Hitenol HS-20.In the reactor of heating, add this monomer/surfactant mixture of 29.1g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g tertbutyl peroxide (t-BHP) in the 11g 60%NPG aqueous solution, add the solution of 0.0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor by the transparent white that becomes the blueing white tone, showing has small-particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.51g90wt% tertbutyl peroxide in the 56g 60%NPG aqueous solution again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.With the granularity of latex that dynamic light scattering determination obtains is respectively at the bimodal distribution of 691nm and 211nm.Example 41
In the 2L reactor that has the condenser of steam jacket, water cooled condenser and Dean-Stark trap, add 496g neopentyl glycol (NPG), 86g TriMethylolPropane(TMP) (TMP) and 460g m-phthalic acid (IPA).Contain example 40 latex of NPG to wherein adding 250g.Reaction is heated to 150 ℃.After arriving 150 ℃, add 1.5gFastcat 4100 (tin catalyst).Behind the 1h, temperature is elevated to 220 ℃, keeps 3h under this temperature.In distillate, collect 140mL water altogether.Subsequently, reactor cooling to 120 ℃ adds 477g 1, and (1,4-CHDA), temperature is elevated to 230 ℃ to the 4-cyclohexane dicarboxylic acid again.Be reflected at 230 ℃ and keep 2.5h, then cooling.Collect 241mL water altogether (theoretical amount 88%) during the entire reaction.In resin, add 325g dimethylbenzene subsequently.Resin is kept the muddy character of its latex.Do not observe any sign of acrylic rubber agglomerative.
Prepared enamel paint by vibrin that contains latex and Resimene 745 (hexamethoxy methyl cyanuramide).Resin/linking agent weight ratio is 70/30.With 0.3%pTSA as catalyzer; 0.4%FC430 is as glidant.Prepare to scrape on Bonderite 1000 plates with wire bar applicator and film.Plank is at 160 ℃ of baking 30min.The methylethylketone of this coating (MEK) is back and forth wiped number of times and is surpassed 500, shows and solidifies well.Example 42 (prediction example)
Prepare blend by follow procedure.Methyl glutarate (1mol), ethylene glycol (1.5mol), glycol ether (0.5mol) and titanium tetraisopropylate (100ppm is by final polymer weight) are placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere.Mixture becomes even at 200 ℃, the slow about 10min of stirring heating under the nitrogen gas stream protection until mixture.In 20min, in reaction, add 100g poly-(vinylbenzene (95mol%)-copolymerization-glycidyl methacrylate (5mol%)) emulsion based on ethylene glycol, at 200 ℃ of following reheat 45min, 210 ℃ of following 2h, temperature is elevated to 250 ℃ then.Begin to vacuumize this moment, make pressure be reduced to 0.3～0.5 holder from 1 normal atmosphere in 35min, pressure is kept 45min in 0.3～0.5 holder then, simultaneously viscous melt is stirred.Remove heating and allow the polymkeric substance cooling.Isolate elastomer polymer.
Above, just the concrete preferred embodiment of the present invention describes in detail the present invention, yet will know, still can make various variations and modification in spirit and scope of the invention.Example 43
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add, and 341.88g ethylene glycol and 37.99g 15wt%Rhodafac RE-610 (phosphate ester surfactants, Luo Na. Planck provides).Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 182.34g 2-ethylhexyl acrylate, 27.35g vinylbenzene, 18.23g glycidyl methacrylate, 30.39g Rhodafac RE-610 and 45.58g ethylene glycol.In the reactor of heating, add this monomer/surfactant mixture of 30.39g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.51g tertbutyl peroxide (t-BHP) in 11g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observe reactor and become little white that has the blueing tone by light gray-white, showing has particle to generate.In 215min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.68g SFS in 28g distilled water.In reactor, add the solution of 0.65g 70wt% tertbutyl peroxide in 45.6g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.The latex that obtains filters by 100 eye mesh screens.Example 44
Prepared urethanum/vinylformic acid matrix material by follow procedure.The latex that in the 50mL flask, adds 14.61g methylene-bis (4-cyclohexyl isocyanate) and 5.75g example 43.In mixture, add catalyzer dibutyltin diacetate (0.1g).In 1h, exothermic heat of reaction also generates the hard polymer porous plastics that contains latex.Example 45
In the 1L jacket reactor that has condenser, nitrogen purging and agitator, add 395.93g ethylene glycol and 7.90g Hitenol HS-20.Material is heated to 65 ℃ in the reactor.In independent 500mL flask, monomer/surfactant mixture that preparation is made up of 180.62g 2-ethylhexyl acrylate, 22.58g vinylbenzene, 11.29g allyl methacrylate, 11.29g methacrylic acid, 4.52g HitenolHS-20 and 57.57g ethylene glycol.In the reactor of heating, add this monomer/surfactant mixture of 28.79g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.50g 90wt% tertbutyl peroxide (t-BHP) in 11.2g ethylene glycol, add the solution of 0.23g sodium formaldehyde sulphoxylate (SFS) in 11.2g distilled water subsequently.After several minutes, observing reactor is the white that has little blueing tone by the light gray leucismus, and showing has particle to generate.In 195min, remaining monomer mixture is fed in the reactor.Meanwhile, in reactor, add the solution of 0.65g SFS in 28g distilled water.In reactor, add the solution of 0.50g 90wt% tertbutyl peroxide in 56g ethylene glycol again.After all monomer finishes, be reflected at 65 ℃ and keep 0.5h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Granularity with latex that dynamic light scattering determination obtains is 100nm.Example 46
Prepare blend by follow procedure.(0.32mol 61.9g), the latex and the catalyst metal of 56.5g example 45, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere dimethyl terephthalate (DMT).Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, subsequently at 210 ℃ of following 2h.This moment, reaction mixture is warming up to 280 ℃, begins then to vacuumize, and makes pressure be reduced to 0.2～0.5 holder from 1 normal atmosphere in 11min, and pressure is kept 1h in 0.3～0.5 holder then, simultaneously viscous melt is stirred.Remove heating and allow polymkeric substance cooling, grinding then.Polymer property viscosity is 0.35dl/g.Example 47
In the 2L jacket reactor that has condenser, nitrogen purging and agitator, add 515.76g ethylene glycol, 164.80g water and 12.28g 70wt%Tergitol 15-S-40 (nonionogenic tenside that Union Carbide Corporation makes) solution.Material is heated to 85 ℃ in the reactor.In independent 1500mL flask, monomer/surfactant mixture that preparation is made up of triacrylate, 7.37g 70%Tergitol 15-S-40 and the 103.2g ethylene glycol of 325.65g 2-ethylhexyl acrylate, 17.19g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 45.44g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.69g Sodium Persulfate in 17g water.After several minutes, observe reactor by the transparent blueing white tone that becomes, showing has small-particle to generate.In 90min, remaining monomer mixture is fed in the reactor.In reactor, adding the monomeric while, in reactor, adding the solution of 1.72g Sodium Persulfate in 34g water.After all monomer finishes, be reflected at 85 ℃ and keep 1h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Effective diameter with dynamic light scattering determination is 194nm.Example 48
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1mol 62.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, subsequently at 210 ℃ of following 2h.Temperature of reaction rises to 280 ℃, closes nitrogen then and begins to vacuumize.(reach 0.35 holder) after vacuumizing 10min, stop to vacuumize, and be blown into nitrogen, in 20min, add the latex of 56.5g example 47 then by 125mL pressure equalization funnel so that pressure is elevated to atmospheric pressure.Close nitrogen once more and vacuumize.Pressure is kept 1h in 0.3～0.5 holder, simultaneously viscous melt is stirred.Remove heating and allow polymkeric substance cooling, grinding then.At 240 ℃ of fusion compression moulding 15s, thereby obtain tough and tensile, opaque, white film.Limiting viscosity is 0.80dl/g; Tg is 61.3 ℃ (the 2nd circulations); Tm is 212.3 ℃ (the 2nd circulations).TEM (transmission electron microscope) shows that rubber grain is dispersed in the polyester matrix with the granularity of 0.2～0.9 μ m.Example 49
In the 2L jacket reactor that has condenser, nitrogen purging and agitator, add 656.7g ethylene glycol and 26.86g Disponil FES 77 (anion surfactant, Henkel is produced).Material is heated to 85 ℃ in the reactor.In independent 1500mL flask, monomer/surfactant mixture that preparation is made up of triacrylate, 103.2g ethylene glycol and the 16.12g Disponil FES 77 of 326.7g 2-ethylhexyl acrylate, 17.19g TriMethylolPropane(TMP).In the reactor of heating, add this monomer/surfactant mixture of 46.3g.Allow the material of reactor again after the balance, in reactor, add the solution of 0.69g Sodium Persulfate in 16.8g water.After several minutes, observe reactor by the transparent blueing white tone that becomes, showing has small-particle to generate.In 90min, remaining monomer mixture is fed in the reactor.In reactor, add the monomeric while, in reactor, add the solution of 1.72g Sodium Persulfate in 33.6g water.After all monomer finishes, be reflected at 85 ℃ and keep 1h again, this moment, make reactor cooling to room temperature.
The latex that obtains filters by 100 eye mesh screens.Effective diameter with dynamic light scattering determination is 155nm.Example 50
Prepare blend by follow procedure.Dimethyl terephthalate (DMT) (0.5mol, 97.0g), (1mol 62.0g) and catalyst metal, is placed in the 0.5L polymerization reactor under the 1 normal atmosphere nitrogen atmosphere ethylene glycol.Mixture is at 200 ℃, slow stirring heating 1h under the nitrogen gas stream protection, subsequently at 210 ℃ of following 2h.Temperature of reaction rises to 280 ℃, closes nitrogen then and begins to vacuumize.(reach 0.35 holder) after vacuumizing 10min, stop to vacuumize, and be blown into nitrogen, in 10min, add the latex of 56.6g example 49 then by 125mL pressure equalization funnel so that pressure is elevated to atmospheric pressure.Close nitrogen once more and vacuumize.Pressure is kept 1h in 0.3～0.5 holder, simultaneously viscous melt is stirred.Remove heating and allow polymkeric substance cooling, grinding then.At 240 ℃ of fusion compression moulding 15s, thereby obtain tough and tensile, opaque, white film.Limiting viscosity is 0.82dl/g; Tg is 60.1 ℃ (the 2nd circulations); Tm is 212.2 ℃ (the 2nd circulations).TEM shows that rubber grain is dispersed in the polyester matrix with the granularity of 0.2～0.9 μ m.

Claims (120)

1. a method for preparing polycondensate/the 1st polymeric matrix comprises the following steps:
(a) preparation polymeric colloid system, it comprises the 1st polymkeric substance that is dispersed in the continuous liquid phase; And
(b) the polymeric colloid system is incorporated in the condensation reaction medium, can before the condensation reaction or during implement, wherein the condensation reaction medium comprises (1) diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether or above-mentioned mixture
Wherein continuously liquid phase, condensation reaction medium or the two comprise diol component, so just form polycondensate/the 1st polymeric matrix.
2. the process of claim 1 wherein that continuous liquid phase comprises diol component.
3. the method for claim 2, wherein liquid phase is the diol component of 25～100wt% continuously.
4. the method for claim 2, wherein liquid phase is the diol component of 50～100wt% continuously.
5. the method for claim 2, wherein liquid phase is the diol component of 75～100wt% continuously.
6. the method for claim 2, wherein liquid phase is the diol component of 90～100wt% continuously.
7. the method for claim 2, wherein liquid phase is made of diol component substantially continuously.
8. the process of claim 1 wherein that diol component comprises aliphatic series or cycloaliphatic diol or its mixture of 2～10 carbon atoms.
9. the process of claim 1 wherein that diol component comprises ethylene glycol, 1,3-trimethylene, 1, ammediol, tripropylene glycol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, 1,7-heptanediol, 1,8-ethohexadiol, 1,9-nonanediol, neopentyl glycol, suitable-or anti--cyclohexanedimethanol, suitable-or anti--2,2,4,4-tetramethyl--1,3-cyclobutanediol, glycol ether or its mixture.
10. the process of claim 1 wherein that diol component comprises ethylene glycol, propylene glycol, tripropylene glycol, 1,4-butyleneglycol, glycol ether, neopentyl glycol, suitable-or anti--cyclohexanedimethanol or its mixture.
11. the process of claim 1 wherein that diol component comprises neopentyl glycol, ethylene glycol, suitable-or anti--cyclohexanedimethanol, 1,4-butyleneglycol or its mixture.
12. the process of claim 1 wherein that diol component is present in the continuous liquid phase, and liquid phase is made of diol component substantially continuously.
13. the process of claim 1 wherein that the condensation reaction medium comprises diol component.
14. the process of claim 1 wherein that the 1st polymkeric substance comprises the residue of ethylene linkage unsaturated monomer.
15. the process of claim 1 wherein that the 1st polymkeric substance comprises non-sour vinyl monomer, sour vinyl monomer or its mixture.
16. the process of claim 1 wherein that the 1st polymkeric substance comprises the residue of following non-sour vinyl monomer: the methacrylic ester of acetoacetyl ethyl, the acrylate of acetoacetyl ethyl, methyl acrylate, methyl methacrylate, ethyl propenoate, Jia Jibingxisuanyizhi, butyl acrylate, butyl methacrylate, isobutyl acrylate, Propenoic acid, 2-methyl, isobutyl ester, the vinylformic acid (ethyl hexyl) ester, methacrylic acid 2-(ethyl hexyl) ester, 2-ethylhexyl acrylate, isoprene, Octyl acrylate, Octyl methacrylate, Isooctyl acrylate monomer, Isooctyl methacrylate, the triacrylate of TriMethylolPropane(TMP), vinylbenzene, alpha-methyl styrene, glycidyl methacrylate, the methacryloyl carbodiimide, Ba Dousuan C 1～C 18Alkyl ester, n-butyl maleate, α-or β-vinyl naphthalene, dioctyl maleate, allyl methacrylate, toxilic acid diallyl ester, propanedioic acid diallyl ester, methacrylic acid methoxy base butenyl esters, isobornyl methacrylate, the hydroxyethyl methacrylate butenyl esters, (methyl) hydroxyethyl acrylate, (methyl) vinylformic acid hydroxypropyl ester, vinyl cyanide, vinylchlorid, vinylidene chloride, vinyl acetate between to for plastic, vinyl 1,2-ethylidene carbonic ether, the epoxy butylene, 3,4-dihydroxyl butylene, (methyl) hydroxyethyl acrylate, Methacrylamide, acrylamide, N-butyl acrylamide, the N-ethyl acrylamide, divinyl, (methyl) vinylformic acid vinyl ester, the different propylene ester of (methyl) vinylformic acid, (methyl) vinylformic acid cyclic aliphatic epoxy ester, ethyl-formamide, 4-vinyl-1,3-dioxolane-2-ketone, 2,2-dimethyl-4-vinyl-1,3-dioxolane (dioxolate) and 3,4-diacetoxyl-1-butylene or its mixture.
17. the process of claim 1 wherein that the 1st polymkeric substance comprises the residue of following sour vinyl monomer: vinylformic acid, methacrylic acid, methylene-succinic acid, Ba Dousuan or its mixture.
18. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% butyl acrylates.
19. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% isoprene.
20. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% divinyl.
21. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% vinyl cyanide.
22. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% vinylbenzene.
23. the process of claim 1 wherein that the 1st polymkeric substance comprises 50～100% 2-ethylhexyl acrylates.
24. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% butyl acrylates.
25. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% isoprene.
26. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% divinyl.
27. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% vinyl cyanide.
28. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% vinylbenzene.
29. the process of claim 1 wherein that the 1st polymkeric substance comprises 80～100% 2-ethylhexyl acrylates.
30. the process of claim 1 wherein that the 1st polymkeric substance comprises following residues of monomers: acrylate, methacrylic ester, vinylbenzene, vinylchlorid, vinylidene chloride, vinyl cyanide, vinyl acetate between to for plastic, divinyl, isoprene or its mixture.
31. the process of claim 1 wherein that the 1st polymkeric substance comprises the residue of 2-ethylhexyl acrylate.
32. the process of claim 1 wherein that the 1st polymkeric substance comprises the functional group that can react with diacid, vulcabond, diaryl carbonate, dialkyl carbonate, dihalo-carbonic ether or diol component.
33. the method for claim 31, wherein functional group comprises epoxy, acid, hydroxyl, isocyanic ester, amine, acid amides, carbonate group or its mixture.
34. the process of claim 1 wherein that the polymeric colloid system is crosslinked.
35. the process of claim 1 wherein that the 1st polymkeric substance is a core-shell polymer.
36. the process of claim 1 wherein that the 1st polymkeric substance is non-core-shell polymer.
37. the process of claim 1 wherein that polymeric colloid system external phase and condensation reaction medium all comprise diol component.
38. component of the process of claim 1 wherein (b) (1) comprises diacid, thereby generates the polyester as polycondensate.
39. the method for claim 38, wherein polyester comprises sour residue and diol residue.
40. the method for claim 39, wherein polyester also comprises the modification residue.
41. the method for claim 38, wherein the polymeric colloid system is to adopt the latex of emulsion polymerization prepared.
42. the method for claim 41, wherein the 1st polymkeric substance comprises core-shell polymer.
43. the method for claim 41, wherein the 1st polymkeric substance comprises non-core-shell polymer.
44. the method for claim 41, wherein external phase is made up of water substantially.
45. the method for claim 41, wherein external phase is made up of glycol substantially.
46. the method for claim 41, wherein latex comprises the functional group that can react with diacid, vulcabond, diaryl carbonate, dialkyl carbonate, dihalo-carbonic ether or diol component.
47. the method for claim 46, wherein functional group comprises epoxy, acid, hydroxyl, amine, acid amides, carbonate group or its mixture.
48. the process of claim 1 wherein that it is zero substantially that polycondensate has the Tg and the degree of crystallinity that are lower than 40 ℃.
49. the process of claim 1 wherein that polycondensate has is higher than 40 ℃ Tg.
50. the process of claim 1 wherein that polycondensate is a thermosetting polymer.
51. the process of claim 1 wherein that the polymeric colloid system is to adopt the latex of emulsion polymerization prepared.
52. the method for claim 51, wherein external phase is made of water substantially.
53. the method for claim 51, wherein external phase is made of glycol substantially.
54. the process of claim 1 wherein that the polymeric colloid system is to adopt the dispersion polymerization preparation.
55. the method for claim 54, wherein external phase is made of water substantially.
56. the method for claim 54, wherein external phase is made of glycol substantially.
57. the process of claim 1 wherein that the polymeric colloid system is to adopt suspension polymerization.
58. the method for claim 57, wherein external phase is made of water substantially.
59. the method for claim 57, wherein external phase is made of glycol substantially.
60. the process of claim 1 wherein that the polymeric colloid system is to adopt the machinery emulsification preparation.
61. the method for claim 60, wherein external phase is made of water substantially.
62. the method for claim 60, wherein external phase is made of glycol substantially.
63. the process of claim 1 wherein that the polymeric colloid system introduced before condensation reaction causes.
64. the process of claim 1 wherein that the polymeric colloid system introduces in the transesterify stage.
65. the process of claim 1 wherein that the polymeric colloid system introduces in polycondensation phase.
66. a method for preparing polycondensate/latex matrix comprises the following steps:
(1) preparation colloid diol combination thing, said composition comprises
(a) contain the latex polymer particles of the residue of ethylene linkage unsaturated monomer, wherein the granularity of latex polymer particles is lower than 1000nm;
(b) tensio-active agent; And
(c) comprise the continuous liquid phase of diol component, wherein diol component accounts for 60～100wt% of latex diol combination thing; And
(2) this diol latex compositions is incorporated in the condensation reaction medium, this condensation reaction medium comprises diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether or above-mentioned mixture.
67. the method for claim 66, wherein diol latex compositions does not comprise polymerization stabilizer.
68. the method for claim 66, wherein tensio-active agent comprises negatively charged ion, positively charged ion, nonionogenic tenside or its mixture.
69. the method for claim 66, wherein tensio-active agent comprises polymerizable or non-polymerizable alkyl ethoxylated sulfate (sulfate), alkylphenol ethoxylated sulfate (sulfate), alkylethoxylate, alkylphenol ethoxylate or its mixture.
70. the method for claim 66, wherein latex particle comprises the functional group that can react with diacid, vulcabond, diaryl carbonate, dialkyl carbonate, dihalo-carbonic ether or diol component.
71. the method for claim 70, wherein functional group comprises epoxide group, acetoacetyl group, carbonate group, oh group, amine groups, isocyanate groups, amide group or its mixture.
72. the method for claim 66, wherein latex polymer particles is crosslinked.
73. the method for claim 66, wherein latex polymer is a core-shell polymer.
74. the method for claim 66, wherein latex polymer is non-core-shell polymer.
75. the method for claim 66, wherein latex polymer particles comprises the residue of ethylene linkage unsaturated monomer.
76. the method for claim 66, wherein latex polymer particles comprise non-sour vinyl monomer-, the residue of sour vinyl monomer or its mixture.
77. the method for claim 66, wherein latex polymer particles comprises the residue of following non-sour vinyl monomer: the methacrylic ester of acetoacetyl ethyl, the acrylate of acetoacetyl ethyl, methyl acrylate, methyl methacrylate, ethyl propenoate, Jia Jibingxisuanyizhi, butyl acrylate, butyl methacrylate, isobutyl acrylate, Propenoic acid, 2-methyl, isobutyl ester, the vinylformic acid (ethyl hexyl) ester, methacrylic acid 2-(ethyl hexyl) ester, 2-ethylhexyl acrylate, isoprene, Octyl acrylate, Octyl methacrylate, Isooctyl acrylate monomer, Isooctyl methacrylate, the triacrylate of TriMethylolPropane(TMP), vinylbenzene, alpha-methyl styrene, glycidyl methacrylate, the methacryloyl carbodiimide, Ba Dousuan C 1～C 18Alkyl ester, n-butyl maleate, α-or β-vinyl naphthalene, dioctyl maleate, allyl methacrylate, toxilic acid diallyl ester, propanedioic acid diallyl ester, methacrylic acid methoxy base butenyl esters, isobornyl methacrylate, the hydroxyethyl methacrylate butenyl esters, (methyl) hydroxyethyl acrylate, (methyl) vinylformic acid hydroxypropyl ester, vinyl cyanide, vinylchlorid, vinylidene chloride, vinyl acetate between to for plastic, vinyl 1,2-ethylidene carbonic ether, the epoxy butylene, 3,4-dihydroxyl butylene, (methyl) hydroxyethyl acrylate, Methacrylamide, acrylamide, N-butyl acrylamide, the N-ethyl acrylamide, divinyl, (methyl) vinylformic acid vinyl ester, the different propylene ester of (methyl) vinylformic acid, (methyl) vinylformic acid cyclic aliphatic epoxy ester, ethyl-formamide, 4-vinyl-1,3-dioxolane-2-ketone, 2,2-dimethyl-4-vinyl-1,3-dioxolane (dioxolate) and 3,4-diacetoxyl-1-butylene or its mixture.
78. the method for claim 66, wherein latex polymer particles comprises the 2-ethylhexyl acrylate residue.
79. the method for claim 66, wherein latex polymer comprises the residue of following sour vinyl monomer: vinylformic acid, methacrylic acid, methylene-succinic acid, Ba Dousuan or its mixture.
80. the method for claim 66, wherein latex polymer particles comprises following residues of monomers: acrylate, methacrylic ester, vinylbenzene, vinylchlorid, vinylidene chloride, vinyl cyanide, vinyl acetate between to for plastic, divinyl, isoprene or its mixture.
81. the method for claim 66, wherein diol component comprises aliphatic series or cycloaliphatic diol or its mixture of 2～10 carbon atoms.
82. the method for claim 66, wherein diol component comprises ethylene glycol, 1,3-trimethylene, propylene glycol, tripropylene glycol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, 1,7-heptanediol, 1,8-ethohexadiol, 1,9-nonanediol, neopentyl glycol, suitable-or anti--cyclohexanedimethanol, suitable-or anti--2,2,4,4-tetramethyl--1,3-cyclobutanediol, glycol ether or its mixture.
83. the method for claim 66, wherein diol component comprises ethylene glycol, propylene glycol, tripropylene glycol, 1,4-butyleneglycol, glycol ether, neopentyl glycol, cyclohexanedimethanol or its mixture.
84. the method for claim 66, wherein diol component comprises neopentyl glycol, ethylene glycol, 1,4-butyleneglycol and suitable-or anti--cyclohexanedimethanol.
85. the method for claim 66, wherein diol component is 65～100wt% of external phase.
86. the method for claim 66, wherein diol component is 75～100wt% of external phase.
87. the method for claim 66, wherein diol component is 90～100wt% of external phase.
88. the method for claim 66, wherein external phase is made of diol component substantially.
89. the method for claim 66, wherein external phase also comprises cosolvent, and the latter's content is less than or equal to the 40wt% of external phase.
90. the method for claim 66, wherein cosolvent comprises water, methyl alcohol, ethanol, propyl alcohol, propyl carbinol or its mixture.
91. the method for claim 66, wherein the weight-average molecular weight of latex polymer particles is pressed gel permeation chromatography, is 1,000～1,000,000.
92. the method for claim 66, wherein external phase also comprises polyvalent alcohol.
93. product by the preparation of the method for claim 1.
94. product by the preparation of the method for claim 66.
95. a blend polymer that comprises the 1st polymkeric substance and polycondensate, wherein the 1st polymkeric substance is by the non-core-shell polymer of polymeric colloid system deutero-.
96. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% 2-ethylhexyl acrylates.
97. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% butyl acrylates.
98. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% isoprene.
99. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% divinyl.
100. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% vinyl cyanide.
101. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% vinylbenzene.
102. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 70～100% vinylbenzene.
103. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% 2-ethylhexyl acrylates.
104. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% butyl acrylates.
105. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% isoprene.
106. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% divinyl.
107. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% vinyl cyanide.
108. the blend polymer of claim 95, wherein the 1st polymkeric substance comprises 50～100% vinylbenzene.
109. the blend polymer of claim 95, wherein polycondensate is a polyester.
110. the blend polymer of claim 95, wherein the Tg of polycondensate is greater than 40 ℃.
111. the blend polymer of claim 110, wherein the 1st polymkeric substance comprises following residues of monomers: 2-ethylhexyl acrylate, butyl acrylate, isoprene, divinyl, lauryl acrylate, vinyl cyanide, vinylidene chloride or its mixture.
112. the blend polymer of claim 95, wherein the Tg of polycondensate is less than 40 ℃.
113. the blend polymer of claim 112, wherein the 1st polymkeric substance comprises following residues of monomers: vinylchlorid, vinylbenzene, alpha-methyl styrene, methyl methacrylate, vinyl naphthalene, isobornyl methacrylate or its mixture.
114. the blend polymer of claim 112, wherein blend polymer is an elastomerics.
115. comprise the powder coating of the blend polymer of claim 95.
116. a method for preparing polycondensate/the 1st polymeric matrix comprises the following steps:
The polymeric colloid system is incorporated in the condensation reaction medium, can before the condensation reaction or during implement, wherein the condensation reaction medium comprises (1) diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether or above-mentioned mixture, wherein the polymeric colloid system comprises the 1st polymkeric substance that is dispersed in the continuous liquid phase
Wherein polymeric colloid system external phase, condensation reaction medium or the two comprise diol component, so generate polycondensate/the 1st polymeric matrix.
117. a method for preparing polycondensate/the 1st polymeric matrix comprises the following steps:
Before the condensation reaction or during, this diol latex system is incorporated in the condensation reaction, wherein this condensation reaction medium comprises
(1) diacid, vulcabond, dialkyl carbonate, diaryl carbonate, dihalo-carbonic ether or above-mentioned mixture, wherein latex glycol system comprises:
(a) contain the latex polymer particles of the residue of ethylene linkage unsaturated monomer, wherein the granularity of latex polymer particles is lower than 1000nm;
(b) tensio-active agent; And
(c) comprise the continuous liquid phase of diol component, wherein diol component accounts for 60～100wt% of latex diol combination thing; Thereby form polycondensate/latex matrix.
118. comprise the impact modified polyester of the blend polymer of claim 95.
119. comprise the hydroxyl-functional polyester coating resin of the blend polymer of claim 95.
120. the method for claim 66, wherein the condensation reaction medium also comprises diol component.
CN98810633A 1997-08-28 1998-08-28 Modified condensation polymer Pending CN1278286A (en)

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US5771497P 1997-08-28 1997-08-28
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US14105198A 1998-08-27 1998-08-27
US60/058,008 1998-08-27
US60/057,714 1998-08-27
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