CN1635039A - Method for preparing novel B level high speed polyurethane enamelled wire paint - Google Patents
Method for preparing novel B level high speed polyurethane enamelled wire paint Download PDFInfo
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Abstract
The invention discloses a method for preparing novel B level high speed polyurethane enamelled wire paint, wherein the hydroxyl preparation consists of, using organic titanium-antimony complex as catalyst, substituted aromatic dibasic alcohol as adjuvant, for polycondensation 5 hours at 130-200 deg. C under atmosphere pressure, and closed constituent preparation consists of using substituted aromatic tertiary amine as catalyst, thus reacting 44'-methyl diphenylene diisocyanate with trimethylolpropane, and obtaining a proportion of isocyanate urea rings with thermotolerant structure.
Description
Technical field:
The present invention relates to a kind of preparation method of novel B level high speed polyurethane wire enamel.
Background technology:
Wire enamel is the important electric insulation coating of a class, mainly is coated in the skin of the not collinear footpath of all kinds nude copper cash.Generally be with enamelling machine on conductor, wire enamel is applied repeatedly, high temperature cures and forms.The effect of wire enamel is: make to produce a kind of good insulation performance layer in the winding between the lead and lead, to stop the circulation of electric current.This layer insulating can make moist for a long time, be heated, chemical dipping and be subjected to still keeping its original performance under the effect of various mechanical forces as friction, bending, stretching, compression, impact etc.Therefore the basic demand decapacitation of enameled wire is satisfied outside the good insulating property, also should possess higher physical strength, thermotolerance, winter hardiness, chemical resistant properties, ageing resistance etc.The common resins that is used to produce wire enamel has polyester polyol, polyester-imide, polyvinyl formal, polyvinyl butyral acetal, polymeric amide, polyimide, polyamidoimide, urethane etc.
Polyurethane wire enamel generally is made up of hydroxy component, closure component and solvent etc.Hydroxy component mainly is the end capped polyester polyol of hydroxyl; The closure component is that polyisocyanates forms through the phenolic compound sealing; Solvent generally is the mixture of cresols and dimethylbenzene; In the baking stage after japanning, the closure dephenolize generates free isocyanate group group and hydroxy component fully reacts, crosslinking curing, thereby forms the polyurethane paint rete with pre-determined characteristics.Polyurethane enamelled wire also has following characteristics except that the performance with general enameled wire:
(1) directly weldering property is good, polyurethane enamelled wire when welding, needn't remove paint film layer in advance, and scolding tin temperature low (being lower than 370 ℃), speed fast (less than 3 seconds), paint film property keeps good around the welding;
(2) dyeability is good, and polyurethane wire enamel can be miscible with multiple dyestuff, makes various colored enameled wires, is applicable to many solder joints occasion;
(3) high frequency performance is good, and the dielectric loss angle tangent of paint film under high frequency is smaller, can be used for preparing the corona-resistant wire enamel that variable-frequency motor is used;
(4) polyurethane wire enamel has coating processes and film integrity preferably, and the enameled wire after modification can reach zero pin hole;
(5) but low-temperature and high-speed is coated with line, storing temperature is lower about 100 ℃ than polyester enameled wire, is coated with linear velocity simultaneously and also wants fast 2～4 times, has improved production efficiency widely;
Exist advantage, especially its cryogenic direct-welding of above-mentioned uniqueness based on polyurethane wire enamel, make polyurethane enamelled wire be widely used in fields such as the more colour TV of solder joint, instrument, computer.
But some shortcomings that polyurethane wire enamel self exists, as the enameled wire coat temperature tolerance that coats is poor, anti-aromatic solvent difference etc., thus limited its application in a lot of fields.
Improvement in performance about polyurethane wire enamel, method of modifying commonly used both at home and abroad at present is to introduce acid amides, imide, amide imide group and isocyanurate ring in the polyurethane molecular structure, perhaps in the manufacturing process of enameled wire, adopt thin layer overbrushing and the compound method that is coated with line, the modified feedstock of improved polyurethane wire enamel because of being adopted, synthetic method and to be coated with Wiring technology different and differ from one another can satisfy different application requiring.Existing in the field abroad patent report, representative report has: JP11035884, it is with trimellitic acid 1,2-anhydride and 4, the imide acid of 4-diphenylmethanediisocyanate (being called for short MDI) preparation is as properties-correcting agent, prepared a kind of electrical isolation polyurethane coating, 328 ℃ of softening temperatures, 7.3 kilovolts of voltage breakdowns also have weldability preferably.JP11001538 reports a kind of modified polyurethane enameled wire lacquer, and its hydroxy component is made up of with the reactant that contains the polycarbonate of imide Sai Ke.11.2 kilovolts of the enameled wire voltage breakdowns that coats, the 1.2 seconds scolding tin time (420 ℃), softening 306 ℃ of the temperature that puncture, enameled wire also has overload-resistant preferably electric current.But also there are some patents in implementation process, still to have some problems.As: USP3174950 has reported a kind of high speed, low temperature scolding tin based polyurethane wire enamel that adopts the modification of match gram, but the not enough F level of temperature resistant grade.USP3869428 has reported a kind of polyurethane wire enamel that contains imide group, weldability can compare favourably with general polyurethane wire enamel, and has a resistance toheat of polyester-imide wire enamel, but the solid content of lacquer liquid is lower, about about 25%, solvent-oil ratio is big, applies often the energy consumption height.USP4578312 has reported a kind of high wire enamel that divides admittedly, contains high molecular weight polyesters in the component, but actual the use proved that the lacquer fluid viscosity is bigger, and the paint film that coats easily chaps, and the insulating property instability.USP5514747 has reported a kind of F level polyurethane enamelled wire that does not contain polyester.Hydroxy component " is generated by excessive polyvalent alcohol, vulcabond, polyvalent alcohol, diacid, trimellitic acid 1,2-anhydride and an amount of encapsulant reaction ".Isocyanate component " is generated by excessive vulcabond, polyvalent alcohol, diacid, trimellitic acid 1,2-anhydride and an amount of encapsulant reaction ".The lacquer fluid solid content is more than 40%, and the paint film over-all properties that coats is better, but reaction is reinforced for multistep, complex steps, and cost is higher.
At present, the production method that generally adopts of polyurethane wire enamel is as follows:
The preparation of step 1, hydroxy component:
With phthalic anhydride, dimethyl terephthalate (DMT), ethylene glycol, glycerine is that main raw material carries out copolycondensation, and catalyzer adopts zinc acetate, and solvent adopts cresols and dimethylbenzene.Maximum temperature reaches 250 ℃, and the production cycle needs more than 24 hours.The old technology that has also needs long-time high temperature, vacuum polycondensation, and time-consuming especially, effort increases energy consumption, and has a certain amount of waste discharge, has polluted environment.
The preparation of step 2, closure:
4,4 '-diphenylmethanediisocyanate, tolylene diisocyanate and xylenol with liquefaction are the main body reaction material, and reaction medium adopts the mixture of dimethylbenzene and cresols.Use liquefaction 4,4 '-diphenylmethanediisocyanate to increase raw materials cost.Use tolylene diisocyanate not only to increase cost, the more important thing is that tolylene diisocyanate has extremely strong volatilization toxicity, pollute production environment, the grievous injury workman is healthy.
The preparation of step 3, finished product lacquer:
The hydroxy component and the closure component of above-mentioned production are mixed stirring with a certain proportion of solvent and zinc naphthenate, remove by filter visible impurity and get product.
In order further to improve the quality of wire enamel, the manufacturer of wire enamel has also taked some innovative approachs both at home and abroad, but great majority only rest on the horizontal level that increases additive, inherent law to raw material structure and product performance lacks systematic study, traditional processing technology to wire enamel does not thoroughly improve, and most for applied basic research and prospect prediction, play-by-play is done at production formula, catalyzer, product over-all properties and a whole set of production technique end.Show that according to consulting in detail of documents and materials existing polyurethane wire enamel product remains in following problem demanding prompt solution with market study:
(1) the quality instability between the wire enamel batch;
(2) enameled wire exists more serious volts lost and salt solution pin hole problem after storing for some time;
(3) it is not good enough that the surface of enameled wire not only reaches hot punching performance;
(4) stability in storage of wire enamel is relatively poor;
(5) production cycle of wire enamel long, energy consumption is big etc.
Existing wire enamel can only use in the less demanding occasion of enameled wire, along with development of science and technology, people are more and more higher to the requirement of wire enamel, therefore, must join some shortcomings that wire enamel self exists to poly-ammonia and improve, keep its good characteristic unaffected simultaneously.
Summary of the invention:
The objective of the invention is to: the preparation method that a kind of novel B level high speed polyurethane wire enamel is provided.
Main raw material(s) involved in the present invention and source thereof:
Terephthalic acid Yangzi Petrochemical Corporation
Tetra hydro Phthalic anhydride Korea S AEKYUNG petro-chemical corporation
Hexanodioic acid Shanghai is rich along trade Co., Ltd
Neopentyl glycol MIT
2-methyl isophthalic acid, ammediol MIT
Huaiyin, glycerine Jiangsu brilliance laboratory
1,1,1-TriMethylolPropane(TMP) Germany BAYER company
4,4 '-diphenylmethanediisocyanate Yantai Wanhua Polyurethane Co., Ltd
Xylenol Shanghai Baoshan Iron and Steel Company
The cresols Mitsui
Dimethylbenzene Ningbo petrochemical industry import and export corporation, Korea S produces
The positive inferior Organic Chemical Plant in dimethyl formamide Changzhou
The positive inferior Organic Chemical Plant in N,N-DIMETHYLACETAMIDE Changzhou
Imperial chemical plant is avenged in zinc naphthenate (4%) Changzhou Wujin
The preparation method of novel B level polyurethane enamelled wire lacquer of the present invention comprises the steps:
The preparation of step 1, disubstituted fragrant dibasic alcohol
Adopt excessive dibasic alcohol (neopentyl glycol or 2-methyl isophthalic acid, ammediol) carries out esterification with aromatic dibasic acid (terephthalic acid or m-phthalic acid or phthalic acid) and prepare the disubstituted fragrant dibasic alcohol, catalyzer is organic titanium-antimony mixture, its consumption is 0.2%～1.5% of a reactant quality, wherein aromatic dibasic acid (terephthalic acid or m-phthalic acid or phthalic acid) and dibasic alcohol (neopentyl glycol or 2-methyl isophthalic acid, ammediol) mass ratio is 1: (2～5), above-mentioned reaction mass generated target product (disubstituted fragrant dibasic alcohol) in about 3 hours in reaction between 130 ℃～200 ℃, the fusing point of disubstituted fragrant dibasic alcohol is 40 ℃～50 ℃, hydroxyl value is 300～800, acid number≤3, more than fusing point, the disubstituted fragrant dibasic alcohol is a colourless transparent solution.Its reaction formula is as follows:
The disubstituted fragrant dibasic alcohol
Or
The preparation of step 2, hydroxy component
Hydroxy component is by the disubstituted fragrant dibasic alcohol, Tetra hydro Phthalic anhydride, hexanodioic acid, glycerine or 1,1, the 1-TriMethylolPropane(TMP), neopentyl glycol or 2-methyl 1, raw materials such as ammediol carry out melt co-polycondensation earlier and generate polyester polyol resin, and then add the mixed solvent of some amount and mix, the mass ratio of each reactant is: disubstituted fragrant dibasic alcohol: Tetra hydro Phthalic anhydride: hexanodioic acid: glycerine or 1,1,1-TriMethylolPropane(TMP): neopentyl glycol or 2-methyl isophthalic acid, ammediol equals 1: (2～6): (0.5～1.5): (1～3): (3～5), catalyzer is organic titanium-antimony mixture, its consumption is 0.2%～1.5% of a reactant quality, and the component of mixed solvent and mass ratio are: cresols: dimethylbenzene: dimethyl formamide or N,N-DIMETHYLACETAMIDE equal 2: (0.5～1.5): (0.5～1.5).The mass ratio of polyester polyol resin and mixed solvent is 1 in the hydroxy component: (0.8～1.5).In addition, at the initial stage of synthesis of hydroxy component, add 1%～5% of reactor volume.Dimethylbenzene, purpose is in time to remove in the system water that reaction generates, and accelerates reaction process.
In hydroxy component, add disubstituted fragrant dibasic alcohol and other raw material and carry out esterifying polycondensation, can make like this that system is in homogeneous state in the whole process of synthesizing polyester polyvalent alcohol, the top temperature of preparation polyester polyol is no more than 200 ℃, and normal pressure esterification and polycondensation time are no more than 5 hours; Avoided Yin Gaowen, the by product that brings of polycondensation for a long time effectively, stablized the quality of polyester polyol, thermotolerance and the thermal shock resistance properties of urethane paint film have also obtained improvement to a certain degree simultaneously.
In hydroxy component, introduce a certain amount of hexanodioic acid, can accelerate esterification, condensation polymerization speed on the one hand; Can increase the snappiness of paint film on the other hand.
Introduce a certain amount of trivalent alcohol in hydroxy component, purpose is to prepare the polyhydroxy polycarboxylic ester polyol, when film-forming and isocyanate reaction form thermal characteristics and the mechanical property that cross-linked network strengthens polyurethane wire enamel.But the trivalent alcohol consumption can cause that too much hydroxy component forms gel in building-up process, causes the polyester polyol downgrade, increases technology difficulty.
The alkyd ratio has bigger influence to molecular weight, acid number and the hydroxyl value etc. of polyester polyol in hydroxy component.Molecular weight is crossed conference and is caused the polyester polyol decreased solubility, and the lacquer fluid viscosity increases, and solid content descends, and is coated with the Wiring technology difficulty and increases; Too small thermal characteristics and the mechanical property that influences paint film of molecular weight.Acid number is bigger than normal, and residual carboxyl meeting catalysis hydrolysis of ester group influences the performance of paint film; Acid number too small meeting causing hydroxy component forms gel in building-up process, cause the polyester polyol downgrade, increases technology difficulty.The acid number of the polyester polyol of the present invention preparation for≤1, number-average molecular weight is 3000～6000, molecular weight distributing index is about 1.5～3.
In the reaction later stage of preparation polyester polyol, under the vacuum tightness of 0.01MPa-0.1MPa, 190 ℃ of pumpdown times are no more than 0.5 hour, and purpose is to extract the intact polyvalent alcohol of unreacted, less water and band aqua dimethylbenzene, impels polycondensation complete simultaneously.
The preparation of step 3, closure component:
With the reactor oven dry, add 4,4 '-diphenylmethanediisocyanate, dimethyl formamide or N,N-DIMETHYLACETAMIDE more earlier.Start stirrer, after the system for the treatment of fully all equates, Ji Liang adding 1 again, 1, the 1-TriMethylolPropane(TMP), stirring makes it dissolving, treat that system temperature is stable after, add the substituted aroma tertiary amine catalyst, slowly be warming up to 40 ℃-80 ℃, keep this thermotonus 1～3 hour, and adopted Di-n-Butyl Amine method titration isocyano-content, the transformation efficiency of control isocyano 2%～5%, add phenol (phenol or cresols or xylenol) then immediately, allow system temperature rise to 120 ℃～130 ℃ naturally, keep 135 ℃～138 ℃ reactions 3～4 hours, sampling and measuring isocyanic acid root gets final product less than 0.1%.
4,4 '-diphenylmethanediisocyanate, 1 in the raw material, 1, the mass ratio of 1-TriMethylolPropane(TMP), dimethyl formamide or N,N-DIMETHYLACETAMIDE, phenol is 1: (0.1～0.6): (1～7): (1～4), the consumption of substituted aroma tertiary amine catalyst are 0.01%～1% of reactant total mass.
The preparation of step 4, polyurethane wire enamel:
Hydroxy component, closure component and the mixed solvent of metering are mixed, the mass ratio of hydroxy component, closure component and mixed solvent is 1: (1～1.5): (1～3), mixed solution is heated to 30 ℃～80 ℃, and then the siccative zinc naphthenate of adding metering, and stir, after removing suspended impurity, press filtration makes the finished product lacquer.The lacquer liquid outward appearance be glassy yellow clear liquid, viscosity by the respective country standard test for being coated with four glasss 25 ℃, 20 seconds～60 seconds.
Above-mentioned mixed solvent is mixed by cresols, dimethylbenzene, dimethyl formamide or N,N-DIMETHYLACETAMIDE and forms, and their mass ratio is: cresols: dimethylbenzene: dimethyl formamide or N,N-DIMETHYLACETAMIDE equal 3: (1～2): (1～2); The consumption of zinc naphthenate is 0.1%～5% of lacquer liquid quality.
Originality that the present invention has and advantage:
1, in the production technique of hydroxy component, adopting organic titanium-antimony mixture is catalyzer, and with the disubstituted fragrant dibasic alcohol as reaction promoter, can be under the condition of 130 ℃-200 ℃ and synthesis under normal pressure, react and to produce the polyester polyol resin that every technical indicator all meets the polyurethane wire enamel service requirements in 5 hours, production cycle is about half of present industrial production cycle, simultaneously, has improved the thermotolerance and the mechanical property of the finished product.
2, in the production technique of closure component, adopt a kind of catalysis technique of substituted aroma tertiary amine, make 4,4 '-diphenylmethanediisocyanate and 1,1, in the time of the reaction of 1-TriMethylolPropane(TMP), 4,4 '-diphenylmethanediisocyanate self has 2%～5% energy trimerization Cheng Huan, form the isocyanurate ring that certain proportion has heat resistant structure, improve the mechanical property and the hot punching performance of enameled wire coat.
3, adopt solid 4,4 '-diphenylmethanediisocyanate replaces liquefied mdi, can stabilized product quality and reduction material cost.
4, in the production process of closure, be reaction medium with dimethyl formamide or N,N-DIMETHYLACETAMIDE, impel reacting balance to carry out effectively, reduce or avoid the generation of side reaction.
5, in lacquer man's skill of polyurethane wire enamel, add dimethyl formamide or N,N-DIMETHYLACETAMIDE, they can play the dual function of solvent and thinner, viscosity and the solid content that can regulate lacquer liquid in very wide scope are to satisfy different be coated with Wiring technology (felt and die methods) and the different requirements that are coated with line equipment (horizontal and vertical), be coated with the enameled wire of making various not collinear footpaths, wire range is 0.015mm～2.0mm, simultaneously, can reduce the consumption of toxic phenol again, help environmental protection, widened the application surface of polyurethane wire enamel.
Embodiment:
Embodiment 1
The preparation of step 1, disubstituted fragrant dibasic alcohol:
With 34 kilograms of terephthalic acids, 69 kilograms of neopentyl glycol, 0.16 kilogram of organic titanium-antimony composite catalyst, reaction can generate 92～95 kilograms of disubstituted fragrant dibasic alcohol in about 3 hours between 130 ℃-150 ℃, the disubstituted fragrant dibasic alcohol is colourless transparent solution more than fusing point, its fusing point is 45 ℃-50 ℃, and hydroxyl value is 550, acid number 2.7.
Synthesizing of step 2, hydroxy component:
47 kilograms of disubstituted fragrant dibasic alcohol, 94 kilograms of Tetra hydro Phthalic anhydrides, 25 kilograms of hexanodioic acids, 50 kilograms of glycerine, 150 kilograms of neopentyl glycol, organic titanium-0.6 kilogram and 10 kilograms dimethylbenzene of antimony composite catalyst are added in the reactor successively.Start heating unit, between 140 ℃～180 ℃, reacted 2 hours; Being warming up to 190 ℃ then kept 2 hours; Between 195 ℃-200 ℃, reacted 1 hour again; Begin to vacuumize, keep 190 ℃, 0.05MPa～0.1MPa, be evacuated to not have and slip out till the thing.Sampling records that acid number is 0.9, number-average molecular weight is 5500, molecular weight distributing index is 2.4.Add 160 kilograms of cresols, 80 kilograms of dimethylbenzene at last, 80 kilograms of N,N-DIMETHYLACETAMIDEs moltenly between 150 ℃～180 ℃ get final product to the system clear, obtain 650～660 kilograms hydroxy component.
The preparation of step 3, closure component:
With the reactor oven dry, add 4 again, 120 kilograms of 4 '-diphenylmethanediisocyanates, 140 kilograms of dimethyl formamides earlier.Start stirrer, behind the complete homogeneous phase of the system for the treatment of, adding 1,1,20 kilograms of 1-TriMethylolPropane(TMP)s stir and make it dissolving, after treating that system temperature is stable, start heating unit, slowly be warming up to 50 ℃～80 ℃, kept this thermotonus 1～3 hour, adopt Di-n-Butyl Amine method titration isocyano-content, the trimerization of control isocyano 2%～5% becomes the ring rate, when the content of isocyano reaches preset value, adds 150 kilograms of xylenols immediately, allow system rise to 120 ℃～130 ℃ naturally, keep 135 ℃～138 ℃ reactions 3～4 hours, sampling and measuring isocyanic acid root gets final product less than 0.1%, obtains 428～430 kilograms closure component.
The preparation of step 4, polyurethane wire enamel and enameled wire performance:
255 kilograms of hydroxy components, 325 kilograms of closures, 300 kilograms in cresols, 110 kilograms of dimethylbenzene, 110 kilograms of addings of N,N-DIMETHYLACETAMIDE are joined in the lacquer still, and then add 8 kilograms of zinc naphthenate siccative and stir, after removing suspended impurity, press filtration makes the finished product lacquer.The outward appearance of lacquer liquid is a glassy yellow clear liquid, and viscosity is for being coated with four glasss, 25 ℃, 35 seconds, and solid content is 26% (1 restrain, 180 ℃, 1 hour), obtains 1104～1108 kilograms B level high speed polyurethane wire enamel.The softening puncture temperature of enameled wire reaches 200 ℃, and it is 155 ℃ that heat is dashed, 30min, and 1D does not split, and 8000 volts～9000 volts of room temperature voltage breakdowns stretch and bending salt solution pin hole is zero hole, and 375 ℃ of solderabilities were less than 1 second.
Embodiment 2
The preparation of step 1, disubstituted fragrant dibasic alcohol
With 22 kilograms of terephthalic acids, 99 kilograms of neopentyl glycol, 0.24 kilogram of organic titanium-antimony composite catalyst, reaction can generate 114～115 kilograms of disubstituted fragrant dibasic alcohol in about 3 hours between 130 ℃-150 ℃, the disubstituted fragrant dibasic alcohol is colourless transparent solution more than fusing point, its fusing point is 42 ℃-46 ℃, and hydroxyl value is 750, acid number 1.6.
Synthesizing of step 2, hydroxy component
With 70 kilograms of 50 kilograms of disubstituted fragrant dibasic alcohol, 250 kilograms of Tetra hydro Phthalic anhydrides, hexanodioic acid, 1,1,150 kilograms of 1-TriMethylolPropane(TMP)s, 200 kilograms of neopentyl glycol, organic titanium-4 kilograms and 60 kilograms dimethylbenzene of antimony composite catalyst are added in the reactor successively.Start heating unit, between 140 ℃～180 ℃, reacted 2 hours; Being warming up to 190 ℃ then kept 2 hours; Between 195 ℃-200 ℃, reacted 1 hour again; Begin to vacuumize, keep 190 ℃, 0.05MPa～0.1MPa, be evacuated to not have and slip out till the thing.Sampling records that acid number is 0.6, number-average molecular weight is 4800, molecular weight distributing index is 2.1.Add 340 kilograms of cresols, 170 kilograms of dimethylbenzene at last, 180 kilograms of N,N-DIMETHYLACETAMIDEs moltenly between 150 ℃～180 ℃ get final product to the system clear, obtain 1380～1390 kilograms hydroxy component.
The preparation of step 3, closure
With the reactor oven dry, add 4 again, 200 kilograms of 4 '-diphenylmethanediisocyanates, 400 kilograms of dimethyl formamides earlier.Start stirrer, behind the complete homogeneous phase of the system for the treatment of, adding 1,1,90 kilograms of 1-TriMethylolPropane(TMP)s stir and make it dissolving, after treating that system temperature is stable, start heating unit, slowly be warming up to 50 ℃～80 ℃, kept this thermotonus 1～3 hour, adopt Di-n-Butyl Amine method titration isocyano-content, the trimerization of control isocyano 2%～5% becomes the ring rate, when the content of isocyano reaches preset value, adds 220 kilograms of xylenols immediately, allow system rise to 120 ℃～130 ℃ naturally, keep 135 ℃～138 ℃ reactions 3～4 hours, sampling and measuring isocyanic acid root gets final product less than 0.1%, obtains 908～910 kilograms closure component.
The preparation of step 4, polyurethane wire enamel and enameled wire performance
With 800 kilograms of hydroxy components, 900 kilograms of closures, 365 kilograms in cresols, 230 kilograms of dimethylbenzene, 200 kilograms of addings of dimethyl methyl ethanamide join the lacquer still in, 50 ℃, stir to clarify transparent.And then add 23 kilograms of zinc naphthenate siccative and stir, after removing suspended impurity, press filtration makes the finished product lacquer.The outward appearance of lacquer liquid is a glassy yellow clear liquid, and viscosity is for being coated with four glasss, 25 ℃, 25 seconds, and solid content is 36% (1 restrain, 180 ℃, 1 hour), obtains 2510～2518 kilograms B level high speed polyurethane wire enamel.The softening puncture temperature of enameled wire reaches 200 ℃, and it is 155 ℃ that heat is dashed, 30min, and 1D does not split, and 9000 volts～9500 volts of room temperature voltage breakdowns stretch and bending saline infusion needle zero hole, and 375 ℃ of solderabilities were less than 1 second.
Embodiment 3
The preparation of step 1, disubstituted fragrant dibasic alcohol
With 10 kilograms of terephthalic acids, 45 kilograms of 2-methyl isophthalic acid, ammediols, 0.15 kilogram of organic titanium-antimony composite catalyst, reaction can generate 47～48 kilograms of disubstituted fragrant dibasic alcohol in about 3 hours between 130 ℃-150 ℃, the disubstituted fragrant dibasic alcohol is colourless transparent solution more than fusing point, its fusing point is 40 ℃-45 ℃, and hydroxyl value is 760, acid number 1.7.
Synthesizing of step 2, hydroxy component
With 40 kilograms of 40 kilograms of disubstituted fragrant dibasic alcohol, 160 kilograms of Tetra hydro Phthalic anhydrides, hexanodioic acid, 1,1,80 kilograms of 1-TriMethylolPropane(TMP)s, 2-methyl isophthalic acid, 160 kilograms of ammediols, organic titanium-1.5 kilograms and 35 kilograms dimethylbenzene of antimony composite catalyst are added in the reactor successively.Start heating unit, between 140 ℃～180 ℃, reacted 2 hours; Being warming up to 190 ℃ then kept 2 hours; Between 195 ℃-200 ℃, reacted 1 hour again; Begin to vacuumize, keep 190 ℃, 0.05MPa～0.1MPa, be evacuated to not have and slip out till the thing.Sampling records that acid number is 0.3, number-average molecular weight is 3800, molecular weight distributing index is 2.5.Add 220 kilograms of cresols, 110 kilograms of dimethylbenzene at last, 120 kilograms of N,N-DIMETHYLACETAMIDEs moltenly between 150 ℃～180 ℃ get final product to the system clear, obtain 905～910 kilograms hydroxy component.
The preparation of step 3, closure
With the reactor oven dry, add 4 again, 200 kilograms of 4 '-diphenylmethanediisocyanates, 400 kilograms of dimethyl formamides earlier.Start stirrer, behind the complete homogeneous phase of the system for the treatment of, adding 1,1,90 kilograms of 1-TriMethylolPropane(TMP)s stir and make it dissolving, after treating that system temperature is stable, start heating unit, slowly be warming up to 50 ℃～80 ℃, kept this thermotonus 1～3 hour, adopt Di-n-Butyl Amine method titration isocyano-content, the trimerization of control isocyano 2%～5% becomes the ring rate, when the content of isocyano reaches preset value, adds 220 kilograms of xylenols immediately, allow system rise to 120 ℃～130 ℃ naturally, keep 135 ℃～138 ℃ reactions 3～4 hours, sampling and measuring isocyanic acid root gets final product less than 0.1%, obtains 908～910 kilograms closure component.
The preparation of step 4, polyurethane wire enamel and enameled wire performance
With 800 kilograms of hydroxy components, 900 kilograms of closures, 395 kilograms in cresols, 200 kilograms of dimethylbenzene, 200 kilograms of addings of dimethyl methyl ethanamide join the lacquer still in, 50 ℃, stir to clarify transparent.And then add 23 kilograms of zinc naphthenate siccative and stir, after removing suspended impurity, press filtration makes the finished product lacquer.The outward appearance of lacquer liquid is a glassy yellow clear liquid, and viscosity is for being coated with four glasss, 25 ℃, 25 seconds, and solid content is 36% (1 restrain, 180 ℃, 1 hour), obtains 2510～2518 kilograms B level high speed polyurethane wire enamel.The softening puncture temperature of enameled wire reaches 200 ℃, and it is 155 ℃ that heat is dashed, 30min, and 1D does not split, and 10000 volts～12000 volts of room temperature voltage breakdowns stretch and bending saline infusion needle zero hole, and 375 ℃ of solderabilities were less than 2 seconds.
Above-mentioned is of the present invention three routine specific embodiments, and embodiments of the present invention are a lot, as long as comprise above-mentioned four steps among the preparation method, in each step, the proportioning of each component all belongs to protection scope of the present invention within the limits prescribed.
Claims (2)
1, a kind of preparation method of novel B level polyurethane enamelled wire lacquer comprises the steps:
The preparation of step 1, disubstituted fragrant dibasic alcohol
Carry out esterification with aromatic dibasic acid and dibasic alcohol and prepare the disubstituted fragrant dibasic alcohol, catalyzer is organic titanium-antimony mixture, its consumption is 0.2%～1.5% of a reactant quality, wherein the mass ratio of aromatic dibasic acid and dibasic alcohol is 1: (2～5), above-mentioned reaction mass generated the disubstituted fragrant dibasic alcohol in about 3 hours in reaction between 130 ℃～200 ℃, the fusing point of disubstituted fragrant dibasic alcohol is 40 ℃～50 ℃, hydroxyl value is 300～800, acid number≤3, more than fusing point, the disubstituted fragrant dibasic alcohol is a colourless transparent solution, and its reaction formula is as follows:
The disubstituted fragrant dibasic alcohol
Or
The preparation of step 2, hydroxy component
Hydroxy component is by the disubstituted fragrant dibasic alcohol, Tetra hydro Phthalic anhydride, hexanodioic acid, glycerine or 1,1, the 1-TriMethylolPropane(TMP), neopentyl glycol or 2-methyl 1, raw materials such as ammediol carry out melt co-polycondensation earlier and generate polyester polyol, and then add the mixed solvent of some amount and mix, the mass ratio of each reactant is: disubstituted fragrant dibasic alcohol: Tetra hydro Phthalic anhydride: hexanodioic acid: glycerine or 1,1,1-TriMethylolPropane(TMP): neopentyl glycol or 2-methyl isophthalic acid, ammediol equals 1: (2～6): (0.5～1.5): (1～3): (3～5), catalyzer is organic titanium-antimony mixture, its consumption is 0.2%～1.5% of a reactant quality, the component of mixed solvent and mass ratio are: cresols: dimethylbenzene: dimethyl formamide or N,N-DIMETHYLACETAMIDE equal 2: (0.5～1.5): (0.5～1.5), the mass ratio of polyester polyol resin and mixed solvent is 1 in the hydroxy component: (0.8～1.5), in addition, at the initial stage of synthesis of hydroxy component, add 1%～5% of reactor volume.Dimethylbenzene; The maximum temperature of polyester polyol≤200 ℃, polycondensation time≤5 hour; In the reaction later stage of preparation polyester polyol, under the vacuum tightness of 0.01MPa-0.1MPa, 190 ℃ of pumpdown times are no more than 0.5 hour;
The preparation of step 3, closure component
With 4,4 '-diphenylmethanediisocyanate, dimethyl formamide or N,N-DIMETHYLACETAMIDE, 1,1, the 1-TriMethylolPropane(TMP) mixes stirring, after treating that system temperature is stable, add the substituted aroma tertiary amine catalyst, slowly be warming up to 40 ℃-80 ℃, kept this thermotonus 1～3 hour, adopt Di-n-Butyl Amine method titration isocyano-content, the transformation efficiency of control isocyano 2%～5% adds phenol then immediately, allows system temperature rise to 120 ℃～130 ℃ naturally, keep 135 ℃～138 ℃ reactions 3～4 hours, sampling and measuring isocyanic acid root gets final product less than 0.1%; 4,4 '-diphenylmethanediisocyanate, 1 in the raw material, 1, the mass ratio of 1-TriMethylolPropane(TMP), dimethyl formamide or N,N-DIMETHYLACETAMIDE, phenol is 1: (0.1～0.6): (1～7): (1～4), the consumption of substituted aroma tertiary amine catalyst are 0.01%～1% of reactant total mass;
The preparation of step 4, polyurethane wire enamel
Hydroxy component, closure component and the mixed solvent of metering are mixed, the mass ratio of hydroxy component, closure component and mixed solvent is 1: (1～1.5): (1～3), mixed solution is heated to 30 ℃～80 ℃, and then the siccative zinc naphthenate of adding metering, and stir, after removing suspended impurity, press filtration makes the finished product lacquer.The lacquer liquid outward appearance be glassy yellow clear liquid, viscosity by the respective country standard test for being coated with four glasss 25 ℃, 20 seconds～60 seconds; Above-mentioned mixed solvent is mixed by cresols, dimethylbenzene, dimethyl formamide or N,N-DIMETHYLACETAMIDE and forms, and their mass ratio is: cresols: dimethylbenzene: dimethyl formamide or N,N-DIMETHYLACETAMIDE equal 3: (1～2): (1～2); The consumption of zinc naphthenate is 0.1%～5% of lacquer liquid quality.
2, the preparation method of novel B level polyurethane enamelled wire lacquer according to claim 1, it is characterized in that: in step 1, described aromatic dibasic acid is any in terephthalic acid, m-phthalic acid, the phthalic acid; Described dibasic alcohol is neopentyl glycol or 2-methyl 1, ammediol; In step 3, described phenol is any in phenol, cresols, the xylenol.
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| Application Number | Priority Date | Filing Date | Title |
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| CN 200310112742 CN1635039A (en) | 2003-12-25 | 2003-12-25 | Method for preparing novel B level high speed polyurethane enamelled wire paint |
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| CN 200310112742 CN1635039A (en) | 2003-12-25 | 2003-12-25 | Method for preparing novel B level high speed polyurethane enamelled wire paint |
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| CN104017476A (en) * | 2014-05-30 | 2014-09-03 | 百川化工(如皋)有限公司 | Production method of 180-level polyurethane wire enamel |
| CN104017476B (en) * | 2014-05-30 | 2016-02-24 | 百川化工(如皋)有限公司 | A kind of production method of 180 level polyurethane enamelled wire paints |
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