CN104119543B - A kind of preparation method of nonionic ultraviolet light solidfication water polyurethane acrylate - Google Patents

A kind of preparation method of nonionic ultraviolet light solidfication water polyurethane acrylate Download PDF

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CN104119543B
CN104119543B CN201410337993.1A CN201410337993A CN104119543B CN 104119543 B CN104119543 B CN 104119543B CN 201410337993 A CN201410337993 A CN 201410337993A CN 104119543 B CN104119543 B CN 104119543B
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isocyanate ester
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CN104119543A (en
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刘晓亚
袁妍
刘敬成
张燕
刘仁
李治全
张胜文
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Weifang Wanfang Waterproof Engineering Co ltd
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Jiangnan University
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Abstract

A kind of preparation method of nonionic ultraviolet light solidfication water polyurethane acrylate, concrete preparation process is as follows: (1) is at 40 50 DEG C, to react 13 hours under the effect of poly glycol monomethyl ether and isocyanate ester compound catalyst, then add with isocyanate ester compound with the polyhydroxy base class secondary amine of mole at 50 60 DEG C;(2) by dihydroxylic alcohols and isocyanate ester compound with catalyst 40 50 DEG C of reactions, add the chain extender that step (1) obtains, after 50 70 DEG C of reactions 13 hours, add and dihydroxylic alcohols with the photosensitive monomer acrylate of mole 60 70 DEG C of reactions;(3) step (2) is obtained prepolymer and adds deionized water under stirring and light trigger carries out emulsifying 12 hours.This method building-up process is simple, and condition is controlled, and the emulsion obtained has good storage stability, and solid content is higher, can be used for functional paint, and fabric finish etc..

Description

A kind of preparation method of nonionic ultraviolet light solidfication water polyurethane acrylate
Technical field
The present invention relates to technical field of polymer materials, especially relate to two kinds of methods preparing ultraviolet light solidfication water polyurethane acrylate.
Background technology
The advantage that ultraviolet light solidfication water polyurethane combines photocuring technology and water paint, have efficiently, energy-saving and environmental protection, economy, the advantage of wide adaptability, it is applied in terms of the coating of woodenware, metal and plastic basis material, thus obtains the extensive concern of domestic and international researcher.What research in recent years was more is the aqueous polyurethane of anionic and cationic, because it contains ionic group, good hydrophilic property, there is easily emulsification, the advantage that emulsion storage stability is good, but the ultraviolet light solidfication water polyurethane of ionic is the most sensitive to electrolyte etc., is therefore subject to certain restrictions in the occasion being applied to electrolyte.Non-ion aqueous polyurethane does not have an ionic group, thus to acid, alkali, salt stability all preferable, and unparalleled electron structure, the most insensitive to electrolyte.
The method generally preparing non-ion aqueous polyurethane has two kinds, and one is that high speed shear obtains emulsion in the presence of external emulsifying agent, and another is hydrophilic radical or the hydrophilic segment of nonionic to be introduced in molecular structure.Using the emulsion that external emulsifying agent obtains, its technical process is difficult to control, and the polyaminoester emulsion storage stability obtained is poor, thus the method that the hydrophilic segment without ionic group is incorporated in polymer architecture generally used now so that it is there is hydrophilic interaction.
The many reports of patent is the preparation method about ionic photocuring waterborne polyurethane resin the most both at home and abroad.As the patent of number of patent application 200610038981.4 used dihydromethyl propionic acid introduce carboxyl, and introduce double bond, there is after neutralization hydrophily, obtain anionic photocuring aqueous polyurethane coating.This kind of method mainly increases the content of double bond by adding reactive diluent, in the patent of number of patent application 200810045778.9, point out that the patent of application number 200610038981.4 uses reactive diluent to increase the way of double bond content, cause adhesive force poor, and workmen's health is caused damage by the excitant of reactive diluent.
The patent of number of patent application 201110178207.6 use in-situ method prepare photocuring Waterborne Polyurethane Prepolymer, butyl acrylate (BA) and tripropylene glycol double methacrylate (TPGDA) is selected to regulate soft or hard section ratio as reactive diluent, the emulsion prepared is homogeneous, stable, has preferable mechanical property.But light-cured polyurethane double bond content prepared by the method is not the highest, causes hardening time longer, and gel content is the highest.
United States Patent (USP) US3920598 utilizes zerewitinoff Method by organic compound and the side chain with active hydrogen atom with repetitive (CH2CH2O) di-isocyanate reaction, obtains the non-ionic water polyurethane that can be dispersed in water.Polyethylene glycol is introduced in molecular structure, play the mainly methylol groups of hydrophilic interaction, have document report ethoxy repeating units to be positioned at side chain better than the hydrophily being positioned at main chain.With trimethylolpropane polyethoxy ether as hydrophilic chain extender in patent CN101638472A, hydrophilic radical polyethoxy is incorporated on side-chain structure, prepares the non-ion aqueous polyurethane emulsion with side-chain structure.Patent CN102432992A is pointed out, through repeatedly testing, the shelf-life of the non-ion aqueous polyurethane that use trimethylolpropane polyethoxy ether obtains is the shortest, and process of depositing easily is degraded rotten.
Summary of the invention
The problems referred to above existed for prior art, the applicant provides the preparation method of two kinds of nonionic ultraviolet light solidfication water polyurethane acrylate emulsions.This method building-up process is simple, and condition is controlled, and the emulsion obtained has good storage stability, and solid content is higher, can be used for functional paint, and fabric finish etc..
Technical scheme is as follows:
The preparation method of the first nonionic ultraviolet light solidfication water polyurethane acrylate, concrete preparation process is as follows:
(1) at 40-50 DEG C, poly glycol monomethyl ether and isocyanate ester compound are reacted 1-3 hour under the effect of catalyst with the ratio of mol ratio 1:1, wherein catalyst is the 0.02-0.03% of poly glycol monomethyl ether and isocyanate ester compound gross mass, then add with isocyanate ester compound with the polyhydroxy base class secondary amine of mole at 50-60 DEG C, continue reaction to the infrared transform spectrometer of Fourier and record the disappearance of NCO characteristic absorption peak, stop reaction, i.e. obtain the side chain chain extender with hydrophilic long-chain polymer;
(2) by dihydroxylic alcohols and isocyanate ester compound with the ratio of mol ratio 1:2 with catalyst 40-50 DEG C of reaction, wherein catalyst is the 0.02-0.03% of dihydroxylic alcohols and isocyanate ester compound gross mass, after measuring, by toluene-di-n-butylamine back titration method, the 2.6-2.8% that NCO group content reaches the most all addition reactant gross masses, add the chain extender that step (1) obtains, after 50-70 DEG C of reaction 1-3 hour, add and stop reaction with the photosensitive monomer acrylate of mole in 60-70 DEG C of reaction to the characteristic absorption peak disappearance recording NCO with FTIS with dihydroxylic alcohols, obtain nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer;
(3) step (2) is obtained prepolymer and under the mechanical agitation that temperature is 30 DEG C, adds deionized water and light trigger carries out emulsification 1-2 hour, obtain the emulsion that solid content is 10-40%.One or more in polyester diol and polyether Glycols of described dihydroxylic alcohols.
The preparation method of the second nonionic ultraviolet light solidfication water polyurethane acrylate emulsion, concrete preparation process is as follows:
(1) at 40-50 DEG C, poly glycol monomethyl ether and isocyanate ester compound are reacted 1-3 hour under the effect of catalyst with the ratio of mol ratio 1:1, wherein catalyst is the 0.01-0.05% of poly glycol monomethyl ether and isocyanate ester compound gross mass, then add with isocyanate ester compound with the polyhydroxy base class secondary amine of mole at 50-60 DEG C, continue reaction to the infrared transform spectrometer of Fourier and record the disappearance of NCO characteristic absorption peak, stop reaction, i.e. obtain the side chain chain extender with hydrophilic long-chain polymer;
(2) by PCDL and isocyanate ester compound with the ratio of mol ratio 1:2 with catalyst 40-50 DEG C of reaction, wherein catalyst is the 0.01-0.05% of PCDL and isocyanate ester compound gross mass, after measuring, by toluene-di-n-butylamine back titration method, the 2.6%-2.8% that NCO group mass content reaches the most all addition reactant gross masses, add the chain extender that step (1) obtains, after 50-70 DEG C of reaction 1-3 hour, add and stop reaction with the photosensitive monomer acrylate of mole in 60-70 DEG C of reaction to the characteristic absorption peak disappearance recording NCO with FTIS with PCDL, obtain nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer;
(3) step (2) is obtained prepolymer and under the mechanical agitation that temperature is 30 DEG C, adds deionized water and light trigger carries out emulsification 1-2 hour, obtain the emulsion that solid content is 10-40%.Described PCDL is selected from one or more in Merlon i.e. PCD, and T5650J, T5651, T5652 series PCDL of being produced of Asahi Kasei Corporation.
The molecular weight of described poly glycol monomethyl ether is 500-2000;
One or more in IPDI, toluene di-isocyanate(TDI), MDI, hexamethylene diisocyanate, meta-xylene diisocyanate or 4,4 '-dicyclohexyl methyl hydride diisocyanate of described isocyanate ester compound;
One or more in the secondary amine with two and two or more hydroxy functional group of described polyhydroxy base class secondary amine, preferably one or more in diethanol amine, diisopropanolamine (DIPA), methyl diethanolamine;
One or more in hydroxyethyl methacrylate, hydroxy-ethyl acrylate, hydroxypropyl acrylate, pentaerythritol triacrylate of described photosensitive monomer acrylate;
Step (1) and one or more in tertiary amine catalyst, organic tin catalyst of (2) described catalyst;
Described light trigger includes radical photoinitiator, cationic photoinitiator, alpha-alcohol ketone photoinitiator or α-aminoketone photoinitiator, consumption is the 1-5% of step (2) gained prepolymer gross mass, concrete, light trigger includes one or more in 1173,184,2959,907,369;
Wherein, reactant gross mass in the 2.6-2.8% of all addition reactant gross masses " NCO group content reach " in the step (2) of two kinds of methods, refer to the dihydroxylic alcohols in the poly glycol monomethyl ether in step (1), isocyanate ester compound, catalyst, polyhydroxy base class secondary amine, and step (2), isocyanate ester compound, the gross mass of catalyst.
The present invention uses three-step reaction, is accessed on urethane acrylate side chain by hydrophilic long-chain polymer, and then obtains novel nonionic ultraviolet light solidfication water polyurethane acrylate emulsion.Detailed process is: first passes through poly glycol monomethyl ether and reacts with isocyanates and polyhydroxy secondary amine, prepares the side chain glycol chain extender with hydrophilic long-chain;The intermediate obtaining two ends with unreacted isocyanate group is reacted subsequently with dihydroxylic alcohols and isocyanates;Last chain extender and the photosensitive monomer acrylate that the addition first step obtains in above-mentioned intermediate continues reaction, finally give nonionic ultraviolet light solidfication water polyurethane acrylate performed polymer, by emulsified in mechanical agitation according to a certain ratio to this performed polymer and deionized water, prepare nonionic ultraviolet light solidfication water polyurethane acrylate emulsion.
Specific to detailed raw material and step, the preparation thinking of the present invention is such that first passing through poly glycol monomethyl ether and prepares the side chain hydrophilic chain extender with polyethoxy group with IPDI and diethanol amine reaction, by two-step method reaction, the above-mentioned chain extender prepared is incorporated in urethane acrylate segmented structure, prepare nonionic UV-cured polyurethane acrylate prepolymer, and then obtain photocuring aqueous polyurethane acrylate emulsion.
Useful the having the technical effect that of the present invention
The nonionic ultraviolet light solidfication water polyurethane acrylate that the present invention prepares, it is not necessary to additional emulsifying agent can be dispersed in water;By preparing the side chain method with hydrophilic long-chain polymer chain extender, the emulsion storage stability prepared is preferable;The advantage of photocuring technology being combined with non-ionic water polyurethane acid and alkali-resistance, salt tolerant, the performance of electrolyte-resistant, expand the range of application of non-ionic water polyurethane, the coating obtained has the excellent properties such as high, water-fast, the acid and alkali-resistance of intensity;The final products emulsion particle diameter obtained, within 50-200nm, has good storage stability, and solid content is high, and curing rate is fast, environmentally friendly.
Accompanying drawing explanation
Fig. 1 is embodiment 1 ~ 3 nonionic ultraviolet light solidfication water polyurethane acrylate infrared spectrum;
Fig. 2 is embodiment 1 ~ 3 nonionic ultraviolet light solidfication water polyurethane acrylate emulsion particle diameter distribution map;
Fig. 3 is embodiment 5 nonionic ultraviolet light solidfication water polyurethane acrylate infrared spectrum;
Fig. 4 is embodiment 5 nonionic ultraviolet light solidfication water polyurethane acrylate emulsion particle diameter distribution map.
Detailed description of the invention
Embodiment 1
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic long-chain polymer
Take 11.12 grams of (0.05mol) IPDIs and add in there-necked flask, and take 50 grams of poly glycol monomethyl ether (molecular weight: 1000,0.05mol), add the catalyst dibutyltin dilaurylate of 0.018 gram, dropping is started at 45 DEG C, react 2 hours, until recording NCO group content by toluene-di-n-butylamine method to reach theoretical value 3.44%, add diethanol amine 5.26 grams (0.05mol), it is warming up to 50 DEG C, continue reaction 2 hours, stop to recording the disappearance of NCO characteristic absorption peak with the infrared transform spectrometer of Fourier;
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the PTMG dihydroxylic alcohols (PTMG) 100 grams (0.1mol) of 110mgKOH/g, IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 3 hours under 40 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 55 DEG C and reacts 2 hours;After NCO content reaches 2.61%, adding the photosensitive monomer hydroxyethyl methacrylate (HEMA) 13 grams (0.1mol) with unsaturated double-bond and be warming up to 60 DEG C of reactions 3 hours, disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction;
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
The prepolymer 10 grams obtained by (2) is put in there-necked flask, 0.417 gram of light trigger 184 is added at 30 DEG C, mechanical agitation 30 minutes, after add under high velocity agitation deionized water 24.3 grams emulsify 1.5 hours, obtain the nonionic ultraviolet light solidfication water polyurethane emulsion of transparent blue light.The emulsion obtained is deviate from solvent in 30 minutes 35 DEG C of decompression distillations, obtains the nonionic ultraviolet light solidfication water polyurethane emulsion that solid content is 30%.
Embodiment 2
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic long-chain polymer
As shown in embodiment 1 step (1);
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the polyoxypropyleneglycol (PPG) 100 grams (0.1mol) of 110mgKOH/g, IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 3 hours under 40 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 55 DEG C and reacts 2.5 hours;After NCO content reaches 2.71%, adding the photosensitive monomer hydroxyethyl methacrylate (HEMA) 13 grams (0.1mol) with unsaturated double-bond and be warming up to 65 DEG C of reactions 2 hours, disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction;
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
As shown in embodiment 1 step (3).
Embodiment 3
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic radical
As shown in embodiment 1 step (1);
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the polycaprolactone glycol (PCL) 100 grams (0.1mol) of 109-119mgKOH/g, IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 1 hour under 50 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 60 DEG C and reacts 2 hours;After NCO content reaches 2.63%, adding the photosensitive monomer hydroxyethyl methacrylate (HEMA) 13 grams (0.1mol) with unsaturated double-bond and be warming up to 70 DEG C of reactions 1.5 hours, disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction;
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
As shown in embodiment 1 step (3).
Embodiment 4
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic radical
As shown in embodiment 1 step (1);
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the polycaprolactone glycol (PCL) 100 grams (0.1mol) of 109-119mgKOH/g, IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 3 hours under 45 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 55 DEG C and reacts 3 hours;After NCO content reaches 2.68%, addition hydroxyl value is 160mgKOH/g, photosensitive monomer pentaerythritol triacrylate (PETA) 34.9 grams (0.1mol) with unsaturated double-bond is warming up to 60 DEG C of reactions 1.5 hours, and disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction;
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
As shown in embodiment 1 step (3).
Fig. 1 is the infrared spectrum of embodiment 1-3, is positioned at 2270cm in figure-1Place's NCO group characteristic peak all disappears, and indicates carrying out completely of reaction;
Fig. 2 is the emulsion particle diameter figure of embodiment 1-3, and along with the difference of addition dihydroxylic alcohols kind in figure, emulsion particle diameter differs, in the range of being positioned at 70-160 nm.Wherein WPU is aqueous polyurethane.
Embodiment 5
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic long-chain polymer
Take 11.12 grams of (0.05mol) IPDIs and add in there-necked flask, and take 50 grams of poly glycol monomethyl ether (molecular weight: 1000,0.05mol), add the catalyst dibutyltin dilaurylate of 0.018 gram, dropping is started at 45 DEG C, react 3 hours, until recording NCO group content by toluene-di-n-butylamine method to reach theoretical value 3.44%, add diethanol amine 5.26 grams (0.05mol), it is warming up to 50 DEG C, continue reaction 2 hours, stop to recording the disappearance of NCO characteristic absorption peak with the infrared transform spectrometer of Fourier.
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the PCDL (PCD) 50 grams (0.1mol) of 100-120mgKOH/g, IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 2.5 hours under 45 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO functional group content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 50 DEG C and reacts 3 hours;After NCO functional group content reaches 2.61%, adding and be warming up to 60 DEG C with the photosensitive monomer hydroxyethyl methacrylate (HEMA) 13 grams (0.1mol) of unsaturated double-bond and react 2 hours, Fig. 3 uses FTIS to record to be positioned at 2250 cm-1The characteristic absorption peak of place NCO, along with reaction is carried out, NCO characteristic peak is progressively smaller until disappearance, illustrates that reaction carries out completely, can stop reaction.
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
The prepolymer 10 grams obtained by (2) is put in there-necked flask, 0.417 gram of light trigger 184 is added at 30 DEG C, mechanical agitation 30 minutes, after add under high velocity agitation deionized water 24.3 grams emulsify 1.5 hours, obtain the nonionic ultraviolet light solidfication water polyurethane emulsion of transparent blue light.The emulsion obtained is deviate from solvent in 30 minutes 35 DEG C of decompression distillations, obtains the nonionic ultraviolet light solidfication water polyurethane emulsion that solid content is 30%.
Embodiment 6
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic radical
As shown in embodiment 5 step (1).
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
It is 1000 by number-average molecular weight, hydroxyl value is the PCDL (T5651) 50 grams (0.1mol) of 100-120mgKOH/g, toluene di-isocyanate(TDI) (TDI) 34.8 grams (0.2mol) joins in reaction vessel, reacts 3 hours under 50 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 9.91%, adds chain extender 66.3 grams prepared by (1), is warming up to 50 DEG C and reacts 2 hours;After NCO content reaches 2.78%, adding the photosensitive monomer hydroxyethyl methacrylate (HEMA) 13 grams (0.1mol) with unsaturated double-bond and be warming up to 65 DEG C of reactions 3 hours, disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction.
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
As shown in embodiment 5 step (3).
Embodiment 7
(1) side chain is with the synthesis of the chain extender with two hydroxyls of hydrophilic radical
As shown in embodiment 5 step (1).
(2) synthesis of nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer
Being 2000 by number-average molecular weight, PCDL (T5652) 200 grams (0.1mol), IPDI (IPDI) 44.4 grams (0.2mol) joins in reaction vessel, reacts 3 hours under 40 DEG C of mechanical agitation;Toluene-di-n-butylamine method records after NCO content reaches 8.90%, adds chain extender 66.3 grams prepared by (1), is warming up to 55 DEG C and reacts 1.5 hours;After NCO content reaches 2.61%, addition hydroxyl value is 160mgKOH/g, photosensitive monomer pentaerythritol triacrylate (PETA) 34.9 grams (0.1mol) with unsaturated double-bond is warming up to 70 DEG C of reactions 1 hour, and disappearing to the characteristic absorption peak recording NCO with FTIS to stop reaction.
(3) synthesis of nonionic ultraviolet light solidfication water polyurethane emulsion
As shown in embodiment 5 step (3).Fig. 4 gives the grain size distribution of embodiment 5 and 7 gained aqueous polyurethane emulsion.It can be seen that the HEMA end-blocking emulsion particle diameter using the photosensitive monomer PETA that degree of functionality is big to block gained emulsion particle diameter less than degree of functionality is big.
Above-described embodiment is used for illustrating the present invention rather than limiting the invention, in the protection domain of spirit and claims of the present invention, and any modifications and changes that the present invention is made, both fall within protection scope of the present invention.

Claims (13)

1. a preparation method for nonionic ultraviolet light solidfication water polyurethane acrylate, concrete preparation process is as follows:
(1) at 40-50 DEG C, poly glycol monomethyl ether and isocyanate ester compound are reacted 1-3 hour under the effect of catalyst with the ratio of mol ratio 1:1, wherein catalyst is the 0.02-0.03% of poly glycol monomethyl ether and isocyanate ester compound gross mass, then add with isocyanate ester compound with the polyhydroxy base class secondary amine of mole at 50-60 DEG C, continue reaction to the infrared transform spectrometer of Fourier and record the disappearance of NCO characteristic absorption peak, stop reaction, i.e. obtain the side chain chain extender with hydrophilic long-chain polymer;
Characterized by further comprising:
(2) by dihydroxylic alcohols and isocyanate ester compound with the ratio of mol ratio 1:2 with catalyst 40-50 DEG C of reaction, wherein catalyst is the 0.02-0.03% of dihydroxylic alcohols and isocyanate ester compound gross mass, after measuring, by toluene-di-n-butylamine back titration method, the 2.6-2.8% that NCO group content reaches the most all addition reactant gross masses, add the chain extender that step (1) obtains, after 50-70 DEG C of reaction 1-3 hour, add and stop reaction with the photosensitive monomer acrylate of mole in 60-70 DEG C of reaction to the characteristic absorption peak disappearance recording NCO with FTIS with dihydroxylic alcohols, obtain nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer;
(3) step (2) is obtained prepolymer and under the mechanical agitation that temperature is 30 DEG C, adds deionized water and light trigger carries out emulsification 1-2 hour, obtain the emulsion that solid content is 10-40%.
2. a preparation method for nonionic ultraviolet light solidfication water polyurethane acrylate emulsion, concrete preparation process is as follows:
(1) at 40-50 DEG C, poly glycol monomethyl ether and isocyanate ester compound are reacted 1-3 hour under the effect of catalyst with the ratio of mol ratio 1:1, wherein catalyst is the 0.01-0.05% of poly glycol monomethyl ether and isocyanate ester compound gross mass, then add with isocyanate ester compound with the polyhydroxy base class secondary amine of mole at 50-60 DEG C, continue reaction to the infrared transform spectrometer of Fourier and record the disappearance of NCO characteristic absorption peak, stop reaction, i.e. obtain the side chain chain extender with hydrophilic long-chain polymer;
Characterized by further comprising:
(2) by PCDL and isocyanate ester compound with the ratio of mol ratio 1:2 with catalyst 40-50 DEG C of reaction, wherein catalyst is the 0.01-0.05% of PCDL and isocyanate ester compound gross mass, after measuring, by toluene-di-n-butylamine back titration method, the 2.6%-2.8% that NCO group mass content reaches the most all addition reactant gross masses, add the chain extender that step (1) obtains, after 50-70 DEG C of reaction 1-3 hour, add and stop reaction with the photosensitive monomer acrylate of mole in 60-70 DEG C of reaction to the characteristic absorption peak disappearance recording NCO with FTIS with PCDL, obtain nonionic ultraviolet light solidfication water polyurethane acrylate prepolymer;
(3) step (2) is obtained prepolymer and under the mechanical agitation that temperature is 30 DEG C, adds deionized water and light trigger carries out emulsification 1-2 hour, obtain the emulsion that solid content is 10-40%.
Preparation method the most according to claim 1, it is characterised in that one or more in polyester diol and polyether Glycols of described dihydroxylic alcohols.
Preparation method the most according to claim 2, it is characterised in that described PCDL is selected from one or more in Merlon i.e. PCD, and T5650J, T5651, T5652 series PCDL of being produced of Asahi Kasei Corporation.
Preparation method the most according to claim 1 and 2, it is characterised in that the molecular weight of described poly glycol monomethyl ether is 500-2000.
Preparation method the most according to claim 1 and 2, it is characterized in that one or more in IPDI, toluene di-isocyanate(TDI), MDI, hexamethylene diisocyanate, meta-xylene diisocyanate or HMDI of described isocyanate ester compound.
Preparation method the most according to claim 1 and 2, it is characterised in that one or more in the secondary amine with two and two or more hydroxy functional group of described polyhydroxy base class secondary amine.
8. according to the preparation method described in claim 1 or 2 or 7, it is characterised in that one or more in diethanol amine, diisopropanolamine (DIPA), methyl diethanolamine of described polyhydroxy base class secondary amine.
Preparation method the most according to claim 1 and 2, it is characterised in that one or more in hydroxyethyl methacrylate, hydroxy-ethyl acrylate, hydroxypropyl acrylate, pentaerythritol triacrylate of described photosensitive monomer acrylate.
Preparation method the most according to claim 1 and 2, it is characterised in that step (1) and one or more in tertiary amine catalyst, organic tin catalyst of (2) described catalyst.
11. preparation methods according to claim 1 and 2, it is characterised in that described light trigger includes one or more in radical photoinitiator, cationic photoinitiator, consumption is the 1-5% of step (2) gained prepolymer gross mass.
12. preparation method according to claim 1 and 2, it is characterised in that described light trigger includes one or more in alpha-alcohol ketone photoinitiator or α-aminoketone photoinitiator.
13. preparation methods according to claim 1 and 2, it is characterised in that described light trigger includes one or more in 1173,184,2959,907,369.
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