CN104231209B - Preparation method for high-hardness waterborne polyurethane dispersion - Google Patents
Preparation method for high-hardness waterborne polyurethane dispersion Download PDFInfo
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- CN104231209B CN104231209B CN201410498604.3A CN201410498604A CN104231209B CN 104231209 B CN104231209 B CN 104231209B CN 201410498604 A CN201410498604 A CN 201410498604A CN 104231209 B CN104231209 B CN 104231209B
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- C08G18/00—Polymeric products of isocyanates or isothiocyanates
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- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
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Abstract
The invention discloses a preparation method for high-hardness waterborne polyurethane dispersion. An inorganic nano material and waterborne polyurethane are grafted through an in-situ polymerization method, so that the hybridization reaction of inorganic materials and the organic materials is realized and complementary advantages are realized. The preparation method comprises the following operation steps: adding polyisocyanate, macromolecule polyol, a catalyst, a chain extender and a silane coupling agent according to certain weight ratio in a flask for reacting to obtain a polyurethane prepolymer; after the reaction is ended, sequentially adding a neutralizer, inorganic nano material dispersion liquid and deionized water under the condition of low-temperature and high-speed stirring; finally, heating under the vacuum condition for removing the solvent to obtain the high-hardness waterborne polyurethane dispersion. Compared with the traditional inorganic and organic blending process, the preparation method has the characteristics that products prepared through the preparation method have the advantages of good stability, excellent water resistance, long-time aging resistance, excellent and high adhesion, high drying speed, high hardness, good fullness, higher light transmittance and the like, and are wide in application range.
Description
Technical field
The invention belongs to water-based industrial paint uses emulsion technology field, more particularly to a kind of high rigidity aqueous polyurethane point
The preparation method of dispersion liquid.
Background technology
From early 1990s, World Developed Countries have just started " Green revolution ", drive paint industry to " green
The big step of the color " line of production is strided forward.It is into 21 century since, further perfect with environmental regulation, to mitigate earth load be
Purpose and the research of the water paint of low VOC emission carried out, just become the emphasis of research and development increasingly.Traditional oiliness industrial paint is big
The discharge Organic substance of amount, on the one hand directly affects the healthy of people;On the other hand it can in atmosphere with other chemicals
There is chemical reaction in matter, form PM2.5, cause atmospheric pollution, and annual solvent based coating is discharged organic in use
The PM2.5 that volatile matter is formed, is only second to the pollution that vehicle exhaust is caused to air.And by contrast, water-based industrial paint has nothing
Poison ring guarantor, odorlessness, volatilizable thing is few, the advantages of do not fire not quick-fried, can effectively solve the formed PM2.5's of solvent based coating
Emission problem, therefore the Water-borne modification of industrial paint will be trend of the times.Aqueous pu dispersions are plentiful, beautiful because of its paint film, tool
Have the advantages that excellent rotproofness, chemical proofing, weatherability, resistance to water, adhesive force are good, but its difference of hardness, easily scratch, it is dry
Dry slow the shortcomings of, significantly limit application of the aqueous pu dispersions in water-based industrial paint.Traditional inorganic material with
Aqueous polyurethane blending method, although can effectively solve the problem that the problem of waterborne polyurethane paint film lower hardness, but also to a great extent
On have impact on the water resistance of waterborne polyurethane paint film, it is impossible to tackle the problem at its root.
The content of the invention
It is an object of the invention to overcome the deficiencies in the prior art, there is provided a kind of system of high rigidity aqueous pu dispersions
Preparation Method, can be on the premise of not affecting paint film water-fast, and effectively solving aqueous pu dispersions hardness of paint film is low, easily draw
Wound, the problem of slow drying speed.
Another object of the present invention is to solve inorganic material in coating production process be difficult to be distributed in water-base resin
Problem, improves the storage stability of coating.
In order to achieve the above object, the present invention is employed the following technical solutions, and its step of preparation process is as follows:
1st, macromolecular polyol is added in flask, in temperature 100-140 DEG C, bar of the vacuum in 0.01-0.04MPa
1-3 hours are dehydrated under part, 30-90 DEG C is cooled to;
2nd, will be 1 with macromolecular polyol weight ratio:During the polyisocyanates of 1.5-50 adds flask, lead to nitrogen protection,
1-2 hours are reacted at 60-100 DEG C, adopts di-n-butylamine titrimetry to judge reaction end in course of reaction;
3rd, it is 1 to add in flask with macromolecular polyol weight ratio at 40-70 DEG C:The hydrophilic chain extender of 0.1-0.8,
Small molecule chain extender and account for dispersion quality fraction 0.01-0.1% catalyst that dispersion quality fraction is 0.1-2% are accounted for, then
2-4 hours are reacted at 70-85 DEG C;
4th, 40-70 DEG C is cooled to, addition accounts for dispersion quality fraction 20-80% solvents and reduces system viscosity, continues reaction 1-
2 hours;
5th, 10-40 DEG C is cooled to, addition accounts for the silane coupler of the 0.5-5% of dispersion quality fraction, 10-100 point of reaction
Clock, obtains base polyurethane prepolymer for use as;
6th, it is under low whipping speed is for the stirring condition of 300-1500rpm, described in base polyurethane prepolymer for use as Deca and step (3)
Hydrophilic chain extender material amount ratio be 1:The nertralizer of 0.8-1.2, reacts 1-10 minutes, obtains the polyurethane prepolymer for neutralizing
Body;
7th, under low whipping speed is for the stirring condition of 300-1500rpm, adds in the base polyurethane prepolymer for use as of neutralization and account for point
The nano inorganic material aqueous solution of prose style free from parallelism mass fraction 10-50%, concentration for 10-60wt%, reacts 1-10 minutes;
8th, under low whipping speed is for the stirring condition of 300-1500rpm, continue in above-mentioned base polyurethane prepolymer for use as, slowly
Deca accounts for the deionized water that dispersion quality fraction is 60~70%, finally adds the 0.5-5%'s that accounts for dispersion quality fraction
Rear chain extender reacts 10-60 minutes, forms dispersions of polyurethanes;
9th, under the conditions of vacuum is 0.01-0.04MPa, 20-80 minutes are reacted in 40-80 DEG C, during elimination reaction
The solvent for being added, is just obtained a kind of high rigidity aqueous pu dispersions.
Macromolecular polyol described in step (1) selected from molecular weight be the polyether polyol of 600-5000, PEPA,
One or more amount in sulfonated polyether polyhydric alcohol, sulfonated polyester polyol and reduced branching degree PEPA.
Polyisocyanates described in step (2) selected from toluene di-isocyanate(TDI) (TDI), 4,4 '-diphenyl methane two is different
Cyanate (MDI), 4,4'- dicyclohexyl methyl hydride diisocyanates (HMDI), isophorone diisocyanate (IPDI), six first
In group diisocyanate (HDI), XDI (XDI) and poly methylene poly phenyl poly isocyanate (PAPI)
One or more.
Hydrophilic chain extender described in step (3) is selected from dihydromethyl propionic acid (DMPA), dimethylolpropionic acid (DMBA), second two
One or more in amido ethyl sulfonic acid sodium and 1,4- butanediol -2- sodium sulfonates.
Small molecule chain extender described in step (3) selected from diglycol, 1,4- butanediols, neopentyl glycol, oneself two
One or more in alcohol, trimethylolpropane.
Catalyst described in step (3) be selected from dibutyl tin laurate, stannous octoate, N, mono- dimethyl cyclohexyl amines of N,
One or more in triethylenediamine.
One or more in solvent selected from acetone, butanone or toluene described in step (4).
Silane coupler described in step (5) selected from methacryloxypropyl trimethoxy silane (KH570), γ-
Aminopropyl triethoxysilane (KH550), γ-glycidyl ether oxygen propyl trimethoxy silicane (KH560), anilinomethyl three
One kind in methoxy silane, anilino- triethoxysilane.
The one kind of nertralizer described in step (6) in sodium hydroxide, ammonia, triithylamine.
Nano inorganic material aqueous solution described in step (7) is selected from Ludox, nano silicon aqueous solution, nano-silica
Change the one kind in aluminum water solution, nano-calcium carbonate aqueous solution.
Rear chain extender described in step (8) is selected from ethylenediamine, in diamidogen, diethylenetriamines and isophorone diamine
It is a kind of.
Nano inorganic material and aqueous polyurethane by situ aggregation method, are carried out graft reaction, are utilized by patent of the present invention
The reaction of the isocyano of the hydroxyl of nano inorganic material particle surface and base polyurethane prepolymer for use as in nano inorganic material aqueous solution
Activity, is better than the reactivity of water and the isocyano of base polyurethane prepolymer for use as, gathers so as to nano inorganic material is grafted to aqueouss
The hydridization reaction of inorganic-organic material on urethane strand, is realized well, both ensure that resistance to water and the attachment of paint film
Power, the problems such as efficiently solve low waterborne polyurethane paint film hardness, easy scuffing and slow drying speed again.Because inorganic material with it is organic
The membrane formation mechanism of material is different, and inorganic material is grafted on the strand of organic resin, can effectively improve the dry of water-based industrial paint
Dry speed.Inorganic material has the advantages such as hardness is high, ageing-resistant, chemicals-resistant is good, and organic material has water-tolerant, gloss
Degree is high, the excellent advantage of adhesive force, and the two makes up for each other's deficiencies and learn from each other, and reaches effective performance complement, excellent so as to forming properties
Water-based industrial paint.The present invention makes inorganic material effectively be distributed to aqueouss tree using rationally perfect operating procedure and technological parameter
In fat, the storage stability of coating is improve.
Specific embodiment
The invention is further illustrated by the following examples, but the embodiment is merely to illustrate the present invention rather than restriction
The present invention.
Embodiment 1
The PEPA that molecular weight is 2000 is added in four-neck flask, is 120 DEG C in temperature, vacuum is
Under conditions of 0.02MPa, be dehydrated 2 hours, cool to 60 DEG C it is standby.Toluene di-isocyanate(TDI) (TDI) and PEPA are pressed
Weight compares 1:During 3 dehydrations add four-neck flask, lead to nitrogen protection, react 2 hours at 70 DEG C, be cooled at 60 DEG C and add and polyester
Polyol quality ratio is 1:0.2 dimethylolpropionic acid, 1,4 butanediols for accounting for dispersion quality fraction 4% and account for dispersion quality
The dibutyl tin laurate of fraction 0.05%, then reacts 4 hours at 80 DEG C;60 DEG C are cooled to, addition accounts for dispersion quality
The acetone of fraction 20% reduces system viscosity, reacts 1 hour.Continue to be cooled to 30 DEG C, addition accounts for dispersion quality fraction 1%
KH550, reacts 20 minutes, and it is 1 to be rapidly added under 500rpm stirrings with the amount ratio of the material of dimethylolpropionic acid:1 three second
Ammonia, subsequent low whipping speed are 500rpm, sequentially add and account for dispersion quality fraction 10%, and concentration is 30wt% nano silicons
Aqueous solution and the deionized water that dispersion quality fraction is 70% is accounted for, add the second two for accounting for that dispersion quality fraction is 0.5%
Amine react 10 minutes, formed dispersions of polyurethanes, finally by above-mentioned dispersion vacuum be 0.02MPa, temperature is 60 DEG C
Under the conditions of react 60 minutes, remove acetone, obtain aqueous pu dispersions.It is applied on glass plate, film thickness is 20
Micron, its hardness >=2H, water-fast 120 hours non-whitenings, 15 minutes non-whitenings of resistance to boiling water, alkaline-resisting, resistance to alcohol without exception, painting in 1 hour
Layer light transmittance is unchanged.
Embodiment 2
The sulfonated polyester polyol that molecular weight is 2000 is added in four-neck flask, is 120 DEG C in temperature, vacuum is
Under conditions of 0.02MPa, be dehydrated 2 hours, cool to 60 DEG C it is standby.By methyl diphenylene diisocyanate (MDI) and molecular weight
For 2000 PEPA by weight 1:During 4 dehydrations add four-neck flask, lead to nitrogen protection, react 1 hour at 70 DEG C, drop
It is 1 that temperature is added with sulfonated polyester polyol mass ratio to 60 DEG C:0.1 dimethylolpropionic acid, addition account for dispersion quality fraction and are
2% diglycol and the dibutyl tin laurate that dispersion quality fraction is 0.02% is accounted for, then 4 are reacted at 80 DEG C
Hour;Addition accounts for the acetone that dispersion quality fraction is 45% and reacts 30 minutes, is cooled to 30 DEG C, and addition accounts for dispersion quality point
Number is 2.5% silane coupler KH560, is reacted 30 minutes, and low whipping speed is 1300rpm, is rapidly added and dimethylolpropionic acid
The amount ratio of material is 1:1 triithylamine, it is 20wt% subsequently to sequentially add concentration, accounts for the nanometer two that dispersion quality fraction is 10%
Calcium oxide aqueous solution and account for the deionized water that dispersion quality fraction is 60% and add that to account for dispersion quality fraction be 1.5%
Isophorone diamine, reacts 20 minutes, forms dispersions of polyurethanes, is 0.02MPa in vacuum by above-mentioned dispersion, and temperature is
Under the conditions of 60 DEG C, 30 minutes removing butanone are reacted, aqueous pu dispersions are obtained.It is applied on glass plate, film thickness
For 10 microns, up to >=2H, water-fast 120 hours non-whitenings, 15 minutes non-whitenings of resistance to boiling water, alkaline-resisting, resistance to alcohol are as good as its hardness for 1 hour
Often, coating light transmittance is unchanged.
Claims (1)
1. a kind of preparation method of high rigidity aqueous pu dispersions, it is characterised in that operating procedure is as follows:
The PEPA that molecular weight is 2000 is added in flask, is 120 DEG C in temperature, bar of the vacuum in 0.02MPa
It is dehydrated 2 hours under part, cools to 60 DEG C;
To be 1 with the PEPA weight ratio:During 3 toluene di-isocyanate(TDI) adds flask, lead to nitrogen protection, at 70 DEG C
It is lower reaction 2 hours, be cooled at 60 DEG C add with the PEPA weight ratio be 1:0.2 dimethylolpropionic acid, account for point
The BDO of the 4% of prose style free from parallelism mass fraction and the dibutyl tin laurate for accounting for dispersion quality fraction 0.05%, Ran Hou
React 4 hours at 80 DEG C;
60 DEG C are cooled to, addition accounts for the acetone of dispersion quality fraction 20% and reduces system viscosity, continues reaction 1 hour;
30 DEG C are cooled to, addition accounts for the Silane coupling agent KH550 of the 1% of dispersion quality fraction, are reacted 20 minutes,
Low whipping speed is for, under the stirring condition of 500rpm, Deca is 1 with the amount ratio of the material of dimethylolpropionic acid:1 three second
Amine, under subsequent low whipping speed is for the stirring condition of 500rpm, adds in the base polyurethane prepolymer for use as of neutralization and accounts for dispersion quality
Fraction 10%, concentration for 30wt% nano silicon aqueous solution and account for the deionized water that dispersion quality fraction is 70%, then
Addition accounts for the reacting ethylenediamine 10 minutes that dispersion quality fraction is 0.5%, forms dispersions of polyurethanes;
By the dispersion under the conditions of vacuum is 0.02MPa, react 60 minutes in 60 DEG C, remove acetone, obtain the height
Hardness aqueous pu dispersions.
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