Water-dilutable or water soluble blocked polyisocyanates for producing aqueous 1K PU coating with rapid initial physical drying

Abstract
The present invention relates to new water-dilutable or water-soluble blocked polyisocyanates which allow the preparation of bakeable one-component (1K) polyurethane coating materials which exhibit rapid initial physical drying, exhibit reduced thermal yellowing and lead to haze-free coatings, to a process for preparing them, and to their use.
Description
EXAMPLES

Unless noted otherwise, all percentages are by weight.


Unless noted otherwise, all analytical measurements relate to temperatures of 23° C.


The reported viscosities were determined by means of rotational viscometry in accordance with DIN 53019 at 23° C. using a rotational viscometer from Anton Paar Germany GmbH, Ostfildern, DE.


NCO contents, unless expressly mentioned otherwise, were determined volumetrically in accordance with DIN-EN ISO-11 909.


The particle sizes reported were determined by means of laser correlation spectroscopy (instrument: Malvern Zetasizer 1000, Malvern Instr. Limited).


The solids contents were determined by heating of a weighed sample at 120° C. When constant weight was reached, the sample was weighed again to allow calculation of the solids content.


Monitoring for free NCO groups was carried out by means of IR spectroscopy (band at 2260 cm−1).


The adhesion was determined by means of DIN EN ISO 2409 crosshatch.


The König pendulum hardness was determined in accordance with DIN 53157.


Thermal yellowing was determined by the CIELAB method corresponding to DIN 6174.


Chemicals:


Desmodur® Z 4470 M/X:


Aliphatic polyisocyanate based on isophorone diisocyanate as a 70% strength solution in a mixture of methoxypropyl acetate and xylene (1/1), isocyanate content approximately 12%, Bayer MaterialScience AG, Leverkusen, DE.


Carbowax® 750:


Methoxypolyethylene glycol with an average molar mass of 750 g/mol from The Dow Chemical Company, Stade, Del.


Bayhydrol® A 145:


Water-dilutable, OH-functional polyacrylate dispersion, approximately 45% in water/solvent naphtha 100/2-butoxyethanol, neutralized with dimethylethanolamine, proportion approximately 45.6:4:4:1.4; OH content approximately 7.3%, Bayer MaterialScience AG, Leverkusen, DE


Bayhydrol® VP LS 2239:


Water-dilutable, hydroxyl-containing polyurethane dispersion, approximately 35% in water/NMP (60:5), OH content approximately 1.6%, Bayer MaterialScience AG, Leverkusen, DE


Bayhydur® VP LS 2240:


Hydrophilicized, blocked polyisocyanate crosslinker based on Desmodur® W, approximately 35% in water/MPA/xylene (56:4.5:4.5), NCO content (blocked) approximately 2.5%, Bayer MaterialScience AG, Leverkusen, DE


The other chemicals were purchased from the fine chemicals business of Sigma-Aldrich GmbH, Taufkirchen, DE.


Example 1

Not inventive, preparation of a crosslinker dispersion blocked with butanone oxime


At 70° C. in a standard stirred apparatus with nitrogen blanketing, 359.0 g of Desmodur® Z 4470 M/X were admixed in succession with a solution of 4.7 g of dimethylolpropionic acid in 9.4 g of N-methylpyrrolidone (NMP), 37.5 g of Carboxwax® 750 and 3.39 g of neopentyl glycol. The batch was then heated to 80° C. and stirred until a constant NCO value of 8.02% (calculated: 8.27%) was reached. It was cooled to 70° C. Then 71.0 g of butanone oxime were added at a rate such that the temperature in the reaction vessel did not exceed 80° C. This was followed by further stirring at 80° C. until NCO groups were no longer detectable by IR spectroscopy, then by cooling to 70° C. and addition of 2.50 g of dimethylethanolamine. After further cooling to 60° C., the batch was dispersed with 570.8 g of deionized water at 25° C. It was conditioned at 50° C., stirred for 1 hour and left to cool to room temperature with stirring.


The properties of the resulting dispersion were as follows:


















Solids content
35.8%



pH
8.02



Viscosity (Haake rotational viscometer, 23° C.)
60 mPas



Particle size (laser correlation spectroscopy, LCS)
99 nm










Example 2

Not inventive, preparation of a crosslinker dispersion blocked with acetone oxime


At 70° C. in a standard stirred apparatus with nitrogen blanketing, 466.66 g of Desmodur® Z 4470 M/X were admixed with a solution of 13.1 g of dimethylolpropionic acid in 26.2 g of N-methylpyrrolidone (NMP). The batch was then heated to 80° C. and stirred until a constant NCO value of 9.12% (calculated: 9.17%) was reached. Then 48.75 g of Carbowax® 750 were added and the mixture was stirred at 75° C. until an NCO value of 7.84 (calculated: 7.87%) was reached. It was then cooled to 70° C. and thereafter 76.0 g of acetone oxime were added at a rate such that the temperature in the reaction vessel did not exceed 80° C. This was followed by further stirring at 80° C. until NCO groups were no longer detectable by IR spectroscopy, then by cooling to 70° C. and addition of 8.70 g of dimethylethanolamine. After further cooling to 60° C., the batch was dispersed with 1548 g of deionized water at 25° C. It was conditioned at 50° C., stirred for 1 hour and left to cool to room temperature with stirring.


The properties of the resulting dispersion were as follows:


















Solids content
31.4%



pH
8.14



Viscosity (Haake rotational viscometer, 23° C.)
900 mPas



Particle size (laser correlation spectroscopy, LCS)
45 nm










Example 3

Not inventive, preparation of a crosslinker dispersion blocked with caprolactam


At 70° C. in a standard stirred apparatus with nitrogen blanketing, 359.0 g of Desmodur® Z 4470 M/X were admixed in succession with a solution of 4.7 g of dimethylolpropionic acid in 9.4 g of N-methylpyrrolidone (NMP), 37.5 g of Carboxwax® 750 and 3.39 g of neopentyl glycol. The batch was then heated to 80° C. and stirred until a constant NCO value of 8.02% (calculated: 8.27%) was reached. It was cooled to 70° C. and then 92.3 g of ε-caprolactam were added. This was followed by further stirring at 100° C. until NCO groups were no longer detectable by IR spectroscopy, then by cooling to 70° C. and addition of 2.50 g of dimethylethanolamine. After further cooling to 60° C., the batch was dispersed with 770.53 g of deionized water at 25° C. It was conditioned at 50° C., stirred for 1 hour and left to cool to room temperature with stirring.


The properties of the resulting dispersion were as follows:


















Solids content
36.5%



pH
7.75



Viscosity (Haake rotational viscometer, 23° C.)
85 mPas



Particle size (laser correlation spectroscopy, LCS)
82 nm










Example 4

Inventive, preparation of a crosslinker dispersion blocked mixedly


At 70° C. in a standard stirred apparatus with nitrogen blanketing, 359.0 g of Desmodur® Z 4470 M/X were admixed in succession with a solution of 4.7 g of dimethylolpropionic acid in 9.4 g of N-methylpyrrolidone (NMP), 37.5 g of Carbowax® 750 and 3.39 g of neopentyl glycol. The batch was then heated to 80° C. and stirred until a constant NCO value of 8.24% (calculated: 8.27%) was reached. It was cooled to 70° C. and then 63.4 g of ε-caprolactam were added. Stirring was continued at 100° C. until a constant NCO value of 1.75% (calculated: 1.76%) was reached, followed by cooling to 75° C. and addition of 17.4 g of butanone oxime. Stirring was continued until NCO groups were no longer detectable by IR spectroscopy, then by cooling to 70° C. and addition of 2.50 g of dimethylethanolamine. After further cooling to 60° C., the batch was dispersed with 582 g of deionized water at 25° C. It was conditioned at 50° C., stirred for 1 hour and left to cool to room temperature with stirring.


The properties of the resulting dispersion were as follows:


















Solids content
35.9%



pH
8.55



Viscosity (Haake rotational viscometer, 23° C.)
138 mPas



Particle size (laser correlation spectroscopy, LCS)
87 nm










Example 5

Inventive, preparation of a crosslinker dispersion blocked mixedly


The procedure described in Example 4 was repeated but using 74.7 g of ε-caprolactam and 8.7 g of butanone oxime as blocking agents.


The properties of the resulting dispersion were as follows:


















Solids content
36.9%



pH
8.07



Viscosity (Haake rotational viscometer, 23° C.)
120 mPas



Particle size (laser correlation spectroscopy, LCS)
88 nm










Example 6

Inventive, preparation of a crosslinker dispersion blocked mixedly


The procedure described in Example 4 was repeated but using 52.1 g of ε-caprolactam and 26.1 g of butanone oxime as blocking agents.


The properties of the resulting dispersion were as follows:


















Solids content
36.3%



pH
8.62



Viscosity (Haake rotational viscometer, 23° C.)
113 mPas



Particle size (laser correlation spectroscopy, LCS)
86 nm










Example 7

Inventive, preparation of a crosslinker dispersion blocked mixedly


The procedure described in Example 4 was repeated but using 19.2 g of 3,5-dimethylpyrazole instead of butanone oxime as blocking agent.


The properties of the resulting dispersion were as follows:


















Solids content
36.2%



pH
8.4



Viscosity (Haake rotational viscometer, 23° C.)
160 mPas



Particle size (laser correlation spectroscopy, LCS)
97 nm










Example 8

Inventive, preparation of a crosslinker dispersion blocked mixedly


The procedure described in Example 4 was repeated but using 55.4 g of δ-valerolactam (instead of ε-caprolactam) and 17.4 g of butanone oxime as blocking agents.


The properties of the resulting dispersion were as follows:


















Solids content
36.8%



pH
7.8



Viscosity (Haake rotational viscometer, 23° C.)
100 mPas



Particle size (laser correlation spectroscopy, LCS)
93 nm










For determination of the performance data, the blended coating materials of Examples 9 to 18 were formulated in accordance with Table 1, applied and cured. The performance data are contained in Table 2.


Table 1


Clearcoat materials 9 to 18 were prepared by mixing the blocked polyisocyanates with the polyol component in the ratio of their equivalent weights (BNCO:OH 1:1). To improve their adhesion, the coating materials include commercially customary additives (1.1%, calculated on the basis of solid binder).














TABLE 1







Ingredients
Example 09
Example 10
Example 11
Example 12
Example 13





Crosslinker
61.00 g


Bayhydur ®


VP LS 2240


Crosslinker of

53.89


Example 1


Crosslinker of


57.10


Example 2


Crosslinker of



55.04


Example 3


Crosslinker




56.50


mixture of


Example 1


with 3


(26.3:73.7)


Bayhydrol ®
37.00
44.11
40.9
42.96
41.40


VP LS 2239


Silquest ® A
 2.00 g
2.00
2.00
2.00
2.00


189


(Crumbton


GmbH)/


Dynasilan


AMEO


(ABCR


Chemie


GmbH), 20%


in dipropylene


glycol





Ingredients
Example 14
Example 15
Example 16
Example 17
Example 18





Crosslinker of
56.51


Example 4


Crosslinker of

57.70


Example 4 +


Bayhydur ®


2240 (1:1


blend)


Crosslinker of


46.00


Example 4


Crosslinker of



56.32


Example 7


Crosslinker of




55.52


Example 8


Bayhydrol ®
41.49
40.3
52.00
41.68
42.48


VP LS 2239


Bayhydrol ®


A 145


Silquest ® A
 2.00
2.00
2.00
2.00
2.00


189


(Crumbton


GmbH)/


Dynasilan


AMEO


(ABCR


Chemie


GmbH), 20%


in dipropylene


glycol









The above clearcoat materials were applied to glass plates 3 mm thick, from Schlier & Hennes, using a coating knife from Deka (No. 120) and were baked in a forced-air oven at 170° C. for 30 minutes. This gave dry film thicknesses of approximately 25-30 μm.


Table 2:


The following technical properties were found:














TABLE 2







Technical







properties of


coating materials
Example 09
Example 10
Example 11
Example 12
Example 13





Adhesion*
0
0
0
0
0


König pendulum
158
190
196
191
192


hardness (s)



a)Solvent resistance*

0001
0001
0001
0002
0002


exposure time: 5 min


(xylene, MPA, ethyl


acetate/acetone)



b)NaOH resistance*

0
0
0
0
0


(5% strength NaOH


at 70° C., 8 h


exposure)


Yellowing (Δb value)
1.60
0.74
1.10
1.10
0.90



c)Initial physical

5
3
3-4
0-1
1


drying* (3 min at


80° C.)



d)Film hazing

0
0
0
4
4


(visual)





Technical


properties of


coating materials
Example 14
Example 15
Example 16
Example 17
Example 18





Adhesion*
0
0
0
0
0


König pendulum
195
182
204
206
216


hardness (s)



a)Solvent resistance*

0002
0002
0002
0002
0002


exposure time: 5 min


(xylene, MPA, ethyl


acetate/acetone)



b)NaOH resistance*

0
0
0
0
0


(5% strength NaOH


at 70° C., 8 h


exposure)


Yellowing (Δb value)
0.62
0.87
0.65
0.69
1.70



c)Initial physical

0-1
1-2
1
1
1


drying* (3 min at


80° C.)



d)Film hazing

0
0
0
0
0


(visual)





*Assessment: 0 = good, 5 = poor






Descriptions of Test Methods


a) Solvent Resistance

    • To determine the solvent resistance, a cottonwool pad soaked with solvent was placed onto a coated substrate and covered with a watch glass. After the exposure time, the cottonwool pad and any solvent residues are removed and the surface of the coating material is rated by inspection.


b) Sodium Hydroxide Resistance

    • To determine the sodium hydroxide resistance, the substrates under investigation were immersed vertically halfway into a bath containing 5% strength aqueous sodium hydroxide solution, covered and heated at 70° C. for 8 h. Thereafter the plates were rinsed off with deionized water and rated by inspection.


c) Initial Physical Drying

    • For the investigation of the initial physical drying, the corresponding clearcoat materials were applied to 3 mm glass plates from Schlier & Hennes using a coating knife from Deka (No. 120), subjected to preliminary drying at 80° C. for 3 minutes and then investigated for the absence of tack (0=tack-free to 5=highly tacky).


d) Film Hazing

    • The coating films were inspected after baking for signs of haze (0=nothing found to 5=very hazy)


Requirements with Regard to the Individual Technical Properties:


















a) Adhesion:
max. 1



b) Pendulum hardness
min. >140, better >150



c) Solvent resistance
each individual value not more than 2



d) NaOH resistance
max. 1



e) Yellowing
<2.0, better <1.0



f) Initial physical drying
max. 2



g) Film hazing
max. 1










Evaluation of Results:


With the non-inventive self-crosslinking baking systems it is not possible using the prior-art crosslinker dispersions to achieve a sufficient profile of properties in respect of initial physical drying, low thermal yellowing and absence of haze from the films (Examples 9-12). Even the blend of two non-inventive crosslinker dispersions shown in Example 13 (Example 1: oxime-blocked, Example 3: lactam-blocked) in the preparation of a self-crosslinking dispersion did not result in acceptable coatings.


Only when the inventive crosslinker dispersions were used, reacted with a lactam and with a further blocking agent (Examples 14-18), is it possible to achieve an optimum profile of the critical properties. The other film properties as well, such as the hardness of the coating film, solvent resistance and sodium hydroxide resistance, correspond to the requirements imposed on a high-value coating system.


Although the invention has been described in detail in the foregoing for the purpose of illustration, it is to be understood that such detail is solely for that purpose and that variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention except as it may be limited by the claims.

Claims
  • 1. Process for preparing aqueous dispersions of mixedly blocked polyisocyanate prepolymers, comprising: 1) preparing a polyisocyanate prepolymer by reacting: a) 100 equivalents of at least one polyisocyanate component,b) 10 to 75 equivalents of one or more lactams, as blocking agent(s) for isocyanate groups,c) 2 to 50 equivalents of blocking agents for isocyanate groups, other than b),d) 0 to 15 equivalents of at least one nonionic hydrophilicizing agent containing isocyanate-reactive groups,e) 0.5 to 13 equivalents of at least one (potentially) anionic hydrophilicizing agent containing isocyanate-reactive groups,f) 0 to 30 equivalents of one or more amino-free compounds having a molecular weight of from 62 to 250 g/mol and which have either 2 to 4 OH groups or at least one OH group and at least one further isocyanate-reactive group, andg) 0 to 30 equivalents of one or more (cyclo)aliphatic compounds having a molecular weight of from 32 to 300 g/mol and which have either 2 to 4 amino groups or at least one amino group and at least one further isocyanate-reactive group,2) dissolving or dispersing the polyisocyanate prepolymer in water during or after reaction of components a) to g) with one another, and3) at least partially deprotonating the potentially anionic groups of the hydrophilicizing agents used in e) with a base before, during or after step 2).
  • 2. Process for preparing aqueous dispersions of mixedly blocked polyisocyanate prepolymers according to claim 1, wherein polyisocyanates based on hexamethylene diisocyanate, isophorone diisocyanate and/or 4,4′-diisocyanatodicyclohexylmethane are used in component a).
  • 3. Process for preparing aqueous dispersions of mixedly blocked polyisocyanate prepolymers according to claim 1, wherein ε-caprolactam is used as a blocking agent in component b).
  • 4. Process for preparing aqueous dispersions of mixedly blocked polyisocyanate prepolymers according to claim 1, wherein butanone oxime, acetone oxime, 3,5-dimethylpyrazole and/or mixtures thereof are used as blocking agent(s) in component c).
  • 5. Process for preparing aqueous dispersions of mixedly blocked polyisocyanate prepolymers according to claim 1, wherein the equivalent ratio of the isocyanate component (a) to isocyanate-reactive groups of components b), c), d), f) and g) is 1:0.7 to 1:1.3.
  • 6. Aqueous dispersions of mixedly blocked polyisocyanate prepolymers obtained by a process according to claim 1.
  • 7. Mixedly blocked polyisocyanate prepolymers comprising A) at least one structural unit of the formula (I)
  • 8. Aqueous coating compositions comprising mixedly blocked polyisocyanate prepolymers according to claim 7.
  • 9. Aqueous coating compositions according to claim 8, wherein the coating compositions are baking systems.
  • 10. Aqueous coating compositions according to claim 8, wherein the coating compositions further comprise water-soluble or -dispersible polyhydroxy compounds and optionally auxiliaries and adjuvants.
  • 11. Coatings obtained from aqueous coating compositions according to claim 8.
  • 12. Substrates coated with coatings according to claim 11.
Priority Claims (1)
Number Date Country Kind
102006038941.7 Aug 2006 DE national