Glycidyl esters of alpha, alpha branched acids compositions

Abstract

The invention relates to compositions of ,-branched alkane carboxylic acids glycidyl esters with a define isomeric composition where the sum of the concentration of the blocked and of the highly branched isomers is at least 50%, preferably above 60% and most preferably above 75% on total composition.

Claims

1. A composition of ,-branched alkane carboxylic glycidyl esters from butene oligomers, comprising a glycidyl ester mixture of neo-acid based on dimer or trimer of butene having both blocked isomers and highly branched isomers wherein a sum of a concentration of the blocked isomers and of the highly branched isomers is at least 60% weight based on the weight of the composition, wherein a blocked isomer comprises neo-acids having tertiary or quaternary carbon atoms in the position and a highly branched isomer comprises neo-acids having at least 5 methyl groups, wherein the glycidyl ester mixture comprises 2,2-dimethyl 3,3-dimethyl pentanoic acid glycidyl ester in 10 to 14 weight %, 2-methyl 2-isopropyl 3-methyl butanoic acid glycidyl ester in 20 to 28 weight % and 2-methyl 2-ethyl 3,3-dimethyl butanoic acid glycidyl ester in 17 to 22 weight % based on the weight of the glycidyl ester mixture, wherein the total amount of the glycidyl ester mixture is 100 weight %.

2. A binder composition for paints or adhesives comprising the composition of claim 1 as a reactive diluent or as a monomer.

3. A resin comprising the composition of claim 1 wherein the resin is selected from the group consisting of a polyester polyol resin, an acrylic polyol resin, a polyether polyol resin, or an epoxy resin formulation.

4. A composition of ,-branched alkane carboxylic glycidyl esters from butene oligomers, comprising a glycidyl ester mixture of neo-acid based on dimer or trimer of butene having both blocked isomers and highly branched isomers wherein a sum of a concentration of the blocked isomers and of the highly branched isomers is at least 60% weight based on the weight of the composition, wherein a blocked isomer comprises neo-acids having tertiary or quaternary carbon atoms in the position and a highly branched isomer comprises neo-acids having at least 5 methyl groups, wherein the glycidyl ester mixture comprises 2,2-dimethyl 3-methyl 4-methyl pentanoic acid glycidyl ester in 10 to 18 weight % and 2,2-dimethyl 4,4-dimethyl pentanoic acid glycidyl ester in 15 to 22 weight % based on the weight of the composition.

5. A binder composition for paints or adhesives comprising the composition of claim 4 as a reactive diluent or as a monomer.

6. A resin comprising the composition of claim 4 wherein the resin is selected from the group consisting of a polyester polyol resin, an acrylic polyol resin, a polyether polyol resin, or an epoxy resin formulation.

Description

EXAMPLES

(1) Chemicals Used

(2) Cardura E10: available from Momentive Specialty Chemicals Neononanoic glycidyl ester from Momentive Specialty Chemicals GE9S: neononanoic glycidyl ester of composition A (see table 2 below) GE9H: neononanoic glycidyl ester of composition B (see table 2 below) Neononanoic glycidyl ester of composition C (see table 2 below) Neononanoic glycidyl ester of composition D (see table 2 below) Neononanoic glycidyl ester of composition E (see table 2 below)

(3) TABLE-US-00002 TABLE 2 Composition of the neononanoic glycidyl ester (according to the described gas chromatography method for glycidyl esters of neo-acid) Glycidyl ester of acid V9XX (described in Table 1) A (%) B (%) C (%) D (%) E (%) V901 6.5 0.1 3.7 0.1 0.1 V902 0.6 2.55 0.6 2.4 2.65 V903 1.1 0.7 0.3 1.0 0.4 V904 0.8 1 0.1 2.2 0.4 V905 0.2 13.1 0.5 4.1 14.5 V906 0.4 11.6 0.4 9.6 12.6 V907 0.2 15.4 0.1 36.4 5.6 V908 0.1 0 0.1 0.0 0.0 V909 54.8 2.55 52.8 2.4 2.65 V910 K1 7.8 0 10.0 0.0 0.0 V910 K2 7.7 0.6 12.8 0.4 0.7 V911 2.4 1.2 0.7 2.0 0.8 V912 0.0 28.3 0.0 22.4 33.5 V913 6.8 0.1 6.4 0.1 0.1 V914 4.5 0 3.8 0.0 0.0 V915 0.6 22.3 0.6 16.8 25.3 V916 4.4 0.1 5.2 0.1 0.1 V917 1.1 0.4 2.1 0.1 0.4 GE5: glycidyl ester of pivalic acid obtained by reaction of the acid with epichlorhydrin. Ethylene glycol from Aldrich Monopentaerythritol: available from Sigma-Aldrich Methylhexahydrophtalic anhydride: available from Sigma-Aldrich Boron trifluoride diethyl etherate (BF3.OEt2) from Aldrich Acrylic acid: available from Sigma-Aldrich Hydroxyethyl methacrylate: available from Sigma-Aldrich Styrene: available from Sigma-Aldrich 2-Ethylhexyl acrylate: available from Sigma-Aldrich Methyl methacrylate: available from Sigma-Aldrich Butyl acrylate: available from Sigma-Aldrich Xylene Di-t-Amyl Peroxide is Luperox DTA from Arkema tert-Butyl peroxy-3,5,5-trimethylhexanoate: available from Akzo Nobel n-Butyl Acetate from Aldrich Dichloromethane from Biosolve Thinner: A: is a mixture of Xylene 50 wt %, Toluene 30 wt %, ShellsolA 10 wt %, 2-Ethoxyethylacetate 10 wt %. Thinner B: is butyl acetate Curing agents, HDI: 1,6-hexamethylene diisocyanate trimer, Desmodur N3390 BA from Bayer Material Science or Tolonate HDT LV2 from Perstorp Leveling agent: BYK 10 wt % which is BYK-331 diluted at 10% in butyl acetate Catalyst: DBTDL 1 wt % which is Dibutyl Tin Dilaurate diluted at 1 wt % in butyl acetate

Example 1 Comparative

(4) The following constituents were charged to a reaction vessel equipped with a stirrer, a condenser and a thermometer: 92.4 grams of GE9S, 24.0 grams of Butyl Acetate. That initial reactor charge has been heated up to 135 C. Then, the following mixture was added over a period of 1 h20 while keeping the temperature constant: 30.7 grams of acrylic acid, 1.2 grams of Di-t-Amyl Peroxide, 12.0 grams of n-Butyl Acetate. After further adding 1.2 grams of Di-t-Amyl Peroxide and 20.4 grams of n-Butyl Acetate, a post-cooking was pursued at 135 C. for 1 h. The acrylic polyol had a molecular weight (Mw) of 11400 Daltons and a Tg of about 10 C.

Example 2

(5) The following constituents were charged to a reaction vessel equipped with a stirrer, a condenser and a thermometer: 92.4 grams of GE9H, 24.0 grams of Butyl Acetate. That initial reactor charge has been heated up to 135 C. Then, the following mixture was added over a period of 1 h18 while keeping the temperature constant: 30.2 grams of acrylic acid, 1.2 grams of Di-t-Amyl Peroxide, 12.0 grams of n-Butyl Acetate. After further adding 1.2 grams of Di-t-Amyl Peroxide and 20.4 grams of n-Butyl Acetate, a post-cooking was pursued at 135 C. for 1 h. The acrylic polyol had a molecular weight (Mw) of 8600 Daltons and a Tg of about +26 C.

(6) Observations: Tg of acrylic polyols is impacted by the composition of the neononanoic glycidyl ester (see examples 1, 2).

Example 3

(7) The Adducts of Glycidyl Neononanoate, GE9H and Acrylic Acid or Methacrylic Acid

(8) The adducts of Glycidyl neononanoate GE9H (see table 3) with acrylic acid (ACE-adduct) and with methacrylic acid (MACE-adduct) are acrylic monomers that can be used to formulate hydroxyl functional (meth)acrylic polymers.

(9) TABLE-US-00003 TABLE 3 Compositions of the adducts intakes in parts by weight Acrylic acid Meth acrylic adduct acid adduct Initial reactor charge GE9H 250 250 Acrylic acid 80 Methacrylic acid 96.5 Radical Inhibitor 4-Methoxy phenol 0.463 0.463 Catalyst DABCO T9 (0.07 wt % 0.175 0.175 on Glycidyl ester) DABCO T9 and 4-Methoxy phenol (185 ppm calculated on glycidyl ester weight), are charged to the reactor. The reaction is performed under air flow (in order to recycle the radical inhibitor). The reactor charge is heated slowly under constant stirring to about 80 C., where an exothermic reaction starts, increasing the temperature to about 100 C. The temperature of 100 C. is maintained, until an Epoxy Group Content below 30 meq/kg is reached. The reaction mixture is cooled to room temperature.

Example 4

(10) Acrylic Resins for High Solids Automotive Refinish Clearcoats

(11) A glass reactor equipped with stirrer was flushed with nitrogen, and the initial reactor charge (see table 4) heated to 160 C. The monomer mixture including the initiator was then gradually added to the reactor via a pump over 4 hours at this temperature. Additional initiator was then fed into the reactor during another period of 1 hour at 160 C. Finally the polymer is cooled down to 135 C. and diluted to a solids content of about 68% with xylene.

(12) TABLE-US-00004 TABLE 4 Acrylic resins recipe Weight % in Reactor 1 L (g) Initial Reactor Charge GE9H or GE9S (Comparative) 28.2 169.1 Xylene 2.7 16.2 Feeding materials Acrylic acid 10 59.8 Hydroxy ethyl methacrylate 16.0 96.0 Styrene 30.0 180.0 Methyl methacrylate 15.8 95.0 Di t-Amyl peroxide 4.0 24.0 Xylene 8.3 49.8 Post cooking Di t-Amyl peroxide 1.0 6.0 Xylene 3.0 18.0 Solvent adding at 130 C. Xylene 50.8 305.0 Final solids content 61.8% Hydroxyl content 4.12%

Example 5

(13) Clear Coats for Automotive Refinish

(14) Solvents were blended to yield a thinner mixture of the following composition (table 5):

(15) TABLE-US-00005 TABLE 5 Thinner composition A clearcoat was then formulated (table 6) with the following ingredients (parts by weight): Weight % in Thinner solvent blend, theory Toluene 30.1% ShellSolA 34.9% 2-ethoxyethyl acetate 10.0% n-Butyl acetate 25.0% Total 100%

(16) TABLE-US-00006 TABLE 6 Clearcoat formulation Resin of example Desmodur BYK 10 DBTDL 1 ex 4 N3390 wt % in ButAc wt % in ButAc Thinner 80.1 27.01 0.53 1.17 40.45

(17) TABLE-US-00007 GE9S Clearcoat properties GE9H (Comparative) Volatile organic content 480 g/l 481 g/l Initial viscosity 54 cP 54 cP Dust free time 12 minutes 14.5 minutes Koenig Hardness 8.3 s 7.1 s after 6 hours

Example 6

(18) Acrylic Resins for First Finish Automotive Topcoats

(19) GE9H Based (28%) Acrylic Polymers for Medium Solids First-finish Clear Coats

(20) A reactor for acrylic polyols is flushed with nitrogen and the initial reactor charge (see table 7) heated to 140 C. At this temperature the monomer mixture including the initiator is added over 4 hours to the reactor via a pump. Additional initiator is fed into the reactor during one hour, and then the mixture is kept at 140 C. to complete the conversion in a post reaction. Finally the polymer is cooled down and diluted with butyl acetate to a solids content of about 60%.

(21) TABLE-US-00008 TABLE 7 Acrylic resins recipe Intakes (parts by weight ) Initial reactor charge GE9H 164.40 Xylene 147.84 Monomer mixture Acrylic acid 53.11 Butyl methacrylate 76.88 Butyl acrylate 48.82 Hydroxy-ethyl methacrylate 27.20 Styrene 177.41 Methyl methacrylate 47.31 Initiator Di-tert.-amyl peroxide (DTAP) 8.87 Post addition Di-tert.-amyl peroxide 5.91 Solvent (to dilute to 60% solids) Butyl acetate 246.00 Total 1000.0
Clear Lacquer Formulation

(22) Clear lacquers are formulated (see table 8) from the acrylic polymers by addition of Cymel 1158 (curing agent from CYTEC), and solvent to dilute to spray viscosity. The acidity of the polymer is sufficient to catalyze the curing process, therefore no additional acid catalyst is added. The lacquer is stirred well to obtain a homogeneous composition.

(23) TABLE-US-00009 TABLE 8 Clear lacquer formulations and properties of the polymers Intakes (part by weight) Ingredients Acrylic polymer 60.0 Cymel 1158 8.8 Butyl acetate (to application 24.1 viscosity) Properties Solids content [% m/m] 45.3 Density [g/ml] 0.97 VOC [g/l] 531
Application and Cure

(24) The coatings are applied with a barcoater on Q-panels to achieve a dry film thickness of about 40 m. The systems are flashed-off at room temperature for 15 minutes, then baked at 140 C. for 30 minutes. Tests on the cured systems are carried out after 1 day at 23 C.

Example 7

(25) In a reactor equipped with an anchor stirrer, a thermometer, condenser and monomer/initiator feeding system, 188.6 g of GE9H and 90 g of ethoxypropanol (EPR) were loaded and heated to about 150 C. (see table 9). A mixture of 52 g of hydroxyethylmethacrylate (HEMA), 160 g of styrene, 68 g of acrylic acid (AA), 10 g of dicumylperoxide (DCP), 37.7 g of GE9H and 40 g of ethoxypropanol (EPR) were added over 2 hours 30 minutes to the reactor while keeping its content at 150 C. After the feed, the reactor content was held for 30 minutes at this temperature. After the 30 minutes hold period, 108 g of HEMA, 30 g of AA, 142 g of isobutyl methacrylate (IBMA), 5 g of DCP and 45 grams of EPR were added over 2 hours and 30 minutes at about 150 C. followed by a rinsing step for the feed system with 5 g of EPR. After the rinsing step, the content of the reactor was held for 2 hours at 150 C. The reactor content was cooled down to 100 C. and 100 parts of EPR were distilled off at atmospheric pressure.

(26) The polyacrylate polyol has a solids content of the solution of 90% by weight.

(27) TABLE-US-00010 TABLE 9 Composition of polyol Materials Intake (g) Initial charge EPR 90 GE9H 188.6 Monomer Addition 1 AA 68 Styrene 160 GE9H 37.7 HEMA 52 EPR 40 DCP 10 Monomer Addition 2 AA 30 IBMA 142 HEMA 108 DCP 5 EPR 45 TOTAL 976.3

Example 8 Comparative

(28) The following constituents were charged to a reaction vessel: 0.7153 grams of a neononanoic glycidyl ester of composition C, 0.5958 grams of hexahydro-4-methylphthalic anhydride, 0.0014 grams of ethylene glycol. The reaction took place for 3 to 4 days at 140 C. The sample has been dried by evaporation. The polyester had a molecular weight (Mn) of 4700 Daltons and a Tg of +18.8 C.

Example 9

(29) The following constituents were charged to a reaction vessel: 0.5823 grams of a neononanoic glycidyl ester of composition D, 0.4775 grams of hexahydro-4-methylphthalic anhydride, 0.0011 grams of ethylene glycol, 0.2841 grams of n-Butyl Acetate. The reaction took place for 3 to 4 days at 120-140 C. and the solvent was then thoroughly removed by evaporation. The polyester had a molecular weight (Mn) of 5000 Daltons and a Tg of +43.7 C.

Example 10

(30) The following constituents were charged to a reaction vessel: 0.5846 grams of a neononanoic glycidyl ester of composition E, 0.4786 grams of hexahydro-4-methylphthalic anhydride, 0.0011 grams of ethylene glycol, 0.2847 grams of n-Butyl Acetate. The reaction took place for 3 to 4 days at 120-140 C. and the solvent was then thoroughly removed by evaporation. The polyester had a molecular weight (Mn) of 3800 Daltons and a Tg of +48.1 C.

(31) Observations: Tg of polyesters is impacted by the composition of the neononanoic glycidyl ester (see examples 8, 9, 10).

(32) The resins of the examples can be formulated in coating compositions such as 2K (polyurethane) with a low VOC (volatile organic compound) level and still providing and excellent appearance.

Example 11 Comparative

(33) Monopentaerythritol, methylhexahydrophthalic anhydride and n-Butyl Acetate (see 1/in Table 10) were charged to a reaction vessel and heated at 140 C. until complete conversion. Cardura E10P (see 1/in Table 10) was then dropwise added and the reaction pursued until acceptable acid value. The polyester had a solid content of 76.0 wt %. At a suitable temperature, Cardura E10P and xylene (see 2/in Table 10) were then added. The mixture was heated to about 157 C. and the monomers, radical initiator and solvent (see 3/in Table 10) were fed for 6 hours at that temperature. A post-cooking (1 h) then took place with additional radical initiator (see 4/in Table 10). After further addition of n-butyl acetate (see 5/in Table 10), the final resin had a solid content of 66.2 wt %.

Example 12

(34) Recipe of example 11 was used with the amount indicated in table 10 while using GE9H instead of Cardura E10P for the polyester cooking. The intermediate polyester and the final resin had a solid content of 78.4 wt % and 66.8 wt %, respectively.

Example 13

(35) Recipe of example 12 was used with the amount indicated in table 10 while using GE9H instead of Cardura E10P for the acrylic polyol cooking. The intermediate polyester and the final resin had a solid content of 78.4 wt % and 68.3 wt %, respectively.

(36) TABLE-US-00011 TABLE 10 Constituents for the polyester based acrylic polyol cooking Example 11 Example 12 Example 13 1/Polyester cooking, constituent (g) Monopentaerythritol 4.0 4.2 3.4 Methylhexahydrophthalic 15.2 15.9 12.7 anhydride n-Butyl acetate 10.0 10.4 8.3 Cardura E10P 22.3 GE9H 21.9 17.5 2/Acrylic polyol cooking, initial reactor charge (g) Polyester (from above) 51.5 52.3 41.8 Cardura E10P 33.2 31.3 GE9H 24.9 Xylene 3.6 3.4 2.9 3/Acrylic polyol cooking, feeding material (g) Acrylic Acid 9.5 9.0 7.6 Hydroxyethyl methacrylate 23.9 22.5 19.0 Styrene 39.8 37.5 31.7 Butyl Acrylate 0.0 0.0 0.8 Methyl methacrylate 26.3 24.8 21.6 Xylene 11.0 10.4 8.8 Di-t-Amyl Peroxide 5.3 5.0 4.2 4/Acrylic polyol post cooking, feeding material (g) Di-t-Amyl Peroxide 1.3 1.3 1.1 5/Acrylic polyol solid content adjustment, solvent adding (g) n-Butyl acetate 55.7 52.6 44.4
Formulation of the Clear Coats

(37) A clear coat is formulated with one of the polyester based acrylic polyol (from examples 11, 12 or 13, the curing agent (HDI, Desmodur N3390), the thinner, the levelling agent (BYK-331) and the catalyst (dibutyltin dilaurate, DBTDL) according to the amounts indicated in table 11.

(38) TABLE-US-00012 TABLE 11 Clear coats, formulations Binder Binder BYK DBTDL Thinner CE-Example (ID) (g) HDI (g) 10 wt % (g) 1 wt % (g) A (g) CE-11 From Example 11 92.1 34.7 0.67 1.47 37.2 CE-12 From Example 12 91.3 36.0 0.66 1.46 37.4 CE-13 From Example 13 91.3 36.9 0.68 1.50 39.7
Characterization of the Clear Coats

(39) The clearcoat formulations (from table 11) are barcoat applied on degreased Q-panel. The panels are dried at room temperature, optionally with a preliminary stoving at 60 C. for 30 min. Clear coats have been characterized among others by measuring the dust free time and Koenig hardness development (see table 12).

(40) TABLE-US-00013 TABLE 12 Clear coats, drying (curing) properties CE-11 CE-12 CE-13 1/Dust free time (Room temperature drying panels) (min) Dust free time (min) 39 35 24 2/Koenig Hardness (Room temperature drying panels) (sec) 6 hours 3 4 7 24 hours 31 38 49 7 days 156 167 179 3/Koenig Hardness (Stoved Q panels) (sec) Out of the oven 12 15 24 6 hours 15 18 29 24 hours 48 55 67 7 days 178 180 190

(41) Observation (see table 12): significant improvement (lower dust free time and quicker hardness development) is observed when replacing Cardura E10P by GE9H for the polyester cooking. Improvement is even more significant when Cardura E10P is complementary replaced by GE9H for the acrylic polyol cooking.

Example 14 Comparative

(42) Monopentaerythritol/Methylhexahydrophtalic anhydride/GE9S (1/3/3 molar ratio)=CE-GE9S

(43) 80.4 g amount of butylacetate, 68.3 g of monopentaerythritol, 258.2 g of methylhexahydrophthalic anhydride are loaded in a glass reactor and heated to reflux until complete dissolution. Afterwards, the temperature is decreased down to 120 C. and 333.0 g of GE9S are added over about one hour. The cooking is pursued at 120 C. for the time needed to decrease epoxy group content and acid value down to an acid value below 15 mg KOH/g. Then, further 82.4 g of butylacetate are added. Test results are indicated in table 13.

Example 15a

(44) Monopentaerythritol/Methylhexahydrophtalic anhydride/GE9H (1/3/3 molar ratio)=CE-GE9Ha

(45) 80.4 g amount of butylacetate, 68.3 g of monopentaerythritol, 258.2 g of methylhexahydrophthalic anhydride are loaded in a glass reactor and heated to reflux until complete dissolution. Afterwards, the temperature is decreased down to 120 C. and 337.1 g of GE9H are added over about one hour. The cooking is pursued at 120 C. for the time needed to decrease epoxy group content and acid value down to an acid value below 15 mg KOH/g. Then, further 83.4 g of butylacetate are added. Test results are indicated in table 13.

Example 15b

(46) Monopentaerythritol/Methylhexahydrophtalic Anhydride/GE9H (1/3/3 Molar Ratio)=CE-GE9Hb

(47) CE-GE9Hb is a duplication of Example 15a performed in very close experimental conditions.

Example 16a Comparative According to EP 0996657

(48) Monopentaerythritol/Methylhexahydrophtalic Anhydride/GE5 (1/3/3 Molar Ratio) CE-GE5a

(49) 71.3 g amount of butylacetate, 60.5 g of monopentaerythritol, 228.90 g of methylhexahydrophthalic anhydride are loaded in a glass reactor and heated to reflux until complete dissolution. Afterwards, the temperature is decreased down to 120 C. and 214.3 g of GE5 are added over about one hour. The cooking is pursued at 120 C. for the time needed to decrease epoxy group content and acid value down to an acid value below 15 mg KOH/g. Then, further 52.1 g of butylacetate are added. Test results are indicated in table 13.

Example 16b Comparative According to EP 0996657

(50) Monopentaerythritol/Methylhexahydrophtalic Anhydride/GE5 (1/3/3 Molar Ratio) CE-GE5b

(51) CE-GE5b is a duplication of comparative example 16a performed in very close experimental conditions except for the higher amount of butylacetate added at the end of the reaction.

(52) TABLE-US-00014 TABLE 13 Polyesters characterization Mw Mn Mw/Mn Polyester resin SC (%) (Da) (Da) (PDI) Viscosity (cP) CE-GE9S 78.6 974 919 1.06 2450 (25.9 C.) CE-GE9Ha 80.0 921 877 1.05 6220 (25.9 C.) CE-GE9Hb 80.0 1014 975 1.04 11740 (21.6 C.) CE-GE5a 79.3 914 886 1.03 5080 (26.0 C.) CE-GE5b 68.3 1177 1122 1.05 102.3 (22.0 C.) SC: solids content

Example 17 Comparative

(53) Acrylic Resin Synthesis

(54) Cardura E10 Based Acrylic Polyol Resin: Acryl-CE(10)

(55) 105.0 g amount of CE10 (Cardura E10-glycidyl ester of Versatic acid) and 131.6 g of Shellsol A are loaded in a glass reactor and heated up to 157.5 C. Then, a mixture of monomers (37.4 g acrylic acid, 107.9 g hydroxyethyl methacrylate, 180.0 g styrene, 100.2 g butyl acrylate, 69.6 g methyl methacrylate) and initiator (12.0 g Di-tert-butyl peroxide) is fed into the reactor at a constant rate in 5 hours. Then post cooking started: a mixture of 6.0 g Di-tert-butyl peroxide and 18.0 g n-butyl acetate is fed into the reactor at a constant rate in 0.5 hour, then temperature maintained at about 157.5 C. for a further 0.5 hour. Finally, 183.2 g of n-butyl acetate is added under stirring to achieve a polyol resin with the target solids content. Test results are indicated in table 14.

(56) TABLE-US-00015 TABLE 14 Acryl-CE(10) characterization SC (%)- Mw Mn Mw/Mn Acryl- measured (Da) (Da) (PDI) CE(10) 65.2 5094 2629 1.94

(57) Three types of formulations have been prepared: Blend Acryl-CE(10) blend with CE-GEx polyester with Desmodur as hardener (Part 1) CE-GEx polyester alone with Tolonate HDT LV2 as hardener (0.03 wt % DBTDL)(Part 2) CE-GEx polyester alone with Tolonate HDT LV2 as hardener (0.09 wt % DBTDL) (Part 3)

(58) Part 1: CE-GEx Polyesters Blend with Acryl-CE(10) Formulation

(59) TABLE-US-00016 TABLE 15 Clear coats, formulations BYK 10 DBTDL Binder 1 Binder 2 HDI wt % 1 wt % Thinner A CE-GEx (g) (g) (g) (g) (g) (g) GE9Hb 71.6 16.9 31.2 0.63 1.39 86.33 GE5b 79.1 12.4 31.2 0.63 1.39 89.30 Binder 1: Acryl-CE(10) Binder 2: CE-GEx polyesters

(60) Part 2CE-GEx Polyesters Alone, No Acryl-CE(10) Formulation (0.03 wt % DBTDL)

(61) TABLE-US-00017 TABLE 16 Clear coats, formulations DBTDL Binder HDI BYK 10 1 wt % Thinner CE-GEx 2 (g) (g) wt % (g) (g) B (g) GE9S 80.0 36.56 0.72 3.15 89.75 GE9Ha 80.4 37.27 0.73 3.20 87.83 GE5a 79.9 43.18 0.76 3.36 94.82

(62) Part 3CE-GEx Polyesters Alone, No Acryl-CE(10) Formulation (0.09 wt % DBTDL)

(63) TABLE-US-00018 TABLE 17 Clear coats, formulations BYK DBTDL Binder HDI 10 wt % 1 wt % Thinner CE-GEx 2 (g) (g) (g) (g) B (g) GE9Ha 60.0 28.10 0.54 7.18 15.40 GE5a 59.8 32.54 0.57 7.57 17.79
Characterization of the Clear Coats

(64) The clearcoat formulations are barcoat applied on degreased Q-panel for Parts 2 & 3; sprayed for the Part 1 on Q-panel with a basecoat. The panels are dried at room temperature, optionally with a preliminary stoving at 60 C. for 30 min.

(65) Part 1CE-GEx Polyesters Blend with Acryl-CE(10)/Room Temperature curing

(66) TABLE-US-00019 TABLE 18 Clear coats, performances Drying DFT (min) CE-GEx SC (%) Potlife (h) conditions Cotton Balls GE9Hb 47.1 4.5 RT 15 GESb 46.2 4.0 RT 19 SC: solids content, RT: room temperature

(67) Part 2CE-GEx Polyesters Alone, No Acryl-CE(10)/Room Temperature Curing and Room Temperature Drying after Stoving

(68) TABLE-US-00020 TABLE 19 Clear coats, performances DFT (min) SC Drying Cotton Koenig Hardness (s) CE-GEx (%) conditions Balls 6 h 24 h 7 d GE9S 48.4 RT 223 3 17 159 GE9Ha 49.2 RT 91 3 36 212 GE5a 49.5 RT 114 1 29 216 GE9S 48.4 Stoving 30 Dust free 4 44 174 min/60 C. out of oven GE9Ha 49.2 Stoving 30 Dust free 10 55 211 min/60 C. out of oven GE5a 49.5 Stoving 30 Dust free 6 49 216 min/60 C. out of oven

(69) Part 3CE-GEx Polyesters Alone, No Acryl-CE(10)/Room Temperature Curing and Room Temperature Drying after Stoving (0.09 wt % DBTDL)

(70) TABLE-US-00021 TABLE 20 Clear coats, performances DFT Pot- (min) SC life Drying Cotton Koenig Hardness (s) CE-GEx (%) (min) conditions Balls 6 h 24 h 7 d GE9Ha 69.8 42.4 RT 47 3 66 193 GE5a 68.5 61.3 RT 73 3 55 191 GE9Ha 69.8 42.4 Stoving 30 Dust free 29 102 210 min/60 C. out of oven GE5a 68.5 61.3 Stoving 30 Dust free 12 69 205 min/60 C. out of oven
Observations
Part 1

(71) The potlife is about the same, the dust free time is shorter for GE9Hb vs. GE5b.

(72) Part 2

(73) The 24 h hardness order GE9H, GE5 and GE9S and the dust free time at room temperature is the best for GE9H.

(74) Part 3

(75) The hardness development is the best for GE9H at room temperature and heat cure, the dust free time at room temperature is quicker for GE9H than for GE5; and with a volatile organic content of 300 g/l.

Example 18

(76) The following constituents were charged to a reaction vessel: 2.5500 grams of a neononanoic glycidyl ester of composition D, 1.1571 grams of dichloromethane, 0.0137 grams of boron trifluoride diethyl etherate. The reaction took place for 3 days at room temperature and the solvent was then thoroughly removed by evaporation. The polyether had a molecular weight (Mw) of 1900 Daltons and a Tg of 40.5 C.

Example 19 Comparative

(77) The following constituents were charged to a reaction vessel: 2.5438 grams of a neononanoic glycidyl ester of composition C, 1.0150 grams of dichloromethane, 0.0128 grams of boron trifluoride diethyl etherate. The reaction took place for 3 days at room temperature and the solvent was then thoroughly removed by evaporation. The polyether had a molecular weight (Mw) of 1500 Daltons and a Tg of 51.1 C.

(78) Observations: Tg of the modified polyether resin is impacted by the composition of the neononanoic glycidyl ester (see examples 18, 19).

Example 20

(79) Polyether Resin

(80) The following constituents were charged to a reaction vessel equipped with a stirrer, a thermometer and a condenser: 134 grams of di-Trimethylol propane (DTMP), 900 grams of glycidyl neononanoate, GE9H, 135.5 grams of n-butylacetate (BAC) and 2.5 grams of Tin 2 Octoate. The mixture was heated to its reflux temperature of about 180 C. for about 4 hours till the glycidyl neononaoate was converted to an epoxy group content of less than 0.12 mg/g. After cooling down the polyether had a solids content of about 88%.

Example 21 Comparative

(81) Polyether Resin

(82) The following constituents were charged to a reaction vessel equipped with a stirrer, a thermometer and a condenser: 28.8 grams of monopentaerythritol, 201.5 grams of Cardura E10P, 19.4 grams of n-butylacetate and 0.3552 grams of Tin (II) 2-ethylhexanoate. The mixture was heated to a temperature of about 180 C. for about 6 hours till the Cardura E10P was converted to an epoxy group content of about 25 mmol/kg. After cooling down the polyether had a solids content of about 94%.

Example 22 Comparative

(83) Polyether Resin

(84) The following constituents were charged to a reaction vessel equipped with a stirrer, a thermometer and a condenser: 28.8 grams of monopentaerythritol, 187.1 grams of GE9S, 18.3 grams of n-butylacetate and 0.3550 grams of Tin (II) 2-ethylhexanoate. The mixture was heated to a temperature of about 180 C. for about 5.5 hours till the GE9S was converted to an epoxy group content of about 29 mmol/kg. After cooling down the polyether had a solids content of about 95%.

Example 23

(85) Polyether Resin

(86) The following constituents were charged to a reaction vessel equipped with a stirrer, a thermometer and a condenser: 28.8 grams of monopentaerythritol, 189.4 grams of GE9H, 18.5 grams of n-butylacetate and 0.3572 grams of Tin (II) 2-ethylhexanoate. The mixture was heated to a temperature of about 180 C. for about 4 hours till the GE9H was converted to an epoxy group content of about 27 mmol/kg. After cooling down the polyether had a solids content of about 95%.

Example 24 Comparative

(87) Polyether Resin

(88) The following constituents were charged to a reaction vessel equipped with a stirrer, a thermometer and a condenser: 29.0 grams of monopentaerythritol, 136.7 grams of GE5, 14.0 grams of n-butylacetate and 0.3597 grams of Tin (II) 2-ethylhexanoate. The mixture was heated to a temperature of about 180 C. for about 5.7 hours till the GE5 was converted to an epoxy group content of about 27 mmol/kg. After cooling down the polyether had a solids content of about 94%.

(89) Formulation of the Clear Coats

(90) A clear coat is formulated with one of the polyether (from examples 21, 22, 23 or 24, the curing agent (HDI, Desmodur N3390), the thinner (Methyl Amyl Ketone), the levelling agent (BYK-331) and the catalyst (dibutyltin dilaurate, DBTDL) according to the amounts indicated in table 21.

(91) TABLE-US-00022 TABLE 21 Clear coats, formulations BYK DBTDL CEP- Binder Binder HDI 10 wt % 1 wt % Thinner Example (ID) (g) (g) (g) (g) (g) CEP-21 From Exam- 40.1 30.7 0.47 1.03 15.1 ple 21 CEP-22 From Exam- 40.0 33.0 0.48 1.07 >12.5 ple 22 CEP-23 From Exam- 40.0 32.5 0.48 1.06 17.7 ple 23 CEP-24 From Exam- 40.1 42.9 0.54 1.20 17.7 ple 24
Characterization of the Clear Coats

(92) The clearcoat formulations (from table 21) are barcoat applied on degreased Q-panel, optionally on basecoated Q-panel. The panels are dried at room temperature after a preliminary stoving at 60 C. for 30 min. Clear coats have been characterized among others by measuring the Koenig hardness development (see table 22).

(93) TABLE-US-00023 TABLE 22 Clear coats, drying (curing) properties CEP-21 CEP-22 CEP-23 CEP-24 1/Koenig Hardness (Degreased Q panels) (sec) 6 hours 8 10 11 10 24 hours 10 11 47 42 7 days 18 20 94 122 2/Koenig Hardness (Basecoated Q panels) (sec) 6 hours 7 8 7 8 24 hours 8 8 14 17 7 days 12 13 34 48

(94) Observation (see table 22): significant improvement (quicker hardness development) is observed when replacing Cardura E10P or GE9S by GE9H for the polyether cooking. Early hardness improvement on degreased Q-panels is better for example CEP-23 than for example CEP-24.

Example 25

(95) Preparation for Vacuum Infusion of Composite Structures

(96) A resin for vacuum infusion of large structures such as yacht and wind turbines was prepared by mixing 27.7 part by weight of curing agent blend and 100 part of epoxy resins blend described here:

(97) Epoxy resins blend: 850 part by weight Epikote 828 and 150 part of glycidyl neononanoate, GE9H.

(98) Curing Agent blend: 650 part by weight of Jeffamine D230 and Jeffamine D230 is a polyoxyalkyleneamines available from Huntsman Corporation. Epikote 828 is an epoxy resin available from Momentive Specialty Chemicals.

Example 26

(99) Example of Trowellable Floor and Patching Compound

(100) The ingredients presented in the table 23 below were mixed for the preparation of a trowellable flooring compound

(101) TABLE-US-00024 TABLE 23 Preparation of a trowellable flooring compound Weight Volume (parts) (parts) Supplier BASE COMPONENT EPIKOTE 828LVEL 63.2 126.3 Momentive GE9H 11.1 22.3 Byk A530 4.8 13.4 Byk Chemie Mix the additives into the EPIKOTE resin before filler addition Total 79.1 162.0 FILLERS Sand 1-2 mm 582.3 496.4 SCR Sibelco Sand 0.2-0.6 mm 298.4 254.4 SCR Sibelco Total 880.7 750.8 Disperse into the base component using a concrete mixer CURING AGENT COMPONENT EPIKURE F205 40.2 87.2 Momentive Total 40.2 87.2 Mix the curing agent well with the EPIKOTE resin base and Fillers before application Total formulation 1000.0 1000.0

Example 27

(102) Formulation for a Water Based Self-leveling Flooring

(103) The ingredients presented in the table 24 below were mixed for the preparation of a waterbased self leveling flooring system.

(104) TABLE-US-00025 TABLE 24 Preparation of a waterbased self leveling flooring system Weight (parts) Supplier Comment CURING AGENT COMPONENT (A) EPIKURE 8545-W-52 164.00 Momentive (HEW = 320 g/eq) EPIKURE 3253 4.00 Momentive Accelerator BYK 045 5.00 BYK CHEMIE defoamer Antiterra 250 4.00 BYK CHEMIE Dispersing Byketol WS 5.00 BYK CHEMIE Wetting agent Bentone EW (3% in water) 20.00 Elementis Anti-settling Mix the additive into the EPIKURE curing agents before filler addition Titanium dioxide 2056 50.00 KronosTitan Disperse the pigment for 10 minutes at 2000 rpm. EWO-Heavy Spar 195.00 Sachtleben Barium Chemie sulphate Quartz powder W8 98.00 Westdeutsche Quarzwerke Disperse fillers at 2000 rpm for 10 minutes Water 55.00 Sand 0.1-0.4 min 400.00 Euroquarz Total component A 1000.00 RESIN COMPONENT (B) EPIKOTE 828LVEL 81.00 Momentive GE9H 19.00 Mix (B) into (A) Total formulation A + B 1081.00

(105) TABLE-US-00026 Formulation characteristics Fillers + Pigment/Binder ratio 3.9 by weight PVC 37.7% v/v Density 1.9 g/ml Water content 12.5% m/m