HIGH CREEP RECOVERY, LOW MODULUS POLYMER SYSTEMS AND METHODS OF MAKING THEM

Abstract

Disclosed herein are methods of making an adhesive composition, the methods comprising providing a polyurethane acrylate and combining with a vinyl ether and co-curing the combination to form an adhesive composition, wherein after curing the adhesive composition has a modulus at −20° C. of less than about 10.0 mPa and a creep recovery of greater than about 50%. Also disclosed are the resulting adhesive compositions.

Claims

1. A method of making an adhesive composition comprising: combining a polyurethane acrylate and a vinyl ether to form a mixture and co-curing the mixture to form the adhesive composition, wherein after curing the adhesive composition has a modulus of less than about 10.0 mPa at −20° C. and a creep recovery of greater than about 50%.

2. The method of claim 1, wherein the polyurethane acrylate is created by: providing a highly branched diol; reacting the highly branched diol with a diisocyanate to obtain a polyurethane; and reacting the polyurethane with an acrylate to form a polyurethane acrylate.

3. The method of claim 2 wherein the highly branched diol is a polyfarnesene or a dimer acid polyester.

4. The method of claim 2, wherein the diol has a molecular weight of greater than about 1000 g/mol.

5. The method of claim 1, wherein the co-curing is done by light curing or heat curing.

6. The method of claim 1, wherein the diisocyanate is an aliphatic diisocyanate.

7. The method of claim 1, wherein the polyurethane acrylate is combined with vinyl ether in a molar ratio of vinyl ether to polyurethane acrylate of less than about 1.

8. The method of claim 1, wherein the polyurethane acrylate has a molecular weight of over about 25000 g/mol.

9. The method of claim 1, wherein the adhesive composition has a modulus of less than about 1.0 mPa at −20° C. and a creep recovery of greater than about 70%.

10. The method of claim 1, wherein the adhesive composition has a modulus of less than about 0.3 mPa at −20° C. and a creep recovery of greater than about 90%.

11. The method of claim 1, wherein the polyurethane acrylate has a glass transition temperature of less than 10° C.

12. The method of claim 1, wherein the polyurethane acrylate has a glass transition temperature of less than −30° C.

13. The method of claim 1, further comprising combining the polyurethane acrylate with a photoinitiator or a thermal initiator before the co-curing step.

14. The method of claim 1, wherein the vinyl ether is a member selected from poly(butyl vinyl ether), poly(ethyl vinyl ether), poly(hexyl vinyl ether), poly(isobutyl vinyl ether), poly(isopropyl vinyl ether), poly(methyl vinyl ether), poly(octyl vinyl ether), poly(propyl vinyl ether), and combinations thereof.

15. The method of claim 1, wherein the polyurethane acrylate is selected from poly(2-ethylhexyl acrylate), poly(2,2,3,3,-tetrafluoropropyl acrylate), poly(4-cyanobutyl acrylate), poly(butyl acrylate), poly(dodecyl acrylate), poly(ethyl acrylate), poly(hexyl acrylate), poly(isobutyl acrylate), poly (isopropyl acrylate), poly (nonyl acrylate), poly(propyl acrylate), poly(sec-butyl acrylate), poly (tetrahydrofurfural acrylate), poly decyl methacrylate), poly(dodecyl methacrylate), poly(hexyl methacrylate), poly(isodecyl methacrylate), poly(octyl methacrylate), and combinations thereof.

16. An adhesive composition comprising a co-cured mixture of polyurethane acrylate and vinyl ether, wherein the adhesive composition has a modulus of less than about 10.0 mPa at −20° C. and a creep recovery of greater than about 50%.

17. The adhesive composition of claim 16, wherein the adhesive composition has a modulus of less than about 1.0 mPa at −20° C. and a creep recovery of greater than about 70%.

18. The adhesive composition of claim 16, wherein the adhesive composition has a modulus at −20° C. of less than about 0.3 mPa and a creep recovery of greater than about 90%.

19. The adhesive composition of claim 16, wherein the molar ratio of the vinyl ether to the acrylic monomer is equal to or less than about 1.

20. The adhesive composition of claim 16, wherein there is no solvent present in the composition.

21. The adhesive composition of claim 16, wherein the composition further comprises a thermal initiator or a photoinitiator.

22. The adhesive composition of claim 16, wherein the vinyl ether is a member selected from poly(butyl vinyl ether), poly(ethyl vinyl ether), poly(hexyl vinyl ether), poly(isobutyl vinyl ether), poly(isopropyl vinyl ether), poly(methyl vinyl ether), poly(octyl vinyl ether), poly(propyl vinyl ether), and combinations thereof.

23. The adhesive composition of claim 16, wherein the polyurethane acrylate is selected from poly(2-ethylhexyl acrylate), poly(2,2,3,3,-tetrafluoropropyl acrylate), poly(4-cyanobutyl acrylate), poly(butyl acrylate), poly(dodecyl acrylate), poly(ethyl acrylate), poly(hexyl acrylate), poly(isobutyl acrylate), poly (isopropyl acrylate), poly (nonyl acrylate), poly(propyl acrylate), poly(sec-butyl acrylate), poly (tetrahydrofurfural acrylate), poly decyl methacrylate), poly(dodecyl methacrylate), poly(hexyl methacrylate), poly(isodecyl methacrylate), poly(octyl methacrylate), and combinations thereof.

Description

DETAILED DESCRIPTION

[0011] Disclosed herein is a new co-cured polyacrylate/vinyl ether adhesive polymer composition that exhibits very low modulus at −20° C. (less than 10.0 mPa) and exhibits excellent creep recovery (greater than 50%). The polymer composition produced by this method achieves a combination of low modulus and high creep recovery, in particular a creep recovery from >70% to >90% and a modulus at −20° C. from <1.0 mPa to <0.3 mPa.

[0012] Also disclosed herein is a method of making an adhesive composition comprising co-curing a polyurethane acrylate and a vinyl ether resin to form the adhesive composition, wherein after curing the adhesive composition has a modulus at −20° C. of less than about 10.0 mPa and a creep recovery of greater than about 50%. The polymer composition achieves a combination of low modulus and high creep recovery, in particular a creep recovery from >70% to >90% and a modulus at −20° C. from <1.0 mPa to <0.3 mPa.

[0013] The polyurethane acrylate utilized herein may be made by the reacting a highly branched diol with a diisocyanate to obtain a polyurethane and reacting the polyurethane with an acrylate to form the polyurethane acrylate, as described in more detail below.

[0014] The resulting polyurethane acrylate/vinyl ether adhesive composition exhibits very low modulus at −20° C. and exhibits excellent creep recovery. Particularly, the creep recovery can be greater than about 70%, for example greater than about 90% while the modulus at −20° C. can be less than about 4.0 mPa, for example less than about 1.0 mPa, and even less than about 0.3 mPa.

[0015] In addition to the polyurethane acrylate and the vinyl ether, the adhesive composition may also include other ingredients.

[0016] Suitable polyurethane acrylates for use in the present invention include the following:

TABLE-US-00001 Polymer Tg (° C.) Poly(2-ethylhexyl acrylate) −53 Poly(2,2,3,3-tetrafluoropropyl acrylate) −24 Poly(4-cyanobutyl acrylate) −38 Poly(butyl acrylate) −53 Poly(dodecyl acrylate) −19 Poly(ethyl acrylate) −23 Poly(hexyl acrylate) −59 Poly(isobutyl acrylate) −34 Poly(isopropyl acrylate)  −2 Poly(nonyl acrylate) −74 Poly(propyl acrylate) −42 Poly(sec-butyl acrylate) −21 Poly(tetrahydro furfuryl acrylate) −14

TABLE-US-00002 Polymer Tg (° C.) Poly(decyl methacrylate) −63 Poly(dodecyl methacrylate) −55 Poly(hexyl methacrylate)  −5 Poly(isodecyl methacrylate) −41 Poly(octyl methacrylate) −45

[0017] Vinyl ethers useful in the present invention include the following:

##STR00001##

TABLE-US-00003 Polymer Tg (° C.) Poly(butyl vinyl ether) −54 Poly(ethyl vinyl ether) −41 Poly(hexyl vinyl ether) −76 Poly(isobutyl vinyl ether) −19 Poly(isopropyl vinyl ether)  −3 Poly(methyl vinyl ether) −28 Poly(octyl vinyl ether) −80 Poly(propyl vinyl ether) −49

[0018] The adhesive polymer formed by co-curing a polyurethane acrylate and vinyl ether surprisingly possesses extremely high creep recovery combined with a very low modulus. Applicant has found that introducing a vinyl ether monomer into an acrylate polymer system can significantly reduce the modulus and Tg of the resulting polymer while also yielding a very high creep recovery at very low modulus. This combination of physical properties of very low modulus at low temperature with very high creep recovery has not previously been exhibited in polymer adhesive systems and is an unexpected beneficial result.

[0019] In one embodiment, the method of making an adhesive composition comprises combining a polyurethane acrylate and a vinyl ether to form a mixture and co-curing the mixture to form the adhesive composition, wherein after curing the adhesive composition has a modulus of less than about 10.0 mPa at −20° C. and a creep recovery of greater than about 50%.

[0020] In another embodiment, the polyurethane acrylate used in the method is created by providing a highly branched diol; reacting the highly branched diol with a diisocyanate to obtain a polyurethane; and reacting the polyurethane with an acrylic group to form a polyurethane acrylate. The diol may have a molecular weight of greater than about 1000 g/mol.

[0021] In another embodiment, the co-curing is done by light curing or heat curing.

[0022] In another embodiment, the diisocyanate is an aliphatic diisocyanate.

[0023] In another embodiment, the polyurethane acrylate is combined with vinyl ether in a molar ratio of vinyl ether to polyurethane acrylate of equal to or less than about 1.

[0024] In another embodiment, the polyurethane acrylate has a molecular weight of over about 25000 g/mol.

[0025] In another embodiment, the adhesive composition has a modulus of less than about 1.0 mPa at −20° C. and a creep recovery of greater than about 70%.

[0026] In another embodiment, the adhesive composition has a modulus or less than about 0.3 mPa at −20° C. and a creep recovery of greater than about 90%.

[0027] In another embodiment, the polyurethane acrylate has a glass transition temperature of less than 10° C.

[0028] In another embodiment, the polyurethane acrylic polymer has a glass transition temperature of less than −30° C.

[0029] In another embodiment, the polyurethane acrylic polymer is combined with a photoinitiator or a thermal initiator before the co-curing step.

[0030] In another embodiment, the vinyl ether may be selected from poly(butyl vinyl ether), poly(ethyl vinyl ether), poly(hexyl vinyl ether), poly(isobutyl vinyl ether), poly(isopropyl vinyl ether), poly(methyl vinyl ether), poly(octyl vinyl ether), poly(propyl vinyl ether), and combinations thereof.

[0031] In another embodiment, the polyurethane acrylate may be selected from poly(2-ethylhexyl acrylate), poly(2,2,3,3,-tetrafluoropropyl acrylate), poly(4-cyanobutyl acrylate), poly(butyl acrylate), poly(dodecyl acrylate), poly(ethyl acrylate), poly(hexyl acrylate), poly(isobutyl acrylate), poly (isopropyl acrylate), poly (nonyl acrylate), poly(propyl acrylate), poly(sec-butyl acrylate), poly (tetrahydrofurfural acrylate), poly decyl methacrylate), poly(dodecyl methacrylate), poly(hexyl methacrylate), poly(isodecyl methacrylate), poly(octyl methacrylate), and combinations thereof.

[0032] The disclosure also provides an adhesive composition comprising: a co-cured mixture of polyurethane acrylate and vinyl ether, wherein the adhesive composition has a modulus of less than about 10.0 mPa at −20° C. and a creep recovery of greater than about 50%.

[0033] In one embodiment, the adhesive composition has a modulus of less than about 1.0 mPa at −20° C. and a creep recovery of greater than about 70%.

[0034] In one embodiment, the adhesive composition has a modulus of less than about 0.3 mPa at −20° C. and a creep recovery of greater than about 90%.

[0035] In another embodiment, the molar ratio of the vinyl ether to the acrylic monomer is less than about 1.

[0036] In another embodiment, there is no solvent present in the composition.

[0037] In another embodiment, the composition further comprises a thermal initiator or a photoinitiator.

[0038] In another embodiment, the diol used to prepare the polyurethane acrylate used in the invention has a highly branched polymer backbone as exemplified below:

##STR00002##

Synthesis of Polyurethane Acrylates

[0039] ##STR00003##

[0040] (NBJ408535) A 3000 g/mol dihydroxylated polyfarnesene (CVX50452, 40 g, 0.0133 mol) was added to a 100 mL reactor equipped with an overhead stirrer that was heated to 80 C. Isodecyl acrylate (18.8 g, 0.0887 mol) was added, followed by dibutyltin dilaurate (0.03 g, 0.0001 mol) and irganox 1010 (0.03 g). Subsequently IPDI (3.46 g, 0.0156 mol) was added in two portions (95% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (0.11 g, 0.0008 mol) was added after the isocyanate concentration stabilized as observed by infrared spectroscopy. After an hour butanol (0.06 g, 0.0008 mol) was added to finish quenching the reaction. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=19.9 kg/mol, Mw=39.9 kg/mol, Ð=2.

[0041] (NBJ408536) A 3000 g/mol dihydroxylated polyfarnesene (CVX50452, 100 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. Heptane (133 g) was added, followed by dibutyltin dilaurate (0.07 g). Subsequently IPDI (8.165) was added in two portions (93% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (0.2 g) and butanol (0.11 g) were added together, after the isocyanate concentration stabilized as observed by infrared spectroscopy. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=75.2 kg/mol, Mw=164.0 kg/mol, Ð=2.18.

[0042] (NBJ408537) A 3000 g/mol dihydroxylated polyfarnesene (CVX50452, 152 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. Isodecyl acrylate (65 g) was added, followed by dibutyltin dilaurate (0.106 g) and Irganox 1010 (0.106 g). Subsequently IPDI (12.90948 g) was added in two portions (92% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (0.617 g) and butanol (0.317 g) were added together, after the isocyanate concentration stabilized as observed by infrared spectroscopy. This combination was targeted to get a statistical 25:50:25 ratio of di:mono:non-functional polymer chains. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=40.9 kg/mol, Mw=156.7 kg/mol, Ð=3.82.

[0043] (NBJ408541) A 3000 g/mol dihydroxylated polyol (Priplast 3196—Croda, 155.5 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. 2-ethylhexyl acrylate (66.6 g) was added, followed by dibutyltin dilaurate (0.108 g) and Irganox 1010 (0.108 g). Subsequently IPDI (12.844 g) was added in two portions (92% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (1.98 g) and butanol (2.04 g) were added together, after the isocyanate concentration stabilized as observed by infrared spectroscopy. This combination was targeted to get a statistical 10:45:45 ratio of di-:mono-:non-functional polymer chains. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=8.1 kg/mol, Mw=85 kg/mol, Ð=10.4.

[0044] (NBJ408544) A 3000 g/mol dihydroxylated polyol (Priplast 3196—Croda, 305.88 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. 2-ethylhexyl acrylate (131.1 g) was added, followed by dibutyltin dilaurate (0.214 g) and Irganox 1010 (0.214 g). Subsequently IPDI (25.69 g) was added in two portions (92% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (1.05 g) and butanol (1.08 g) were added together, after the isocyanate concentration stabilized as observed by infrared spectroscopy. This combination was targeted to get a statistical 10:45:45 ratio of di-:mono-:non-functional polymer chains. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=30.3 kg/mol, Mw=580 kg/mol, Ð=19.1.

[0045] (NBJ408546) A 3000 g/mol dihydroxylated polyol (Priplast 3196—Croda, 217.76 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. 2-ethylhexyl acrylate (93.3 g) was added, followed by dibutyltin dilaurate (0.152 g) and Irganox 1010 (0.152 g). Subsequently IPDI (18.29 g) was added in two portions (92% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 4-hydroxybutyl acrylate (2.72 g) was added, after the isocyanate concentration stabilized as observed by infrared spectroscopy. This combination was targeted to get a statistical 100:0:0 ratio of di-:mono-:non-functional polymer chains. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=22.8 kg/mol, Mw=111.2 kg/mol, Ð=4.87.

[0046] (NBJ408550) A 3000 g/mol dihydroxylated polyol (Priplast 3196—Croda, 176.1 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. 2-ethylhexyl acrylate (75.47 g) was added, followed by dibutyltin dilaurate (0.123 g) and Irganox 1010 (0.123 g). Subsequently IPDI (14.794 g) was added in two portions (92% in first shot). The reaction was monitored by infrared spectroscopy, and the persistence of the isocyanate peak (ca. 2200 cm-1) was confirmed before addition of hydroxyl quenching agent. 1,4-butanediol vinyl ether (2.72 g) and butanol (0.557) were added together, after the isocyanate concentration stabilized as observed by infrared spectroscopy. This combination was targeted to get a statistical 25:50:25 ratio of di-:mono-:non-functional polymer chains. Infrared spectroscopy was used to confirm the complete conversion of isocyanate. The results of the synthesis were as follows: Mn=25.5 kg/mol, Mw=131.3 kg/mol, Ð=5.14.

[0047] (NBJ408553) A 5000 g/mol polyfarnesene mono-ol (CVX50457, 105 g) was added to a 1.5 L reactor equipped with an overhead stirrer that was heated to 80 C. Dibutyltin dilaurate (0.073 g) and Irganox 1010 (0.073 g) were added. Subsequently AOI (3.33 g) was added in one portion. The reaction was monitored by infrared spectroscopy, and the disappearance of the isocyanate peak (ca. 2200 cm-1) was confirmed to yield fully monofunctional material.

[0048] Another set of polymers was designed and synthesized by the similar methodology.

##STR00004##

[0049] By adjusting the feed ratio of end-cap group, a statistical mono-functional polymer can be made, as described below. In the above depiction, GI-2000IPDIn=7-10O-butyl4-HBA-OGI-2000n4-HBA-OPPGO-butylmGI-2000n4-HBA-OPriplastO-butylmIPDIIPDIIPDIIPDIIPDIIPDIIPDI.

[0050] MJ408666G GI2000 blended with PPG with 0.33 HBA end functionality.

[0051] MJ408657D GI2000 blended with PPG with 0.50 HBA end functionality.

[0052] MJ408650E GI2000 blended with PPG2000 with 0.50 HBA end functionality.

[0053] MJ408619F GI2000 blended with PPG with 0.33 end functionality.

[0054] MJ408690F GI2000 with 0.5 4-hydroxy butyl vinyl ether end functionality.

[0055] MJ408642D GI2000 with 0.5 HBA end functionality.

[0056] These resins were synthesized by the procedure described above, using the appropriate starting materials.

[0057] The following abbreviations are used herein: 4-HBA—4-hydroxybenzoic acid; IDA—iminodiacetic acid; IPDI—isophorone diisocyanate; IBA—isobornyl acrylate; AOI; 2-BCA; VE—vinyl ester; 2-EHA—2-ethylhexyl acrylate; 2-EH VA; 2-EHVE—2-ethylhexyl vinyl ether; 4-HBVE—4-hydroxybutyl vinyl ether. Irganox 1010 is the trade name for pentaerythritol tetrakis(3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate).

Synthesis of 2-decyl-1-tetradecanol acrylate

[0058] ##STR00005##

[0059] This acrylate was synthesized by reacting 2-decyl-1-tetradecanol 100.0 g (0.281 mol) with acryloyl chloride 33.38 g (0.369 mol) in toluene, using triethylamine as catalyst. The product is a colorless low viscosity liquid.

Synthesis of High MW Polymers

[0060] ##STR00006##

[0061] The synthesis of ultrahigh MW polyacrylate was done by a known synthetic procedure of SET-LRP, described as follow:

[0062] To a 250 ml four neck round bottom flask, with mechanical stirrer, condenser, additional funnel and rubber septum, was added acetonitrile (13 g), t-butyl acrylate (12.80 g, 100 mmol), copper mesh (0.43 g) (treated with 0.1 N hydrochloric acid aqueous solution for, risen with acetone), copper (II) bromide (0.013 g, 0.05 mmol, or using CuBr.sub.2 stock solution in CH.sub.3CN), the mixture was purged with nitrogen for 30 min, then raised to temperature ˜45° C., to the above solution was injected initiator tert-Butyl α-bromoisobutyrate (1.115 g, 5 mmol) and ligand Me.sub.6TREN (0.12 g, 0.50 mmol, or using stock solution in CH.sub.3CN) via air tight syringes, the reaction was monitored with .sup.1H NMR until the conversion of t-butyl acrylate >85% (˜2 hrs.) and GPC.

[0063] Following the above process but using the appropriate starting materials, the following were prepared.

##STR00007##

[0064] Synthesis of tert-polymer of methacrylate acrylate n-butyl acrylate and t-butyl acrylate (NBJ408529).

[0065] The synthesis procedure was described with the feed ratio of:

TABLE-US-00004 MW grams Moles Mole Ratio wt % methyl acrylate 86.09 0.00 0.0000 0.0 0.00% tert-butyl acrylate 128.17 0.00 0.0000 0.0 0.00% n-butyl acrylate 128.17 615.22 4.8000 8000.0 57.35% Dimethyl sulfoxide 78.13 336.1 31.33% Ethyl Acetate 88.11 121.2 11.30% Copper (II) Bromide 223.37 0.001 0.0000 0.010 0.00% diethymeso-2,5- 360.40 0.22 0.0006 1.00 0.02% dibromoadipate Me-6TREN 230.50 0.014 0.00006 0.100 0.00%

[0066] The GPC scan with the reaction time was listed as follow:

TABLE-US-00005 Rx IR Scan Rx Time GPC Mn 97 0 0.000 401 2.53 88.739 762 5.53 105.821 1052 21.7 193.614 1082 27.1 217.315 1196 46.64 402.576

[0067] Synthesis of tert-polymer of 2-ethylhexyl acrylate n-butyl acrylate and 4-hydroxybutyl acrylate (NBJ408530).

[0068] The synthesis procedure was described with the feed ratio of:

TABLE-US-00006 MW grams Moles Mole Ratio Wt % 2-ethylhexyl acrylate 184.00 220.80 1.2000 2000.0 18.70% 4-hydroxybutyl acrylate 144.00 138.24 0.9600 1600.0 11.71% n-butyl acrylate 128.17 338.37 2.6400 4400.0 28.65% Dimethyl sulfoxide 78.13 355.2 30.08% Ethyl Acetate 88.11 128.1 10.85% Copper (II) Bromide 223.37 0.001 0.0000 0.010 0.00% diethymeso-2,5- 360.40 0.22 0.0006 1.00 0.02% dibromoadipate Me-6TREN 230.50 0.014 0.00006 0.100 0.00%

[0069] GPC scan of MW vs. reaction time:

TABLE-US-00007 Rx IR Scan Rx Time GPC Mn 97 0 0.000 401 2.53 88.739 762 5.53 105.821 1052 21.7 193.614 1082 27.1 217.315 1196 46.64 402.576

[0070] Synthesis of tert-polymer of 2-ethylhexyl acrylate n-butyl acrylate and 4-hydroxybutyl acrylate (NBJ408534).

[0071] The synthesis procedure was described with the feed ratio of:

TABLE-US-00008 MW grams Moles Mole Ratio Wt % 2-ethylhexyl acrylate 184.00 750.72 4.0800 6800.0 54.07% 4-hydroxybutyl acrylate 128.17 30.76 0.2400 400.0 2.22% n-butyl acrylate 128.17 61.52 0.4800 800.0 4.43% Dimethyl sulfoxide 78.13 400.7 28.86% Ethyl Acetate 88.11 144.5 10.41% Copper (II) Bromide 223.37 0.001 0.0000 0.010 0.00% diethymeso-2,5- 360.40 0.22 0.0006 1.00 0.02% dibromoadipate Me-6TREN 230.50 0.014 0.00006 0.100 0.00%

[0072] GPC scan vs reaction time

TABLE-US-00009 Rx IR Scan Rx Time GPC Mn 97 0 0.000 401 2.53 88.739 762 5.53 105.821 1052 21.7 193.614 1082 27.1 217.315 1196 46.64 402.576

Formulation Testing

Modulus

[0073] The Optically Clear Adhesive (OCA) formulations having the compositions described below were tested on an Anton Paar MCR 302 rheometer for both modulus and creep recovery. To establish good contact with the rheometer plates, the initially liquid test sample was photo-cured to form a 600-um film through the bottom quartz plate at 100 mW/cm2 of UVA for 90 seconds. The modulus measurement was generally conducted with a 8-mm aluminium parallel plate and a liquid nitrogen cooling unit from −25 to 25° C. at 0.1% strain, 1 Hz oscillation frequency, and zero normal force. A heating rate of 3° C./min of heating rate was originally used, then switched to 5° C./min.

[0074] The moduli of the formulations at −20 and 25° C., along with the Tg values are listed in Table 1 through 6. For consistent reporting and fast data analysis, an auto-analysis macro was set up using the Anton Paar RheoPlus software to determine the moduli in megapascal (MPa) at the temperatures of interest, as well as the Tg values. In this study, the temperature corresponding to the maximum of the tan(δ) peak was taken to be the Tg. If a tan(δ) peak was not fully captured in the temperature range studied, the Tg is considered lower than −25° C., and reported as “<−25” ° C. in the tables below.

Creep Recovery

[0075] After the temperature sweep described above, the creep recovery test was performed on select formulations by straining the cured sample to 200% in 0.2 sec, allowing it to relax for 20 min at constant strain of 200%, and then monitoring the strain recovery after instantly removing all the accumulated shear stress. The strain at 2400 s of the test run was recorded, and the recovery calculated using the following equation:

[00001]$\mathrm{Recovery}=\frac{200-\mathrm{Strain}@2400s}{200}*100$

[0076] The 70D formulation described below shows a remarkably higher creep recovery of 98%. At the same time, the formulation has a modulus of 0.18 MPa at −20° C., and a modulus of 0.02 MPa at 25° C.

TABLE-US-00010 Formulation 70D Ingredient Weight (g) SB407914 4.054 IDA 0.506 Dodecyl VE 2.006 4-HBA 0.457 819 mix 0.045 7.068

Temperature Sweep Results

[0077]

TABLE-US-00011 TABLE 1 Run #1-10 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 62B 21.08 0.07 −11 62C 4.35 0.04 −15 62D 15.80 0.06 −11 63B 1.74 0.04 −18 63C 1.09 0.03 −18 63D 1.49 0.05 −20 64A 2.07 0.03 −18 64B 3.58 0.04 −16 65C 3.12 0.10 −20 65E 82.83 0.10  −6

TABLE-US-00012 TABLE 2 Run #11-20 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 66A 43.84 0.08 −10 66B 29.98 0.05 −10 66D 1.46 0.05 −22 66E 1.23 0.04 −22 67A 1.02 0.05 −24 67B 0.64 0.03 −23 67C 4.20 0.11 −21 67D 4.82 0.09 −19 68B 66.9 0.11  −5 69A 0.89 0.04 <−25 

TABLE-US-00013 TABLE 3 Run #21-30 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 69B 1.06 0.04 −23 69C 2.51 0.02 −14 69D 3.38 0.08 −20 69E 4.86 0.10 −20 70A 6.64 0.12 −19 70B 0.42 0.02 <−25  70C 0.53 0.02 <−25  70D 0.18 0.02 <−25  71A 0.19 0.02 <−25  71B 0.31 0.03 <−25 

TABLE-US-00014 TABLE 4 Run #31-40 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 71E 0.01 0.004 <−25  71E (dried) 1.58 0.08 <−25  71F 0.97 0.04 <−25  72A 0.59 0.02 <−25  72B 6.27 0.09 −18 72C 7.13 0.08 −18 73E 0.73 0.09 <−25  74B 0.54 0.06 <−25  74C 0.67 0.05 <−25  74D 0.56 0.07 <−25 

TABLE-US-00015 TABLE 5 Run #41-50 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 75A 1.35 0.09 −16 75C 0.67 0.04 <−25  75D 0.53 0.03 <−25  75E 1.28 0.06 <−25  75F 7.90 0.11 −17 76A 3.84 0.08 −19 76B 4.56 0.08 −19 76C 4.82 0.07 −17 76D 1.16 0.07 <−25  76F 0.72 0.06 <−25 

TABLE-US-00016 TABLE 6 Run #51-60 G′ @ −20° C. G′ @ 25° C. T.sub.g Formulations (MPa) (MPa) (° C.) 77A 0.95 0.06 <−25  77B 4.29 0.08 −18 77C 1.93 0.03 <−25  77D 0.33 0.06 <−25  77E 0.26 0.04 <−25  78A 0.39 0.09 <−25  78B 0.44 0.05 <−25  79F 0.46 0.09 <−25  80B 0.10 0.0008 <−25  80C 0.13 0.003 <−25 

[0078] Applicant has surprisingly found that introducing a vinyl ether monomer into an acrylate system can significantly reduce the modulus and Tg of the resulting polymer, while simultaneously achieving a high creep recovery rate at very low modulus. This combination of physical properties of very low modulus at low temperature with very high creep recovery rate has never before been observed and is an unexpected result.

[0079] The formulations tested above have the following compositions:

TABLE-US-00017 62B 62C 62D 63B 58C 6.492 58C 5.853 58C 5.139 53A 8.119 58A 0.662 58A 0.607 62A 1.045 58A 0.828 MBF 0.359 184/819/MBF 0.101 58A 0.626 mix 0.107 Sum 7.513 6.561 184/819/ 0.467 9.049 MBF 7.277 52C 63A 63C 63D 7929-19HNV 33.619 7929-19HNV 50.058 63A 8.545 63A 6.781 7929-50K 6.983 7929-50K 10.4 62A 0.739 62A 0.678 10AH-15X 7.918 10AH-15X 11.696 mix 0.105 mix 0.051 IDA 10.149 IDA 15.008 58A 0.975 7.51 4-HBA 3.379 4-HBA 5.112 10.364 I80A 4.073 92.274 66.121 64A 64B 65C 65D 52A 8.162 PEM-X264 7.188 SB407914 4.036 SB407914 9.778 59E 0.906 59E 1.267 IDA 2.542 59E 9.36 mix 0.083 2-BCA 0.489 4-HBA 0.456 19.138 9.151 mix 0.071 mix 0.08 9.015 7.114 65E 66A 66B 66D 65D 5.392 65D 6.749 65D 5.277 PEM-X264 6.464 IDA 0.494 IDA 1.706 IDA 1.96 mix 0.056 4-HBA 0.643 4-HBA 0.459 4-HBA 0.494 6.52 mix 0.067 mix 0.104 mix 0.233 6.596 9.018 7.964 66E 67A 67B 67C PEM-X264 5.452 PEM-X264 3.979 PEM-X264 6.049 MJ408642D 7.151 4-HBA 0.229 JY220-083 0.828 PIB DA 0.393 mix 0.05 mix 0.056 mix 0.027 2-BCA 0.063 7.201 5.737 4.834 mix 0.027 6.532

TABLE-US-00018 67D 68B 68D 69A MJ408642D 6.378 SB407914 3.441 7929-19HNV 15.948 PEM-X264 6.036 4-HBA 0.303 59E 3.297 7929-50K 6.611 2-BCA 0.065 2-BCA 0.1 CR551 0.624 4-HBA 1.142 Mix 0.024 mix 0.051 4-HBA 0.802 23.701 6.125 6.832 mix 0.084 8.248 69B 69C 69D 69E PEM-X264 5.305 68D 6.66 MJ408642 7.455 MJ408642 9.855 2-BCA 0.148 2-BCA 0.116 2-BCA 0.07 2-BCA 0.301 Mix 0.026 Mix 0.023 mix 0.029 mix 0.042 5.479 6.799 7.554 10.198 70A 70B 70C MJ408642 6.931 NBJ408535 6.605 NBJ408535 6.004 2-BCA 0.376 2-BCA 0.193 DMAA 0.12 mix 0.035 mix 0.027 mix 0.037 7.342 70D 71A 71B SB407914 4.054 70E 7.132 70E 5.072 IDA 0.506 mix 0.026 2-BCA 0.022 Dodecyl VE 2.006 mix 0.106 4-HBA 0.457 mix 0.045 7.068 71E 71F 71G NBJ408536 6.554 NBJ408537 7.717 52A 5 2-BCA 0.13 2-BCA 0.217 59E 0.515 mix 0.028 mix 0.063 NBJ408534 61.058 0.073 72A 72B 72C SB407914 3.417 MJ408646D 7.121 MJ408645E 7.766 59E 3.365 2-BCA 0.212 2-BCA 0.249 CM1007 2.14 mix 0.053 mix 0.053 4-HBA 2.153 IDA 0.763 mix 0.122

TABLE-US-00019 72D 73B 73E NBJ408649 6.948 MJ408646D 6.726 MJ408646D 3.705 2-BCA 0.19 Dodecyl VE 0.495 NBJ408537 3.091 mix 0.056 2-BCA 0.195 2-BCA 0.22 mix 0.056 mix 0.05 73D 72E 73F MJ408646D 3.705 MJ408650E 6.901 MJ408650E 6.075 NBJ408537 2.184 2-BCA 0.241 2-BCA 0.223 PIB DA 1.094 mix 0.061 mix 0.052 2-BCA 0.215 dodecyl VE 0.683 mix 0.05 74A 74B 74C MJ408650E 6.043 MJ408650E 6.133 MJ408646D 6.101 2-BCA 0.223 2-BCA 0.222 2-BCA 0.228 mix 0.039 15D 0.053 15D 0.045 2-EHA 0.633 2-EH VA 0.702 dodecyl VE 0.682 Polycaprolactone 0.729 DMA 74D 75A 75B MJ408650E 6.425 MJ408650E 5.872 MJ408646D 53.181 2-BCA 0.291 2-BCA 0.231 2-BCA 1.435 CM1007 0.737 CD9075 0.697 15D 0.404 15D 0.052 15D 0.051 76D 76F 77A MJ408661F 5.801 MJ408661F 8.207 SB407914 5.985 2-EHVE 0.585 2-EHVE 1.259 Dodecyl VE 0.62 BCA 0.202 BCA 0.334 BCA 0.193 15D 0.059 15D 0.086 15D 0.068 6.866 77B 77C MJ408646D 5.88 MJ408646D 4.454 4-HB VE 0.684 Octyldecyl VE 0.451 BCA 0.212 BCA 0.153 15D 0.069 15D 0.052

[0080] Although Applicant has provided descriptions and examples of various embodiments of the invention, the scope thereof is not to be limited to the specific embodiments but is defined only in the appended claims. Those of skill in the art would understand that various modifications to the embodiments of this disclosure may be made without departing from the spirit and scope of the present disclosure.