Process for continuously preparing copolyamides from lactams and salts of diamines and dicarboxylic acids
US-9200115-B2 · Dec 1, 2015 · US
US10442928B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10442928-B2 |
| Application number | US-201715650407-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 14, 2017 |
| Priority date | Jul 28, 2016 |
| Publication date | Oct 15, 2019 |
| Grant date | Oct 15, 2019 |
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Compositions of polyamide resins containing a low level of polyamide 66 comonomer are provided, which are useful in producing blown films. A method of forming a blown film includes: extruding a polyamide copolymer to form a polyamide film. The polyamide copolymer is formed from a mixture of caprolactam and hexamethylenediamine adipate where the caprolactam comprises from 85 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate.
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The invention claimed is: 1. A method of forming a blown film, the method comprising: extruding a polyamide copolymer to form a polyamide film, wherein the polyamide copolymer consists of caprolactam and hexamethylenediamine adipate monomers, wherein the caprolactam monomers are present in an amount of from 85 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers, the polyamide copolymer further having: an isothermal crystallization time, measured by Differential Scanning Calorimetry (DSC) according to ASTM E2070, of between 4 minutes and 14 minutes; and a degree of randomness of between 0.95 and 1.25; and wherein extruding the polyamide copolymer includes forming a bubble in the extruded polyamide copolymer by injecting air through an injection port and gathering the extruded polyamide copolymer with one or more rollers into the polyamide film. 2. The method of claim 1 , wherein the caprolactam monomers are present in an amount of from 90 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers. 3. The method of claim 1 , wherein the caprolactam monomers are present in an amount of from 92 mol. % to 96 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers. 4. The method of claim 1 , where the polyamide copolymer is formed by a first step of blending caprolactam and an aqueous solution of AH salt under agitation at a temperature between 150° C. and 170° C., followed by a second step of polymerizing the mixture of caprolactam and hexamethylenediamine adipate in a continuous polymerization train at an elevated temperature above 170° C. 5. The method of claim 1 , further comprising: extruding a polyethylene polymer to form a polyethylene film, and combining the polyamide film and polyethylene film to form a multilayer film. 6. The method of claim 1 , wherein the polyamide copolymer has a crystallization temperature of 140° C. to 160° C. 7. The method of claim 1 , wherein the polyamide copolymer has a melt point of 190° C. to 210° C. 8. The method of claim 1 , wherein the polyamide copolymer has a puncture resistance of 55 in-lb f to 95 in-lb f . 9. A blown film comprising a polyamide layer, the polyamide layer comprising a polyamide copolymer consisting of caprolactam and hexamethylenediamine adipate monomers, wherein the caprolactam monomers are present in an amount of from 85 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers, the polyamide copolymer further comprising: an isothermal crystallization time, measured by Differential Scanning calorimetry (DSC) according to ASTM E2070, of between 4 minutes and 14 minutes; and a degree of randomness of between 0.95 and 1.25. 10. The blown film of claim 9 , wherein the caprolactam monomers are present in an amount of from 90 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers. 11. The blown film of claim 9 , wherein the caprolactam monomers are present in an amount of from 92 mol. % to 96 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers. 12. The blown film of claim 9 , wherein the polyamide copolymer has a crystallization temperature of 140° C. to 170° C. 13. The blown film of claim 9 , wherein the polyamide copolymer has a crystallization temperature of 140° C. to 160° C. 14. The blown film of claim 9 , wherein the polyamide copolymer has a melt point of 190° C. to 210° C. 15. The blown film of claim 9 , wherein the polyamide copolymer has an isothermal crystallization time of 1.25 min to 12 min at 170° C. 16. The blown film of claim 9 , further comprising a polyethylene layer. 17. The blown film of claim 9 , wherein the polyamide copolymer has a degree of randomness between 0.95 to 1.1. 18. The blown film of claim 9 , wherein the polyamide copolymer has a puncture resistance of 55 in-lb f to 95 in-lb f . 19. A polyamide copolymer consisting of caprolactam and hexamethylenediamine adipate monomers, wherein the caprolactam monomers are present in an amount of from 85 mol. % to 99 mol. % of the total moles of caprolactam and hexamethylenediamine adipate monomers, and wherein the copolymer has a melt point of 190° C. to 205° C., an isothermal crystallization time, measured by Differential Scanning calorimetry (DSC) according to ASTM E2070, of between 4 minutes and 14 minutes; and a degree of randomness of between 0.95 and 1.25. 20. The polyamide copolymer of claim 19 , wherein the copolymer has a degree of randomness of 0.95 to 1.1. 21. The polyamide copolymer of claim 19 , wherein the copolymer has a puncture resistance of 55 in-lb f to 95 in-lb f .
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