Process for filament winding

• US 20050038222A1
• Filed: 09/21/2004
• Published: 02/17/2005
• Est. Priority Date: 03/29/2002
• Status: Abandoned Application

• Current Assignee: Huntsman International LLC (Huntsman Corporation)
• Original Assignee: Huntsman International LLC (Huntsman Corporation)
• Inventors: Joshi, Ravi R., Cheolas, Evan H.
• Application Number:
  US10/947,113
• Publication Number:
  US 20050038222A1
• Time in Patent Office: Days
• US Class Current: 528/44
• CPC Class Codes: B29C 35/00 Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor moulds with incorporated heating or cooling means B29C33/02 ; thermal after-treatment of shaped articles B29C71/02; curing devices for plastics dental prostheses A61C13/14; before moulding B29B13/00
• CPC Class Codes: B29C 53/587 having a non-uniform wall-structure, e.g. with inserts, perforations, locally concentrated reinforcements
• CPC Class Codes: B29C 53/8066 Impregnating impregnating as pretreatment B29B15/10
• CPC Class Codes: B29K 2075/00 Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
• CPC Class Codes: C08G 18/289 containing silicon
• CPC Class Codes: C08G 18/36 Hydroxylated esters of higher fatty acids
• CPC Class Codes: C08G 18/4018 Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
• CPC Class Codes: C08G 18/4812 Mixtures of polyetherdiols with polyetherpolyols having at least three hydroxy groups
• CPC Class Codes: C08G 18/6674 with compounds of group C08G18/3203
• CPC Class Codes: C08G 18/6696 with compounds of group C08G18/36 or hydroxylated esters of higher fatty acids of C08G18/38

Abstract

Filament winding process based on the mixing initiated polymerization of an at least two-component resin system, the system comprising an organic polyisocyanate and a polyfunctional active hydrogen composition as the principle isocyanate reactive species. The invention further provides improved composite articles produced by the filament winding process.

Claims

1. A reaction system for use in filament winding comprising:

a. an organic polyisocyanate;

b. an organic polyfunctional active hydrogen resin containing a plurality of active hydrogen groups that are reactive towards organically bound isocyanate groups; and

c. optionally, a catalyst that promotes the reaction of organically bound isocyanate groups with active hydrogen groups,

wherein the reaction system is substantially free of styrene, methyl methacrylate, and organic resins or organic monomers boiling at less than 185°

C. at 1 atmosphere pressure;

wherein the number averaged functionality of the organic polyisocyanate or the organic polyfunctional active hydrogen resin is greater than two;

wherein the reaction system exhibits a gel time of 1500 seconds or greater, as measured from the completion of mixing at 25°

C.; and

wherein the reaction system exhibits a gel time from 25 to 45 seconds, as measured from the completion of mixing at 45°

C.

2. The reaction system of claim 1 wherein the organic polyisocyanate is selected from the group consisting of 4,4′

-diphenylmethane diisocyanate, 2,4′

-diphenylmethane diisocyanate, polymethylene polyphenylene polyisocyanates, and mixtures thereof.

3. The reaction system of claim 1 wherein the reaction system comprises a catalyst and the catalyst comprises bismuth.

5. The reaction system of claim 1 wherein the reaction system further comprises an inert hydrocarbon oil having an initial boiling point greater than 200°

C. at 1 atmosphere pressure.

6. The reaction system of claim 1 wherein the reaction system further comprises at least one member selected from the group consisting of castor oil and isocyanate terminated prepolymers derived from castor oil.

7. The reaction system of claim 1 wherein the reaction system further comprises a fire retardant.

8. The reaction system of claim 1 wherein the reaction system further comprises an adhesion promoter.

9. The reaction system of claim 1 wherein the number averaged functionality of both the organic polyisocyanate and the organic polyfunctional active hydrogen resin is greater than two.

4. A reaction system for use in filament winding comprising:

a. an organic polyisocyanate;

b. an organic polyfunctional active hydrogen resin containing a plurality of active hydrogen groups that are reactive towards organically bound isocyanate groups; and

c. a catalyst that comprises bismuth, which catalyst promotes the reaction of organically bound isocyanate groups with active hydrogen groups,

wherein the reaction system is substantially free of styrene, methyl methacrylate, and organic resins or organic monomers boiling at less than 185°

C. at 1 atmosphere pressure; and

wherein the number averaged functionality of the organic polyisocyanate or the organic polyfunctional active hydrogen resin is greater than two.

10. A process for producing a filament wound thermoset composite article comprising the steps of:

a. mixing an organic polyisocyanate, an organic polyfunctional active hydrogen resin containing a plurality of active hydrogen groups that are reactive towards organically bound isocyanate groups, and optionally, a catalyst that promotes the reaction of organically bound isocyanate groups with active hydrogen groups in a suitable ratio to form a reaction system;

b. applying the reaction system to a filament in order to form a resin treated filament;

c. winding the resin treated filament around a mandrel in order to form a shaped article; and

d. curing the resin in order to form a cured shaped article,

wherein the reaction system is substantially free of styrene, methyl methacrylate, and organic resins or organic monomers boiling at less than 185°

C. at 1 atmosphere pressure;

wherein the number averaged functionality of the organic polyisocyanate or the organic polyfunctional active hydrogen resin is greater than two;

wherein the reaction system exhibits a gel time of 1500 seconds or greater, as measured from the completion of mixing at 25°

C.; and

wherein the reaction system exhibits a gel time from 25 to 45 seconds, as measured from the completion of mixing at 45°

C.

11. The process of claim 10 wherein the reaction system is substantially free of any organic species, with the exception of carbon dioxide, having a boiling point less than 200°

C. at 1 atmosphere pressure.

12. The process of claim 10 wherein the reaction system is substantially free of any organic species having a boiling point less than 260°

C. at 1 atmosphere pressure.

13. The process of claim 10 wherein the reaction system is substantially free of any organic species having a vapor pressure greater than or equal to 0.1 mmHg at 25°

C.

14. The process of claim 10 wherein the organic polyisocyanate is selected from the group consisting of 4,4′

-diphenylmethane diisocyanate, 2,4′

-diphenylmethane diisocyanate, polymethylene polyphenylene polyisocyanates, and mixtures thereof.

15. The process of claim 10 wherein the reaction system comprises a catalyst and the catalyst comprises bismuth.

18. The process of claim 10 wherein the reaction system further comprises a fire retardant.

19. The process of claim 10 wherein the reaction system further comprises an adhesion promoter.

20. The process of claim 10 wherein the reaction system further comprises an inert hydrocarbon oil having an initial boiling point greater than 200°

C. at 1 atmosphere pressure.

21. The process of claim 10, wherein the polyfunctional active hydrogen resin comprises at least one hydrophobic polyol selected from the group consisting of hydrocarbon backbone polyols and fatty polyester polyols.

22. The process of claim 10, wherein the organic polyisocyanate comprises an isocyanate terminated prepolymer derived from at least one hydrophobic polyol selected from the group consisting of hydrocarbon backbone polyols and fatty polyester polyols.

23. The process of claim 10 wherein the number averaged functionality of both the organic polyisocyanate and the organic polyfunctional active hydrogen resin is greater than two.

24. The process of claim 10, wherein the resin cures by forming a covalently crosslinked network structure.

16. A process for producing a filament wound thermoset composite article comprising the steps of:

a. mixing an organic polyisocyanate, an organic polyfunctional active hydrogen resin containing a plurality of active hydrogen groups that are reactive towards organically bound isocyanate groups, and a catalyst that comprises bismuth, which catalyst promotes the reaction of organically bound isocyanate groups with active hydrogen groups in a suitable ratio to form a reaction system;

b. applying the reaction system to a filament in order to form a resin treated filament;

c. winding the resin treated filament around a mandrel in order to form a shaped article; and

d. curing the resin in order to form a cured shaped article,

wherein the reaction system is substantially free of styrene, methyl methacrylate, and organic resins or organic monomers boiling at less than 185°

C. at 1 atmosphere pressure; and

wherein the number averaged functionality of the organic polyisocyanate or the organic polyfunctional active hydrogen resin is greater than two.

17. The process of claim 16 wherein the reaction system further comprises at least one member selected from the group consisting of castor oil and isocyanate terminated prepolymers derived from castor oil.