Granted Patent B2

US 7,435,787 · App. 11/226,694 · Granted Oct 14, 2008

Abstract

Claims (76)

1. A process for the continuous production of silylated prepolymer resin which comprises:

a) continuously metering into a feed line a predetermined quantity of reactants to form a mixture comprising:

(i) a polyol;

(ii) a silylating agent; and

(iii) optionally, at least one additive;

b) continuously introducing the mixture of step (a) into a first tubular reactor with an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheated using an external heat source to a temperature ranging from about 120° C. up to about 200° C.;

c) continuously mixing, heating to the reaction temperature, drying, devolatilizing and grinding the mixture of step (b) in the tubular reactor with an internal static mixer;

d) continuously feeding a stream containing catalysts which is introduced into a second tubular reactor downstream of the inlet into which combined feeds (i), (ii) and, optionally, (iii) are introduced;

e) continuously reacting the ingredients of step (d) as the ingredients move linearly through the second tubular reactor under reaction conditions of temperature and time sufficient to complete the endcapping reaction in the tubular reactor and produce a silylated prepolymer resin; and,

f) continuously removing the silylated prepolymer resin from the second tubular reactor and directing the silylated prepolymer resin continuously into a cooler which cools the silylated prepolymer resin to a temperature of from about 20° C. to about 80° C.

2. The process of claim 1 wherein the polyol is selected from the group consisting of polyester polyols, polyesteramide polyols, polyether polyols, polythioether polyols, polycarbonate polyols, polyacetal polyols, polyolefin polyols and polysiloxane polyols.

3. The process of claim 1 wherein the silylating agent is an isocyanatosilane.

4. The process of claim 3 wherein the isocyanatosilane is selected from the group consisting of 3-isocyanatopropylmethyldimethoxysilane, 3-isocyanatopropyltrimethoxysilane and 3-isocyanatopropyltriethoxysilane.

5. The process of claim 1 wherein the polyol is reacted with a polyisocyanate prior to the addition of the silylating agent to provide a polymer having repeating urethane groups.

6. The process of claim 5 wherein the polyisocyanate is selected from the group consisting of ethylene diisocyanate, 1,6-hexamethylene diisocyanate, isophorone diisocyanate, cyclohexane-1,4-diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, p-xylylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, 4,4′-diphenylmethane diisocyanate, 2,4′-diphenylmethane diisocyanate, polymethylene polyphenyl polyisocyanates and 1,5-naphthylene dilsocyanate.

7. The process of claim 5 wherein an excess of polyol is reacted with the polyisocyanate so as to produce a polyurethane terminated with hydroxyl groups.

8. The process of claim 1 wherein the silylating agent corresponds to the formula:

Y—R 1 —Si(Me) n (OR 2 ) 3−n

wherein

Y is —NCO,

R is an alkyl group having from 1-10 carbon atoms,

R 1 is a divalent hydrocarbon group having from 1-10 carbon atoms,

Me is methyl,

OR 2 is an alkoxy group wherein R 2 has from 1 to 5 carbon atoms, and

n=0 to 3.

9. The process of claim 1 wherein the silylated prepolymer is continuously blended with one or more additives for providing a finished product.

10. The process of claim 9 wherein the finished product is a sealant and/or adhesive and/or coating composition.

11. The process of claim 9 wherein the additive comprises one or more compounds selected from the group consisting of plasticizers, colorants, stabilizers, thixotropes and fillers.

12. A process for the continuous production of silylated prepolymer resin which comprises:

a) continuously metering into a feed line a predetermined quantity of reactants to form a mixture comprising:

(i) a polyol;

(ii) a polyisocyanate; and

(iii) optionally, plasticizers, colorants, stabilitizers, thixotropes, and fillers;

b) continuously introducing the premixed reactants of step (a) into a first tubular reactor with an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheated using an external heat source to a temperature ranging from about 80° C. up to about 200° C.;

c) continuously mixing, heating to the reaction temperature, drying, devolatilizing and grinding the mixture of step (b) in the first tubular reactor with an internal static mixer and moving the mixture from the first tubular reactor to a second tubular reactor;

d) continuously introducing a stream containing catalysts to the mixture of step (c) at a position between the first tubular reactor and the second tubular reactor;

e) continuously moving the mixture linearly through the second tubular reactor, said second tubular reactor including an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1, and preheating the mixture of reactants and catalyst of step (d) using an external heat source to a temperature ranging from about 80° C. up to about 200° C. under reaction conditions of temperature and time sufficient to cause a chain extension reaction to occur to provide a polymer having repeating urethane groups so as to produce a polyurethane with hydroxyl groups; and

f) continuously introducing a predetermined quantity of silylating agent to the mixture of step (e) between the second tubular reactor and a third tubular reactor;

g) continuously introducing the mixture of step (f) exiting the second tubular reactor into the third tubular reactor, wherein the third tubular reactor includes an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheated using an external heat source to a temperature ranging from about 120° C. up to about 200° C.;

h) continuously reacting the ingredients of step (g) as the ingredients move linearly through the third tubular reactor under reaction conditions of temperature and time sufficient to complete the endcapping reaction in the third tubular reactor and produce a silylated prepolymer resin; and

i) continuously removing the silylated prepolymer resin from the third tubular reactor and cooling the silylated prepolymer resin in a cooler to a temperature from about 20° C. to about 80° C.

13. The process of claim 12 wherein the polyol is selected from the group consisting of polyester polyols, polyesteramide polyols, polyether polyols, polythioether polyols, polycarbonate polyols, polyacetal polyols, polyolefin polyols and polysiloxane polyols.

14. The process of claim 12 wherein the silylating agent is an isocyanatosilane.

15. The process of claim 12 wherein the isocyanatosilane is selected from the group consisting of 3-isocyanatopropylmethyldimethoxysilane, 3-isocyanatopropyltrimethoxysilane and 3-isocyanatopropyltriethoxysilane.

16. The process of claim 15 wherein the polyol is reacted with a polyisocyanate prior to the addition of the silylating agent to provide a polymer having repeating urethane groups so as to produce a polyurethane with hydroxyl groups.

17. The process of claim 16 wherein the polyisocyanate is selected from the group consisting of ethylene diisocyanate, 1,6-hexamethylene diisocyanate, isophorone diisocyanate, cyclohexane-1,4-diisocyanate, 4,4′-dicyclohexylmethane diisocyanate, p-xylylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-toluene diisocyanate, 2,6-toluene diisocyanate, 4,4′-diphenylmethane diisocyanate, 2,4′-diphenylmethane diisocyanate, polymethylene polyphenyl polyisocyanates and 1,5-naphthylene diisocyanate.

18. A process for the continuous production of silylated prepolymer resin which comprises:

a) continuously metering into a feed line a predetermined quantity of reactants to form a mixture comprising:

(i) a polyol;

(ii) an excess of polyisocyanate; and

(iii) optionally, plasticizers, colorants, stabilitizers, thixotropes, and fillers;

b) continuously introducing the premixed reactants of the feed line step (a) into a first tubular reactor with an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheated using an external heat source to a temperature ranging from about 80° C. up to about 200° C.;

c) continuously mixing, heating to the reaction temperature, drying, devolatilizing and grinding the mixture of step (b) in the tubular reactor with an internal static mixer and moving the mixture from the first tubular reactor to a second tubular reactor;

d) continuously introducing a stream containing catalysts to the mixture of step (c) between the first tubular reactor and the second tubular reactor;

e) continuously moving the mixture linearly through the second tubular reactor, said second tubular reactor including an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheating the mixture of reactants and catalyst of step (d) using an external heat source to a temperature ranging from about 80° C. up to about 200° C. under reaction conditions of temperature and time sufficient to cause a chain extension reaction to occur and to provide a polymer having repeating urethane groups so as to produce a polyurethane with isocyanate groups; and

f) continuously introducing a predetermined quantity of silylating agent to the mixture of step (e) between the second tubular reactor and a third tubular reactor;

g) continuously introducing the mixture of step (f) into the third tubular reactor, said third tubular reactor having an internal static mixer with a ratio of length to diameter of from about 10:1 to about 50:1 and preheated using an external heat source to a temperature ranging from about 120° C. up to about 200° C.;

h) continuously reacting the ingredients of step (g) as the ingredients move linearly through the third tubular reactor under reaction conditions of temperature and time sufficient to complete the endcapping reaction in the tubular reactor and produce a silylated prepolymer resin; and

i) continuously removing the silylated prepolymer resin from the third tubular reactor and directing the silylated prepolymer resin into a cooler which cools the silylated prepolymer resin to a temperature from about 20° C. to about 80° C.

19. The process of claim 18 wherein an excess of polyisocyanate is reacted with the polyol so as to produce a polyurethane terminated with isocyanate groups.

20. The process of claim 19 wherein the silylating agent is an aminosilane.

21. The process of claim 20 wherein the aminosilane is selected from the group consisting of 4-amino-3,3-dimethylbutyltrimethoxysilane, 4-amino-3,3-dimethylbutyldimethoxymethylsilane, N-methyl-4-amino-3,3-dimethylbutyltrimethoxysilane, aminoisopropoxyethyltrimethoxysilane, aminoisopropoxypropyltrimethoxysilane, 4-amino-3,3 -dimethylbutyltriethoxysilane, 4-amino-3,3-dimethylbutyldiethoxymethylsilane, N-methyl-4-amino-3,3 -dimethylbutyltriethoxysilane and aminoisopropoxyethyltriethoxysilane.

22. The process of claim 18 wherein the silylating agent is an aminosilane.

23. The process of claim 22 wherein the aminosilane is selected from the group consisting of 4-amino-3,3-dimethylbutyltrimethoxysilane, 4-amino-3 ,3-dimethylbutyldimethoxymethylsilane, N-methyl-4-amino-3,3-dimethylbutyltrimethoxysilane, aminoisopropoxyethyltrimethoxysilane, aminoisopropoxypropyltrimethoxysilane, 4-amino-3,3-dimethylbutyltriethoxysilane, 4-amino-3,3-dimethylbutyldiethoxymethylsilane, N-methyl-4-amino-3,3-dimethylbutyltriethoxysilane and aminoisopropoxyethyltriethoxysilane.

24. The process of claim 18 wherein the silylating agent corresponds to the formula:

Y—R 1 —Si(Me) n (OR 2 ) 3−n

wherein

Y is —NHR, —NH 2, or —SH,

R is an alkyl group having from 1-10 carbon atoms,

R 1 is a divalent hydrocarbon group having from 1-10 carbon atoms,

Me is methyl,

OR 2 is an alkoxy group wherein R 2 has from 1 to 5 carbon atoms, and

n=0 to 3.

25. The process of claim 18 wherein the silylated prepolymer is continuously blended with one or more additives for providing a finished product.

26. The process of claim 25 wherein the finished product is a sealant and/or adhesive and/or coating composition.

27. The process of claim 25 wherein the additive comprises one or more compounds selected from the group consisting of plasticizers, colorants, stabilizers, thixotropes and fillers.

Assignments (23)