Method for producing a low viscosity spray polyol by reacting an alkylene oxide with the reaction product of a phenol, an amine and a smaller formaldehyde portion

Claim 1

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol, an amine and formaldehyde, (1) the amine being selected from the group consisting of ammonia and alkanolamines having the formula: ##STR7## where R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and --(CHR) n --OH and n is a positive integer having a value of two to five, (2) the molar ratio of phenol to amine being about 1:2, and (3) the molar ratio of formaldehyde to phenol being from about 1.25:1 to about 1.75:1; b. heating the resulting mixture at a temperature within the range of from about 50 to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; c. stripping the water from the reaction product; d. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30 to 200° C.; and e. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 2

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol, an amine and formaldehyde, (1) the amine being selected from the group consisting of ammonia and alkanolamines having the formula: ##STR7## where R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and --(CHR) n --OH and n is a positive integer having a value of two to five, (2) the molar ratio of phenol to amine being about 1:2, and (3) the molar ratio of formaldehyde to phenol being from about 1.25:1 to about 1.75:1; b. heating the resulting mixture at a temperature within the range of from about 50 to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; c. stripping the water from the reaction product; d. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30 to 200° C.; and e. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 7

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol and an alkanolamine selected from the group consisting of alkanolamines having the formula: ##STR8## wherein R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and--(CHR) n --OH and n is a positive integer having a value of two to five, the molar ratio of phenol to alkanolamine being about 1:2; b. adding formaldehyde to the mixture in proportions such that the molar ratio of formaldehyde to phenol ranges from about 1.25:1 to about 1.75:1; c. heating the resulting mixture at a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 8

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol and an alkanolamine selected from the group consisting of alkanolamines having the formula: ##STR8## wherein R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and--(CHR) n --OH and n is a positive integer having a value of two to five, the molar ratio of phenol to alkanolamine being about 1:2; b. adding formaldehyde to the mixture in proportions such that the molar ratio of formaldehyde to phenol ranges from about 1.25:1 to about 1.75:1; c. heating the resulting mixture at a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 13

A method for producing a low viscosity, nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing nonylphenol and diethanolamine, the molar ratio of nonylphenol to diethanolamine being about 1:2; b. adding formaldehyde to the mixture in proportions such that the molar ratio of formaldehyde to nonylphenol is in the range of about 1.25:1 to about 1.75:1; c. heating the resulting mixture at a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding propylene oxide and ethylene oxide separately or together to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 14

A method for producing a low viscosity, nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing nonylphenol and diethanolamine, the molar ratio of nonylphenol to diethanolamine being about 1:2; b. adding formaldehyde to the mixture in proportions such that the molar ratio of formaldehyde to nonylphenol is in the range of about 1.25:1 to about 1.75:1; c. heating the resulting mixture at a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding propylene oxide and ethylene oxide separately or together to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 16

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol and formaldehyde such that the molar ratio of formaldehyde to phenol is in the range of about 1.25:1 to about 1.75:1; b. adding an alkanolamine selected from the group consisting of alkanolamines having the formula: ##STR9## wherein R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and --(CHR) n --OH and n is a positive integer of two to five, the molar ratio of phenol to alkanolamine being about 1:2; c. heating the resulting mixture of a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.

Claim 17

A method for producing a low viscosity nitrogen-containing polyol suitable for use in sprayed, high density, rigid polyurethane foam, comprising the steps of a. mixing a phenol and formaldehyde such that the molar ratio of formaldehyde to phenol is in the range of about 1.25:1 to about 1.75:1; b. adding an alkanolamine selected from the group consisting of alkanolamines having the formula: ##STR9## wherein R is selected from the group consisting of hydrogen and C 1 -C 4 alkyl, R' is selected from the group consisting of hydrogen, C 1 -C 4 alkyl and --(CHR) n --OH and n is a positive integer of two to five, the molar ratio of phenol to alkanolamine being about 1:2; c. heating the resulting mixture of a temperature within the range of from about 50° to 150° C. for a period of time sufficient to reduce the formaldehyde content to no more than about 1 wt.%; d. stripping the water from the reaction product; e. adding separately or together at least two different alkylene oxides selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, styrene oxide, and glycidol to said stripped reaction product at a temperature within the range of about 30° to 200° C.; and f. recovering a nitrogen-containing polyol having a hydroxyl number of from about 250 to about 900, a nitrogen content of from about 1 to about 15 wt.% and a viscosity of 15,000 centipoise or less at 25° C.