Binder for foundry process

Claim 2

The process of preparing shaped foundry products which comprises: (a) forming a foundry mix by uniformly distributing on a foundry aggregate containing sand as a major constituent a binding amount of up to 10% based on the weight of the aggregate of a binder comprising a mixture of low molecular weight mononuclear methylolated phenols substantially free of dinuclear and polynuclear species; (b) mixing therewith a polyisocyanate in a concentration of 10 to 500% by weight of the phenolic resin; (c) shaping the foundry mix in a mold; and (d) permitting said binder resin composition to react with sand polyisocyanate to form a thermoset copolymer and to bind the shaped foundry mix.

Claim 3

The process of claim 1, comprising the additional step of passing a gaseous tertiary amine through the shaped foundry mix.

Claim 4

The process of claim 1, wherein said binder comprises from 5 to 20% by weight of water, based on the weight of said mononuclear methylolated phenol mixture.

Claim 5

The process of claim 3, wherein said binder is substantially free of fugitive organic solvents.

Claim 6

The process of claim 3, wherein the foundry mix of (a) includes a tertiary amine catalyst.

Claim 7

The process of claim 5, wherein the tertiary amine catalyst is selected from the group consisting of 4-phenyl propyl pyridine and 4-picoline.

Claim 8

The process of claim 5, wherein an organo-metallic co-catalyst is added to the tertiary amine catalyst.

Claim 9

The process of claim 7, wherein the co-catalyst is an organo-tin compound.

Claim 10

The process of claim 8, wherein the co-catalyst is dibutyl tin dilaurate.

Claim 11

The process of preparing shaped foundry products which comprises: (a) forming a foundry mix by uniformly distributing on a foundry aggregate containing sand as a major constituent a binding amount of up to 10% based on the weight of the aggregate of a binder comprising a major portion of a mixture of low molecular weight mononuclear methylolated phenols, substantially free of dinuclear and polynuclear forms, and a minor proportion of a polyether polyol having an average molecular weight between about 75 and 5000 and having an average hydroxyfunctionality between about 2 and 4; (b) mixing therewith a polyisocyanate in a concentration of 10 to 500% by weight of the phenolic resin; (c) shaping the foundry mix in a mold; and (d) permitting said binder resin composition to react with said polyisocyanate to form a thermoset copolymer and to bind the shaped foundry mix.

Claim 12

The process of preparing shaped foundry products which comprises: (a) forming a foundry mix by uniformly distributing on a foundry aggregate containing sand as a major constituent a binding amount of up to 10% based on the weight of the aggregate of a binder comprising a major portion of a mixture of low molecular weight mononuclear methylolated phenols, substantially free of dinuclear and polynuclear forms, and a minor proportion of a polyether polyol having an average molecular weight between about 75 and 5000 and having an average hydroxyfunctionality between about 2 and 4; (b) mixing therewith a polyisocyanate in a concentration of 10 to 500% by weight of the phenolic resin; (c) shaping the foundry mix in a mold; and (d) permitting said binder resin composition to react with said polyisocyanate to form a thermoset copolymer and to bind the shaped foundry mix.

Claim 13

The process of claim 10, said binder comprises from 5 to 20% by weight of water based on the weight of said mononuclear methylolated phenol mixture.

Claim 14

The process of claim 11, wherein said binder is substantially free of fugitive organic solvents.

Claim 15

The process of claim 11, wherein said foundry mix of (a) includes a tertiary amine catalyst.

Claim 16

The process of claim 13, wherein the tertiary amine catalyst is selected from the group consisting of 4 -phenyl propyl pyridine and 4-picoline.

Claim 17

The process of claim 13, wherein an organo-metallic co-catalyst is added to the tertiary amine catalyst.

Claim 18

The process of claim 15, wherein the co-catalyst is an organo-tin compound.

Claim 19

The process of claim 16, wherein the co-catalyst is dibutyl tin dilaurate.

Claim 20

A process as described in claim 10, wherein the binder resin composition includes from about 10 to about 40% by weight of said polyol, based on the weight of said mononuclear methylolated phenol mixture.

Claim 21

The process of claim 18, wherein said binder is substantially free of fugitive organic solvents.

Claim 22

The process of claim 18, wherein said foundry mix of (a) includes a tertiary amine catalyst.

Claim 23

The process of claim 20, wherein the tertiary amine catalyst is selected from the group consisting of 4-phenyl propyl pyridine and 4-picoline.

Claim 24

The process of claim 10, wherein a tertiary amine catalyst is added to the foundry mix following the mixing of the polyisocyanate (b) with the foundry mix (a).

Claim 25

The process of claim 22, wherein the tertiary amine catalyst is selected from a group consisting of 4-phenyl propyl pyridine and 4-picoline.

Claim 26

The process of claim 22, wherein an organo-metallic co-catalyst is added to the tertiary amine catalyst.