Process for the preparation of low molecular weight polyhydroxyl compounds

Claim 2

In a process for the production of a polyether comprising alkoxylating an active hydrogen-containing material, the improvement wherein the active hydrogen containing material is produced by the reduction of formose at a temperature of from 80° to 220° C. and a hydrogen pressure of from 50 to 300 bar in the presence of a metal catalyst characterized in that (1) a solution at a concentration of at least 20% of the product which is required to be reduced is introduced batch-wise into a reactor so that the proportion of reducible groups, determined as carbonyl groups, in the product mixture inside the reactor does not exceed 2% by weight, (2) the pH of the hydrogenation reaction is adjusted to between 7.5 and 12.5, (3) the total quantity of catalyst used, based on the total quantity of starting material which is to be reduced, is from 10 -4 to 5×10 -2 % by weight, the catalyst content remaining constant in the reactor, and (4) the reaction product is withdrawn batch-wise from the reactor after the proportion of reducible groups (determined as carbonyl groups) has fallen below 0.15% by weight.

Claim 3

In a process for the production of a polyester polyol by reacting a carboxylic acid with a polyhydroxyl material, the improvement wherein the polyhydroxyl material is produced by the reduction of formose at a temperature of from 80° to 220° C. and a hydrogen pressure of from 50 to 300 bar in the presence of a metal catalyst, characterized in that (1) a solution at a concentration of at least 20% of the product which is required to be reduced is introduced batch-wise into a reactor so that the proportion of reducible groups, determined as carbonyl groups, in the product mixture inside the reactor does not exceed 2% by weight, (2) the pH of the hydrogenation reaction is adjusted to between 7.5 and 12.5, (3) the total quantity of catalyst used, based on the total quantity of starting material which is to be reduced, is from 10 -4 to 5×10 -2 % by weight, the catalyst content remaining constant in the reactor, and (4) the reaction product is withdrawn batch-wise from the reactor after the proportion of reducible groups (determined as carbonyl groups) has fallen below 0.15% by weight.

Claim 4

In a process for the production of a polyester polyol by reacting a carboxylic acid with a polyhydroxyl material, the improvement wherein the polyhydroxyl material is produced by the reduction of formose at a temperature of from 80° to 220° C. and a hydrogen pressure of from 50 to 300 bar in the presence of a metal catalyst, characterized in that (1) a solution at a concentration of at least 20% of the product which is required to be reduced is introduced batch-wise into a reactor so that the proportion of reducible groups, determined as carbonyl groups, in the product mixture inside the reactor does not exceed 2% by weight, (2) the pH of the hydrogenation reaction is adjusted to between 7.5 and 12.5, (3) the total quantity of catalyst used, based on the total quantity of starting material which is to be reduced, is from 10 -4 to 5×10 -2 % by weight, the catalyst content remaining constant in the reactor, and (4) the reaction product is withdrawn batch-wise from the reactor after the proportion of reducible groups (determined as carbonyl groups) has fallen below 0.15% by weight.

Claim 5

Process for the preparation of cellular or non-cellular polyurethane resins by the reaction of (a) polyisocyanates with (b) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 32 to 400, optionally (c) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 400 to 10,000, and optionally (d) blowing agents, catalysts and other known additives, characterized in that the compounds used as component (b) comprise polyhydric alcohols prepared by the reduction of formose at a temperature of from 80° to 220° C. and a hydrogen pressure of from 50 to 300 bar in the presence of a metal catalyst, characterized in that (1) a solution at a concentration of at least 20% of the product which is required to be reduced is introduced batch-wise into a reactor so that the proportion of reducible groups, determined as carbonyl groups, in the product mixture inside the reactor does not exceed 2% by weight (2) the pH of the hydrogenation reaction is adjusted to between 7.5 and 12.5, (3) the total quantity of catalyst used, based on the total quantity of starting material which is to be reduced, is from 10 -4 to 5×10 -2 % by weight, the catalyst content remaining constant in the reactor, and (4) the reaction product is withdrawn batch-wise from the reactor after the proportion of reducible groups (determined as carbonyl groups) has fallen below 0.15% by weight.

Claim 6

Process for the preparation of cellular or non-cellular polyurethane resins by the reaction of (a) polyisocyanates with (b) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 32 to 400, optionally (c) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 400 to 10,000, and optionally (d) blowing agents, catalysts and other known additives, characterized in that the compounds used as component (b) comprise polyhydric alcohols prepared by the reduction of formose at a temperature of from 80° to 220° C. and a hydrogen pressure of from 50 to 300 bar in the presence of a metal catalyst, characterized in that (1) a solution at a concentration of at least 20% of the product which is required to be reduced is introduced batch-wise into a reactor so that the proportion of reducible groups, determined as carbonyl groups, in the product mixture inside the reactor does not exceed 2% by weight (2) the pH of the hydrogenation reaction is adjusted to between 7.5 and 12.5, (3) the total quantity of catalyst used, based on the total quantity of starting material which is to be reduced, is from 10 -4 to 5×10 -2 % by weight, the catalyst content remaining constant in the reactor, and (4) the reaction product is withdrawn batch-wise from the reactor after the proportion of reducible groups (determined as carbonyl groups) has fallen below 0.15% by weight.