Urea-formaldehyde resin manufacture

Claim 2

A resin comprising a reaction product of urea and formaldehyde having a ratio of formaldehyde to urea which is between 2.0:1 and 1.1:1 wherein the degree of condensation of the resin is between 25% and 45%, and the resin is a solid at room temperature.

Claim 3

A solid resin according to claim 1 in which the degree of condensation is between 30% and 43%.

Claim 4

A solid resin according to claim 1 in which the degree of condensation is between 30% and 40%.

Claim 5

A solid resin according to claim 1 which comprises also units derived from an amide, a reactive hydroxyl compound or an amino-triazine compound or a formaldehyde reaction product of one of these compounds, said units comprising not more than 4 per cent by weight of the resin.

Claim 6

A solid resin according to claim 4 in which said units are selected from the group consisting of units derived from acetamide, sulphanilamide, malonamide, p-toluene sulphonamide, succinamide, dicyandiamide, phenol, o-cresol or a partially condensed melamine-formaldehyde resin.

Claim 7

A solid resin according to claim 4 in which the units comprise not more than 2.00 percent by weight of the resin.

Claim 8

A process for the manufacture of a solid ureaformaldehyde resin as claimed in claim 1 which comprises the steps of (a) reacting a solution of formaldehyde in water with urea at a molar ratio of formaldehyde to urea which is greater THAN 2.5:1. (b) concentrating the solution so made until its total water content was less than 50% by weight. (c) adding further urea to adjust the molar ratio of formaldehyde to urea to between 2.0:1 and 1.1:1 and (d) concentrating the solution further without precipitation of solid resin to reduce the water content to such a level that on cooling the liquid resin product a friable solid is obtained, wherein a stabilization agent is reacted into said solution of formaldehyde or urea and formaldehyde prior to step (d) in order to prevent precipitation of resin in step (d).

Claim 9

A process according to claim 7 in which step (a) is carried out at a pH in the range of 5.5 to 6.5.

Claim 10

A process according to claim 7 in which water is allowed to distil off the reacting mixture in step (a).

Claim 11

A process according to claim 7 in which the resin is taken to a degree of condensation not greater than 40% through all of steps (a) to (d).

Claim 12

A process according to claim 7 in which the stabilization agent is selected from the group consisting of melamine, partially condensed, melamine-formaldehyde resins, acetamide, sulphanilamide, malonamide, p-toluene sulphonamide, succinamide, dicyandiamide, ethylene glycol, phenol and o-cresol

Claim 13

A process according to claim 10 in which the molar ratio of formaldehyde to urea is adjusted to a value in the range 1.2:1 to 1.6:1 in step (c).

Claim 14

A process according to claim 7 in which in step (a) a mixture of urea and another amino monomer is used, the proportion of the latter being no more than 40 mole % of the mixture.

Claim 15

A process according to claim 7 in which step (b) is carried out under mildly alkaline conditions.

Claim 16

A process according to claim 14 in which step (d) is carried out under neutral to mildly alkaline conditions.