US 4,293,692 AGranted

Continuous process for manufacturing substantially fully methylated substantially fully methylolated melamine compositions

AssigneeAmerican Cyanamid Company

InventorsVenkatrao K. Pai, Joseph F. Skrivan

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Abstract

The manufacture of a substantially fully methylated, substantially fully methylolated melamine composition is carried out by a continuous process in which the methylolation of melamine is conducted in two stages, the first stage being effected at an acidic pH and the second stage being effected at an alkaline pH. The reaction mixture is then concentrated and reacted with methanol after which all of the unreacted volatiles and precipitated salts are removed to provide the product composition.

Claims11

Dependent claims

A continuous process for making a substantially fully methylated, substantially fully methylolated melamine composition comprising the steps of:

(1) conducting the methylolation of melamine in two stages as follows:
(a) in a first stage, continuously charging melamine and aqueous formaldehyde to a first reaction zone in a ratio of from about 9 to about 18 moles of formaldehyde per mole of melamine while controlling the pH of the reaction mixture thus formed in the reaction zone at from about 4 to 6 and also controlling the temperature of the reaction mixture at from about 45.degree. C. to about 75.degree. C. and the residence time of the mixture in said zone for a period sufficiently long to allow the melamine to become methylolated to an average of about 4.5 to 5.5, said methylolated product being from about 40% to about 70% in the oligomeric state and from about 30% to about 60% in the monomeric state, then (b), in a second stage, passing the reaction mixture from the first reaction zone to a second reaction zone and adjusting the pH of the mixture in the second zone to from above 7 to about 10 and holding the temperature at about 45.degree. C. to about 75.degree. C. for a residence time sufficient for the melamine monomers and oligomers to become substantially fully methylolated;
(2) withdrawing the methylolated reaction mixture from the second reactor and removing about 70-95% of the water content thereof;
(3) passing the concentrated reaction mixture to a third reaction zone along with from about 20 to about 30 moles of methanol per mole of melamine utilized in step 1(a) while controlling the pH of the mixture at from about 1.2 to about 2.5, the temperature of the reaction mixture at from about 30.degree. C. to about 55.degree. C. and the residence time of the mixture in the reaction zone for a period sufficient to effect an average degree of methylation of the methylolmelamine of at least 4.5;
(4) withdrawing the reaction mixture from the third reaction zone into a neutralization zone and adjusting the pH thereof to from about 9 to 12;
(5) withdrawing the mixture from the neutralization zone to a distillation column and distilling off unreacted methanol therefrom;
(6) passing the bottoms from the distillation column to a stripping zone and stripping off substantially all of the water and unreacted formaldehyde therefrom;
and
(7) treating the bottoms from step 6 in a solids separation unit to remove precipitated salts therefrom and provide the substantially fully methylated, substantially fully methylolated melamine composition product.

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A continuous process for making a substantially fully methylated, substantially fully methylolated melamine composition comprising the steps of:

(1) conducting the methylolation of melamine in two stages as follows:
(a) in a first stage, continuously charging melamine and aqueous formaldehyde to a first reaction zone in a ratio of from about 9 to about 18 moles of formaldehyde per mole of melamine while controlling the pH of the reaction mixture thus formed in the reaction zone at from about 4 to 6 and also controlling the temperature of the reaction mixture at from about 45.degree. C. to about 75.degree. C. and the residence time of the mixture in said zone for a period sufficiently long to allow the melamine to become methylolated to an average of about 4.5 to 5.5, said methylolated product being from about 40% to about 70% in the oligomeric state and from about 30% to about 60% in the monomeric state, then (b), in a second stage, passing the reaction mixture from the first reaction zone to a second reaction zone and adjusting the pH of the mixture in the second zone to from above 7 to about 10 and holding the temperature at about 45.degree. C. to about 75.degree. C. for a residence time sufficient for the melamine monomers and oligomers to become substantially fully methylolated;
(2) withdrawing the methylolated reaction mixture from the second reactor and removing about 70-95% of the water content thereof;
(3) passing the concentrated reaction mixture to a third reaction zone along with from about 20 to about 30 moles of methanol per mole of melamine utilized in step 1(a) while controlling the pH of the mixture at from about 1.2 to about 2.5, the temperature of the reaction mixture at from about 30.degree. C. to about 55.degree. C. and the residence time of the mixture in the reaction zone for a period sufficient to effect an average degree of methylation of the methylolmelamine of at least 4.5;
(4) withdrawing the reaction mixture from the third reaction zone into a first neutralization zone and adjusting the pH thereof to from about 9 to 12;
(5) withdrawing the mixture from the neutralization zone to a distillation column and distilling off unreacted methanol therefrom;
(6) passing the bottoms from the distillation column to a first stripping zone and stripping off substantially all of the water and unreacted formaldehyde therefrom;
(7) passing the bottoms from the first stripping zone to a fourth reaction zone along with sufficient methanol to provide about 5-10 additional moles of methanol per mole of melamine used in step 1(a) and controlling the pH of the mixture at 1.2-2.5, the temperature at from about 30.degree. C. to about 55.degree. C. and the residence time to a period sufficient to give an average degree of methylation of at least 5.3;
(8) passing the reaction mixture from the fourth reactor to a second neutralization zone and adjusting the pH thereof to about 8-10;
(9) passing the reaction mixture from the second neutralization zone to a second stripping zone and stripping off all the volatiles therefrom and finally
(10) treating the bottoms from the second stripping zone in a solids separation unit to remove precipitated salts therefrom and provide the substantially fully methylated, substantially fully methylolated melamine composition product.

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Dependencies are inferred from the claim text.

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Abstract

A continuous process for making a substantially fully methylated, substantially fully methylolated melamine composition comprising the steps of:

(1) conducting the methylolation of melamine in two stages as follows:
(a) in a first stage, continuously charging melamine and aqueous formaldehyde to a first reaction zone in a ratio of from about 9 to about 18 moles of formaldehyde per mole of melamine while controlling the pH of the reaction mixture thus formed in the reaction zone at from about 4 to 6 and also controlling the temperature of the reaction mixture at from about 45.degree. C. to about 75.degree. C. and the residence time of the mixture in said zone for a period sufficiently long to allow the melamine to become methylolated to an average of about 4.5 to 5.5, said methylolated product being from about 40% to about 70% in the oligomeric state and from about 30% to about 60% in the monomeric state, then (b), in a second stage, passing the reaction mixture from the first reaction zone to a second reaction zone and adjusting the pH of the mixture in the second zone to from above 7 to about 10 and holding the temperature at about 45.degree. C. to about 75.degree. C. for a residence time sufficient for the melamine monomers and oligomers to become substantially fully methylolated;
(2) withdrawing the methylolated reaction mixture from the second reactor and removing about 70-95% of the water content thereof;
(3) passing the concentrated reaction mixture to a third reaction zone along with from about 20 to about 30 moles of methanol per mole of melamine utilized in step 1(a) while controlling the pH of the mixture at from about 1.2 to about 2.5, the temperature of the reaction mixture at from about 30.degree. C. to about 55.degree. C. and the residence time of the mixture in the reaction zone for a period sufficient to effect an average degree of methylation of the methylolmelamine of at least 4.5;
(4) withdrawing the reaction mixture from the third reaction zone into a neutralization zone and adjusting the pH thereof to from about 9 to 12;
(5) withdrawing the mixture from the neutralization zone to a distillation column and distilling off unreacted methanol therefrom;
(6) passing the bottoms from the distillation column to a stripping zone and stripping off substantially all of the water and unreacted formaldehyde therefrom;
and
(7) treating the bottoms from step 6 in a solids separation unit to remove precipitated salts therefrom and provide the substantially fully methylated, substantially fully methylolated melamine composition product.

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