Continuous process for producing alkylene glycols from alkylene carbonates

Claim 2

A continuous process for making glycols of the formula HOCHRCH.sub.2 OH by the base hydrolysis of an alkylene carbonate of the formula ##STR2## in which each R is either hydrogen or methyl, which comprises: (A) providing the alkylene carbonate in admixture of water, carbon dioxide, alkylene glycol and potassium carbonate catalyst, to form a homogeneous liquid phase mixture; (B) providing said mixture in a reaction zone wherein the temperature of said mixture is at least 100° C; (c) evolving carbon dioxide from said homogeneous liquid phase mixture; (D) separating the potassium carbonate catalyst in a mixture with alkylene glycol from glycol product; (E) recycling said catalyst-glycol mixture to step (A); and (F) periodically feeding potassium carbonate catalyst make-up to said catalyst-glycol mixture before it is fed to step (A).

Claim 3

the continuous process of claim 1, wherein the potassium carbonate catalyst is utilized in an amount of between about 0.03 to about 10 weight percent, based on the weight of alkylene carbonate fed to the reaction.

Claim 4

The continuous process of claim 2, wherein the amount of potassium carbonate catalyst is between about 0.1 to about 5.0 weight percent.

Claim 5

The continuous process of claim 3, wherein the amount of potassium carbonate catalyst is between 0.25 and about 1.5 weight percent.

Claim 6

The continuous process of claim 1, wherein the temperature of step (B) is between 100° and 300° C.

Claim 7

The continuous process of claim 5, wherein the temperature is between about 120° and about 200° C.

Claim 8

The continuous process of claim 1, wherein pressure in the reaction zone of step (B) is greater than about 80 psig.

Claim 9

The continuous process of claim 7, wherein the pressure is greater than about 80 psig and less than about 2000 psig.

Claim 10

The continuous process of claim 8, wherein the pressure is greater than about 80 psig and less than about 750 psig.

Claim 11

The continuous process of claim 1, wherein the amount of water combined with the alkylene carbonate is at least one mole of water for each mole of alkylene carbonate.

Claim 12

The continuous process of claim 10, wherein the amount of water is at least about 1.2 moles of water to about 10 moles of water for each mole of alkylene carbonate.

Claim 13

The continuous process of claim 11, wherein the mole ratio of water is 1.5 to 2.5 moles for each mole of alkylene carbonate.

Claim 14

The continuous process of claim 1, wherein the alkylene carbonate is ethylene carbonate.

Claim 15

The continuous process of claim 1, wherein the glycol product is ethylene glycol.

Claim 16

A continuous process for making glycols of the formula HOCHRCH.sub.2 OH by the base hydrolysis of an alkylene carbonate of the formula ##STR3## in which each R is either hydrogen or methyl, which comprises: (A) providing the alkylene carbonate in admixture of water, carbon dioxide, alkylene glycol and potassium carbonate catalyst, to form a homogeneous liquid phase mixture; (B) providing said mixture in a reaction zone wherein the temperature of said mixture is at least 100° C; (c) evolving carbon dioxide from said homogeneous liquid phase mixture; (D) separating the potassium carbonate catalyst in admixture with alkylene glycol from glycol product; (E) recycling said catalyst-glycol mixture to step (A); (f) periodically feeding potassium carbonate catalyst make-up to said catalyst-glycol mixture before it is fed to step (A); (g) separating water from glycol product in step (D); and (H) recycling said water to step (A).

Claim 17

A continuous process for making glycols of the formula HOCHRCH.sub.2 OH by the base hydrolysis of an alkylene carbonate of the formula ##STR3## in which each R is either hydrogen or methyl, which comprises: (A) providing the alkylene carbonate in admixture of water, carbon dioxide, alkylene glycol and potassium carbonate catalyst, to form a homogeneous liquid phase mixture; (B) providing said mixture in a reaction zone wherein the temperature of said mixture is at least 100° C; (c) evolving carbon dioxide from said homogeneous liquid phase mixture; (D) separating the potassium carbonate catalyst in admixture with alkylene glycol from glycol product; (E) recycling said catalyst-glycol mixture to step (A); (f) periodically feeding potassium carbonate catalyst make-up to said catalyst-glycol mixture before it is fed to step (A); (g) separating water from glycol product in step (D); and (H) recycling said water to step (A).