Anhydride separation

Claim 2

In a process for separating maleic anhydride or phthalic anhydride from a gaseous mixture by absorption into an organic absorbent flowing downwardly and countercurrently to the gaseous mixture in an absorption column having at least 4 stages, the improvement which comprises removing heat from a zone of the absorption column above the gaseous mixture feed point and below the top 2 stages of the column in a sufficient amount so that more than half of the temperature gradient for the absorbent liquid in the column is across at least 2 stages above the gaseous mixture feed point and below the top 2 stages of the column, thereby substantially avoiding the formation of solids when removing heat from the absorption column.

Claim 3

A process in accordance with claim 1 wherein the anhydride is maleic anhydride.

Claim 4

A process in accordance with claim 2 wherein more than 70 percent of the temperature gradient for the absorbent liquid in the column is across at least 2 stages above the gaseous mixture feed point and below the top 2 stages of the column.

Claim 5

A process in accordance with claim 2 wherein more than 90 percent of the temperature gradient from the absorbent liquid in the column is across at least 2 stages above the gaseous mixture feed point and below the top 2 stages of the column.

Claim 6

A process in accordance with claim 1 wherein the heat is removed by withdrawing a stream of absorbent from the lower part of the column, cooling the steam, and then recycling the resulting cooled absorbent to the column.

Claim 7

A process in accordance with claim 2 wherein the column has between about 10 and 50 stages.

Claim 8

A process in accordance with claim 5 wherein said heat is withdrawn from the column in a zone between about the second and tenth stages above the gaseous mixture feed point.

Claim 9

A process in accordance with claim 7 wherein said heat is removed by withdrawing a stream of absorbent from the lower part of the column, cooling the stream, and then recycling the resulting cooled absorbent to the column.

Claim 10

A process for separating maleic or phthalic anhydride from a gaseous mixture containing the anhydride which comprises: a. introducing the gaseous mixture to an absorption column having at least four stages at a mixture feed point near the bottom of the column; b. introducing stripped organic absorbent to the column at an absorbent feed point near the top of the column; c. countercurrently contacting the gaseous mixture in the absorption column with a downwardly flowing stream of the organic absorbent effective to preferentially absorb the anhydride and obtain rich absorbent; d. withdrawing a stream of the absorbent from the column; e. cooling at least a portion of said withdrawn stream to obtain cooled absorbent; f. recycling the cooled absorbent to the column at a point at least two stages above the mixture feed point and at least two stages below the absorbent feed point, thereby removing heat from the column so that more than half of the temperature gradient for the absorbent liquid in the column is across at least 2 stages above the gaseous mixture feed point and below the top 2 stages of the column, and substantially avoiding the formation of solids when removing heat from the absorption column; g. withdrawing the rich absorbent from the bottom of the column; and h. stripping anhydride from the absorbent to obtain a separated anhydride and said stripped absorbent.

Claim 11

A process for separating maleic or phthalic anhydride from a gaseous mixture containing the anhydride which comprises: a. introducing the gaseous mixture to an absorption column having at least four stages at a mixture feed point near the bottom of the column; b. introducing stripped organic absorbent to the column at an absorbent feed point near the top of the column; c. countercurrently contacting the gaseous mixture in the absorption column with a downwardly flowing stream of the organic absorbent effective to preferentially absorb the anhydride and obtain rich absorbent; d. withdrawing a stream of the absorbent from the column; e. cooling at least a portion of said withdrawn stream to obtain cooled absorbent; f. recycling the cooled absorbent to the column at a point at least two stages above the mixture feed point and at least two stages below the absorbent feed point, thereby removing heat from the column so that more than half of the temperature gradient for the absorbent liquid in the column is across at least 2 stages above the gaseous mixture feed point and below the top 2 stages of the column, and substantially avoiding the formation of solids when removing heat from the absorption column; g. withdrawing the rich absorbent from the bottom of the column; and h. stripping anhydride from the absorbent to obtain a separated anhydride and said stripped absorbent.

Claim 12

A process in accordance with claim 9 wherein said column has between about 10 and 50 stages and wherein said heat is removed from said column in a zone between about the second and tenth stages above the gaseous mixture feed point.

Claim 13

A process in accordance with claim 10 wherein a sufficient amount of heat is withdrawn so that more than about 70% of the temperature gradient for the absorbent in the column is across said zone.

Claim 14

A process in accordance with claim 11 wherein the anhydride is maleic anhydride and wherein the gaseous mixture is fed to the column at a temperature between about 200° and 275° F.