Alcohol distillation process

Claim 2

In a continuous process for the distillation and purification of a crude alcohol-containing mixture, wherein a feed stream containing a saturated aliphatic alcohol having not more than three carbon atoms and associated impurities is introduced into an extractive distillation tower, water is introduced into the upper portion of said extractive distillation tower, an overhead stream containing substantially all of said impurities is removed from said extractive distillation tower, a dilute aqueous stream containing a low concentration of said alcohol is withdrawn from the bottom of said extractive distillation tower and is introduced into a rectifying tower, a desired alcohol product is withdrawn and recovered from the upper portion of said rectifying tower, and a stripped aqueous effluent stream is withdrawn from the bottom of said rectifying tower and a part thereof is recycled to the upper portion of said extractive distillation tower, and wherein said alcohol product may contain trace impurities which cannot readily be separated by distillation; the improved method of removing said trace impurities without adversely affecting the operation of said extractive distillation tower which comprises: introducing into said rectifying tower an aqueous solution of an alkali metal compound selected from the group consisting of the alkali metal hydroxides and carbonates; and regulating the feed rate of said aqueous solution to said rectifying tower so that the concentration of said alkali metal compound in said stripped aqueous effluent stream withdrawn from the bottom of said rectifying tower is from about 0.10 to about 0.24 gram per liter; the recycled part of said stripped aqueous effluent stream being recycled to said extractive distillation tower without neutralization.

Claim 3

The process of claim 1 further characterized in that said alkali metal compound concentration is from about 0.12 to about 0.18 gram per liter.

Claim 4

The process of claim 1 further characterized in that said alkali metal compound is sodium hydroxide.

Claim 5

The process of claim 1 further characterized in that said alcohol is ethanol.

Claim 6

In a continuous process for the purification of crude alcohol-containing mixtures comprising introducing into the middle portion of a first distillation tower comprising an extractive distillation zone a feed stream containing a saturated aliphatic alcohol having not more than three carbon atoms and associated lower boiling and higher boiling impurities; introducing water into the upper portion of said first distillation tower; removing an overhead stream from said first distillation tower containing substantially all of said impurities; withdrawing from the bottom of said first distillation tower a dilute aqueous stream containing said alcohol at a concentration of from about 5 wt.% to about 10 wt.% and also containing minor amounts of said lower boiling and said higher boiling impurities; introducing said dilute aqueous stream withdrawn from the bottom of said first distillation tower into a second distillation tower comprising a rectifying or alcohol concentrating zone; withdrawing and recovering from the upper portion of said second distillation tower an alcohol product stream comprising said alcohol in highly concentrated and purified form; withdrawing a stripped aqueous effluent stream from the bottom of said second distillation tower and recycling the same in part to the upper portion of said first distillation tower; withdrawing from said second distillation tower an overhead purge stream containing said lower boiling impurities; withdrawing from an intermediate portion of said second distillation tower at least one purge stream containing said higher boiling impurities; introducing into a third distillation tower comprising an impurities concentrating zone said purge streams from said second distillation tower and said overhead stream from said first distillation tower; withdrawing from said third distillation tower said lower boiling and said higher boiling impurities; and withdrawing from said third distillation tower an alcohol-containing stream and recycling the same to said first distillation tower in combination with said feed stream; and wherein said alcohol product stream may contain trace impurities which cannot readily be separated by distillation; the improved method of removing said trace impurities without adversely affecting the operation of said first distillation tower which comprises: introducing into said second distillation tower, below the point of withdrawal of said alcohol product stream but above the point of introduction of said aqueous stream from the bottom of said first distillation tower, an aqueous solution of an alkali metal compound selected from the group consisting of the alkali metal hydroxides and carbonates; and regulating the feed rate of said aqueous solution to said second distillation tower so that the concentration of said alkali metal compound in said stripped aqueous effluent stream withdrawn from the bottom of said second distillation tower is from about 0.10 to about 0.24 gram per liter; the recycled part of said stripped aqueous effluent stream being recycled to said first distillation tower without neutralization.

Claim 7

In a continuous process for the purification of crude alcohol-containing mixtures comprising introducing into the middle portion of a first distillation tower comprising an extractive distillation zone a feed stream containing a saturated aliphatic alcohol having not more than three carbon atoms and associated lower boiling and higher boiling impurities; introducing water into the upper portion of said first distillation tower; removing an overhead stream from said first distillation tower containing substantially all of said impurities; withdrawing from the bottom of said first distillation tower a dilute aqueous stream containing said alcohol at a concentration of from about 5 wt.% to about 10 wt.% and also containing minor amounts of said lower boiling and said higher boiling impurities; introducing said dilute aqueous stream withdrawn from the bottom of said first distillation tower into a second distillation tower comprising a rectifying or alcohol concentrating zone; withdrawing and recovering from the upper portion of said second distillation tower an alcohol product stream comprising said alcohol in highly concentrated and purified form; withdrawing a stripped aqueous effluent stream from the bottom of said second distillation tower and recycling the same in part to the upper portion of said first distillation tower; withdrawing from said second distillation tower an overhead purge stream containing said lower boiling impurities; withdrawing from an intermediate portion of said second distillation tower at least one purge stream containing said higher boiling impurities; introducing into a third distillation tower comprising an impurities concentrating zone said purge streams from said second distillation tower and said overhead stream from said first distillation tower; withdrawing from said third distillation tower said lower boiling and said higher boiling impurities; and withdrawing from said third distillation tower an alcohol-containing stream and recycling the same to said first distillation tower in combination with said feed stream; and wherein said alcohol product stream may contain trace impurities which cannot readily be separated by distillation; the improved method of removing said trace impurities without adversely affecting the operation of said first distillation tower which comprises: introducing into said second distillation tower, below the point of withdrawal of said alcohol product stream but above the point of introduction of said aqueous stream from the bottom of said first distillation tower, an aqueous solution of an alkali metal compound selected from the group consisting of the alkali metal hydroxides and carbonates; and regulating the feed rate of said aqueous solution to said second distillation tower so that the concentration of said alkali metal compound in said stripped aqueous effluent stream withdrawn from the bottom of said second distillation tower is from about 0.10 to about 0.24 gram per liter; the recycled part of said stripped aqueous effluent stream being recycled to said first distillation tower without neutralization.

Claim 8

The process of claim 5 further characterized in that said alcohol is ethanol.

Claim 9

The process of claim 5 further characterized in that said alkali metal compound is sodium hydroxide.

Claim 10

The process of claim 5 further characterized in that the concentration of said alkali metal compound is from about 0.12 to about 0.18 gram per liter.

Claim 11

The process of claim 5 further characterized in that the acetaldehyde content of the ethanol product stream is not greater than about 0.24 gram per 100 liters of ethanol.

Claim 12

The process of claim 1 further characterized in that said aqueous solution is the sole treating agent introduced into said rectifying tower for removing said trace impurities, and the essential active ingredient of said aqueous solution consists of said alkali metal compound.

Claim 13

The process of claim 1 further characterized in that sid alkali metal compound is sodium hydroxide and said alcohol is ethanol.

Claim 14

The process of claim 11 further characterized in that the concentration of said sodium hydroxide is from about 0.12 to about 0.18 gram per liter.

Claim 15

The process of claim 5 further characterized in that said aqueous solution is the sole treating agent introduced into said second distillation tower for removing said trace impurities, and the essential active ingredient of said aqueous solution solution consists of said alkali metal compound.

Claim 16

The process of claim 5 further characterized in that said alcohol is ethanol and said alkali metal compound is sodium hydroxide.

Claim 17

The process of claim 14 further characterized in that the concentration of said sodium hydroxide is from about 0.12 to about 0.18 gram per liter.

Claim 18

The process of claim 14 further characterized in that the acetaldehyde content of the ethanol product stream is not greater than about 0.24 gram per 100 liters of ethanol.