Process for the purification of ε-caprolactam

Claim 2

A process for purifying a dehydrated ε-caprolactam product obtained by rearrangement of cyclohexanone oxime in the presence of sulfuric acid or oleum by distilling said caprolactam under reduced pressure to separate out low-boiling and high-boiling impurities from said caprolactam to yield a very pure polymerizable grade ε-caprolactam product, said process comprising the combination of steps of: A. conducting said distillation of untreated ε-caprolactam in a first and in a second stage wherein said first stage and said second stage each includes an evaporator and a rectification column containing packing material such that the pressure drop across each theoretic tray in the respective rectification columns is less than about 2.5 mbar; B. supplying said impure caprolactam to said rectification column in said first stage; C. separating out as a top product the low-boiling impurities from said caprolactam in said rectification column in said first stage while leaving caprolactam containing high-boiling impurities as a bottom product; D. feeding said bottom product to said second stage and separating out the high-boiling impurities from the caprolactam in said bottom product; and E. recovering polymerizable grade ε-caprolactam having purity greater than 99.9 weight percent as a top product in said second stage.

Claim 3

Process according to claim 1 wherein a bottom temperature of about 115° to about 175° C. is applied in the rectification column of the first stage, while a bottom temperature of about 115 to about 145° C. is applied in the rectification column of the second stage.

Claim 4

A two stage process for purifying a dehydrated impure ε-caprolactam product obtained by rearrangement of cyclohexanone oxime in the presence of sulfuric acid or oleum by distilling the impure ε-caprolactam under reduced pressure to separate out low-boiling and high-boiling impurities to thereby yield a very pure polymerizable grade ε-caprolactam product, said process comprising the combination of steps of: A. supplying said impure ε-caprolactam to a first stage and then distilling said impure ε-caprolactam in said first stage, said first stage including an evaporator and a rectification column, said rectification column containing packing material such that the pressure drop cross each theoretical tray therein is less than about 1.5 mbar, said first stage rectification column having a bottom temperature of about 115° C. to about 175° C.; B. separating out as a top product the low-boiling impurities from said impure ε-caprolactam in said first stage rectification column while leaving a bottom product containing ε-caprolactam and high boiling impurities; C. feeding said bottom product from said first stage to a second stage and then distilling said bottom product in said second stage, said second stage including an evaporator and a rectification column, said second stage rectification column containing packing material such that the pressure drop across each theoretical tray therein is less than about 1.5 mbar, said rectification column having a bottom temperature of about 115° C. to about 145° C.; D. separating out a second stage bottom product from said bottom product of step (b) in said second stage rectification column, said second stage bottom product containing the high-boiling impurities; and E. recovering polymerizable grade ε-caprolactam having a purity greater than 99.9 weight percent as a top product from said second stage rectification column.

Claim 5

A two stage process for purifying a dehydrated impure ε-caprolactam product obtained by rearrangement of cyclohexanone oxime in the presence of sulfuric acid or oleum by distilling the impure ε-caprolactam under reduced pressure to separate out low-boiling and high-boiling impurities to thereby yield a very pure polymerizable grade ε-caprolactam product, said process comprising the combination of steps of: A. supplying said impure ε-caprolactam to a first stage and then distilling said impure ε-caprolactam in said first stage, said first stage including an evaporator and a rectification column, said rectification column containing packing material such that the pressure drop cross each theoretical tray therein is less than about 1.5 mbar, said first stage rectification column having a bottom temperature of about 115° C. to about 175° C.; B. separating out as a top product the low-boiling impurities from said impure ε-caprolactam in said first stage rectification column while leaving a bottom product containing ε-caprolactam and high boiling impurities; C. feeding said bottom product from said first stage to a second stage and then distilling said bottom product in said second stage, said second stage including an evaporator and a rectification column, said second stage rectification column containing packing material such that the pressure drop across each theoretical tray therein is less than about 1.5 mbar, said rectification column having a bottom temperature of about 115° C. to about 145° C.; D. separating out a second stage bottom product from said bottom product of step (b) in said second stage rectification column, said second stage bottom product containing the high-boiling impurities; and E. recovering polymerizable grade ε-caprolactam having a purity greater than 99.9 weight percent as a top product from said second stage rectification column.

Claim 6

Process according to any one of the claims 1 or 3 wherein said initial impure caprolactam supply to said first stage is about 95% to about 99.9% pure by weight.

Claim 7

Process according to any one of the claims 1 or 3 wherein a bottom pressure of about 5 mbar to about 70 mbar is applied in the rectification column of the first stage, and a bottom pressure of about 5 to about 15 mbar is applied in the rectification column of the second stage.

Claim 8

Process according to claim 1 or 3 wherein said impure ε-caprolactam supply to said first stage is about 95% to 99.9% pure by weight, said first stage rectification column having a bottom pressure of about 5 mbar to about 70 mbar, and said second stage rectification column having a bottom pressure of about 5 to about 15 mbar.