Process for removing 2-butanol from tert-butanol/water mixtures
View Patent ↗The invention relates to a process for separating 2-butanol from an industrial mixture which includes 2-butanol, tert-butanol and water by separating water from the industrial mixture by distillation to obtain a distillate, wherein the distillate has, in terms of the 2-butanol, tert-butanol and water in the industrial mixture, a proportion by mass of water, which at a pressure, is greater than the limit concentration of the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water; subsequently changing the pressure so that the mixture has, in terms of the 2-butanol, tert-butanol and water in the distillate, a proportion by mass of water which is less than the limit concentration of the distillation boundary line connecting the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water; and subsequently distilling the mixture at the same pressure into a stream comprising 2-butanol and a stream comprising tert-butanol and water.
1. A process for separating 2-butanol from an industrial mixture which comprises 2-butanol, tert-butanol and water, wherein the proportion by mass of water is greater than the limit concentration of the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water, comprising
(a) separating water from the industrial mixture by distillation to obtain a distillate, wherein the distillate has, in terms of the 2-butanol, tert-butanol and water in the industrial mixture, a proportion by mass of water, which at a pressure, is greater than the limit concentration of the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water;
(b) subsequently changing the pressure so that the mixture has, in terms of the 2-butanol, tert-butanol and water in the distillate, a proportion by mass of water which is less than the limit concentration of the distillation boundary line connecting the distillation boundary line connecting an azeotrope of tert-butanol and water; and an azeotrope of 2-butanol and water; and
(c) subsequently distilling the mixture at the same pressure into a stream comprising 2-butanol and a stream comprising tert-butanol and water.
2. The process as claimed in claim 1 , wherein the distillation in (a) is performed on a distillation column.
3. The process as claimed in claim 2 , wherein the distillation in (a) is performed at a pressure of from 0.7 to 5 bara.
4. The process as claimed in claim 3 , wherein the pressure in (b) and (c) is from 0.05 to not more than 0.7 bara.
5. The process as claimed in claim 3 , wherein the pressure in (b) and (c) is from at least 5 to 15 bara.
6. The process as claimed in claim 3 , wherein the stream comprising 2-butanol contains less than 2% by mass of tert-butanol.
7. The process as claimed in claim 6 , wherein a part of the distillate from (c) is combined with the distillate of (a) and used as a feed to the distillation in (c).
8. The process as claimed in claim 3 , wherein the separating of the stream comprising 2-butanol comprises taking a vapor phase of a vaporizer of a column; or a gaseous or liquid as a side stream in a stripping section of the column.
9. The process as claimed in claim 1 , wherein the distillation in (a) is performed at a pressure of from 0.7 to 5 bara (bar absolute).
10. The process as claimed in claim 9 , wherein the pressure in (b) and (c) is from 0.05 to not more than 0.7 bara.
11. The process as claimed in claim 9 , wherein the pressure in (b) and (c) is from at least 5 to 15 bara.
12. The process as claimed in claim 1 , wherein the stream comprising 2-butanol contains less than 2% by mass of tert-butanol.
13. The process as claimed in claim 12 , wherein the stream comprising 2-butanol contains less than 1.7% by mass of tert-butanol.
14. The process as claimed in claim 12 , wherein a part of the distillate from (c) is combined with the distillate of (a) and used as a feed to the distillation in (c).
15. The process as claimed in claim 1 , wherein the separating of the stream comprising 2-butanol comprises taking a vapor phase of a vaporizer of a column; or a gaseous or liquid as a side stream in a stripping section of the column.
16. The process as claimed in claim 1 , wherein the pressure in (a) is from 0.4 to 5 bara when the proportion of 2-butanol in the industrial mixture is from 0.001 to 30% by mass.
17. The process as claimed in claim 16 , wherein the pressure in (b) is from 5 to 15 bara.
18. The process as claimed in claim 16 , wherein the pressure in (b) is from 5 to 10 bara.
19. The process as claimed in claim 1 , wherein the changing the pressure in (b) comprises increasing the pressure at least 2 times more than the pressure in (a).
20. The process as claimed in claim 1 , wherein the stream comprising tert-butanol and water comprises less than 4% by mass of 2-butanol.
21. The process as claimed in claim 1 , wherein the stream comprising tert-butanol and water comprises less than 3% by mass of 2-butanol.