Separation of aromatics with pervaporation membrane
View Patent ↗Methods and apparatus relate to separating and removing aromatic compounds from a hydrocarbon stream. Splitting of the hydrocarbon stream into constituents as desired relies on a membrane and distillation columns that supply feed into the membrane and receive retentate and permeate streams output from the membrane. Configurations employing the membrane and the distillation columns enable benzene recovery and facilitate efficient separation.
1. A method, comprising:
passing a hydrocarbon stream through a first distillation column to separate a first fraction containing aromatics from a second fraction;
passing the first fraction through a membrane unit to generate a retentate stream and a permeate stream with higher benzene content than the retentate stream;
passing the retentate stream through a second distillation column to provide first fractionated outputs with one further concentrated in toluene relative to the retentate stream; and
passing the permeate stream through a third distillation column to provide second fractionated outputs with one further concentrated in benzene relative to the permeate stream.
2. The method according to claim 1 , wherein the membrane unit includes a pervaporation membrane and a nanofiltration membrane.
3. The method according to claim 1 , wherein the membrane unit comprises multiple membranes with retentate from one membrane being in direct fluid communication with another membrane.
4. The method according to claim 1 , wherein the hydrocarbon stream is output from a reformer and passes through the first distillation column and the membrane unit without passing through an aromatics extraction unit.
5. The method according to claim 1 , wherein the hydrocarbon stream is output from a reformer.
6. The method according to claim 1 , wherein vapor overhead from the second distillation column is removed to recover benzene.
7. The method according to claim 1 , wherein vapor overhead from the second distillation column and an intermediate cut from the third distillation column are removed to recover benzene.
8. The method according to claim 1 , wherein vapor overhead from the second distillation column is removed to recover benzene from remainder of the retentate stream including toluene and vapor overhead from the third distillation column is removed to recover components lighter than benzene from remainder of the permeate stream including benzene.
9. The method according to claim 1 , wherein vapor overhead from the third distillation column is removed to recover benzene.
10. The method according to claim 1 , wherein vapor overhead from the third distillation column is removed to recover benzene from toluene recovered by both liquid removal from the third distillation column and vapor overhead removal from the second distillation column.
11. The method according to claim 1 , wherein the permeate stream contains about 80% aromatic content.
12. The method according to claim 1 , wherein the fractionated outputs from the second and third distillation columns include vapor overheads formed of less than 20% by weight of respective ones of the retentate and permeate streams.
13. The method according to claim 1 , wherein the first fraction is a top cut removed from the first distillation column.
14. The method according to claim 1 , wherein the first fraction is a bottom cut removed from the first distillation column.
15. A method, comprising:
passing a hydrocarbon stream through a first distillation column to separate a top fraction containing aromatics from a bottom fraction;
passing the top fraction through a membrane unit to generate a retentate stream and a permeate stream with higher benzene content than the retentate stream;
passing the retentate stream through a second distillation column for overhead removal of benzene such that remaining output of the second distillation column is further concentrated in toluene relative to the retentate stream; and
passing the permeate stream through a third distillation column for overhead removal of components lighter than benzene such that remaining output of the third distillation column is further concentrated in benzene relative to the permeate stream.
16. The method according to claim 15 , wherein a recovered benzene stream defined by the overhead removal of the benzene from the second distillation column contains at least 99% benzene by weight.
17. The method according to claim 15 , wherein the first distillation column separates the top fraction of C7− from the bottom fraction of C8+.
18. A method, comprising:
passing a hydrocarbon stream through a first distillation column to separate a bottom fraction containing aromatics from a top fraction;
passing the bottom fraction through a membrane unit to generate a retentate stream and a permeate stream with higher benzene content than the retentate stream;
passing the retentate stream through a second distillation column for overhead removal of toluene concentrated relative to the retentate stream due to separation from remaining output of the second distillation column; and
passing the permeate stream through a third distillation column for overhead removal of benzene concentrated relative to the permeate stream due to separation from remaining output of the second distillation column.
19. The method according to claim 18 , wherein a recovered benzene stream defined by the overhead removal of the benzene from the third distillation column contains at least 99% benzene by weight.
20. The method according to claim 18 , wherein the first distillation column separates the bottom fraction of C6+ from the top fraction of C5−.