Recovery and purification of ethylene

• US 7,437,891 B2
• Filed: 12/20/2004
• Issued: 10/21/2008
• Est. Priority Date: 12/20/2004
• Status: Active Grant

• Current Assignee: Ineos USA LLC (Ineos AG)
• Original Assignee: Ineos USA LLC (Ineos AG)
• Inventors: Reyneke, Rian, Sinclair, Iain, Lee, Guang-Chung, Foral, Michael J., Lodgson, Jeffery S., Eng, Wayne W. Y.
• Primary Examiner(s): Caldarola; Glenn
• Assistant Examiner(s): Boyer; Randy
• Application Number:
  US11/017,159
• Publication Number:
  US 20060135840A1
• Time in Patent Office: 1,401 Days
• Field of Search: 626/07, 626/20, 626/22, 626/23, 626/27, 629/31, 629/32, 629/35, 629/39, 208/347, 208/350, 208/353, 208/355, 208/351, 585/800, 585/809
• US Class Current: 62/620
• CPC Class Codes: C07C 11/04 Ethylene
• CPC Class Codes: C07C 7/005 Processes comprising at least two steps in series
• CPC Class Codes: C07C 7/04 by distillation
• CPC Class Codes: C07C 7/167 for removal of compounds containing a triple carbon-to-carbon bond
• CPC Class Codes: F25J 2200/38 using pre-separation or distributed distillation before a main column system, e.g. in a at least a double column system
• CPC Class Codes: F25J 2205/04 in the feed line, i.e. upstream of the fractionation step
• CPC Class Codes: F25J 2210/12 Refinery or petrochemical off-gas
• CPC Class Codes: F25J 2215/62 Ethane or ethylene
• CPC Class Codes: F25J 2270/04 Internal refrigeration with work-producing gas expansion loop
• CPC Class Codes: F25J 2270/90 External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
• CPC Class Codes: F25J 3/0219 Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
• CPC Class Codes: F25J 3/0233 separation of CnHm with 1 carbon atom or more
• CPC Class Codes: F25J 3/0238 separation of CnHm with 2 carbon atoms or more
• CPC Class Codes: F25J 3/0242 separation of CnHm with 3 carbon atoms or more
• CPC Class Codes: F25J 3/0252 separation of hydrogen production of hydrogen containing gas in general C01B3/00, e.g. separation of hydrogen or hydrogen containing gases form gaseous mixtures at low temperatures C01B3/506
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
• CPC Class Codes: Y02P 30/40 Ethylene production
• CPC Class Codes: Y10S 62/932 From natural gas

Abstract

A process for the recovery and purification of ethylene and optionally propylene from a stream containing lighter and heavier components that employs an ethylene distributor column and a partially thermally coupled distributed distillation system.

Claims

1. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (c), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above;

(g) directing at least a portion, of step (c), above, of the low-acetylene first overhead stream to a C2s distributor distillation column and recovering therefrom a C2s distributor overhead stream comprising ethylene, ethane, methane and hydrogen and substantially free of components heavier than ethane, and a C2s distributor bottoms stream comprising ethylene, ethane, and components heavier than ethane and substantially free of components lighter than ethylene;

(h) withdrawing the C2s distributor bottoms stream as the first liquid stream of step (c), above;

(i) directing at least a portion of the C2s distributor overhead stream to an ethylene distributor column and recovering therefrom an ethylene distributor overhead stream comprising ethylene, methane, and hydrogen and substantially free of ethane and an ethylene distributor bottoms stream comprising ethylene and ethane and substantially free of components lighter than ethylene;

(j) withdrawing the ethylene distributor overhead stream as the ethane-free vapor stream of step (c), above; and

(k) withdrawing the ethylene distributor bottoms stream as the second liquid stream of step (c), above.

2. The process of claim 1 wherein the first vapor overhead stream is substantially free of components heavier than ethane.

3. The process of claim 1 wherein the first vapor overhead stream is substantially free of components heavier than propane.

4. The process of claim 1 wherein the step of removing acetylene comprises the hydrogenation of acetylene to ethylene or ethane or both.

5. The process of claim 1 wherein step (b) comprises reacting the acetylene and hydrogen contained in the first overhead stream in the presence of a suitable catalyst to form acetylene hydrogenation products.

6. The process of claim 1 wherein the first vapor overhead stream is compressed before entering the acetylene removal step (b).

7. The process of claim 1 wherein at least a portion of the reflux liquid for the first distillation column is provided by a liquid side draw stream from the ethylene distributor distillation column.

8. The Process of claim 1 wherein the ethylene distributor distillation column operates with a top pressure between 150 psig and 550 psig.

9. The Process of claim 1 wherein the ethylene distributor distillation column operates with a top pressure between 150 psig and 450 psig.

10. The process of claim 1 wherein step (d) comprises:

g. chilling and partially condensing at least a portion of the ethylene distributor overhead stream to provide a partially condensed portion of the ethylene distributor overhead stream;

h. separating the vapor and liquid contained in the partially condensed portion of the ethylene distributor overhead vapor, said separated liquid comprising one of the one or more liquid streams depleted in hydrogen and comprising ethylene; and

i. recovering said vapor stream enriched in hydrogen from the separated vapor of step (h).

11. The process of claim 1 wherein at least a portion of the aforesaid separated vapor of step (h) is subjected to rectification in a rectification column and wherein an overhead vapor stream comprising the vapor stream enriched in hydrogen is withdrawn from the rectification column.

12. The process of claim 1 wherein step (d) comprises rectification of at least a portion of the ethylene distributor overhead stream in a rectification column and withdrawing from the rectification column an overhead vapor stream comprising the vapor stream enriched in hydrogen.

13. The process of claim 1 wherein the demethanizer distillation column is operated at a pressure at least 25 psi lower than that of the ethylene distributor distillation column.

14. The process of claim 1 wherein step (f) comprises directing at least a portion of the ethylene distributor bottoms stream to a C2 splitter distillation column and withdrawing from an upper section of the C2 splitter distillation column a purified ethylene product.

15. The process of claim 1 wherein at least a portion of the stripping vapor for the first distillation column, the ethylene distributor distillation column, and the demethanizer distillation column is provided by the vaporization of at least a part of the respective column bottoms liquid streams in a reboiler exchanger.

16. The process of claim 1 wherein a refrigeration system containing more than one component in the working fluid is used to provide at least a portion of the overhead condensing duty for the ethylene distributor distillation column, at least a portion of the overhead condensing duty of the demethanizer distillation column, and at least a portion of the chilling duty required for the separation of step (d).

17. The process of claim 1 wherein step (f) comprises directing the second liquid stream to a C2 splitter distillation column to produce a C2 splitter bottoms stream comprising primarily ethane, and withdrawing from an upper section of said C2 splitter distillation column the second purified ethylene product.

18. The process of claim 17 wherein step (f) further comprises directing the first liquid stream to a deethanizer distillation column to produce a deethanizer overhead stream comprising primarily ethane and ethylene and a deethanizer bottoms stream comprising C3 components and components heavier than propane, and directing said deethanizer overhead stream to said C2 splitter distillation column.

19. The process of claim 18 wherein a purified propylene product is recovered from the deethanizer bottoms stream and optionally from the first bottoms stream.

20. The process of claim 1 wherein the demethanizer distillation column is operated at a pressure at least 25 psi lower than the pressure of the ethylene distributor column of step (c).

21. The process of claim 1 wherein step (d) comprises:

chilling and partially condensing at least a portion of the ethane-free vapor stream of step (c) to provide a partially condensed portion of the ethane-free vapor stream;

separating the vapor and liquid contained in the partially condensed portion of the ethane-free vapor stream, said separated liquid comprising one of the one or more liquid streams depleted in hydrogen and comprising ethylene of step (d); and

recovering said vapor stream enriched in hydrogen from the separated vapor.

22. The process of claim 21 wherein at least a portion of the aforesaid separated vapor is subjected to rectification in a rectification column and wherein an overhead vapor stream comprising the vapor stream enriched in hydrogen is withdrawn from the rectification column.

23. The process of claim 1 wherein step (d) comprises rectification of at least a portion of the ethane-free vapor from step (c) in a rectification column and withdrawing from the rectification column an overhead vapor stream comprising the vapor stream enriched in hydrogen.

24. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, and optionally components heavier than ethane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene. acetylene, hydrogen and methane and a first bottoms stream comprising components heavier than ethane;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor vapor overhead stream comprising ethylene, methane and hydrogen and substantially free of ethane, and an ethylene distributor bottoms stream comprising ethylene and ethane;

(d) separating the ethylene distributor overhead vapor stream into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethylene distributor overhead vapor stream;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a purified ethylene product from the ethylene distributor bottoms stream; and

(g) splitting gas mixture into at least two fractions, one of said fractions is brought into indirect heat exchange contact with the first overhead vapor stream to warm the first overhead vapor stream and cool said fraction, and wherein the two or more fractions of said gas mixture are introduced into the first distillation column at different locations.

25. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, and optionally components heavier than ethane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen and methane and a first bottoms stream comprising components heavier than ethane;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor vapor overhead stream comprising ethylene, methane and hydrogen and substantially free of ethane, and an ethylene distributor bottoms stream comprising ethylene and ethane;

(d) separating the ethylene distributor overhead vapor stream into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethylene distributor overhead vapor stream;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a purified ethylene product from the ethylene distributor bottoms stream;

(g) withdrawing a vapor stream, in step (c), above, comprising ethylene, methane, and hydrogen from the ethylene distributor distillation column;

(h) chilling said vapor stream of step (a), above, to a temperature no colder than −

50 degree F. to produce a partially condensed vapor stream;

(i) directing said partially condensed vapor stream of step (h), above, to the bottom of a rectification means;

(j) withdrawing an overhead vapor from said rectification means;

(k) chilling said overhead vapor from said rectification means to produce a partially condensed rectification means overhead stream;

(l) directing at least a portion of the liquid fraction of said partially condensed rectification means overhead stream to the top of said rectification means as reflux liquid; and

(m) withdrawing the vapor portion of said partially condensed rectification means overhead stream as said ethylene distributor vapor overhead stream.

26. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, and optionally components heavier than ethane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen and methane and a first bottoms stream comprising components heavier than ethane;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor vapor overhead stream comprising ethylene, methane and hydrogen and substantially free of ethane, and an ethylene distributor bottoms stream comprising ethylene and ethane;

(d) separating the ethylene distributor overhead vapor stream into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethylene distributor overhead vapor stream;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a purified ethylene product from the ethylene distributor bottoms stream directing at least a portion of the ethylene distributor bottoms stream to a C2 splitter distillation column and withdrawing from an upper section of the C2 splitter distillation column a purified ethylene product; and

(g) withdrawing said second purified ethylene product is a liquid from a tray at least one tray below the top of the C2 splitter distillation column, and a portion of the overhead vapor stream from the top of the C2 splitter distillation column is directed to a location at least one tray above the bottom of the demethanizer distillation column.

27. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (C), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above;

(g) directing, of step (c), above, at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor column overhead stream comprising ethylene, methane, and hydrogen and substantially free of ethane and an ethylene distributor column bottoms stream comprising ethylene, ethane and components heavier than ethane and substantially free of components lighter than ethylene;

(h) withdrawing the ethylene distributor column overhead stream as the ethane-free vapor stream of step (c), above;

withdrawing the ethylene distributor column bottoms stream as the first liquid stream of step (c), above;

(j) withdrawing a liquid sidedraw stream from the ethylene distributor column at a point intermediate between the top of the ethylene distributor column and the point where the low-acetylene first overhead stream enters the ethylene distributor column, wherein the liquid sidedraw stream comprises methane, ethylene and ethane and is substantially free of components heavier than ethane;

(k) directing the liquid sidedraw stream to the top of a sidestripper column and recovering therefrom a sidestripper bottoms stream comprising ethylene and ethane and substantially free of components lighter than ethylene, and a sidestripper overhead stream comprising methane;

(l) withdrawing the sidestripper bottoms stream as the second liquid stream of step (c), above; and

(m) directing the sidestripper overhead stream to the ethylene distributor column.

28. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (c), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above;

(g) wherein step (c), above, comprises the steps of directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor column overhead stream comprising ethylene, methane, and hydrogen and substantially free of ethane and an ethylene distributor column bottoms stream comprising ethylene, ethane and components heavier than ethane and substantially free of components lighter than ethylene;

(h) withdrawing the ethylene distributor column overhead stream as the ethane-free vapor stream of step (c), above;

(i) withdrawing the ethylene distributor column bottoms stream as the first liquid stream of step (c), above;

(i) withdrawing a liquid sidedraw stream from the ethylene distributor column at a point intermediate between the top of the ethylene distributor column and the point where the low-acetylene first overhead stream enters the ethylene distributor column, wherein the liquid sidedraw stream comprises methane, ethylene and ethane and is substantially free of components heavier than ethane;

(k) directing the liquid sidedraw stream to the top of a sidestripper column and recovering therefrom a sidestripper bottoms stream comprising ethylene and ethane and substantially free of components lighter than ethylene, and a sidestripper overhead stream comprising methane;

(l) withdrawing the sidestripper bottoms stream as the second liquid stream of step (c), above;

(m) directing the sidestripper overhead stream to the ethylene distributor column; and

(n) combining the separation functions of the ethylene distributor column and the sidestripper column into a single divided wall column.

29. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components. and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (c), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above;

(g) wherein step (c), above, comprises the steps of directing at least a portion of the low-acetylene first overhead stream to an ethylene distributor distillation column and recovering therefrom an ethylene distributor column overhead stream comprising ethylene, methane, and hydrogen and substantially free of ethane and an ethylene distributor column bottoms stream comprising ethylene, ethane and components heavier than ethane and substantially free of components lighter than ethylene;

(h) withdrawing the ethylene distributor column overhead stream as the ethane-free vapor stream of step (c), above;

(i) withdrawing the ethylene distributor column bottoms stream as the first liquid stream of step (c), above;

(i) withdrawing a liquid sidedraw stream from the ethylene distributor column at a point intermediate between the top of the ethylene distributor column and the point where the low-acetylene first overhead stream enters the ethylene distributor column, wherein the liquid sidedraw stream comprises methane, ethylene and ethane and is substantially free of components heavier than ethane;

(k) directing the liquid sidedraw stream to the top of a sidestripper column and recovering therefrom a sidestripper bottoms stream comprising ethylene and ethane and substantially free of components lighter than ethylene, and a sidestripper overhead stream comprising methane;

(l) withdrawing the sidestripper bottoms stream as the second liquid stream of step (c), above;

(m) directing the sidestripper overhead stream to the ethylene distributor column;

(n) combining the separation functions of the ethylene distributor column and the sidestripper column into a single divided wall column; and

(o) producing an overhead product by the divided wall column and two distinct liquid bottoms products, and further wherein the overhead product is withdrawn as the ethane-free vapor stream of step (c), above, and the two bottoms products are withdrawn as the first and second liquid streams of step (c), above.

30. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (c), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above wherein the second liquid stream is directed to a C2 splitter distillation column to produce a C2 splitter bottoms stream comprising primarily ethane, and withdrawing from an upper section of said C2 splitter distillation column the second purified ethylene product;

(g) withdrawing said second purified ethylene product as a liquid from a tray at least one tray below the top of the C2 splitter distillation column, and a portion of the overhead vapor stream from the top of the C2 splitter distillation column is directed to a location at least one tray above the bottom of the demethanizer distillation column.

31. A process for the recovery of ethylene from a gas mixture comprising ethylene, ethane, acetylene, methane, hydrogen, C3 components, and components heavier than propane, comprising:

(a) directing the gas mixture to a first distillation column and recovering therefrom a first vapor overhead stream comprising ethane, ethylene, acetylene, hydrogen, methane, and C3 components, and a first bottoms stream comprising components heavier than propane and optionally C3 components;

(b) removing acetylene from the first vapor overhead stream to produce a low-acetylene first overhead stream;

(c) separating at least a portion of the low acetylene first overhead stream through the use of one or more distillation columns, one of which acts as an ethylene distributor column, to recover an ethane-free vapor stream comprising ethylene, methane and hydrogen and substantially free of ethane, a first liquid stream comprising ethylene, ethane and components heavier than ethane, and a second liquid stream comprising ethylene and ethane and substantially free of components heavier than ethane;

(d) separating the ethane-free vapor stream of step (c), above, into a light stream enriched in hydrogen and one or more streams depleted in hydrogen and comprising ethylene, said separation comprising at least one step of chilling at least a portion of the ethane-free vapor stream of step (c), above;

(e) directing at least a portion of at least one of the one or more streams depleted in hydrogen to a demethanizer distillation column and withdrawing therefrom a demethanizer overhead stream comprising methane and hydrogen and substantially free of ethylene and a demethanizer bottoms stream comprising purified ethylene;

(f) recovering a second purified ethylene product from the first and second liquid streams of step (c), above wherein the second liquid stream is directed to a C2 splitter distillation column to produce a C2 splitter bottoms stream comprising primarily ethane, and withdrawing from an upper section of said C2 splitter distillation column the second purified ethylene product; and

(g) operating the C2 splitter distillation column at a pressure at least 25 psi lower than the pressure at any location in any of the distillation columns employed in step (c), above.