Process for removing oxygenated contaminates from an ethylene stream

Patent metadata

Field	Value
Publication number	US-9963409-B2
Application number	US-201715614997-A
Country	US
Kind code	B2
Filing date	Jun 6, 2017
Priority date	Jul 28, 2011
Publication date	May 8, 2018
Grant date	May 8, 2018

Abstract

The present invention is, in a first embodiment, a process for removing oxygenated contaminants from an ethylene stream comprising: a) providing a dried ethylene stream (A) comprising essentially ethylene, up to 1 w % oxygenates, ethane, CO, CO2, H2, CH4 and C3+ hydrocarbons, b) sending said stream (A) to a stripper (also referred to as a demethanizer) to produce an overhead stream comprising essentially CO, H2 and CH4, a bottom stream comprising essentially ethylene, oxygenates, ethane, CO2 and C3+ hydrocarbons, c) sending said bottom stream of step b) to a deethanizer to produce a bottom stream comprising essentially ethane, oxygenates and C3+ hydrocarbons, an overhead stream consisting essentially of ethylene and CO2, d) sending said overhead of step c) to a fixed bed CO2 adsorption zone to recover an ethylene stream essentially free of CO2. In another embodiment the CO2 adsorption zone can be located at the inlet of the deethanizer. In another embodiment the demethanizer is replaced by two demethanizers. In another embodiment the the deethanizer is replaced by two C2 splitters.

First claim

The invention claimed is:

1. A process for removing oxygenated contaminants from an ethylene stream comprising:
a) providing a dried ethylene stream (A) comprising essentially ethylene, up to 1 w % oxygenates, ethane, CO, CO 2 , H 2 , CH 4 and C 3+ hydrocarbons;
b) sending the dried ethylene stream stream (A) to a stripper to produce an overhead stream comprising essentially CO, H 2 and CH 4 ; and a bottom stream comprising essentially ethylene, oxygenates, ethane, CO 2 and C 3+ hydrocarbons; and performing step (i) or step (ii);

wherein step (i) comprises:
c) sending the bottom stream of step b) to a primary C 2 splitter to produce a bottom stream comprising essentially ethane, oxygenates, C 3+ hydrocarbons and a portion of ethylene; and an overhead stream consisting essentially of ethylene and CO 2 ;
d) sending the overhead of step c) to a fixed bed CO 2 adsorption zone to recover an ethylene stream essentially free of CO 2 ;
e) sending the bottom stream of step c) to a secondary CO 2 splitter to produce a bottom stream comprising essentially ethane, oxygenates and C 3+ hydrocarbons; and an overhead stream consisting essentially of ethylene, optionally recycled to a production zone of the dried ethylene stream (A);

wherein step (ii) comprises:
c1) sending the bottom stream of step b) to a fixed bed CO 2 adsorption zone to recover a stream essentially free of CO 2 , then sending the stream essentially free of CO 2 to a primary CO 2 splitter to produce a bottom stream comprising essentially ethane, oxygenates, C 3+ hydrocarbons and a portion of ethylene; and an overhead stream consisting essentially of ethylene essentially free of CO 2 ;
e1) sending the bottom stream of step c1) to a secondary CO 2 splitter to produce a bottom stream comprising essentially ethane, oxygenates and C 3+ hydrocarbons; and an overhead stream consisting essentially of ethylene, optionally recycled to the production zone of the dried ethylene stream (A).

2. The process of claim 1 , wherein the fixed bed CO 2 adsorption zone is located at an inlet of the primary C 2 splitter.

3. The process of claim 1 , wherein a weight ratio of ethane+CO+CO 2 +H 2 +CH 4 +C 3 +hydrocarbons to ethylene in the dried ethylene stream (A) is less than 10/90.

4. The process of claim 3 , wherein the weight ratio of ethane+CO+CO 2 +H 2 +CH 4 +C 3 +hydrocarbons to ethylene in the dried ethylene stream (A) is above 0.1/99.9.

5. The process of claim 4 , wherein the weight ratio of ethane+CO+CO 2 +H 2 +CH 4 +C 3 +hydrocarbons to ethylene in the dried ethylene stream (A) is less than 5/95.

6. The process of claim 1 , wherein a proportion of oxygenates in the dried ethylene stream (A) is from 50 wppm to 7000 wppm.

7. The process of claim 1 , wherein a proportion of oxygenates in the dried ethylene stream (A) is up to 3000 wppm.

8. The process of claim 1 , wherein the proportion of oxygenates in the dried ethylene stream (A) is up to 2000 wppm.

9. The process of claim 1 , wherein a proportion of H 2 in the dried ethylene stream (A) is from 5 to 1000 wppm.

10. The process of claim 1 , wherein a proportion of H 2 in the dried ethylene stream (A) is up to 800 wppm.

11. The process of claim 1 , wherein a proportion of H 2 in the dried ethylene stream (A) is up to 500 wppm.

12. The process of claim 1 , wherein the dried ethylene stream (A) is originated from the dehydration of ethanol.

Assignees

• Total Res & Technology Feluy
• Ifp Energies Now

Inventors

• Das Babua
• Arratia Manuela
• Boutrot Catherine

Classifications

• C07C7/00 Primary

  Purification; Separation; Use of additives (working-up undefined gaseous mixtures obtained by cracking hydrocarbon oils C10G70/00) · CPC title

• C07C7/005 Primary

  Processes comprising at least two steps in series · CPC title

• C07C7/12

  by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers · CPC title