Gas clean-up for alkane oxidative dehydrogenation effluent

Patent metadata

Field	Value
Publication number	US-11078134-B2
Application number	US-201816486535-A
Country	US
Kind code	B2
Filing date	Feb 20, 2018
Priority date	Feb 22, 2017
Publication date	Aug 3, 2021
Grant date	Aug 3, 2021

Abstract

The invention relates to a process for the production of an alkene by alkane oxidative dehydrogenation, comprising: (a) subjecting a stream comprising an alkane to oxidative dehydrogenation conditions, comprising contacting the alkane with oxygen in the presence of a catalyst comprising a mixed metal oxide, resulting in a stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne; (b) removing water from at least part of the stream comprising alkene, unconverted alkane, water, carbon dioxide, unconverted oxygen, carbon monoxide and optionally an alkyne resulting from step (a), resulting in a stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne; (c) removing unconverted oxygen, carbon monoxide and optionally alkyne from at least part of the stream comprising alkene, unconverted alkane, carbon dioxide, unconverted oxygen, carbon monoxide and optionally alkyne resulting from step (b), wherein carbon monoxide and optionally alkyne are oxidized into carbon dioxide, resulting in a stream comprising alkene, unconverted alkane and carbon dioxide; (d) optionally removing carbon dioxide from at least part of the stream comprising alkene, unconverted alkane in and carbon dioxide resulting from step (c), resulting in a stream comprising alkene and unconverted alkane; (e) optionally separating at least part of the stream comprising alkene and unconverted alkane resulting from step (d), into a stream comprising alkene and a stream comprising unconverted alkane; (f) optionally recycling unconverted alkane from at least part of the stream comprising unconverted alkane resulting from step (e), to step (a).

First claim

That which is claimed is:

1. A process for producing ethylene by ethane oxidative dehydrogenation, comprising:
(a) subjecting a stream comprising ethane to oxidative dehydrogenation conditions, comprising contacting ethane with oxygen in the presence of a catalyst comprising a mixed metal oxide, resulting in a stream comprising ethylene, unconverted ethane, water, carbon dioxide, unconverted oxygen, carbon monoxide and acetylene;
(b) removing water from at least part of the stream comprising ethylene, unconverted ethane, water, carbon dioxide, unconverted oxygen, carbon monoxide and acetylene resulting from step (a), resulting in a stream comprising ethylene, unconverted ethane, carbon dioxide, unconverted oxygen, carbon monoxide and acetylene;
(c) removing unconverted oxygen, carbon monoxide and acetylene from at least part of the stream comprising ethylene, unconverted ethane, carbon dioxide, unconverted oxygen, carbon monoxide and acetylene resulting from step (b), resulting in a stream comprising ethylene, unconverted ethane and carbon dioxide, wherein the removing unconverted oxygen, carbon monoxide and acetylene is carried out by oxidizing carbon monoxide and acetylene with unconverted oxygen into carbon dioxide;
(d) removing carbon dioxide from at least part of the stream comprising ethylene, unconverted ethane and carbon dioxide resulting from step (c), resulting in a stream comprising ethylene and unconverted ethane;
(e) separating at least part of the stream comprising ethylene and unconverted ethane resulting from step (d), into a stream comprising ethylene and a stream comprising unconverted ethane;
(f) optionally recycling ethane from at least part of the stream comprising unconverted ethane resulting from step (e), to step (a).

2. The process according to claim 1 , wherein a temperature in step (c) is in a range of from 100 to 400° C.

3. The process according to claim 1 , wherein a temperature in step (c) is at least 50° C.

4. The process according to claim 1 , wherein a temperature in step (c) is at most 500° C.

5. The process according to claim 1 , wherein additional oxygen is fed to step (c).

6. The process according to claim 1 , wherein step (c) is performed in presence of an oxidation catalyst comprising a transition metal.

7. The process according to claim 6 , wherein the oxidation catalyst comprises one or more metals selected from the group consisting of nickel, copper, zinc, palladium, silver, platinum, gold, iron, manganese, cerium, tin, ruthenium and chromium.

8. The process according to claim 6 , wherein the oxidation catalyst comprises copper and/or platinum.

Assignees

• Shell Oil Co

Inventors

• Mitkidis Georgios
• Van Rossum Guus
• San Roman Macia Maria
• Schoonebeek Ronald Jan
• VERHAAK Michael Johannes Franciscus Maria

Classifications

• B01J35/32

  Bulk density · CPC title

• B01J35/50

  characterised by their shape or configuration · CPC title

• B01J2523/27

  Zinc · CPC title

• C07C5/48 Primary

  with oxygen as an acceptor · CPC title

• B01J23/8926

  Copper and noble metals · CPC title