IP Library Granted Patent US 10,501,390
Granted Patent B2
US 10,501,390 · App. 15/322,479 · Granted Dec 10, 2019

Alkane oxidative dehydrogenation and/or alkene oxidation

Inventors: Alouisius Nicolaas Renée Bos (Amsterdam, NL); Ronald Jan Schoonebeek (Amsterdam, NL); Frank Spies (Amsterdam, NL); Michael Johannes Franciscus Maria Verhaak (Amsterdam, NL)
Assignee: SHELL OIL COMPANY
C07C5/48B01J27/0576B01J35/023B01J35/026B01J37/0036B01J37/0236B01J37/031B01J37/04B01J37/06B01J37/08B01J2523/00C07C2523/28C07C2523/847C07C2527/057Y02P20/52
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Quick Facts
Patent No.
US 10,501,390
App. No.
15/322,479
Granted
Dec 10, 2019
Kind
B2
Abstract

The invention relates to a process of the oxidative dehydrogenation of an alkane containing 2 to 6 carbon atoms and/or the oxidation of an alkene containing 2 to 6 carbon atoms, comprising contacting a first gas stream comprising oxygen and the alkane containing 2 to 6 carbon atoms and/or the alkene containing 2 to 6 carbon atoms with a mixed metal oxide catalyst containing molybdenum, vanadium, niobium and optionally tellurium; followed by contacting a second gas stream comprising methane, an inert gas or oxygen or any combination of two or more of these with the catalyst, wherein the second gas stream comprises 0 to 25 vol. % of the alkane containing 2 to 6 carbon atoms and/or alkene containing 2 to 6 carbon atoms.

Claims (14)

1. A process of the oxidative dehydrogenation of an alkane containing 2 to 6 carbon atoms and/or the oxidation of an alkene containing 2 to 6 carbon atoms, comprising

contacting a first gas stream comprising oxygen and the alkane containing 2 to 6 carbon atoms and/or the alkene containing 2 to 6 carbon atoms with a mixed metal oxide catalyst containing molybdenum, vanadium, niobium and optionally tellurium; followed by

contacting a second gas stream comprising methane with the catalyst, wherein the second gas stream comprises no or substantially no alkane containing 2 to 6 carbon atoms and no or substantially no alkene containing 2 to 6 carbon atoms, followed by

stopping the contacting of the first gas stream while continuing the contacting the second gas stream.

2. The process according to claim 1 , wherein the temperature during the entire process is of from 300 to 500° C.

3. The process according to claim 2 , wherein the temperature during the entire process is of from 310 to 450° C.

4. The process according to claim 1 , wherein the pressure during the entire process is of from 0.1 to 15 bara.

5. The process according to claim 1 , wherein the process is a process of the oxidative dehydrogenation of an alkane containing 2 to 6 carbon atoms and wherein said alkane is ethane or propane.

6. The process according to claim 1 , wherein the process is a process of the oxidation of an alkene containing 2 to 6 carbon atoms and wherein said alkene is ethylene or propylene.

7. The process according to claim 1 , wherein the contacting the first gas stream is done at a first temperature and the contacting the second gas stream is done at a second temperature less than the first temperature.

8. The process according to claim 1 , further comprising stopping the contacting of the second gas stream while gradually introducing the first gas stream.

9. The process according to claim 1 , wherein the second gas stream further comprises an inert gas.

10. The process according to claim 1 , wherein the second gas stream further comprises an inert gas and oxygen.

11. The process according to claim 1 , wherein the second gas stream further comprises oxygen.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 8, 2017
From: VERHAAK, MICHAEL JOHANNES FRANCISCUS MARIA; SCHOONEBEEK, RONALD JAN; BOS, ALOUISIUS NICOLAAS RENEE; SPIES, FRANK
To: SHELL OIL COMPANY
Reel/Frame 041500/0146 →
Priority Claims (1)
EP 14174921 · Jun 30, 2014 · regional
Continuity (1)
Related Publication 20170137347A1 · May 18, 2017