IP Library Granted Patent US 7,902,113
Granted Patent B2
US 7,902,113 · App. 11/220,740 · Granted Mar 8, 2011

Catalyst direct conversion of methane to ethane and ethylene

Assignee: Research Institute of Petroleum Industry (RIPI)
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,902,113
App. No.
11/220,740
Granted
Mar 8, 2011
Kind
B2
Abstract

The present invention relates to an improved catalyst for direct conversion of methane to ethane and ethylene, a method for producing the catalyst and a process making use of the catalyst.

Claims (25)

1. A catalyst for conversion of methane to a C 2 hydrocarbon, said catalyst comprising:

a) a manganese (Mn) oxide, in combination with an alkali metal and tungsten on a silica support; and

b) niobium (Nb) as a promoter.

2. The catalyst of claim 1 , wherein the catalyst further comprises one or more of Eu (Europium), Y (yttrium) and Nd (neodymium).

3. The catalyst of claim 1 , wherein the niobium (Nb) is present in an amount of 0.5 to 5% by weight.

4. The catalyst of claim 3 , wherein the niobium (Nb) is present in an amount of 1.2 to 4% by weight.

5. The catalyst of claim 4 , wherein the niobium (Nb) is present in an amount of 1.9 by weight.

6. The catalyst of claim 3 , wherein the catalyst further comprises one or more of Eu (Europium), Y (yttrium) and Nd (neodymium).

7. The catalyst of claim 1 , wherein the niobium is present as niobium oxide.

8. The catalyst of claim 1 , wherein the catalyst comprises manganese oxide, tungsten, and sodium as the alkali metal.

9. The catalyst of claim 8 , wherein part a) comprises 1.8% manganese oxide, 1.8% sodium oxide and 2.8% tungsten oxide by weight, with the rest silica.

10. The catalyst of claim 1 , wherein the catalyst comprises tungsten, an alkali metal, and an additional metal oxide in addition to manganese oxide.

11. The catalyst of claim 1 , wherein the alkali metal is sodium.

12. The catalyst of claim 1 , wherein the catalyst is prepared by the following process:

a) combining silica with a solution of a soluble manganese salt and a solution of sodium tungstate to obtain a precipitate;

b) drying the precipitate;

c) calcining the precipitate to obtain particles;

d) reducing the size of the particles;

e) combining the particles of step (d) with a solution of a niobium compound to obtain a precipitate; and

f) repeating steps (b), (c) and (d).

13. A process for converting methane to a C 2 hydrocarbon comprising the steps of

a) contacting a mixture of methane, oxygen and an inert gas with the catalyst of claim 1 to obtain the C 2 hydrocarbon; and

b) recovering the C 2 hydrocarbon.

14. The process of claim 13 , wherein the C 2 hydrocarbon recovered is a mixture of ethane and ethylene.

15. The process of claim 13 , wherein the process is carried out at a temperature of 600-900° C.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 14, 2006
From: ZARRINPASHNE, SAEED; AHMADI, REZA; ZEKORDI, SEYYED MADJID
To: RESEARCH INSTITUE OF PETROLEUM INDUSTRY (RIPI)
Reel/Frame 017337/0137 →
Priority Claims (1)
EP 04104290 · Sep 6, 2004 · regional
Continuity (1)
Related Publication 20060155157A1 · Jul 13, 2006