Catalytic compositions useful in removal of sulfur compounds from gaseous hydrocarbons, processes for making these and uses thereof

Patent metadata

Field	Value
Publication number	US-9663725-B2
Application number	US-201213491815-A
Country	US
Kind code	B2
Filing date	Jun 8, 2012
Priority date	Jul 27, 2011
Publication date	May 30, 2017
Grant date	May 30, 2017

Abstract

A catalytic composition is disclosed, which exhibits an X-ray amorphous oxide, with a spinel formula and highly dispersed crystals of ZnO, CuO, and optionally CeO 2 . The composition is useful in oxidative and adsorptive processes for removing sulfur from gaseous hydrocarbons.

First claim

We claim:

1. A method for removing a portion of sulfur contained in a hydrocarbon, comprising contacting said sulfur containing hydrocarbon in gaseous form to a catalytic composition comprising copper oxide in an amount ranging from 20 weight percent (wt %) to 45 wt %, zinc oxide in an amount ranging from 12 wt % to less than 20 wt %, CeO 2 in the form of particles ranging in diameter from 5 nm to 10 nm, in an amount ranging from 0.1 wt % to 10 wt % and aluminum oxide in an amount ranging from 20 wt % to 40 wt %, wherein said catalytic composition has an X-ray amorphous oxide phase, and a formula Cu x Zn 1-x Al 2 O 4 wherein x ranges from 0 to 1, highly dispersed crystalline ZnO and CuO, said contacting occurring in the presence of pure oxygen at a gas hourly space velocity (GHSV) of from 1,000 to 20,000 h −1 , said catalytic composition prepared by:
(i) combining an aqueous solution containing each of copper nitrate, zinc nitrate, and aluminum nitrate with an alkaline solution containing NaOH and/or at least one of (NH 4 ) 2 CO 3 , Na 2 CO 3 and NH 4 HCO 3 , at a temperature of from about 50° C. to about 65° C., and a pH of from about 6.5 to about 14, to form a precipitate containing at least one of (a) a carbonate containing Cu, Zn, and Al, (b) a hydroxide containing Cu, Zn, and Al, and (c) a hydroxycarbonate containing Cu, Zn, and Al;
(ii) aging said precipitate;
(iii) filtering and washing said precipitate;
(iv) drying said precipitate for at least 10 hours, at a temperature of at least 100° C.; and
(v) combining the precipitate with a binder selected from the group consisting of poly-ethylene oxide, polyvinyl alcohol, a sol of aluminum pseudoboehmite, silica gel and mixtures thereof, said binder being added in amount ranging from 1 to 10 weight % of said precipitate, to from an extrudable mixture, extruding said mixture through a die to form an extrudate drying said extrudate for 24 hours at room temperature, followed by drying said extrudate at 100° C. for from 2-4 hours, and raising temperature to 500° C., at a rate of from 2-5° C./minute, to calcine said extrudate for from 2-4 hours.

2. The method of claim 1 , comprising oxidizing sulfur in said sulfur containing hydrocarbon.

3. The method of claim 1 , comprising adsorbing a sulfur containing compound into said catalyst.

4. The method of claim 1 , further comprising regenerating said catalyst.

5. The method of claim 1 , wherein said catalytic composition is in granular form.

6. The method of claim 5 , wherein pores of granules have a diameter of from 8 nm to 12 nm.

7. The method of claim 6 , wherein pores of the granules of said composition have a volume of from about 0.1 cm 3 /g to about 0.5 cm 3 /g.

8. The method of claim 6 , wherein said pores of said catalytic composition have a diameter of from 8 nm to 10 nm.

9. The method of claim 1 , wherein said catalytic composition is formed as a cylinder, a sphere, a trilobe, or a quatrolobe.

10. The method of claim 5 , wherein said catalytic composition is in the form of granules having a diameter of from 1 mm to 4 mm.

11. The method of claim 1 , wherein said catalytic composition has a specific surface area of from 10 m 2 /g to 100 m 2 /g.

12. The method of claim 11 , wherein said catalytic composition has a specific surface area of from 50 m 2 /g to 100 m 2 /g.

13. The method of claim 1 , wherein X is from 0.1 to 0.6.

14. The method of claim 13 , wherein X is from 0.2 to 0.5.

15. The method of claim 1 , wherein said GHSV is from 5,000 h −1 to 15,000 h −1 .

16. The method of claim 15 , wherein said GHSV is from 5,000 h −1 to 10,000 h −1 .

17. The method of claim 1 , wherein said GHSV is 1,000 h −1 or more and less than 3,000 h −1 .

Assignees

• Bourane Abdennour
• Koseoglu Omer Refa
• Ismagilov Zinfer
• Yashnik Svetlana
• Kerzhentsev Mikhail
• Parmon Valentin
• Saudi Arabian Oil Co
• Boreskova Inst Kataliza Sibir

Inventors

• Bourane Abdennour
• Koseoglu Omer Refa
• Ismagilov Zinfer
• Yashnik Svetlana
• Kerzhentsev Mikhail
• Parmon Valentin

Classifications

• B01J23/005

  Spinels · CPC title

• C10G27/04 Primary

  with oxygen or compounds generating oxygen · CPC title

• B01J23/80 Primary

  with zinc, cadmium or mercury · CPC title

• C10G29/16

  Metal oxides · CPC title

• B01J23/94

  of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper · CPC title