Process for selective deep hydrodesulfurization of a hydrocarbon feedstock using an unsupported nanocatalyst made by laser pyrolysis

Patent metadata

Field	Value
Publication number	US-10023813-B2
Application number	US-201615190435-A
Country	US
Kind code	B2
Filing date	Jun 23, 2016
Priority date	Jun 23, 2016
Publication date	Jul 17, 2018
Grant date	Jul 17, 2018

Abstract

A process for producing an unsupported molybdenum sulfide nanocatalyst comprising atomizing a molybdenum oxide solution to form a molybdenum oxide aerosol, pyrolyzing the molybdenum oxide aerosol with a laser beam to form the unsupported molybdenum-based nanocatalyst, and pre-sulfiding at least a portion of the unsupported molybdenum-based nanocatalyst to form an unsupported molybdenum sulfide nanocatalyst, wherein the unsupported molybdenum-based nanocatalyst, the unsupported molybdenum sulfide catalyst or both are in the form of nanoparticles with a diameter of 1-10 nm and in a distorted rutile crystalline structure. A method of selective deep hydrodesulfurization whereby a hydrocarbon feedstock having at least one sulfur-containing component and at least one hydrocarbon is contacted with the unsupported molybdenum sulfide nanocatalyst.

First claim

The invention claimed is:

1. A process for synthesizing an unsupported molybdenum sulfide nanocatalyst, comprising:
atomizing a molybdenum oxide solution comprising at least one molybdenum precursor to form a molybdenum oxide aerosol;
pyrolyzing the molybdenum oxide aerosol with a laser beam having a wavelength of 1.0-30.0 μm, a laser beam power up to 1.2 kW, and a focal length intensity of 1-10 kW/cm 2 to form an unsupported molybdenum-based nanocatalyst; and
pre-sulfiding at least a portion of the unsupported molybdenum-based nanocatalyst to form an unsupported molybdenum sulfide nanocatalyst;
wherein the molybdenum oxide aerosol is pyrolyzed in the presence of an inert carrier gas stream in a volumetric ratio of molybdenum oxide aerosol to the inert carrier gas stream ranging from 1:50 to 1:20; and
wherein the unsupported molybdenum-based nanocatalyst, the unsupported molybdenum sulfide nanocatalyst or both are in the form of nanoparticles with a diameter of 1-10 nm and a distorted rutile crystalline structure.

2. The process of claim 1 , wherein the at least one molybdenum precursor is molybdenum(IV) oxide bis(2,4-pentadionate).

3. The process of claim 1 , wherein the molybdenum oxide solution has a concentration of molybdenum ranging from 0.04-0.2 M.

4. The process of claim 1 , wherein the molybdenum oxide solution further comprises a metal precursor comprising at least one metal selected from the group consisting of Co, Ni, and W, and
the process forms an unsupported mixed metal sulfide nanocatalyst comprising molybdenum and the at least one metal selected from the group consisting of Co, Ni, and W, wherein the unsupported mixed metal sulfide nanocatalyst is in the form of nanoparticles with a diameter of 1-10 mu and a distorted rutile crystalline structure.

5. The process of claim 4 , wherein the metal precursor is cobalt(II) acetylacetonate.

6. The process of claim 4 , wherein the molybdenum oxide solution comprises 1-30 wt % of the at least one metal, relative to the total weight of the molybdenum oxide solution.

7. The process of claim 1 , wherein the molybdenum oxide aerosol is pyrolyzed at a flow rate of 4-12 m/s.

8. The process of claim 1 , wherein the molybdenum oxide aerosol further comprises at least one photosensitizer selected from the group consisting of NH 3 , C 2 H 4 , SF 6 , and O 3 .

9. The process of claim 1 , wherein the pre-sulfiding comprises:
contacting a gaseous mixture with the unsupported molybdenum-based nanocatalyst at an activating temperature of 250-400° C. for 1-8 hrs to form the unsupported molybdenum sulfide nanocatalyst;
wherein the gaseous mixture comprises H 2 and 1-10 mol % H 2 S, relative to the total molar composition of the gaseous mixture.

10. The process of claim 1 , wherein the pre-sulfiding comprises:
contacting a spiked hydrocarbon mixture and hydrogen gas with the unsupported molybdenum-based nanocatalyst for 12-20 hrs at 250-400° C. to form the unsupported molybdenum sulfide nanocatalyst,
wherein the spiked hydrocarbon mixture comprises 1-5% dimethyl disulfide by weight relative to the total weight of the spiked hydrocarbon mixture and a liquid hydrocarbon, and a pressure of the hydrogen gas ranges from 2-10 MPa.

11. A process for synthesizing an amorphous molybdenum sulfide nanocatalyst comprising:
atomizing a molybdenum oxide solution comprising at least one molybdenum precursor and thiouric acid to form an amorphous molybdenum-based aerosol; and
pyrolyzing the amorphous molybdenum-based aerosol with a laser beam having a wavelength of 1.0-30.0 μm, a laser beam power up to 1.2 kW, and a focal length intensity of 1-10 kW/cm 2 to form an amorphous molybdenum sulfide nanocatalyst, wherein the amorphous molybdenum sulfide nanocatalyst does not have a crystalline structure.

Assignees

• Univ King Fahd Pet & Minerals
• Commissariat Energie Atomique

Inventors

• Yamani Zain Hassan
• Tabet Nouar
• Ali Syed Ahmed
• Leconte Yann
• Schuster Frederic
• Quinsac Axelle

Classifications

• C10G45/04

  characterised by the catalyst used · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• B01J37/082

  Decomposition and pyrolysis · CPC title

• B01J37/20

  Sulfiding · CPC title

• B01J27/051

  Molybdenum · CPC title