Temporary desulphurization reactor for pre-treating a hydrocarbon feed before steam reforming with a view to hydrogen production

• US 9,174,901 B2
• Filed: 03/22/2013
• Issued: 11/03/2015
• Est. Priority Date: 03/27/2012
• Status: Active Grant

• Current Assignee: IFP Energies Nouvelles
• Original Assignee: IFP Energies Nouvelles
• Inventors: Giroudiere, Fabrice, Thomas, Michel, Nebois, Cedric
• Primary Examiner(s): Price, Elvis O
• Application Number:
  US13/848,944
• Publication Number:
  US 20130261351A1
• Time in Patent Office: 956 Days
• Field of Search: 568/917, 568/913
• US Class Current: 1/1
• CPC Class Codes: C01B 2203/1229 Ethanol
• CPC Class Codes: C01B 2203/1247 Higher hydrocarbons
• CPC Class Codes: C01B 2203/1258 Pre-treatment of the feed
• CPC Class Codes: C01B 2203/1604 Starting up the process
• CPC Class Codes: C01B 3/323 Catalytic reaction of gaseous or liquid organic compounds other than hydrocarbons with gasifying agents
• CPC Class Codes: C01B 3/38 using catalysts
• CPC Class Codes: C07C 29/76 by physical treatment

Abstract

The present invention describes a process for pre-treating a steam reforming feed containing sulphur-containing compounds, using two desulphurization reactors:

• • a temporary desulphurization reactor (1010) containing an active adsorbent solid;
  • a permanent desulphurization reactor (1003) placed upstream of the steam reforming unit, which contains an adsorbent solid in the passivated state, necessitating a depassivation phase in order to be rendered active;
    the temporary desulphurization reactor (1010) being disconnected as soon as the adsorbent solid of the permanent desulphurization reactor (1003) has been activated, and the volume of the temporary desulphurization reactor being in the range 1/20 to 1/200 times the volume of the permanent desulphurization reactor.

Claims

1. A process for pre-treating a steam reforming feed containing sulphur-containing compounds, said process comprising:

adsorption of said sulphur-containing compounds onto an adsorbent solid, using two desulphurization reactors;

a temporary desulphurization reactor containing an active adsorbent solid;

a permanent desulphurization reactor placed upstream of a steam reforming unit, which contains an adsorbent solid in the passivated state, necessitating a depassivation phase in order to be rendered active;

wherein said temporary desulphurization reactor is disconnected as soon as the adsorbent solid of the permanent desulphurization reactor has been activated, and

wherein the volume of said temporary desulphurization reactor is in the range of 1/20 to 1/200 times the volume of said permanent desulphurization reactor.

2. The process according to claim 1, wherein said process comprises a first phase and a second phase:

wherein in said first phase, termed the activation phase, said steam reforming feed is sent to said temporary desulphurization reactor (1010) containing an active adsorbent solid, and then to said permanent desulphurization reactor (1003) placed upstream of the steam reforming unit, and wherein the period of operation of said temporary desulphurization reactor (1010) is such that it allows said permanent desulphurization reactor (1003) to be activated by depassivation of said adsorbent solid contained in said permanent desulphurization reactor; and

wherein in said second phase, said temporary desulphurization reactor (1010) is disconnected and said steam reforming feed is sent directly to said activated permanent desulphurization reactor (1003).

3. The process according to claim 1, wherein said process comprises a first phase, a second phase, and a third phase:

wherein in said first phase, said steam reforming feed is sent to said temporary desulphurization reactor (1010) and the desulphurized feed obtained from said temporary desulphurization reactor is stored in a drum (1011);

wherein in said second phase, said desulphurized feed contained in said storage drum (1011) is heated in a exchanger (1002), then sent to said permanent pre-treatment reactor (1003), and then cooled in a exchanger (1004) at the outlet from said permanent pre-treatment reactor (1003) before returning to said storage drum (1011), and the flow of desulphurized feed from storage drum (1011) to the permanent pre-treatment reactor (1003) and return to said storage drum (1011) is carried out until said permanent pre-treatment reactor (1003) latter has been activated; and

wherein in said third phase, said temporary desulphurization reactor (1010) is disconnected and said steam reforming feed is sent directly to the activated permanent desulphurization reactor (1003).

4. The process according to claim 1, wherein said adsorbent solid used in said temporary desulphurization reactor and said permanent desulphurization reactor contains nickel or a mixture of nickel and nickel oxide deposited on a silica or silica-alumina support.

5. The process according to claim 1, wherein said steam reforming feed is denatured ethanol containing less than 10 ppm of sulphur.

6. The process according to claim 1, wherein said steam reforming feed is a gasoline or a gas oil containing less than 10 ppm of sulphur.

7. The process according to claim 1, wherein the volume of said temporary desulphurization reactor is in the range of 1/50 to 1/200 times the volume of said permanent desulphurization reactor.