Reforming process with optimized distribution of the catalyst

Patent metadata

Field	Value
Publication number	US-9657235-B2
Application number	US-201514810990-A
Country	US
Kind code	B2
Filing date	Jul 28, 2015
Priority date	Jul 29, 2014
Publication date	May 23, 2017
Grant date	May 23, 2017

Abstract

The invention relates to a process for catalytic reforming of a naphtha hydrocarbon feedstock using a number of reaction zones in series, wherein the reaction zones contain a reforming catalyst bed. The process comprises comprising the following stages:
sending hydrocarbon feedstock that is heated with hydrogen through the reaction zones to convert paraffinic and naphthenic compounds into aromatic compounds, with the effluent that is produced by each reaction zone, except for the last reaction zone, being heated before its introduction into the following reaction zone; drawing off a reformate from the last reaction zone.

First claim

The invention claimed is:

1. A process for catalytic reforming of a naphtha hydrocarbon feedstock using five reaction zones in series, with said reaction zones containing a reforming catalyst bed, with the process comprising the following stages:
a) heating said hydrocarbon feedstock with hydrogen and sending said hydrocarbon feedstock through said five reaction zones to convert paraffinic and naphthenic compounds into aromatic compounds, with the effluent produced by each reaction zone except for the last reaction zone being heated before introduction of the effluent into the following reaction zone; and
b) drawing off a reformate from the last reaction zone,
wherein the reaction in the first reaction zone is performed under the following conditions:
A mean temperature of between 470 and 570° C.;
A pressure of between 0.3 and 1.5 MPa;
A ratio of mass flow rate of feedstock to total catalyst mass of between 50 and 200 h −1 ;
An H 2 /hydrocarbon molar ratio of between 0.8 and 8;
A quantity of catalyst of between 1 and 5% by weight of the total quantity of catalyst used;

wherein the quantity of catalyst in the second reaction zone is between 7 and 15% by weight of the total quantity of catalyst, the quantity of catalyst in the third reaction zone is between 15 and 20% by weight of the total quantity of catalyst, the quantity of catalyst in the fourth reaction zone is between 20 and 30% by weight of the total quantity of catalyst, and the quantity of catalyst in the fifth reaction zone is between 30 and 57% by weight of the total quantity of catalyst.

2. The process according to claim 1 , wherein the overall ratio of mass flow rate of feedstock to total catalyst mass is between 1 and 10 h −1 .

3. The process according to claim 2 , wherein the overall ratio of mass flow rate of feedstock to total catalyst mass is between 1.5 and 5 h −1 .

4. The process according to claim 1 , wherein the second through fifth reaction zones are operated at:
A mean temperature of between 470 and 570° C.;
A pressure of between 0.3 and 1.5 MPa.

5. The process according to claim 1 , wherein each of the reaction zones has a catalytic moving bed.

6. The process according to claim 5 , wherein:
The reformate and the catalyst are drawn off separately from the last reaction zone;
The catalyst obtained from the last reaction zone is sent into a regenerator; and
At least a portion of the regenerated catalyst obtained from the regenerator is transferred into the first reaction zone.

7. The process according to claim 1 , wherein the reaction zones are placed respectively in reactors that are arranged side-by-side.

8. The process according to claim 1 , wherein the reaction zones are placed in a vertical stack in a reactor in such a way that the catalyst flows by gravity from one reaction zone into the next.

9. The process according to claim 1 , wherein each of the reaction zones comprises a catalytic fixed bed.

10. The process according to claim 9 , wherein the reaction zones are placed respectively in reactors that are arranged side-by-side.

11. The process according to claim 9 , wherein the reaction zones are placed in a vertical stack in a reactor.

12. The process according to claim 1 , wherein the quantity of catalyst in the first reaction zone is between 2 and 5% by weight of the total quantity of catalyst used.

13. The process according to claim 1 , wherein the quantity of catalyst in the second reaction zone is between 10 and 15% by weight of the total quantity of catalyst used.

14. The process according to claim 1 , wherein the quantity of catalyst in the fifth reaction zone is between 38 and 57% by weight of the total quantity of catalyst used.

15. The process according to claim 1 , wherein catalyst contains a porous substrate, platinum, and halogen, where in the platinum content is between 0.01 and 5% by weight relative to the total weight of the catalyst, and the halogen content is between 0.5 and 15% by weight relative to the total weight of the catalyst.

Assignees

• Ifp Energies Now

Inventors

• Pagot Alexandre
• Lemaire Eric
• Dreux Heloise

Classifications

• C10G59/02 Primary

  plural serial stages only · CPC title