Reactor for exothermic or endothermic catalytic reactions

Patent metadata

Field	Value
Publication number	US-9387456-B2
Application number	US-201013319930-A
Country	US
Kind code	B2
Filing date	May 10, 2010
Priority date	May 13, 2009
Publication date	Jul 12, 2016
Grant date	Jul 12, 2016

Abstract

Reactor for Fischer-Tropsch reaction which is carried out in a three-phase system essentially consisting of a reacting gaseous phase, a reacted liquid phase and a solid catalytic phase, wherein the solid catalytic phase consists of packed or structured bodies of catalytic material encaged within at least one honeycomb monolithic structure with a high thermal conductivity.

First claim

The invention claimed is:

1. A reactor comprising:
a substantially cylindrical vessel having feeding and discharge means of a thermoregulation fluid of a chemical reaction;
an upper closing element and a lower closing element respectively positioned at a top and at a bottom of the substantially cylindrical vessel;
feeding means of a reagent gaseous phase positioned in the upper closing element, the lower closing element or both;
discharge means of a reacted phase positioned in the upper closing element, the lower closing element or both; and
a plurality of honeycomb monolithic structures, optionally coaxially inserted inside tubular structures, inserted inside the substantially cylindrical vessel between the upper closing element and the lower closing element, each monolithic structure consisting of a substantially cylindrical continuous body having a diameter from 1 to 10 cm inside which there is a series of parallel axial channels, tubes, or both channels and tubes with a square or rectangular cross section with a side length of from 0.5 to 5 mm, which extends from one end to the other, separated by continuous honeycomb matrix, and filled with a catalyst in structured or particle form with an average dimension of from 0.3 mm to less than 3 mm positioned inside each channel, so as to fill the volume for a filling factor, (catalyst(volume)/(volume of the longitudinal channel), ranging from 0.2 to 0.8,
wherein the reactor is suitable for exothermic, endothermic, or both exothermic and endothermic reaction in the presence of the catalyst,
and
wherein the plurality of honeycomb monolithic structures is made of a material having an intrinsic thermal conductivity higher than 10 W/m /K.

2. The reactor according to claim 1 , wherein the reactor is arranged vertically or horizontally.

3. The reactor according to claim 1 , wherein a series of monolithic structures forms a bundle having a diameter which is substantially equal to an internal diameter of the substantially cylindrical vessel, or slightly less, and occupies a volume ranging from 50 to 90% of a total volume of the substantially cylindrical vessel.

4. The reactor according to claim 3 , wherein the bundle comprises from 10 to 20,000 monolithic structures.

5. The reactor according to claim 1 , wherein the plurality of honeycomb monolithic structures appears as a series of longitudinal channels, with a square or rectangular cross section having a length of sides ranging from 0.5 to 5 mm, immersed in a continuous body.

6. The reactor according to claim 1 , wherein the catalyst is solid.

7. The reactor according to claim 1 , wherein the catalyst comprises cobalt or iron supported on an inert solid.

8. The reactor according to claim 1 , wherein the catalyst comprises cobalt dispersed on a solid carrier consisting of at least one oxide of one or more of the following elements Si, Ti, Al, Zr, Mg.

9. The reactor according to claim 8 , wherein the solid carrier is silica, alumina or titania.

10. The reactor according to claim 1 , wherein the catalyst is in the form of granules.

11. The reactor according to claim 1 , wherein the catalyst is in the form of spherical granules.

12. The reactor according to claim 1 , wherein the catalyst is in the form of spherical granules with an average dimension of 0.3 mm to 1 mm.

13. The reactor according to claim 1 , wherein the plurality of honeycomb monolithic structures are coaxially inserted inside tubular structures.

14. The reactor according to claim 1 , wherein the substantially cylindrical vessel has a height of from 1 to 10 m.

15. The reactor according to claim 14 , wherein the substantially cylindrical vessel has a diameter of from 1 to 5 m.

16. A process for carrying a catalytic reaction, the process comprising:
feeding reagents to the reactor according to claim 1 , wherein the catalytic reaction is an exothermic , endothermic, or both exothermic and endothermic catalytic reaction.

17. The process according to claim 16 , wherein the catalytic reaction is a Fischer-Tropsch reaction.

18. The process according to claim 16 , wherein the catalyst is a packed or structured body.

Assignees

• Iovane Massimo
• Zennaro Roberto
• Forzatti Pio
• Groppi Gianpiero
• Lietti Luca
• Tronconi Enrico
• Visconti Carlo Giorgio
• Rossini Stefano
• Mignone Elsa
• Eni Spa

Inventors

• Iovane Massimo
• Zennaro Roberto
• Forzatti Pio
• Groppi Gianpiero
• Lietti Luca
• Tronconi Enrico
• Visconti Carlo Giorgio
• Rossini Stefano
• Mignone Elsa

Classifications

• B01J8/067

  Heating or cooling the reactor (B01J8/062 takes precedence) · CPC title

• B01J2219/2446

  Cell density · CPC title

• B01J19/2485 Primary

  Monolithic reactors · CPC title

• B01J2219/243

  Catalyst in granular form in the channels · CPC title

• B01J2219/2434

  Metals or alloys · CPC title