Multi-bed reactor with mixing device

Patent metadata

Field	Value
Publication number	US-9757703-B2
Application number	US-201514812484-A
Country	US
Kind code	B2
Filing date	Jul 29, 2015
Priority date	Feb 5, 2013
Publication date	Sep 12, 2017
Grant date	Sep 12, 2017

Abstract

A mixing device mounted between two catalyst beds in a multi-bed catalytic reactor with a cylindrical shape. The mixing device has a circular outer rim which corresponds to the inner wall of the reactor, and includes a collecting section for collecting fluid from an up-stream catalytic bed, a mixing section for mixing the collected fluid, and a discharging section for discharging the mixed fluid to a down-stream catalytic bed. The collecting section, the mixing section and the discharging section are disposed outside the center of the circular cross-section of the reactor.

First claim

What is claimed is:

1. A multi-bed catalytic reactor with a cylindrical shape comprising:
a mixing device mounted between two catalyst beds in said reactor, said mixing device has a circular outer rim which corresponds to the inner wall of the reactor, the mixing device comprising:
annularly shaped inlet means for receiving flow from a first catalyst bed and configured to convert axial flow from said reactor to circumferential and axially inclined flow,
collecting means disposed in a collecting section for collecting fluid from said inlet means,
mixing means disposed in a mixing section for mixing the collected fluid, and discharging means disposed in a discharging section for discharging the mixed fluid to a down-stream catalytic bed;
wherein the mixing device has a donut shape and the collecting section, the mixing section and the discharging section are disposed outside the center of the circular cross-section of the reactor.

2. The multi-bed catalytic reactor according to claim 1 , wherein the outer rim of said mixing device is an integrated part of the reactor wall.

3. The multi-bed catalytic reactor according to claim 1 , wherein the collecting section, the mixing section and the discharging section are disposed at the outer one-third of the circular cross-sectional area of the reactor.

4. The multi-bed catalytic reactor according to claim 1 , wherein the collecting means, the mixing means and the discharging means comprise channels comprising circular arc divider walls horizontally dividing one section from another section or dividing one section from the center of the circular cross-section of the reactor.

5. The multi-bed catalytic reactor according to claim 1 , wherein the collecting means has one inlet for collecting the fluid from the up-stream catalytic bed.

6. The multi-bed catalytic reactor according to claim 1 , wherein the mixing device further comprises a quench inlet for adding a quench fluid to the collected fluid, said quench inlet is disposed in the collecting section.

7. The multi-bed catalytic reactor according to claim 1 , wherein the collecting section is disposed in an upstream axial level of the reactor relative to the discharging section.

8. The multi-bed catalytic reactor according to claim 1 , wherein the collecting section is disposed in an outer generally circular cross sectional area of the reactor relative to the mixing section, and the mixing section is disposed in an outer generally circular cross sectional area of the reactor relative to the discharging section.

9. The multi-bed catalytic reactor according to claim 1 , wherein the collecting section, the mixing section and the discharging section each is disposed in at least a 120° sector of the generally circular cross sectional area of the reactor.

10. The multi-bed catalytic reactor according to claim 1 , wherein the discharging means comprise radial discharge guide vanes providing a vertical downward outlet of the fluid from the mixing device.

11. The multi-bed catalytic reactor according to claim 1 , wherein the mixing device forms an integrated part of a catalyst bed support of the reactor.

12. The multi-bed catalytic reactor according to claim 1 , wherein the mixing device has a height of less than 0.5 m with respect to the axial direction of the reactor.

13. A multi-bed catalytic reactor with a cylindrical shape comprising:
a mixing device mounted between two catalyst beds in said reactor, said mixing device has a circular outer rim which corresponds to the inner wall of the reactor, the mixing device comprising:
collecting means disposed in a collecting section for collecting fluid from an up-stream catalytic bed;
mixing means disposed in a mixing section for mixing the collected fluid, and
discharging means disposed in a discharging section for discharging the mixed fluid to a down-stream catalytic bed, said discharging means further comprise an inner circular arc divider walls providing a spilling brim for a liquid phase of the fluid;
wherein the mixing device has a donut shape and the collecting section, the mixing section and the discharging section are disposed outside the center of the circular cross-section of the reactor.

Assignees

• Haldor Topsoe As
• Haldor Topsoe As

Inventors

• Zahirovic Emir
• Risbjerg Jarlkov Klaus
• Shah Louise Jivan
• Brix Jacob
• Boe Michael
• Holm-Christensen Olav

Classifications

• B01J8/0492 Primary

  Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title

• C10G49/002

  Apparatus for fixed bed hydrotreatment processes · CPC title

• C10G65/02

  plural serial stages only · CPC title

• B01J2208/00929

  Provided with baffles · CPC title

• C10G65/00

  Treatment of hydrocarbon oils by two or more hydrotreatment processes only · CPC title