Slurry bubble column reactor for a fischer-tropsch process

Patent metadata

Field	Value
Publication number	US-10590348-B2
Application number	US-201716306264-A
Country	US
Kind code	B2
Filing date	May 19, 2017
Priority date	Jun 2, 2016
Publication date	Mar 17, 2020
Grant date	Mar 17, 2020

Abstract

The disclosure deals with a slurry bubble column reactor for converting a gas mixture comprising carbon monoxide and hydrogen into liquid hydrocarbons. The slurry bubble column reactor features a slurry bed of catalyst particles, an inlet conduit for feeding the gas mixture into the slurry bed, a filtration zone for separating the liquid hydrocarbons from the catalyst particles and a liquid outlet conduit for withdrawing the separated hydrocarbons from the filtration zone. The filtration zone is situated in the slurry bubble column reactor such that the slurry bed is found in a first and a second heat exchange zone with the filtration zone arranged between the first and the second heat exchange zone.

First claim

The invention claimed is:

1. A slurry bubble column reactor for converting a gas mixture comprising carbon monoxide and hydrogen into liquid hydrocarbons featuring a slurry bed of catalyst particles, an inlet conduit for feeding the gas mixture into the slurry bed, a filtration zone for separating the liquid hydrocarbons from the catalyst particles and a liquid outlet conduit for withdrawing the separated hydrocarbons from the filtration zone, wherein the filtration zone is situated in the slurry bubble column reactor such that the slurry bed is found in a first and a second heat exchange zones with the filtration zone arranged between the first and the second heat exchange zones.

2. The slurry bubble column reactor according to claim 1 , wherein each heat exchange zone features a separate heat exchanger.

3. The slurry bubble column reactor according to claim 1 , wherein the slurry bubble column reactor comprises a bottom zone and the inlet conduit is fluently connected to the bottom zone.

4. The slurry bubble column reactor according to claim 3 , wherein the first heat exchange zone is situated next to the bottom zone of the slurry bubble column reactor.

5. The slurry bubble column reactor according to claim 1 , wherein the filtration zone comprises at least one hollow and enclosed filter element and at least one rinsing conduit for cleaning the filter element.

6. The slurry bubble column reactor according to claim 1 , wherein the slurry bubble column reactor features a gas outlet conduit on top to withdraw gaseous products and unreacted synthesis gas.

7. The slurry bubble column reactor according to claim 1 , wherein the filtration zone features a diameter similar to the slurry bubble column reactor diameter and that the beginning of the filtration zone measured from a lower tangent line (L.T.L.) of the slurry bubble column reactor is between 20% and 60% of the height of the slurry bubble column reactor from the lower tangent line (L.T.L.) to an upper tangent line (U.T.L.).

8. The slurry bubble column reactor according to claim 1 , wherein the heat exchange zones feature a diameter similar to the slurry bubble column reactor diameter and that the height of the first heat exchange zone is between 75% and 150% of the height of the second heat exchange zone.

9. A process for converting a gas mixture comprising carbon monoxide and hydrogen into liquid hydrocarbons, when the gas mixture is fed into a slurry bed in a slurry bubble column reactor, where at least part of the gas mixture is converted into liquid hydrocarbons on the catalyst particles in the slurry bed, wherein the obtained liquid hydrocarbons are separated from the catalyst particles in a filtration zone located in the slurry bubble column reactor and wherein at least parts of the separated liquid hydrocarbons are withdrawn from the filtration zone, wherein the gas mixture is converted in two heat exchange zones fluently connected via the filtration zone only.

10. The process according to claim 9 , wherein the temperature inside the slurry bubble column reactor is between 200° C. and 260° C. and/or the pressure inside the slurry bubble column reactor is between 10 and 50 bar g.

Assignees

• Air Liquide
• The Petroleum Oil And Gas Corp Of South Africa Soc Ltd

Inventors

• Brueschke Marc
• Taylor Patrick Otto
• Søraker Pål

Classifications

• B01J8/006

  by filtration · CPC title

• B01J8/22

  gas being introduced into the liquid · CPC title

• B01J2208/00115

  with heat exchange elements inside the bed of solid particles · CPC title

• C10G2/344 Primary

  according to the "fluidised-bed" technique · CPC title

• C10G31/09

  by filtration · CPC title