Method for shutting down a Fischer-Tropsch reactor

Patent metadata

Field	Value
Publication number	US-12577181-B2
Application number	US-202118246254-A
Country	US
Kind code	B2
Filing date	Nov 12, 2021
Priority date	Dec 3, 2020
Publication date	Mar 17, 2026
Grant date	Mar 17, 2026

Abstract

A method is described for shutting down a Fischer-Tropsch reactor fed with a reactant gas mixture comprising a synthesis gas and a recycle gas recovered from the Fischer-Tropsch reactor in a synthesis loop, said Fischer-Tropsch reactor containing a Fischer-Tropsch catalyst cooled indirectly by a coolant under pressure, comprising the steps of: (a) depressurising the coolant to cool the reactant gas mixture to quench Fischer-Tropsch reactions taking place in the Fischer-Tropsch reactor, (b) stopping the synthesis gas feed to the Fischer-Tropsch reactor, and (c) maintaining circulation of the recycle gas through the Fischer-Tropsch reactor during steps (a) and (b) to remove heat from the Fischer-Tropsch reactor. The method safely facilitates a more rapid return to operating conditions than a full shut-down.

First claim

The invention claimed is:

1 . A method for shutting down a Fischer-Tropsch reactor fed with a reactant gas mixture comprising a synthesis gas and a recycle gas recovered from the Fischer-Tropsch reactor in a synthesis loop, said Fischer-Tropsch reactor containing a Fischer-Tropsch catalyst cooled indirectly by a coolant under pressure, comprising:
(a) depressurising the coolant to cool the reactant gas mixture to quench Fischer-Tropsch reactions taking place in the Fischer-Tropsch reactor, (b) stopping the synthesis gas feed to the Fischer Tropsch reactor, and (c) maintaining circulation of the recycle gas through the Fischer-Tropsch reactor during (a) and (b) to remove heat from the Fischer-Tropsch reactor, wherein the Fischer-Tropsch reactor comprises a pressure vessel in which the Fischer-Tropsch catalyst is provided within a plurality of reactor tubes that are bathed in coolant flowing around their outsides.

2 . The method according to claim 1 , wherein the synthesis gas consists essentially of hydrogen and carbon monoxide with a molar ratio of hydrogen to carbon monoxide in the range of 1.6:1 to 2.5:1.

3 . The method according to claim 1 , wherein the Fischer-Tropsch reactor, prior to shut down is operated at a pressure in the range 10 to 100 bar abs and a temperature in the range 170 to 350° C.

4 . The method according to claim 1 , wherein the Fischer-Tropsch catalyst is an iron Fischer-Tropsch catalyst or a cobalt Fischer-Tropsch catalyst.

5 . The method according to claim 1 , wherein the Fischer-Tropsch catalyst is used in combination with a catalyst carrier suitable for use in a tubular Fischer-Tropsch reactor where the catalyst carrier containing the catalyst is disposed within one or more tubes cooled by the coolant under pressure.

6 . The method according to claim 1 , wherein the coolant is boiling water under pressure provided by a steam drum coupled to the Fischer-Tropsch reactor.

7 . The method according to claim 6 , wherein the depressuring step (a) is provided using an orifice and/or a control valve connected to the steam drum.

8 . The method according to claim 1 , wherein the depressuring step (a) is at a rate of 2 to 6 bar per minute.

9 . The method according to claim 1 , wherein a temperature in step (a) is reduced to 150° C. or less.

10 . The method according to claim 1 , wherein the method is followed directly by a start-up of a Fischer-Tropsch process.

11 . The method according to claim 10 , wherein the method further comprises: (d1) reducing the pressure of the Fischer-Tropsch reactor and circulating recycle gas, (e1) adjusting an inert gas content of the circulating recycle gas to a minimum value, (f1) re-pressurising the Fischer-Tropsch reactor with synthesis gas feed, (g1) re-pressurising the coolant thereby increasing a temperature of the Fischer-Tropsch reactor until Fischer-Tropsch reactions begin to occur, and (h1) introducing synthesis gas to the Fischer-Tropsch reactor.

12 . The method according to claim 11 , wherein in step (d1) the pressure of the Fischer-Tropsch reactor is reduced to pressure in the range of 5-10 bara.

13 . The method according to claim 11 , wherein in step (e1) a minimum inert gas content of the circulating recycle gas is in the range of 60 to 80% by volume.

14 . The method according to claim 11 , wherein in step (f1) the pressure is raised to a pressure 60 to 100% of an operating pressure prior to the shutdown.

15 . The method according to claim 11 , wherein in step (g1), where the coolant is boiling water under pressure, re-pressurisation is achieved by pre-pressurising a steam drum coupled to the Fischer-Tropsch reactor using a steam eductor/jet-pump loop.

16 . The method according to claim 1 , wherein the method is followed by a full shut-down of a Fischer-Tropsch process.

17 . The method according to claim 16 , wherein the method further comprises: (d2) stopping the circulation of the recycle gas, (e2) feeding an inert gas feed into the Fischer-Tropsch reactor and loop at a pressure greater than the pressure of the Fischer-Tropsch reactor and loop, and (f2) purging the Fischer-Tropsch reactor and loop of reactant gases using the inert gas feed to displace the recycle gas.

18 . The method according to claim 17 , wherein in step (e2) the inert gas feed is a nitrogen gas feed.

19 . The method according to claim 17 , wherein in step (e2), the inert gas is supplied from a pressurised tank dedicated for the method.

20 . The method according to claim 1 , wherein the method is activated manually or operated autonomously using a computerised plant control system and/or plant safety-instrumented system.

21 . The method according to claim 20 , wherein the computerised plant control system and/or plant safety-instrumented system additionally instructs upstream and/or downstream operations to shut-down or enter a safe-operating state.

Assignees

• Johnson Matthey Davy Technologies Ltd

Inventors

• Baker Robert Miles
• Clarkson Jay Simon
• Coe Andrew James
• Gallen Robert William
• Pearson Richard Philip David
• Tamsett Colin

Classifications

• C07C2523/75

  Cobalt · CPC title

• C07C2523/745

  Iron · CPC title

• C07C1/047

  Processes in which one or more parameters are changed during the process; Starting-up of the process · CPC title

• C07C1/046

  Numerical values of parameters · CPC title

• C07C1/044

  containing iron · CPC title