Catalytic reactor
View Patent ↗A compact catalytic reactor for Fischer-Tropsch synthesis defines a multiplicity of first and second flow channels arranged alternately in the reactor, for carrying a gas mixture which undergoes Fischer-Tropsch synthesis, and a coolant fluid, respectively. Each first flow channel contains a removable gas-permeable catalyst structure incorporating a metal substrate. A multiplicity of flow paths are defined through the catalyst structure, and the voidage, that is to say the proportion of the cross-sectional area of the first flow channel constituted by the said multiplicity of flow paths, is between 25% and 70%. This provides an optimum balance between productivity and selectivity, so that operation of the reactor can be economic and controllable.
1. A compact catalytic reactor for Fischer-Tropsch synthesis defining a multiplicity of first and second flow channels arranged alternately in the reactor;
wherein the first flow channels are configured to carry a gas mixture which undergoes Fischer-Tropsch synthesis;
wherein the second flow channels are configured to carry a coolant fluid; and
wherein each first flow channel contains a removable gas-permeable catalyst structure comprising a non-porous metal substrate with continuous ceramic coating of substantially uniform thickness no more than 200 μm on at least one surface of said substrate, said ceramic coating incorporating catalytic material, said catalyst structure defining mesopores and macropores providing a pore surface area in the range 80-120 m 2 /g, and said catalyst structure being shaped for defining a multiplicity of bulk flow paths therethrough, wherein the voidage which comprises the proportion of the cross-sectional area of the first flow channel constituted by the said multiplicity of bulk flow paths is between 60% and 72%.
2. A reactor as claimed in claim 1 wherein said voidage is about 71%.
3. A reactor as claimed in claim 1 wherein said metal substrate of the catalyst structure comprises an aluminium-bearing ferritic steel.
4. A reactor as claimed in claim 1 , wherein said metal substrate of the catalyst structure comprises a metal foil of thickness less than 100 μm.
5. A reactor as claimed in claim 1 wherein said catalyst structure comprises a ceramic coating of thickness between 60 and 100 μm.
6. A plant for converting natural gas to longer chain hydrocarbons incorporating a steam reforming reactor for generating a synthesis gas, and a Fischer-Tropsch reactor as claimed in claim 1 for generating longer chain hydrocarbons.
7. A reactor as claimed in claim 2 wherein said metal substrate of the catalyst structure comprises an aluminium-bearing ferritic steel.
8. A reactor as claimed in claim 2 wherein said metal substrate of the catalyst structure comprises a metal foil of thickness less than 100 μm.
9. A reactor as claimed in claim 3 wherein said metal substrate of the catalyst structure comprises a metal foil of thickness less than 100 μm.
10. A reactor as claimed in claim 2 wherein said catalyst structure comprises a ceramic coating of thickness between 60 and 100 μm.
11. A reactor as claimed in claim 3 wherein said catalyst structure comprises a ceramic coating of thickness between 60 and 100 μm.
12. A reactor as claimed in claim 4 wherein said catalyst structure comprises a ceramic coating of thickness between 60 and 100 μm.
13. A plant for converting natural gas to longer chain hydrocarbons incorporating a steam reforming reactor for generating a synthesis gas, and a Fischer-Tropsch reactor as claimed in claim 2 for generating longer chain hydrocarbons.
14. A plant for converting natural gas to longer chain hydrocarbons incorporating a steam reforming reactor for generating a synthesis gas, and a Fischer-Tropsch reactor as claimed in claim 3 for generating longer chain hydrocarbons.
15. A plant for converting natural gas to longer chain hydrocarbons incorporating a steam reforming reactor for generating a synthesis gas, and a Fischer-Tropsch reactor as claimed in claim 4 for generating longer chain hydrocarbons.
16. A plant for converting natural gas to longer chain hydrocarbons incorporating a steam reforming reactor for generating a synthesis gas, and a Fischer-Tropsch reactor as claimed in claim 5 for generating longer chain hydrocarbons.