Reactors for heterogeneous synthesis

B - Operations – Transporting – 01 – J

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B01J 8/04 (2006.01) B01J 19/00 (2006.01) C01C 1/04 (2006.01)

Patent

CA 2005077

A B S T R A C T Improved process to convert in situ conventional reactors with four catalytic beds with axial flow and with intermediate quenching (Kellogg reactor), characterized by the fact that the third and fourth original beds are combined thus obtaining a reactor with three beds through which the synthesis gas now flows with a substantially radial flow.

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