Fischer-tropsch process and reactor assembly

1. A method of accommodating a reduction in production capacity of one or more reactors in a multi-reactor assembly adapted for the production of hydrocarbon products from syngas, the syngas being provided by a syngas manufacturing facility and provided to an entry stream system providing syngas to each of the reactors, and having an exit stream system taking at least hydrocarbon products from the reactors, wherein the method comprises the steps of:

redistributing the syngas from the one or more said reactors to one or more other reactors, and

increasing the temperature in the said one or more other reactors to at least partially take over the reduction in production capacity of the one or more reactors.

2. A method as claimed in claim 1 for use with two or more reactors operating in parallel.

3. A method as claimed in claim 1 wherein the syngas entry stream system provides a constant input of syngas to the assembly of reactors.

4. A method as claimed in claim 1 wherein any reduction in the production of syngas by the syngas manufacturing facility is at most 5%.

5. A method as claimed in claim 1 wherein the assembly produces a constant output of hydrocarbon products or a method of accommodating a reduction in production capacity of one or more reactors in a multi-reactor assembly adapted for the production of hydrocarbon products from syngas, the syngas being provided by a syngas manufacturing facility and provided to an entry stream system providing syngas to each of the reactors, and having an exit stream system taking at least hydrocarbon products from the reactors, wherein the method comprises the steps of:

redistributing the syngas from the one or more said reactors to one or more other reactors, and

increasing the temperature in the said one or more other reactors to at least partially take over the reduction in production capacity of the one or more reactors

wherein the assembly produces a constant CO-conversion level.

6. A method as claimed in claim 5 wherein any reduction in the output of hydrocarbon products or CO-conversion level, or both, is at most 5%.

7. A method as claimed in claim 1 wherein the increase in temperature in said one or more other reactors is at most 20° C.

8. A method as claimed in claim 1 for use with a multi-stage hydrocarbon production process, the first stage having at least 3 reactors, and each subsequent stage has 50% or less of the number of reactors in the previous stage, and wherein the syngas is redistributed to the one or more other reactors within the same stage.

9. A method as claimed in claim 1 wherein the reduction in production capacity in the one or more reactors is at most 35% of the steady state production of the reactor assembly.

10. A process for the production of hydrocarbon products from syngas in a multi-reactor assembly having at least two reactors, the reactors having an entry stream system providing syngas to the reactors, and an exit stream system taking at least hydrocarbon products from the reactors, wherein following a reduction in production capacity in one or more of the reactors, syngas is redistributed from the one or more said reactors to one or more other reactors, and the temperature in the one or more said other reactors is increased to at least partially take over the reduction in production capacity of the one or more reactors.

11. A process for the production of hydrocarbon products as claimed in claim 10 further comprising hydroconversion and distillation to obtain hydrocarbon products.