Process for preparing a paraffin product

1. A method for preparing a paraffin product from a carbonaceous feedstock comprising the following steps:

(a) partial oxidation of the carbonaceous feedstock to obtain a mixture comprising hydrogen and carbon monoxide;

(b) performing a Fischer-Tropsch reaction using the mixture as obtained in step (a) and recovering an off-gas from the Fischer-Tropsch reaction and a paraffin product;

(c) subjecting at least a part of the off-gas from the Fischer-Tropsch reaction to conversion of carbon monoxide to carbon dioxide and to hydrogenation using a steam/off-gas mol ratio in the range of between 0.5 and 1.5, and a catalyst comprising copper and zinc;

(d) subjecting at least a part of the gas resulting from step (c) to conversion using a nickel based catalyst comprising at most 0.2 wt % cobalt, at most 0.2 wt % iron and at most 0.2 wt % ruthenium, calculated on the total weight of the catalyst; and,

(e) preparing a hydrogen comprising gas from at least a part of the gas resulting from step (d) using a reforming process.

2. The method of claim 1 , wherein the steam/off-gas mol ratio in step (c) is in the range of between 0.7 and 1.5.

3. The method of claim 1 , wherein the steam/off-gas mol ratio in step (c) is in the range of between 0.8 and 1.2.

4. The method of claim 1 , wherein the reforming comprises a process selected from the group consisting of: a steam reforming process, a steam methane reforming process, an adiabatic steam reforming process, a fired steam reforming process, an auto thermal steam reforming process, and an adiabatic steam reforming process.

5. The method of claim 1 , wherein the inlet temperature used for a reactor used for conversion and hydrogenation step (c) is in the range of between 200 and 300° C.

6. The method of claim 1 , wherein conversion and hydrogenation step (c) is performed using two or more reactors in parallel.

7. The method of claim 1 , wherein the inlet temperature used for a reactor used for step (d) is in the range of between 300 and 500° C.

8. The method of claim 1 , wherein the steam/off-gas mol ratio used for step (c) is in the range of between 0.8 and 1.2.

9. The method of claim 1 , wherein after step (b) and before step (c) hydrocarbons are removed from the off-gas from the Fischer-Tropsch reaction.

10. The method of claim 9 wherein the hydrocarbons are removed from the off-gas from the Fischer-Tropsch reaction by:

I) contacting at least a part of the off-gas from the Fischer-Tropsch reaction with a wash fluid in a scrubber;

II) removing wash fluid and at least a portion of the C3+ hydrocarbons in a stream from the scrubber of step I);

III) removing the remaining off-gas in a separate stream from the scrubber of step I);

IV) providing a feed comprising at least a part of the stream obtained in step II) to a separator;

V) separating at least a part of the stream obtained in step II) in the separator of step IV) into at least one light stream and one heavy stream, said light stream preferably comprising carbon monoxide and carbon dioxide and said heavy stream preferably comprising hydrocarbons with at least 3 carbon atoms;

VI) splitting at least a part of the heavy stream obtained in step V) into at least two streams, whereby at least one stream comprises wash fluid and another stream comprises hydrocarbons with at least 3 carbon atoms and at most 5 vol % of hydrocarbons with 10 or more carbon atoms;

VII) providing a feed comprising at least a part of the wash fluid comprising stream obtained in step VI) to the scrubber of step I).

11. The method of claim 10 further comprising:

VIII) providing a further feed comprising wash fluid to the scrubber of step I), and whereby the light stream preferably comprising carbon monoxide and carbon dioxide which is separated in step V) is subjected to hydrogenation in step (c).