Desulfurisation of fuel

1. A method of removing sulfur from a fuel supply stream for a fuel cell that is capable internally reforming methane to hydrogen at an anode of the fuel cell, which method comprises the step:

(a) hydrogenating the fuel supply stream by contacting it with a hydrogenation catalyst in the presence of hydrogen to convert sulfur-containing compounds in the fuel supply stream into hydrogen sulfide;

(b) removing the hydrogen sulfide to produce a desulfurised fuel stream;

(c) pre-reforming the desulfurised fuel stream in a stream pre-reformer at a temperature no greater than 450° C. to convert higher hydrocarbons in the fuel supply stream and to produce a cell feed stream for delivery to the fuel cell that comprises steam and an amount of methane, the amount of methane being dependent upon the load requirements of the fuel cell;

(d) splitting the fuel cell feed stream into a first portion that is a suitable feed stream for internal reforming of methane at an anode of the fuel cell and a second portion;

(e) delivering the first portion of the fuel cell feed stream to the anode of the fuel cell;

(f) processing the second portion of the fuel cell feed stream using a reformer operated at a temperature of 500 to 850° C. to increase the hydrogen content of the fuel cell feed stream to produce a hydrogen-enriched fuel stream;

(g) cooling and removing excess water from the hydrogen-enriched fuel stream produced in step (f) to produce a cooled and dehydrated hydrogen-enriched fuel stream; and

(h) using the cooled and dehydrated hydrogen-enriched fuel stream produced in step (g) as a source hydrogen to hydrogenate the fuel supply stream in step (a) by mixing the hydrogen-enriched fuel stream with the fuel supply stream prior to hydrogenation in step (a).

2. A method according to claim 1 , wherein the fuel supply stream is gasoline, diesel, kerosene, naphtha, LPG or natural gas.

3. A fuel processing system comprising:

hydrogenation means comprising a hydrogenation catalyst;

hydrogen sulfide removal means provided downstream from and in communication with the hydrogenation means;

a steam pre-reformer provided downstream from and in communication with the hydrogen sulfide removal means, the steam pre-reformer having a maximum operating temperature no greater than 450° C.;

a reformer operable at a temperature of 500 to 850° C. which is provided downstream from and in communication with the steam pre-reformer, upstream from and in communication with the hydrogenation means and upstream in communication with a fuel cell that is capable of internal reforming of methane at an anode of the fuel cell;

a divider to split the output of the steam pre-reformer into a first portion that is to be delivered to the anode of the fuel cell and a second portion that is to be delivered to the reformer, while in use the divider splitting the output of the steam pre-reformer to ensure that the first portion is suitable for delivery to the anode of the fuel cell based upon the load requirements of the fuel cell; and

cooling means and excess water removal means provided downstream from and in communication with the reformer wherein the cooling means and excess water removal means receive the output of the reformer.

4. A fuel cell system comprising the fuel processing system of claim 3 and a fuel cell provided downstream from and in communication with the steam pre-reformer, the anode of the fuel cell receiving a portion of the output of the steam pre-reformer based upon the load requirements of the fuel cell.