Process for preparing a low-sulfur reformate gas for use in a fuel cell system
The invention provides a multistep process for preparing a low-sulfur reformate gas for use in a fuel cell system. The process comprises catalytic steam reforming of a reactant gas mixture comprising sulfur-containing hydrocarbons and steam in a first step to make a reformate, reducing the carbon monoxide content of the reformate in a second step, passing the reformate over a sulfur absorber either directly after the first step or after passage through the second step, and desorbing the sulfur components optionally absorbed on the catalysts in the reforming and reducing process steps by periodically raising the temperature so as to cause the sulfer components to pass to the absorber, wherein the temperature of the absorber during operation of the process is always kept within a temperature interval which is an optimum for the absorber.
1. A multi-step process for preparing a low-sulfur reformate gas for use in a fuel cell system, said process comprising
a) catalytic steam reforming of a reactant gas mixture, comprising sulfur-containing hydrocarbons and steam and characterized by a steam/carbon ratio, in a first step to make a reformate;
b) reducing carbon monoxide content of the reformate in a second step;
c) contacting the reformate with a sulfur absorber after the second step; and
d) desorbing sulfur components, if any, absorbed on catalysts used in the first step and in the second step, by periodically raising temperature, so that the sulfur components are passed to the sulfur absorber, wherein the temperature of the absorber during operation of the process is always kept within a temperature interval in which the absorption capacity of the absorber for the sulfur components is at an optimum.
2. A process according to claim 1 , wherein in the second step the carbon monoxide content of the reformate is reduced on a high temperature shift catalyst.
3. A process according to claim 2 , wherein the process has an additional step in which the carbon monoxide content of the reformate is further reduced on a low temperature shift catalyst.
4. A process according to claim 3 , wherein the sulfur absorber is located between the high temperature shift catalyst and the low temperature shift catalyst.
5. A process according to claim 1 , wherein the increase in temperature required for desorption of the sulfur components is achieved by reducing the steam/carbon ratio of the reactant gas mixture during continuous operation.
6. A process according to claim 1 , wherein the steam reforming procedure is operated autothermally by introducing air into the reactant gas mixture, wherein the air/fuel ratio is used to characterize the proportion of air in the reactant gas mixture and the temperature increase required for desorption of the absorbed sulfur components is achieved by increasing the air/fuel ratio.
7. A process according to claim 6 , wherein the steam/carbon ratio is also reduced in order to increase the temperature.
8. A process according to claim 1 , wherein the temperature of the absorber is kept within the temperature interval by bringing the reformate gas to a constant temperature.
9. A process according to claim 1 , wherein the sulfur absorber is replaced periodically.
10. A process of operating a stationary or mobile fuel cell system in which a low-sulfur reformate gas is used, the process comprising preparing the reformate gas by the process of claim 1 .