Process and apparatus for steam-methane reforming
View Patent ↗Methane is reacted with steam, to generate carbon monoxide and hydrogen in a first catalytic reactor; the resulting gas mixture can then be used to perform Fischer-Tropsch synthesis in a second catalytic reactor. In performing the steam/methane reforming, the gas mixture is passed through a narrow flow channel containing a catalyst structure on a metal substrate, and adjacent to a source of heat, in a time less than 0.5 s, so that only those reactions that have comparatively rapid kinetics will occur. Both the average temperature and the exit temperature of the channel are in the range 750° to 900° C. The ratio of steam to methane should preferably be 1.4 to 1.6, for example about 1.5. Almost all the methane will undergo the reforming reaction, almost entirely forming carbon monoxide. After performing Fischer-Tropsch synthesis, the remaining hydrogen is preferably used to provide heat for the reforming reaction.
1. A process for converting methane to longer chain hydrocarbons, the process comprising the steps of:
(a) mixing a feed gas comprising methane with steam for forming a gas mixture in which the ratio of steam to methane is in the range 1.2 to 2.0;
(b) subjecting the gas mixture to reforming for generating carbon monoxide and hydrogen in a catalytic reactor comprising several narrow flow channels between metal sheets, the flow channels being arranged alternately with channels for an exothermic reaction to provide a source of heat, so that the sheets separate the flow channels from the source of heat, the flow channel containing a fluid-permeable catalyst structure with a metal substrate to enhance heat transfer, and each flow channel being of length at 100 mm, causing the gas mixture to flow through the flow channels, wherein the residence time in the flow channels is less than 500 ms but at least 20 ms, and both the average temperature along the flow channels and the exit temperature of the flow channels are in the range 750° C. to 900° C.;
(c) subjecting the carbon monoxide and hydrogen from the reforming step to a subsequent Fischer-Tropsch synthesis;
(d) separating a gas stream including hydrogen from the resulting longer chain hydrocarbons; and
(e) subjecting the hydrogen-including gas stream to combustion in the channels for the exothermic reaction for providing at least part of the heat source for the reforming step.
2. A process as claimed in claim 1 wherein the reforming reaction step is carried out at atmospheric pressure.
3. A process as claimed in claim 1 wherein the reforming reaction step is carried out at an elevated pressure in the range 0 to 200 kPa above atmospheric pressure.
4. A process as claimed in claim 1 wherein the said ratio is in the range 1.4 to 1.6.
5. A process as claimed in claim 1 including carrying out the Fischer-Tropsch synthesis at a temperature of about 230° C.
6. A process as claimed in claim 1 including the step of compressing the carbon monoxide and hydrogen from the reforming step to a higher pressure before being subjected to the subsequent Fischer-Tropsch synthesis.
7. A process as claimed in claim 1 wherein the residence time of the gas mixture in the reforming reactor is less than 100 ms.