Method for treating a synthesis gas stream
View Patent ↗A process can be used to treat a synthesis gas stream comprising steam reforming firstly in a primary reformer and subsequently in a secondary reformer. Crude synthesis gas exiting the secondary reformer may be cooled in a steam generator and then further cooled in a steam superheater. The crude synthesis gas stream after exiting the secondary reformer may be split into at least two gas substreams, of which only a first gas substream is fed to the steam generator. A second gas substream may be supplied to the steam superheater, bypassing the steam generator. Only the first gas substream, after flowing through the steam generator, may be subjected to a CO conversion reaction in a first CO conversion reactor before the first gas substream is supplied to the steam superheater.
1. A process for treating a synthesis gas stream comprising steam reforming firstly in a primary reformer and subsequently in a secondary reformer, the process comprising:
splitting a crude synthesis gas stream that exits the secondary reformer into a first gas substream and a second gas substream;
feeding the first gas substream to a steam generator;
cooling the first gas substream in the steam generator;
supplying the second gas substream to a steam superheater so as to bypass the steam generator;
cooling the second gas substream in the steam superheater;
subjecting only the first gas substream to a CO conversion reaction in a first CO conversion reactor after the first gas substream passes through the steam generator; and
supplying the first gas substream to the steam superheater after the first gas substream passes through the first CO conversion reactor.
2. The process of claim 1 comprising:
recombining the first and second gas substreams after the first gas substream exits the first CO conversion reactor; and
supplying a partially-converted crude synthesis gas stream, which is formed by recombining the first gas substream and the second gas substream, to the steam superheater.
3. The process of claim 1 comprising feeding a cooled crude synthesis gas stream that exits the steam superheater to a second CO conversion reactor.
4. The process of claim 3 comprising discharging a fully-converted synthesis gas stream from the second CO conversion reactor.
5. The process of claim 1 comprising generating saturated steam in the steam generator and feeding the saturated steam to the steam superheater.
6. The process of claim 1 comprising discharging superheated steam from the steam superheater.
7. The process of claim 1 wherein the crude synthesis gas stream is split such that a ratio m 1 :m 2 of the first gas substream to the second gas substream is 0.9 or less.
8. The process of claim 1 wherein the crude synthesis gas stream is split such that a ratio m 1 :m 2 of the first gas substream to the second gas substream is 0.7 or less.
9. The process of claim 1 wherein the crude synthesis gas stream is split into the first and second gas substreams such that a mixing temperature of a stream formed by recombining the first and second gas substreams is at least 440° C.
10. The process of claim 1 wherein the crude synthesis gas stream is split into the first and second gas substreams such that a mixing temperature of a stream formed by recombining the first and second gas substreams is at least 550° C.
11. A plant for treating a synthesis gas stream, the plant comprising:
a primary reformer;
a secondary reformer downstream of the primary reformer, wherein a crude synthesis gas stream is configured to exit the secondary reformer;
a steam generator downstream of the secondary reformer, wherein a first gas substream of the crude synthesis gas stream is configured to flow through the steam generator;
a steam superheater downstream of the steam generator;
a branch line that branches off downstream of the secondary reformer and is configured to convey a second gas sub stream, wherein the branch line is configured to divert the second gas substream from a region downstream of the secondary reformer and upstream of the steam generator so as to bypass the steam generator; and
a first CO conversion reactor disposed downstream of the steam generator and upstream of the steam superheater, wherein only the first gas substream is configured to flow through the first CO conversion reactor.
12. The plant of claim 11 comprising a second CO conversion reactor disposed downstream of the steam superheater, wherein a combined crude synthesis stream comprised of the first and second gas sub streams is configured to flow through the second CO conversion reactor.
13. The plant of claim 11 configured to perform the process of claim 12 .