Low steam/carbon revamp of a plant comprising a steam reforming section and a water-gas shift section
The present invention relates to a revamp method for increasing the front-end capacity of a plant comprising a reforming section, wherein a feed is reformed in at least one reforming step to a reformed stream comprising CH 4 , CO, CO 2 , H 2 and H 2 O a shift section wherein the reformed stream is shifted in a shift reaction in at least a high temperature shift step, said method comprising the steps of In the High temperature shift step exchanging an original Fe-based catalyst with a non-Fe-based catalyst Increasing the feed flow to the reforming section, and The HTS step is carried out at a reduced steam/dry-gas ratio (S/DG) compared to an original S/DG in the original HTS step with the original Fe-based catalyst.
1. A method for increasing the front-end capacity of a plant comprising
a reforming section, wherein a feed is reformed in at least one reforming step to a reformed stream comprising CH 4 , CO, CO 2 , H 2 and H 2 O,
a shift section wherein the reformed stream is shifted in a shift reaction in at least a high temperature shift step,
said method comprising the steps of
in the High temperature shift step exchanging an original Fe-based catalyst with a non-Fe-based catalyst
increasing the feed flow to the reforming section, and
the HTS step is carried out at a reduced steam/dry-gas ratio (S/DG) compared to an original S/DG in the original HTS step with the original Fe-based catalyst.
2. The method according to claim 1 wherein the feed comprises natural gas, naphtha, rich gases, LPG, or combinations thereof.
3. The method according to claim 1 wherein the plant is a H 2 or NH 3 or synthesis gas for H 2 or NH 3 production plant.
4. The method according to claim 1 wherein the original Fe-based catalyst comprises oxides of iron, chromium and optionally copper.
5. The method according to claim 1 wherein the non-Fe-based catalyst comprises oxides or other compounds of Zn, Al, and alkali metal selected from the group of Na, K, Rb and Cs and optionally Cu.
6. The method according to claim 1 wherein the HTS step is carried out at a reduced S/DG ratio of below 0.9.
7. The method according to claim 1 wherein the feed flow is increased with at least 2%.
8. The method according to claim 1 wherein the S/DG ratio is reduced 1-50% with respect to the original S/DG ratio.
9. The method according to claim 1 wherein the steam addition upstream the HTS step is reduced compared to the original steam addition by 0.1-50.
10. The method according to claim 1 wherein the pressure drop dP is increased compared to the original dP.
11. The method according to claim 1 wherein the reforming section may comprise a performing step.
12. The method according to claim 1 wherein the shift section further comprises one or more medium and/or low temperature shift steps.
13. The method according to claim 1 wherein the reforming section is further revamped.
14. The method according to claim 8 , wherein the S/DG ratio is reduced 5-25% with respect to the original S/DG ratio.
15. The method according to claim 8 , wherein the S/DG ratio is reduced 10-20% with respect to the original S/DG ratio.
16. The method according to claim 8 , wherein the S/DG ratio is reduced 12-17% with respect to the original S/DG ratio.