Fig. 6: Implementing the coke transformation strategy over CAT catalysts in a pilot plant. | Nature Communications

Fig. 6: Implementing the coke transformation strategy over CAT catalysts in a pilot plant.

From: Directed transforming of coke to active intermediates in methanol-to-olefins catalyst to boost light olefins selectivity

Fig. 6

a MTO reaction performances over the CAT-Coked sample completely regenerated by air combustion at 953 K (abbreviated as CAT-Coked@Air) and treated by steam at 953 K with the water feed of 500 g h−1 (abbreviated as CAT-Coked@H2O-a). b MTO reaction performances over the CAT-Coked@Air sample and CAT-Coked sample treated by steam at 953 K with the water feed of 300 g h−1 (abbreviated as CAT-Coked@H2O-b).

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