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- W2393050923 abstract "For deep upgrading heavy oil the surplus of carbon and shortage of hydrogen in the end products will occur. In order to self-balance the ratio of hydrogen to carbon in some extent, it is worthwhile to convert the surplus carbon originated in feed to hydrogen by water-gas reaction in the regenerator system of FCCU, thus the and gasification process could be combined and this process is named refining and gasification combined technology. It was found that during the regeneration of catalyst by a mixture of N_2 and O_2, the content of CO in flue gas increases with the increase of O_2 content in the mixture. In the diffusing control region, temperature rising is bad for increasing CO content. The yield of potent gas (CO+H_2) is about 3.43 l/g (Calculated based on 1 g carbon) in the reaction of steam or CO_2 with coke. But the mass fraction of reacted coke is around 50% in 15 min at 910. As for the reaction of coke with steam and O_2, the potent gas yield is about 1.9 l/g and the mass fraction of reacted coke is over 90% in 10 min at 910." @default.
- W2393050923 created "2016-06-24" @default.
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- W2393050923 date "2005-01-01" @default.
- W2393050923 modified "2023-09-26" @default.
- W2393050923 title "THE EXPLORATION OF PETROLEUM REFINING AND GASIFICATION COMBINED PROCESS" @default.
- W2393050923 hasPublicationYear "2005" @default.
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