Debottlenecking Delta Coke Limited FCC Operations Martin Evans, Bart de Graaf, Paul Diddams Johnson Matthey Process Technologies 214 Bourne Blvd, Savannah, GA USA E-mail: [email protected] Abstract Many FCC units are run hard up against regenerator temperature, air rate or wet gas compressor constraints. Decreasing the delta coke on the catalyst provides a way to relieve these constraints, allowing refiners to run higher rates of heavier feeds, which has a significant positive impact on FCC profitability. FCC Process licensors are well aware of these incentives, and offer a variety of hardware solutions to help reduce delta coke. FCC catalyst suppliers also offer lower activity and lower delta coke catalysts, well suited for running high levels of residue feed. Lower catalyst activity is typically compensated for by higher catalyst addition rates. Rare earth oxides, titanates and various other metals traps have also been used for many years to reduce contaminant delta coke in high Vanadium applications. These materials have been used as trapping agents mainly because of their compatibility with FCC catalyst manufacturing routes. This allows them to be easily incorporated into the main catalyst particle. Using a separate particle trapping approach allows more effective metal trapping components to be used, since compatibility with the binding system of FCC catalyst is no longer a limitation. More effective irreversible trapping of contaminant metals such as vanadium can be achieved using mixed alkaline metal oxides, such as hydrotalcite like materials. The stronger the interaction of contaminant metal with the metal trap, the larger the benefits for the FCC operation. The subsequent reduction in delta coke and gas yield is an effective way to relieve FCC operating constraints, allowing refiners to run heavier feed to the FCC. This paper shows commercial data demonstrating the high affinity of such separate particle additives for contaminant metals. Data is presented from five different FCC operations where separate particle metal traps were used to relieve delta coke constraints. In each case different strategies were used to take advantage of the reduction in delta coke and gas make. In addition to presenting this commercial data, tentative mechanisms will be presented to explain how these additional benefits were achieved. It is interesting to note that in addition to residue feed FCC applications, separate particle metal traps are also becoming popular with refiners operating with lower levels of contaminant metals. These additives are not just vanadium traps – their unique ability to decrease delta coke and dry gas is becoming applicable to a broader range of FCC operations.
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