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troubleshooting catalyst losses

Home Forums CatCracking FCC Operations troubleshooting catalyst losses

This topic contains 2 replies, has 2 voices, and was last updated by  dblewis 10 months, 2 weeks ago.

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  • #28874

    Paul R Orlowski
    Keymaster

    In troubleshooting catalyst losses, can you describe any cases where a unit shutdown was imminent (e.g., severe cyclone failure) if the losses could not be stopped quickly? What is your recommendation for avoiding shutdowns due to excessive catalyst losses?

  • #28875

    Paul R Orlowski
    Keymaster

    There are a number of scenarios that can lead to a FCC unit shutdown due to excessive catalyst losses. Generally, inability to maintain regenerator bed level leads to an imminent unit shutdown. Since the stripper bed level is controlled with the spent catalyst valve any catalyst loss from the reactor or the regenerator is reflected in a loss of regenerator level. Refiners will face the decision to shut down whenever the catalyst loss is so high that:

    – Not enough make-up catalyst (fresh or equilibrium) is available to restore the catalyst lost
    – Catalyst loading via loader or pressuring from the hopper falls short of the required make-up rate
    – Cost of replacing the lost catalyst becomes prohibitive
    – Slurry oil ash or BS&W specifications cannot be met, leading to severe product discounts and loss of sales
    – Wet gas scrubber (WGS) purge solids separation/containment inventory is inadequate
    – Electrostatic precipitator fines collection rate exceeds the number of rolloff bins available
    – Stack opacity/particulate emission limit compliance is difficult to achieve
    – Slurry oil pump reliability and mechanical availability is unacceptable leading to significant feedrate reductions.

    There may be opportunities to mitigate the catalyst loss and delaying the need for shutdown. The delay would allow the refiner to troubleshoot and develop corrective action plans for staying on-line and keeping operating costs down.

    The refiner could consider:

    – Pressure bumping to possibly dislodge an obstruction or aerate a de-fluidized zone
    – Adjusting the fresh catalyst attrition resistance or fines content
    – Making up with equilibrium catalyst versus fresh catalyst
    – Adjusting air/steam rates, as well as the distribution if multiple grids/rings are available
    – Lowering/raising bed levels to check impact on cyclone operation
    – Lowering/raising operating temperature to lower/raise velocities
    – Lowering/raising operating pressure to raise/lower velocities
    – Conducting diagnostic studies to help identify what equipment needs repair.
    posted for B.L.

  • #29186

    dblewis
    Participant

    This scenario revolves around Unit start up. If the cat losses are coming from the Reactor to the Main Fractionator, the decision to bypass and stop cat circulation should happen very quickly. A series of pressure bumps should be performed as part of your start up procedure.

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