Refining Community Logo

Re-foam during steam stripping

Home Forums Coking Technical Antifoam, Quench Oil, Level Control Antifoam Re-foam during steam stripping

This topic contains 1 reply, has 2 voices, and was last updated by  Mike Kimbrell 4 years, 7 months ago.

  • Author
  • #28657


    Dear members,

    In one of our Delayed Coker units we suffer frequent re-foam events: sudden foaming during the steam stripping stage. These events sometimes happen when we turn to stripping to blowdown, so probably the main reason for these events is depressurizing of the coker drum. However, other foaming events happen in the first stege of stripping, when we have stopped feeding VR and we are stripping to main fractionator.
    We always carry out the stripping following the same procedure (steam feedrate, time, etc). However, with some vacuum residues we suffer tese re-foaming events, while other don’t foamover.

    My questions are:
    – What are the best practices to avoid re-foam during steam stripping?
    – What are the main variables that cause re-foam?
    – Is the re-foaming dependent of the VCM of the coke? (this unit has a very short cycle and have a higher VCM in coke)
    – Is the re-foaming dependent of the coke morphology?

    Thank you very much for your help

    Best regards

  • #28668

    Mike Kimbrell

    Refoaming is a coke drum is usually due to excessive amounts of unconverted oil left in the coke drum at the end of the coking phase. Operating the coke drum at a higher drum outlet temperature should help reduce or eliminate the refoaming events. A target drum outlet temperature of 825 F (440 C) is high enough to convert enough of the feed that refoaming will not be a problem.

    The small steam step is used to push the last of the feed into the coke drum up through the coke bed and into the bubbling liquid layer on the top of the bed. This steam also transfers heat from the coke below into the still reacting liquid to complete the coking reactions.

    Superficial vapor velocity is one of the key variables in foam generation, so increasing the height of the foam front when the coke drum is depressurized to the blowdown system is expected. Depressurizing the coke drum slowly, over 10 minutes or so, should limit the increase in foam front depth due to the drum pressure decreasing.

    A high VCM content on the coke is an indication of the coke drum being too cold during the coking phase. Targeting a coke VCM of between 9% and 11% by increasing heater outlet temperatures and steaming the coke bed to blowdown at the big steam rate for a reasonable time should help prevent the refoaming events.

    I think that coke morphology has very little to do with refoaming. Some resids, those produced from paraffinic feeds, need to have more severe conditions to finish the coking reactions completely.

You must be logged in to reply to this topic.

Refining Community