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Whta type & design of K/O upstream recommended for Fume incinerator

Whta type & design of K/O upstream recommended for Fume incinerator

Whta type & design of K/O upstream recommended for Fume incinerator

(OP)
I am specifying a K/O pot-->deflagration arrester-->Fume incinerator.  Upstream is a 500 ft line from a dilute caustic scrubber.  Condensation in the transfer line is likely.  

What design for the K/O to request, like for a flare >300 micron, or <10?  W/ the downstream DA acting as a chevron style separator element I imagine 300 micron is too high.  Comments?

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