Distillation system
AssigneeCatalytic Distillation Technologies
InventorsLawrence A. Smith, Jr., Gary R. Gildert, James R. Fair, A. Frank Seibert
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Abstract
Improved HETP is obtained in the operation of a distillation column containing trays with a packing of a porous container containing a particulate material intimately associated with a resilient component having at least 50 volume % open space, preferably at least 70 volume % positioned on the trays compared to the trays without the packing. The packing may contain a catalytic particulate material and the distillation may involve reaction and distillation of the reaction products. The particulate material may also be inert and the distillation of the conventional type to separate components in the distillation mixture without reaction.
Claims6
In the process of operating a distillation column containing a plurality of trays and downcomers associated therewith wherein the improvement comprises positioning on said trays a packing comprising a porous container containing a particulate material intimately associated with a spacing component, said spacing component being comprised of at least 70 volume % up to about 95 volume % open space, said packing being present in said distillation column in an amount to provide height equivalent to theoretical plates (HETP) of less than the HETP of said trays in the absence of said packing and an equivalent clear liquid level in a downcomer associated with a tray must balance the vapor flow pressure drop as follows:
- hdc−hda=hd+2hL
- where hdc=head of froth in the downcomer, equivalent clear liquid,
- hda=pressure loss for liquid flow under a downcomer baffle,
- hd=pressure loss for flow through one tray, and
- hL=pressure loss for the two-phase flow through said packing.
Dependencies are inferred from the claim text.