Oxidation process
A process for the removal of residual sulfur compounds from rich liquid caustic is disclosed where a single column containing two reaction zones catalytically oxidizes mercaptans to disulfide oils. The second reaction zone utilizes a bundle of vertical hanging fibers and is maintained as a gas continuous phase comprising from about 20% to about 100% by volume vapor. This process is especially useful as part of a hydrocarbon desulfurization process flow scheme.
1. A method of oxidizing mercaptans to disulfide oil comprising:
providing a liquid stream containing mercaptans and a catalyst to a top portion of a column containing a bundle of vertical hanging fibers;
mixing an oxygen containing gas in a first reaction zone with the liquid stream to form an admixture prior to contacting the admixture in an upper section of the top portion with the vertical hanging fibers;
directing the admixture to flow down the fibers and to enter a gas continuous phase reaction zone comprising from about 20% to about 100% by volume vapor;
oxidizing the mercaptans to disulfide oil as the admixture flows down the fibers in the reaction zone;
removing an off gas stream from the upper section; and
collecting, separating and removing the disulfide oil from the column.
2. The method of claim 1 wherein the gas liquid mix flowing into the first reaction zone contacts supported packing material.
3. The method of claim 1 where the catalyst is formed by mixing water, alkali metal hydroxide, and a chelated polyvalent metal catalyst.
4. The method of claim 3 wherein the chelated polyvalent metal catalyst is selected from the group consisting of cobalt phthalocyanine, iron phthalocyanine, vanadium phthalocyanine, and mixtures thereof.
5. The method of claim 1 wherein the oxygen containing gas is injected to achieve an oxygen concentration that is approximately equal to or exceeds the stoichiometric requirement for full oxidation of mercaptans into disulfide oil.
6. The method of claim 1 wherein an interior portion of the upper section of the column above the top tray is maintained as a nonexplosive environment.
7. The method of claim 6 where fuel gas or inert gas is introduced into the interior portion of the upper section.
8. The method of claim 1 where an off gas stream is removed from a second reaction zone located within the shroud.