ThioSolv SWAATS Process (patented)

Effect on Current Operation

The following illustrations show how ThioSolv's SWAATS process can be added to an existing sulfur recovery system to expand capacity and improve operation.

Examples show typical flow rates of sulfur in [tpd] in the streams of an existing operation recovering 100 tpd of sulfur by Claus plus amine-based tail gas treating.

The example assumes 10% of total sulfur produced reaches the SRU via the sour water stripper gas.  Actual may range from slightly less than 10 to over 40%.

Factors are typicals.  Rates in actual units depend on presence of hydrocarbons, CO2, and inerts.

Factors affecting the fraction of total S that is in the SWSG are:

  • N in crude

  • Depth of HDS

  • LCO included in treated diesel

  • Extent of cat feed hydrotreating

  • Residual HDS



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