METHOD FOR ADSORPTION PURIFICATION OF ASSOCIATED OIL GASES FROM MERCAPTANS

Аннотация

The paper examines methods of utilization of zeolite regeneration gases to assess the possibility of
using them in an industrial adsorption unit for drying and purifying gases from hydrogen sulfide and mercaptans. The
most promising is the method of decomposition of mercaptans to hydrogen sulfide and hydrogen on solid catalysts,
which is carried out at a pressure and temperature of 200-350 °C, as well as the method of direct gas-phase catalytic
oxidation of mercaptans with atmospheric oxygen. We carried out experiments on the purification of zeolite
regeneration gases of the Orenburg GPP by oxidation with atmospheric oxygen using an iron oxide catalyst at a
temperature of 180-250 °C. They showed that the gas purified from mercaptans contained elemental sulfur and
disulfides as the main oxidation products, and 0.2% vol. of sulfur dioxide was present as a by-product. The method
of purification from mercaptans and heavy hydrocarbon gases regeneration of composite adsorbent by
thermocatalytic oxidation is also proposed. To reduce the yield of undesirable sulfur dioxide in the regeneration gas
purified from mercaptans, it is proposed to divide the regeneration gas stream into two streams, while the larger part,
comprising about 80-90% vol., is sent to oxidation on a zinc-iron catalyst at 200 °C, the second stream is mixed with
oxidation products in a volume ratio in terms of mercaptans and sulfur dioxide equal to 1.5-2.2÷1, respectively, then
the resulting mixture is passed at 160-200 °C through a titanium oxide catalyst with a gas volumetric velocity of
4000-6000 h-1. The proposed scheme for gas purification from mercaptans and heavy hydrocarbons on a composite
adsorbent with oxidative regeneration makes it possible to carry out the subsequent process of amine purification of
gas from hydrogen sulfide without the complications associated with foaming of the working solution. Furthermore,
it becomes possible to transport gas purified from mercaptans and hydrogen sulfide through the pipeline without
precipitation of condensate.