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In a process to treat gaseous components obtained from an in situ recovery of liquid hydrocarbons from a hydrocarbonaceous deposit the mercaptans and hydrogen sulfide are separated from each other using lean oil and the hydrogen sulfide further processed to obtain a sulfur-free fuel gas product. The

In a process to treat gaseous components obtained from an in situ recovery of liquid hydrocarbons from a hydrocarbonaceous deposit the mercaptans and hydrogen sulfide are separated from each other using lean oil and the hydrogen sulfide further processed to obtain a sulfur-free fuel gas product. The rich oil obtained after treating the gaseous components can be used as a diluent with the liquid hydrocarbons or processed to remove and convert the mercaptans to disulfide oils.

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1. A process for treating hydrocarbons obtained from a hydrocarbonaceous deposit comprising, a) providing a mixture of liquid hydrocarbons and gaseous components obtained from a hydrocarbonaceous deposit, where the gaseous components comprise hydrogen sulfide and mercaptans;b) separating the liquid

1. A process for treating hydrocarbons obtained from a hydrocarbonaceous deposit comprising, a) providing a mixture of liquid hydrocarbons and gaseous components obtained from a hydrocarbonaceous deposit, where the gaseous components comprise hydrogen sulfide and mercaptans;b) separating the liquid hydrocarbons from the gaseous components;c) contacting the gaseous components with a lean oil whereby the mercaptans are absorbed by the lean oil to form a rich oil;d) separating a gaseous product containing the hydrogen sulfide from the rich oil;e) treating the gaseous product to remove the hydrogen sulfide to produce a lean fuel gas; andf) treating the liquid hydrocarbons obtained in step b) to reduce viscosity prior to transporting to a refinery for processing. 2. The process of claim 1 where the mixture of liquid hydrocarbons and gaseous components is obtained using a SAGD process. 3. The process of claim 1 where the liquid hydrocarbons comprise bitumen. 4. The process of claim 1 where the treatment of liquid hydrocarbons in step f) comprises mixing the liquid hydrocarbons with a diluent hydrocarbon. 5. The process of claim 1 where the treatment of liquid hydrocarbons in step f) comprises mixing the liquid hydrocarbons with the rich oil from step d). 6. The process of claim 1 where the treatment of liquid hydrocarbons in step f) comprises mixing the liquid hydrocarbons with a diluent hydrocarbon and the rich oil from step d). 7. The process of claim 1 where the treatment of the gaseous product from step d) comprises contacting the gaseous product with a liquid solution in a gas-liquid contactor to convert the hydrogen sulfide to elemental sulfur. 8. The process of claim 1 where the treatment of the gaseous product from step d) comprises contacting the gaseous product with a liquid solution in a gas-liquid contactor followed by an oxidation reaction to convert the hydrogen sulfide to elemental sulfur. 9. The process of claim 1 where the rich oil from step d) is contacted with caustic to remove the mercaptans to form a regenerated lean oil, whereby the mercaptans are converted to mercaptides and are transferred into the caustic to form a spent caustic. 10. The process of claim 9 where the regenerated lean oil is contacted with the gaseous components in step c) to remove the mercaptans from the gaseous components. 11. The process of claim 9 where the regenerated lean oil is added to the liquid hydrocarbons in step f) to reduce the viscosity of the liquid hydrocarbons. 12. The process of claim 9 further comprises regenerating the spent caustic by a) mixing the spent caustic with an oxygen containing gas;b) oxidizing the spent caustic using a catalyst to form a regenerated caustic, whereby the mercaptides in the spent caustic are oxidized to disulfide oils; andc) separating the regenerated caustic from the disulfide oils and recycling the regenerated caustic for contact with the rich oil from step d) of claim 1. 13. The process of claim 1 where the contacting in step c) comprises contacting the gaseous components in a distillation column with the lean oil and distilling to form a rich oil bottoms and a mercaptan-low gas overhead comprising fuel gas and hydrogen sulfide. 14. The process of claim 1 where the contacting in step c) comprises contacting the gaseous components in a counter current liquid-gas low pressure absorption column with the lean oil. 15. The process of claim 14 further comprises fractionating to remove residual hydrogen sulfide from the rich oil. 16. A process for treating hydrocarbons obtained in situ from oil sands using a SADG process comprising, a) separating bitumen from gaseous components, where the gaseous components comprise hydrocarbons, hydrogen sulfide and mercaptans;b) mixing the bitumen with a sufficient quantity of a hydrocarbon diluent to form a dilbit;c) contacting the separated gaseous components from step a) with a lean oil in a counter current liquid-gas column whereby the mercaptans are absorbed into the lean oil forming a rich oil and where a mercaptan-low gaseous product is recovered; andd) treating the mercaptan-low gaseous product with an aqueous liquid redox catalyst solution to oxidize the hydrogen sulfide to elemental sulfur and to produce a sulfur-flee fuel gas. 17. The process of claim 16 where the rich oil is mixed with the bitumen in forming the dilbit. 18. The process of claim 16 where the rich oil is treated with caustic to remove the mercaptans to form a regenerated lean oil that is recycled and used in step c). 19. The process of claim 18 where spent caustic containing the mercaptans removed from the rich oil is mixed with an oxygen containing gas, is then oxidized using a catalyst to form a regenerated caustic, whereby the mercaptides in the spent caustic are oxidized to disulfide oils that are separated from the regenerated caustic and where the regenerated caustic is recycled for treating the rich oil.