| CPC C10G 53/06 (2013.01) [C25C 3/02 (2013.01); C25C 7/005 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/302 (2013.01); C10G 2300/308 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4012 (2013.01)] | 24 Claims |

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1. A process comprising:
pretreating a hydrocarbon feedstock comprising impurities to provide a purified feedstock and a residual feedstock, wherein
the purified feedstock comprises a lower concentration of impurities than the hydrocarbon feedstock before pretreatment, and
the residual feedstock comprises a higher concentration of impurities than the purified feedstock; and
contacting the residual feedstock with an effective amount of sodium metal and an effective amount of exogenous capping agent at a temperature of 250-500° C., to produce a mixture of sodium salts and a converted feedstock, wherein
the residual feedstock comprises hydrocarbons with a sulfur content of at least 0.5 wt % and an asphaltene content of from 2 wt % to 40 wt %;
the sulfur content comprises asphaltenic sulfur and non-asphaltenic sulfur;
the converted feedstock comprises hydrocarbon oil with a sulfur content less than that in the residual feedstock and an asphaltene content less than that in the residual feedstock; and
the proportion by weight of asphaltenic sulfur to non-asphaltenic sulfur in the converted feedstock is lower than in the residual feedstock.
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