Hydrogenation of solid carbonaceous materials using mixed catalysts
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example 1
[0152]Run 1—A solution of a mixed catalyst precursor iron nitrate (Fe(NO3)3.9H2O) and zinc nitrate (Zn(NO3)2.6H2O) dissolved in methanol was prepared. A sample of moisture-free coal feed (i.e. less than 1% by weight water) having a particle size of less than 100 mesh was impregnated to incipient wetness with the solution, at a solution to coal weight ratio of 1 to 1, to yield an iron to coal loading on a dry, ash-free basis of 1% iron and a zinc to coal loading on a dry, ash-free basis of 1 wt % zinc. The catalyst impregnated coal was then dried under nitrogen at 105° C. for up to 24 hr for to remove the methanol.
[0153]The dried catalyst impregnated coal was mixed with an FCC-type process oil (500° F.+cut) hydrocarbonaceous liquid, at a hydrocarbonaceous liquid to coal ratio of 1.6 to 1. Elemental sulfur was added to sulfide the iron and zinc, at a sulfur to iron molar ratio of 2 to 1 and a sulfur to zinc ratio of 2 to 1.
[0154]The mixture was then heated quickly in a vessel to 200° ...
example 2
[0160]Run 4—Run 1 was repeated. Product yields tabulated for Run 4 in Table I indicate excellent coal conversions and liquid yield for Run 4.
example 3
[0161]Run 5—Run 1 was repeated using a iron nitrate (Fe(NO3)3.9H2O) and zinc nitrate (Zn(NO3)2.6H2O) mixed catalyst precursor at an iron to coal loading on a dry, ash-free basis of 1 wt % iron, and a zinc to coal loading on a dry, ash-free basis of 1 wt % zinc. No elemental sulfur was added. Product yields tabulated for Run 5 in Table I indicate relatively poor coal conversation and liquid yield.
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