Process for producing low-sulfur liquid and solid fuels from coal

Claim 2

An improved solvent refining process for converting coal to clean fuel products without added hydrogen which comprises: a. contacting finely divided coal with a coal liquefaction solvent in the presence of a solid sulfur scavenger selected from the group consisting of metals, metal oxides, metal salts, and mixtures thereof, said sulfur scavenger being capable of conversion to an insoluble sulfide or sulfur complex, at a temperature sufficient to effect coal dissolution and thereby produce (1) a gas phase and (2) a liquid phase comprising a mixture of coal extract, liquefaction solvent, sulfur scavenger and undissolved residue; b. effecting separation of said liquid phase mixture by clarifier settling means to produce (1) a clarified settler overflow containing coal extract and coal liquefaction solvent and (2) a solids-rich settler underflow; and c. thereafter recovering from said overflow a fuel product of reduced sulfur content.

Claim 3

The process of claim 1 wherein the solid sulfur scavenger is a member selected from the group consisting of iron and iron oxides.

Claim 4

The process of claim 2 wherein a cooled heavy cycle oil is added to the clarifier settling means and a heated light cycle oil is added to the liquid phase mixture prior to introduction thereof into said settling means, the specific gravity of the heavy cycle oil entering the settling means being at least 0.05 units greater than the specific gravity of the light cycle oil.

Claim 5

The process of claim 3 wherein the coal liquefaction solvent is a thermally stable, highly aromatic petroleum refinery fraction.

Claim 6

The method of claim 4 wherein large particles of the sulfur scavenger are added to the clarifier settling means as a nucleating agent to help aggregate and precipitate fine solids.

Claim 7

In a refining process for converting coal to clean fuel products, the improvement which comprises: a. contacting finely divided coal with a coal liquefaction solvent in the absence of added hydrogen and in the presence of a solid sulfur scavenger selected from the group consisting of metals, metal oxides, metal salts, and mixtures thereof, said sulfur scavenger being capable of conversion to an insoluble sulfide or sulfur complex at a temperature sufficient to effect coal dissolution and thereby produce (1) a gas phase and (2) a liquid phase comprising a mixture of coal extract, liquefaction solvent, sulfur scavenger and undissolved carbonaceous residue; and, b. introducing said liquid phase and a heated light cycle oil into a clarifier settling zone; c. introducing into said clarifier settling zone a cooled heavy cycle oil having a specific gravity of at least 0.05 units greater than the specific gravity of the liquid phase-heated light cycle oil mixture; d. effecting separation of said liquid phase in the clarified settling zone to produce (1) a clarified settler overhead fraction comprising coal extract and coal liquefaction solvent; and (2) a solids rich settler bottoms fraction; e. introducing said clarified overhead fraction into a distillation zone and thereafter recovering: (1) a light cycle oil overhead fraction, (2) a low-sulfur, solvent refined coal bottoms fraction, (3) a heavy cycle oil, and (4) a heavy oil low-sulfur fuel product.

Claim 8

In a refining process for converting coal to clean fuel products, the improvement which comprises: a. contacting finely divided coal with a coal liquefaction solvent in the absence of added hydrogen and in the presence of a solid sulfur scavenger selected from the group consisting of metals, metal oxides, metal salts, and mixtures thereof, said sulfur scavenger being capable of conversion to an insoluble sulfide or sulfur complex at a temperature sufficient to effect coal dissolution and thereby produce (1) a gas phase and (2) a liquid phase comprising a mixture of coal extract, liquefaction solvent, sulfur scavenger and undissolved carbonaceous residue; and, b. introducing said liquid phase and a heated light cycle oil into a clarifier settling zone; c. introducing into said clarifier settling zone a cooled heavy cycle oil having a specific gravity of at least 0.05 units greater than the specific gravity of the liquid phase-heated light cycle oil mixture; d. effecting separation of said liquid phase in the clarified settling zone to produce (1) a clarified settler overhead fraction comprising coal extract and coal liquefaction solvent; and (2) a solids rich settler bottoms fraction; e. introducing said clarified overhead fraction into a distillation zone and thereafter recovering: (1) a light cycle oil overhead fraction, (2) a low-sulfur, solvent refined coal bottoms fraction, (3) a heavy cycle oil, and (4) a heavy oil low-sulfur fuel product.

Claim 9

The method of claim 6 wherein the settling zone is circular and the diameter thereof is in relationship to the average particle size of solids present therein and the through-put of the liquid phase introduced thereto, said relationship being defined according to the graph set forth in FIG. 2.

Claim 10

The method of claim 6 wherein the sulfur scavenger is separated from the solids rich settler bottoms fraction and is regenerated in the presence of steam and an oxygen-containing gas.

Claim 11

The method of claim 6 wherein said gas phase is separated from the liquid phase and is desulfurized to provide fuel gas of low sulfur content.

Claim 12

The method of claim 6 wherein at least a portion of said low-sulfur solvent refined coal is subjected to coking to provide low-sulfur liquid fuels and a high grade, low-sulfur coke product.