Hydrogenation of coal

Claim 2

A process for the hydrogenation of coal which comprises mixing the coal with an organic solvent having one or more utilizable solvent components, hydrogen, and a catalyst which is a salt or oxide of a non-noble metal, maintaining the resulting mixture at a temperature above the critical temperature of the solvent and below 550° C whereby the solvent is in the aqueous phase and the sum of the reduced partial pressures of the solvent components is at least one, said catalyst being liquid or solid at said temperature, separating the gaseous phase and residue, and condensing hydrogenated products contained in the resulting separated gaseous phase therefrom.

Claim 3

A process as claimed in claim 1, characterized in that the utilizable solvent components are selected from water, hydrocarbons and organic derivatives of hydrocarbons.

Claim 4

A process as claimed in claim 1, characterized in that the coal is in particulate form and at least 90% of the coal particles pass a 1.5 mm mesh screen.

Claim 5

A process as claimed in claim 1, characterized in that the partial pressure of the hydrogen is in the range of 30 to 300 atmospheres.

Claim 6

A process as claimed in claim 1, characterized in that the proportion of utilizable solvent components to coal is 2 to 30 times the weight of coal present.

Claim 7

A process as claimed in claim 1, characterized in that the catalyst is an oxide of a transition metal other than platinum metals selected from Groups VI, VII and VIII of the Periodic Table according to Mendeleef.

Claim 8

A process for hydrogenating coal which comprises mixing coal with a solvent having one or more utilizable solvent components to form a slurry, mixing the slurry with hydrogen under pressure, heating the mixture of slurry and hydrogen under pressure to a temperature above the critical temperature of the solvent in the slurry but below 550° C and wherein the sum of the reduced partial pressures of the solvent components is at least one, contacting the slurry with a salt or oxide of a non-noble metal catalyst which is liquid or solid at the temperature of the slurry until coal is hydrogenated and dissolved in the gaseous phase, separating the gaseous phase from the resulting residue, reducing the pressure on the aqueous phase until extracted hydrogenated products contained therein condense, and separating the condensation product from the gaseous phase.

Claim 9

A process for hydrogenating coal which comprises mixing coal with a solvent having one or more utilizable solvent components to form a slurry, mixing the slurry with hydrogen under pressure, heating the mixture of slurry and hydrogen under pressure to a temperature above the critical temperature of the solvent in the slurry but below 550° C and wherein the sum of the reduced partial pressures of the solvent components is at least one, contacting the slurry with a salt or oxide of a non-noble metal catalyst which is liquid or solid at the temperature of the slurry until coal is hydrogenated and dissolved in the gaseous phase, separating the gaseous phase from the resulting residue, reducing the pressure on the aqueous phase until extracted hydrogenated products contained therein condense, and separating the condensation product from the gaseous phase.

Claim 10

A process for the hydrogenation of coal by extracting the coal with the solvent in the presence of hydrogen, said process characterized in that the solvent is in the gaseous phase and comprises one or more utilizable solvent components which at the extraction temperature, are above their critical temperatures and have a sum of the reduced partial pressures of at least one and in that the solvent extraction is carried out at a temperature below 550° C. in the presence of hydrogen and in the presence of an effective amount of a catalyst which is a salt of one or more of tin, zinc, arsenic, antimony, bismuth, titanium, gallium and mercury and which is liquid or solid at the extraction temperature, the gas phase solvent is separated from the solid residue, and the hydrogenated products are condensed from the solvent in the aqueous or vapor phase.

Claim 11

A process for the hydrogenation of coal by extracting the coal with the solvent in the presence of hydrogen, said process characterized in that the solvent is in the gaseous phase and comprises one or more utilizable solvent components which at the extraction temperature, are above their critical temperatures and have a sum of the reduced partial pressures of at least one and in that the solvent extraction is carried out at a temperature below 550° C. in the presence of hydrogen and in the presence of an effective amount of a catalyst which is a salt of one or more of tin, zinc, arsenic, antimony, bismuth, titanium, gallium and mercury and which is liquid or solid at the extraction temperature, the gas phase solvent is separated from the solid residue, and the hydrogenated products are condensed from the solvent in the aqueous or vapor phase.