Coal liquefaction with subsequent bottoms pyrolysis

Claim 2

In a process for the production of liquid hydrocarbons from coal or similar liquefiable carbonaceous solids wherein said solids are reacted with hydrogen under liquefaction conditions in a first liquefaction zone, a high boiling liquefaction bottoms stream composed primarily of constituents nominally boiling in excess of about 1000° F. is separated from the first liquefaction zone effluent, at least part of said liquefaction bottoms stream is pyrolyzed in a pyrolysis zone, and gases, liquids nominally boiling below about 1000° F., a high boiling pyrolysis bottoms stream boiling in excess of about 1000° F., and coke are recovered from the pyrolysis zone, the improvement which comprises reacting at least a portion of said pyrolysis zone, the improvement which comprises reacting at least a portion of said pyrolysis bottoms stream with hydrogen in the presence of a solvent under liquefaction conditions in a second liquefaction zone external of said first liquefaction zone.

Claim 3

A process as defined by claim 1 wherein said pyrolysis zone is a fluid coking zone.

Claim 4

A process as defined by claim 1 wherein the effluent from said second liquefaction zone is fractionated and a high boiling fraction separated from the second liquefaction zone effluent is in part recycled to said second liquefaction zone.

Claim 5

A process as defined by claim 1 wherein said pyrolysis bottoms stream is reacted with hydrogen in said second liquefaction zone at a temperature between about 750 and about 950° F. and at a pressure between about 1000 and about 3000 psig.

Claim 6

A process as defined by claim 1 wherein the effluent from said second liquefaction zone is fractionated to produce a high boiling fraction boiling in excess of about 1000° F., a major portion of said high boiling fraction is recycled to said second liquefaction zone, and a minor portion of said high boiling fraction is recycled to said pyrolysis zone.

Claim 7

A process as defined by claim 1 wherein the effluent from said second liquefaction zone is separated into a vaporous stream and a liquids stream, said vaporous stream is treated for the removal of contaminants and in part recycled as treat gas to said second liquefaction zone and said liquids stream is fractionated and in part recycled to said second liquefaction zone.

Claim 8

A process as defined by claim 5 wherein from about 3 to about 10% of said high boiling fraction is recycled to said pyrolysis zone.

Claim 9

A coal liquefaction process which comprises reacting feed coal with molecular hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a first liquefaction zone, recovering a high boiling liquefaction bottoms stream composed primarily of constituents nominally boiling in excess of about 1000° F. from the effluent from said first liquefaction zone, pyrolyzing at least part of said liquefaction bottoms stream in a coking zone, recovering gases, liquids nominally boiling below about 1000° F., a high boiling pyrolysis bottoms stream nominally boiling in excess of about 1000° F., and coke from the coking zone, reacting at least part of said pyrolysis bottoms stream with molecular hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a second liquefaction zone, fractionating the effluent from said second liquefaction zone to produce distillable liquid products and a heavier fraction, and recycling at least part of said heavier fraction to said second liquefaction zone.

Claim 10

A coal liquefaction process which comprises reacting feed coal with molecular hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a first liquefaction zone, recovering a high boiling liquefaction bottoms stream composed primarily of constituents nominally boiling in excess of about 1000° F. from the effluent from said first liquefaction zone, pyrolyzing at least part of said liquefaction bottoms stream in a coking zone, recovering gases, liquids nominally boiling below about 1000° F., a high boiling pyrolysis bottoms stream nominally boiling in excess of about 1000° F., and coke from the coking zone, reacting at least part of said pyrolysis bottoms stream with molecular hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a second liquefaction zone, fractionating the effluent from said second liquefaction zone to produce distillable liquid products and a heavier fraction, and recycling at least part of said heavier fraction to said second liquefaction zone.

Claim 11

A process as defined by claim 8 wherein a part of said heavier fraction is recycled to said coking zone.

Claim 12

A process as defined by claim 8 wherein said coking zone is a fluid coking zone and coke produced in said coking zone is gasified to produce a hydrogen-rich gas.

Claim 13

In a process for the production of liquid hydrocarbons from coal or similar liquefiable carbonaceous solids wherein said solids are reacted with hydrogen under liquefaction conditions in a first liquefaction zone, a high boiling liquefaction bottoms stream is separated from the first liquefaction zone effluent, at least part of said liquefaction bottoms stream is pyrolyzed in a pyrolysis zone, and a high boiling pyrolysis bottoms stream is recovered from the pyrolysis products, the improvement which comprises reacting at least a portion of said pyrolysis bottoms stream with hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a second liquefaction zone external of said first liquefaction zone.

Claim 14

In a process for the production of liquid hydrocarbons from coal or similar liquefiable carbonaceous solids wherein said solids are reacted with hydrogen under liquefaction conditions in a first liquefaction zone, a high boiling liquefaction bottoms stream is separated from the first liquefaction zone effluent, at least part of said liquefaction bottoms stream is pyrolyzed in a pyrolysis zone, and a high boiling pyrolysis bottoms stream is recovered from the pyrolysis products, the improvement which comprises reacting at least a portion of said pyrolysis bottoms stream with hydrogen in the presence of a hydrogen-donor solvent at elevated temperature and pressure in a second liquefaction zone external of said first liquefaction zone.