Integrated process for the production of hydrocarbons from coal or the like in which fines from gasifier are coked with heavy hydrocarbon oil

Claim 2

In a process wherein carbonaceous solids are gasified in a fluidized bed gasifier to produce a raw product gas and solid fines are carried overhead from said fluidized bed gasifier with said gas and separated from the gas, the improvement which comprises blending the separated fines with from about 0.1 to about 5 parts by weight per part of said fines of a heavy hydrocarbon oil boiling above about 1000° F., coking the resulting blend at atmospheric pressure and recovering coke particles having an average particle size substantially greater than that of said fines.

Claim 3

A process as defined by claim 1 wherein said heavy oil is a bottoms product derived by the liquefaction of coal.

Claim 4

A process as defined by the claim 1 including the further step of feeding said coke particles to said gasifier for the production of additional gaseous products.

Claim 5

A process as defined by claim 1 wherein said carbonaceous solids comprise coal.

Claim 6

A process as defined by claim 1 wherein said fines are coked in the presence of from about 0.5 to about 2 parts of said oil per part of said fines.

Claim 7

In an integrated process for the production of hydrocarbons from coal wherein feed coal particles are reacted with hydrogen in the presence of a hydrocarbon solvent to produce coal liquids and a heavy bottoms fraction boiling in excess of about 1000° F. is separated from said coal liquids and wherein said hydrogen is generated at least in part by the gasification of carbonaceous solids in a fluidized bed gasifier to produce a hydrogen-containing gas and entrained carbonaceous solid fines are separated from said gas downstream of said gasifier, the improvement which comprises introducing said heavy bottoms fraction and said carbonaceous solid fines into a coking zone in a ratio of from about 0.1 to about 5.0 parts by weight of said bottoms fraction per part of said fines and coking said bottoms fraction and said fines to produce gaseous products, liquids and coke particles having an average particle size greater than the average particle size of said carbonaceous solid fines.

Claim 8

In an integrated process for the production of hydrocarbons from coal wherein feed coal particles are reacted with hydrogen in the presence of a hydrocarbon solvent to produce coal liquids and a heavy bottoms fraction boiling in excess of about 1000° F. is separated from said coal liquids and wherein said hydrogen is generated at least in part by the gasification of carbonaceous solids in a fluidized bed gasifier to produce a hydrogen-containing gas and entrained carbonaceous solid fines are separated from said gas downstream of said gasifier, the improvement which comprises introducing said heavy bottoms fraction and said carbonaceous solid fines into a coking zone in a ratio of from about 0.1 to about 5.0 parts by weight of said bottoms fraction per part of said fines and coking said bottoms fraction and said fines to produce gaseous products, liquids and coke particles having an average particle size greater than the average particle size of said carbonaceous solid fines.

Claim 9

A process as defined by claim 6 wherein said carbonaceous solids comprise coal particles.

Claim 10

A process as defined by claim 6 wherein said coke particles are withdrawn from said coking zone and fed to said fluidized bed gasifier.

Claim 11

A process as defined by claim 6 wherein said carbonaceous solid fines have an average particle size less than about 200 mesh on the U.S. Sieve Series scale.

Claim 12

A process as defined by claim 6 wherein said carbonaceous solid fines and said bottoms fraction are mixed and therafter introduced into said coking zone.

Claim 13

A process as defined by claim 8 wherein said coke particles are treated with a solution of an alkali metal compound before said particles are fed to said gasifier.

Claim 14

A process as defined by claim 10 wherein said fines and said bottoms fraction are mixed in a ratio of from about 0.5 to about 2.0 parts by weight of said bottoms fraction per part of said fines.