Coal liquefaction process

Claim 2

A process for liquefying coal, which comprises: (a) forming a coal-solvent slurry by mixing subdivided coal with a solvent; (b) substantially dissolving said coal in said solvent by heating said slurry to a temperature between 750° and 900° F. thereby forming a mixture comprising solvent, dissolved coal, and insoluble solids; (c) contacting said mixture in a reaction zone with hydrogen and an externally supplied hydrocracking catalyst under hydrocracking conditions including a temperature below 800° F., and lower than the temperature to which said slurry is heated in Step (b); and (d) withdrawing from said reaction zone an effluent stream, the normally liquid portion of which has an API gravity greater than -3.

Claim 3

The process of claim 1 wherein said coal is dissolved in the presence of added hydrogen at a pressure above 500 psig.

Claim 4

The process of claim 2 wherein the normally liquid portion of said effluent stream has an API gravity greater than 0, a sulfur content less than 0.1 weight percent, and a nitrogen content less than 0.5 weight percent.

Claim 5

The process of claim 2 wherein the normally liquid portion of said effluent stream has an API gravity greater than 5, a sulfur content less than 0.02 weight percent, and a nitrogen content less than 0.2 weight percent.

Claim 6

The process of claim 2 wherein said slurry is heated to a temperature between 800° and 850° F. in Step (b), and said hydrocracking is conducted at a temperature in the range 650° to 750° F., and a pressure in the range 1000 to 3000 psig.

Claim 7

The process of claim 2 wherein the weight ratio of solvent to coal in said slurry is in the range 5:1 to 0.5:1 and said solvent comprises a portion of said hydrocracked effluent boiling above 300° F.

Claim 8

The process of claim 2 comprising the additional steps of: (d) separating a normally gaseous fraction from said hydrocracked effluent stream; (e) separating insoluble solids from said hydrocracked effluent stream and recovering a solids-free normally liquid product stream having an API gravity greater than 5, a sulfur content less than 0.02 weight percent, and a nitrogen content less than 0.2 weight percent.

Claim 9

The process of claim 7 wherein at least the major portion of said insoluble solids is separated by gravity settling.

Claim 10

The process of claim 8 wherein said gravity settling is accomplished at a temperature of 200° to 500° F. and a pressure from 0 to 3000 psig.

Claim 11

The process of claim 2 wherein said hydrocracking zone contains a fixed bed of said catalyst.

Claim 12

The process of claim 2 wherein said hydrocracking catalyst comprises a Group VIII metal and an acidic cracking support.

Claim 13

A process for producing a substantially solids-free, low-sulfur and low-nitrogen content, normally liquid fuel from coal, which comprises: (a) forming a coal-solvent slurry by mixing subdivided coal with a solvent; (b) substantially dissolving said coal in said solvent by heating said slurry in the presence of added hydrogen and in the absence of an externally supplied catalyst to a temperature between 800° and 850° F. and at a pressure from 1000 to 3000 psig thereby forming a mixture comprising solvent, dissolved coal, and insoluble solids; (c) contacting said mixture in a reaction zone with hydrogen and a hydrocracking catalyst under hydrocracking conditions including a temperature in the range 650° to 750° F., at a pressure from 1000 to 3000 psig; (d) withdrawing from said reaction zone an effluent stream, separating a normally gaseous fraction and insoluble solids from said effluent stream, and recovering a normally liquid fuel having an API gravity greater than 5, a sulfur content less than 0.02 weight percent and a nitrogen content less than 0.2 weight percent.

Claim 14

A process for producing a substantially solids-free, low-sulfur and low-nitrogen content, normally liquid fuel from coal, which comprises: (a) forming a coal-solvent slurry by mixing subdivided coal with a solvent; (b) substantially dissolving said coal in said solvent by heating said slurry in the presence of added hydrogen and in the absence of an externally supplied catalyst to a temperature between 800° and 850° F. and at a pressure from 1000 to 3000 psig thereby forming a mixture comprising solvent, dissolved coal, and insoluble solids; (c) contacting said mixture in a reaction zone with hydrogen and a hydrocracking catalyst under hydrocracking conditions including a temperature in the range 650° to 750° F., at a pressure from 1000 to 3000 psig; (d) withdrawing from said reaction zone an effluent stream, separating a normally gaseous fraction and insoluble solids from said effluent stream, and recovering a normally liquid fuel having an API gravity greater than 5, a sulfur content less than 0.02 weight percent and a nitrogen content less than 0.2 weight percent.

Claim 15

The process of claim 12 wherein at least the major portion of said insoluble solids is separated by gravity settling.

Claim 16

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products, which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone containing no catalyst, passing the entire effluent from said first zone to a second reaction zone, hydrogenating said effluent in said second zone in the presence of hydrogenation catalyst, the temperature in said second zone being less than the temperature in said first zone, and withdrawing gas and liquid as effluent from said second stage reaction zone.

Claim 17

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products, which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone containing no catalyst, passing the entire effluent from said first zone to a second reaction zone, hydrogenating said effluent in said second zone in the presence of hydrogenation catalyst, the temperature in said second zone being less than the temperature in said first zone, and withdrawing gas and liquid as effluent from said second stage reaction zone.

Claim 18

The process of claim 14 wherein said first stage reaction zone is maintained at a temperature and a pressure which are sufficient to convert said coal primarily to dissolved coal.

Claim 19

The process of claim 15 wherein said first stage reaction zone is maintained at a temperature of from 750° to 900° F. and at a pressure of from 500 to 10,000 psig.

Claim 20

The process of claim 14 wherein said second stage reaction zone is maintained at a temperature of from 650° to 799° F. and at a pressure of from 500 to 5,000 psig.

Claim 21

The process of claim 16 wherein said second stage reaction zone is maintained at a temperature of from 650° to 799° F. and at a pressure of from 500 to 5,000 psig.

Claim 22

The process of claim 18 wherein the temperature of said second stage reaction zone is less than the temperature of said first stage reaction zone.

Claim 23

The process of claim 19 wherein the temperature of said first stage reaction zone is from about 820° to 900° F. and the temperature of said second stage reaction zone is from 650° to 799° F.

Claim 24

The process of claim 14 wherein the solids concentration in said first stage reaction zone is higher than in said second stage reaction zone.

Claim 25

The process of claim 21 wherein the concentration of unconverted coal and ash solids in said first stage reaction zone is less than about 50 weight percent, and the concentration of solids in said second stage reaction zone is less than about 50 weight percent.

Claim 26

The process of claim 14 wherein said particulate coal is mixed with at least about an equal weight of slurrying oil.

Claim 27

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products, which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone, said reaction zone containing no catalyst and being maintained at a temperature and pressure which is sufficient to convert the coal primarily to dissolved coal, passing the entire effluent from said first zone to a second reaction zone, hydrogenating, in said second zone, the entire effluent, said second zone containing a hydrogenation catalyst and being maintained at a temperature which is lower than the temperature in said first-stage reaction zone, and withdrawing gas and liquid as effluent from said second-stage reaction zone.

Claim 28

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products, which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone, said reaction zone containing no catalyst and being maintained at a temperature and pressure which is sufficient to convert the coal primarily to dissolved coal, passing the entire effluent from said first zone to a second reaction zone, hydrogenating, in said second zone, the entire effluent, said second zone containing a hydrogenation catalyst and being maintained at a temperature which is lower than the temperature in said first-stage reaction zone, and withdrawing gas and liquid as effluent from said second-stage reaction zone.

Claim 29

The process of claim 24 wherein the temperature of said first stage reaction zone is from 750° to 900° F., the temperature of said second stage reaction zone is from 650° to 799° F. and the pressure in both said first and second stage reaction zones is from about 500 to about 5000 psig.

Claim 30

The process of claim 25 wherein the temperature of said first stage reaction zone is from about 820° to 900° F. and the temperature of said second stage reaction zone is from 650° to 799° F.

Claim 31

The process of claim 23 wherein the coal-oil slurry contains no more than five parts of slurrying oil per part of coal.

Claim 32

The process of claim 24 further comprising the step of separating a slurrying oil from said effluent, said slurrying oil being recycled and mixed with particulate coal before said coal is contacted with hydrogen in said first zone.

Claim 33

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone containing no catalyst, the concentration of unconverted coal and ash solids in said first reaction zone being maintained at less than about 50 weight percent, passing the entire effluent from said first zone to a second zone, hydrogenating said entire effluent in said second zone, said second zone containing hydrogenation catalyst and being maintained at a temperature which is lower than the temperature in said first zone and having a solids concentration of less than 50 weight percent.

Claim 34

A two-stage process for the hydrogenation of coal to produce hydrocarbon liquids and gaseous products which comprises: mixing particulate coal with a slurrying oil to form a coal-oil slurry, contacting said coal-oil slurry with hydrogen in a first stage reaction zone containing no catalyst, the concentration of unconverted coal and ash solids in said first reaction zone being maintained at less than about 50 weight percent, passing the entire effluent from said first zone to a second zone, hydrogenating said entire effluent in said second zone, said second zone containing hydrogenation catalyst and being maintained at a temperature which is lower than the temperature in said first zone and having a solids concentration of less than 50 weight percent.