Claims Analysis
Total Claims: 35
Claim 1
Independent Claim
301 words
A process for producing fluid hydrocarbon fuel from coal, comprising the steps of a. forming a slurry of finely divided, moisture-free coal and a hydrogen-donor solvent; b. heating said slurry to an elevated temperature up to about 850° F.; c. charging the heated slurry into a drum wherein said coal is further contacted with said hydrogen-donor solvent to raise the temperature of the mass in the drum to between about 650° F. and 800° F.; d. maintaining the pressure within said drum at an elevated pressure no greater than about 150 psig while extracting hydrocarbons from said coal; e. during said extracting, adding hydrocarbon vapor at an elevated temperature up to about 900° F. thereby to agitate said mass within said drum and to further heat it; f. depressurizing said drum to flash off the hydrocarbons while providing the latent heat of vaporization required for the volatilization of said hydrocarbons; g. withdrawing fluid hydrocarbon products from said drum; h. fractionating said fluid hydrocarbons withdrawn from said drum to form at least three cuts comprising a light cut hydrocarbon product, a medium cut hydrocarbon product having a boiling range of 450° F. to 750° F. and a heavy cut hydrocarbon product; i. adding to said drum a hydrocarbon fraction at a temperature sufficient to heat the contents of said drum to about 850° F. to 900° F. in a quantity, for a time and at a pressure sufficient to crack at least a portion of the hydrocarbons extracted from said coal and remaining in said drum and to coke the residual solids in said drum thereby to produce additional fluid hydrocarbon products; j. removing said additional fluid hydrocarbon products from said drum and adding them to said fluid hydrocarbons of step (g); k. decoking said drum to remove the coked residue therefrom.
Claim 2
Dependent Claim
301 words
A process for producing fluid hydrocarbon fuel from coal, comprising the steps of a. forming a slurry of finely divided, moisture-free coal and a hydrogen-donor solvent; b. heating said slurry to an elevated temperature up to about 850° F.; c. charging the heated slurry into a drum wherein said coal is further contacted with said hydrogen-donor solvent to raise the temperature of the mass in the drum to between about 650° F. and 800° F.; d. maintaining the pressure within said drum at an elevated pressure no greater than about 150 psig while extracting hydrocarbons from said coal; e. during said extracting, adding hydrocarbon vapor at an elevated temperature up to about 900° F. thereby to agitate said mass within said drum and to further heat it; f. depressurizing said drum to flash off the hydrocarbons while providing the latent heat of vaporization required for the volatilization of said hydrocarbons; g. withdrawing fluid hydrocarbon products from said drum; h. fractionating said fluid hydrocarbons withdrawn from said drum to form at least three cuts comprising a light cut hydrocarbon product, a medium cut hydrocarbon product having a boiling range of 450° F. to 750° F. and a heavy cut hydrocarbon product; i. adding to said drum a hydrocarbon fraction at a temperature sufficient to heat the contents of said drum to about 850° F. to 900° F. in a quantity, for a time and at a pressure sufficient to crack at least a portion of the hydrocarbons extracted from said coal and remaining in said drum and to coke the residual solids in said drum thereby to produce additional fluid hydrocarbon products; j. removing said additional fluid hydrocarbon products from said drum and adding them to said fluid hydrocarbons of step (g); k. decoking said drum to remove the coked residue therefrom.
Claim 3
Dependent Claim
18 words
A process in accordance with claim 1 wherein said finely divided coal is sized no greater than 8-mesh.
Claim 4
Dependent Claim
21 words
A process in accordance with claim 1 wherein at least about 80% of said finely divided coal is sized minus 200-mesh.
Claim 5
Dependent Claim
24 words
A process in accordance with claim 1 wherein said finely divided coal is preheaated up to about 400° F. prior to forming said slurry.
Claim 6
Dependent Claim
20 words
A process in accordance with claim 1 wherein said hydrogen-donor solvent comprises said medium cut hydrocarbon product subjected to hydrotreating.
Claim 7
Dependent Claim
30 words
A process in accordance with claim 1 wherein the weight ratio of hydrogen-donor solvent to coal in said slurry ranges between about 1 to 1 to about 4 to 1.
Claim 8
Dependent Claim
26 words
A process in accordance with claim 6 wherein said weight ratio of solvent to coal ranges between about 1.5 to 1 to about 3 to 1.
Claim 9
Dependent Claim
29 words
A process in accordance with claim 1 wherein said step of forming said slurry comprises providing said hydrogen-donor solvent at a temperature between about 100° F. and 200° F.
Claim 10
Dependent Claim
29 words
A process in accordance with claim 1 wherein said step of forming said slurry comprises providing said hydrogen-donor solvent at a temperature between about 200° F. and 600° F.
Claim 11
Dependent Claim
45 words
A process in accordance with claim 1 wherein said step of forming said slurry comprises providing one portion of said hydrogen-donor solvent at a temperature between about 100° F. and 200° F. and another portion at a temperature between about 200° F. and 600° F.
Claim 12
Dependent Claim
36 words
A process in accordance with claim 1 wherein said step of forming said slurry is performed in an open system and the temperature of said slurry is maintained below the boiling point of said hydrogen-donor solvent.
Claim 13
Dependent Claim
37 words
A process in accordance with claim 1 wherein said step of forming said slurry is performed in a closed, pressurizable system and the temperature of said slurry is maintained below the peak viscosity point of said slurry.
Claim 14
Dependent Claim
33 words
A process in accordance with claim 1 wherein said heating of said slurry prior to charging it into said drum comprises raising its temperature to between about 700° F. and about 850° F.
Claim 15
Dependent Claim
38 words
A process in accordance with claim 1 wherein the pressure maintained within said drum during said extracting ranges between about 50 psig and about 150 psig whereby a substantial portion of said solvent remains in a liquid state.
Claim 16
Dependent Claim
39 words
A process in accordance with claim 1 wherein the pressure maintained within said drum during said extracting ranges between about 20 psig and 80 psig whereby between about 10% and 70% of said solvent is flashed off for fractionating.
Claim 17
Dependent Claim
27 words
A process in accordance with claim 1 wherein said hydrocarbon vapor used for agitation during said extracting ranges in temperature between about 750° F. and 900° F.
Claim 18
Dependent Claim
23 words
A process in accordance with claim 1 wherein said hydrocarbon vapor used for agitation during said extracting comprises said medium cut hydrocarbon product.
Claim 19
Dependent Claim
38 words
A process in accordance with claim 1 including the step of gradually reducing the pressure within said drum during said extracting to boil off a portion of said solvent and to further agitate said mass within said drum.
Claim 20
Dependent Claim
27 words
A process in accordance with claim 1 wherein the temperature of said mass within said drum during said extracting ranges between about 750° F. and 800° F.
Claim 21
Dependent Claim
26 words
A process in accordance with claim 1 wherein said depressurizing step comprises reducing the pressure in said drum to between about 50 psig and 0 psig.
Claim 22
Dependent Claim
36 words
A process in accordance with claim 1 wherein said step of providing said latent heat of vaporization during depressurizing comprises introducing solvent vapors at a temperature between about 750° F. and 950° F. into said drum.
Claim 23
Dependent Claim
35 words
A process in accordance with claim 21 wherein said solvent vapors used to provide said latent heat of vaporization comprise said medium cut hydrocarbon product at a temperature between about 750° F. and 950° F.
Claim 24
Dependent Claim
40 words
A process in accordance with claim 1 wherein said hydrocarbon fraction added in step (i) to accomplish cracking and coking comprises at least in part said medium cut hydrocarbon product at a temperature between about 850° F. and 900° F.
Claim 25
Dependent Claim
49 words
A process in accordance with claim 1 including the step of further fractionating said heavy cut hydrocarbon product to form a heavy side cut having a boiling range of about 750° F. to 900° F. and a heavy bottom cut having a boiling range in excess of 900° F.
Claim 26
Dependent Claim
46 words
A process in accordance with claim 24 including the step of heating at least a portion of said heavy bottom cut to between about 850° F. and about 900° F. and adding it to said drum in step (i) as a portion of said hydrocarbon fraction.
Claim 27
Dependent Claim
30 words
A process in accordance with claim 24 including the step of coking at least a portion of said heavy bottom cut to form ash-free coke and a light hydrocarbon product.
Claim 28
Dependent Claim
25 words
A process in accordance with claim 26 including the step of using said ash-free coke and said coked residue from step (k) to form hydrogen.
Claim 29
Dependent Claim
34 words
A process in accordance with claim 1 including the step of steam reforming top gas from said drum and at least a portion of said light cut to form hydrogen for hydrotreating and hydrocracking.
Claim 30
Dependent Claim
28 words
A process in accordance with claim 1 including the step of partially oxidizing at least a portion of said heavy cut to form hydrogen for hydrotreating and hydrocracking.
Claim 31
Dependent Claim
21 words
A process in accordance with claim 1 wherein said step (j) of removing said additional fluid hydrocarbon products comprises steam stripping.
Claim 32
Dependent Claim
24 words
A process in accordance with claim 1 wherein steps (a) through (h) are repeated at least once prior to performing steps (i) through (k).
Claim 33
Dependent Claim
18 words
A process in accordance with claim 1 wherein at least two drums operating alternately in parallel are used.
Claim 34
Dependent Claim
22 words
A process in accordance with claim 1 including the step of preheating said drum prior to said charging it with said slurry.
Claim 35
Dependent Claim
25 words
A process in accordance with claim 1 including the step of pressurizing said drum with an inert gas prior to charging it with said slurry.