Upgrading solid fuel-derived tars produced by short residence time low pressure hydropyrolysis

Claim 2

A process of producing and upgrading carbonaceous tars, comprising, in serial combination, a. adding liquid or crushed solid carbonaceous material into a first reaction zone of a reactor having at least two non-catalytic reaction zones, and a pressure of between atmospheric pressure and 450 psia; b. adding hot hydrogen to the stream of carbonaceous material to effect a reaction with same to produce reaction products, the reaction temperature in the reaction zone varying from about 400° to about 2000° C; c. quenching the mixture of step (b) while insuring that the total residence time, including heat-up, reaction and quench time, varies from about 2 milliseconds to about 2 seconds; d. removing at least a portion of the reaction products from said quenched mixture of step (c), leaving a residual carbonaceous material; e. introducing the residual carbonaceous material into a subsequent reaction zone and repeating steps (a)-(d) for said subsequent reaction zone; and f. introducing carbonaceous tars produced in step (d) directly into a fluid coking zone to obtain gas, upgraded tars, and hot coke.

Claim 3

The process of claim 1, wherein the crushed solid material has an average particle size smaller than about 1/2 inch.

Claim 4

The process of claim 2, wherein the ratio of carbonaceous material to hydrogen, in the carbonaceous material-hydrogen mixture in each of said reaction zones varies from about 0.005 to about 4.

Claim 5

The process of claim 3 wherein the heat-up time of said carbonaceous material is between about 500° C/sec and 1° C/sec.

Claim 6

The process of claim 4, wherein the temperature of the quenched mixture in each reaction zone does not exceed about 1200° C.

Claim 7

The process of claim 5, wherein the quenching material is hydrogen at a temperature below 200° C and the carbonaceous material is coal.

Claim 8

The process of claim 6 wherein said reaction zones are superimposed with respect to each other.

Claim 9

The process of claim 7 wherein said reaction products are removed from the surface of carbonaceous material.

Claim 10

The process of claim 8 wherein said reaction includes five reaction zones and said carbonaceous material is gravity fed through each of said reaction zones.

Claim 11

A process for producing and upgrading coal tars comprising the steps of: a. introducing in a continuous stream of finely divided coal into a first reaction zone of a pressure vessel having at least two non-catalytic reaction zones and a pressure between atmospheric pressure and 450 psia; b. continuously adding hot hydrogen to the first reaction zone of the pressure vessel so as to impinge the coal stream and effect a reaction with same to produce coal tar reaction products, the reaction temperature in the reaction zone varying from about 400° to about 2000° C; c. limiting contact between the hydrogen and coal stream within the first reaction zone of the vessel to a period of less than 2 seconds; d. subsequently quenching the hot hydrogen-coal stream within the first reaction zone with cold hydrogen, so that the total residence time, including heat-up, reaction, and quench times, varies from about 2ms. to about 2 secs.; e. removing at least a portion of the coal tars from the quenched hydrocarbon-coal stream leaving residual coal, f. introducing the residual coal into a subsequent reaction zone and repeating the steps (a)-(e) for the subsequent reaction zone, and g. introducing said coal tars produced directly into a fluid coking zone to obtain gas, upgraded tars, and hot coke.

Claim 12

A process for producing and upgrading coal tars comprising the steps of: a. introducing in a continuous stream of finely divided coal into a first reaction zone of a pressure vessel having at least two non-catalytic reaction zones and a pressure between atmospheric pressure and 450 psia; b. continuously adding hot hydrogen to the first reaction zone of the pressure vessel so as to impinge the coal stream and effect a reaction with same to produce coal tar reaction products, the reaction temperature in the reaction zone varying from about 400° to about 2000° C; c. limiting contact between the hydrogen and coal stream within the first reaction zone of the vessel to a period of less than 2 seconds; d. subsequently quenching the hot hydrogen-coal stream within the first reaction zone with cold hydrogen, so that the total residence time, including heat-up, reaction, and quench times, varies from about 2ms. to about 2 secs.; e. removing at least a portion of the coal tars from the quenched hydrocarbon-coal stream leaving residual coal, f. introducing the residual coal into a subsequent reaction zone and repeating the steps (a)-(e) for the subsequent reaction zone, and g. introducing said coal tars produced directly into a fluid coking zone to obtain gas, upgraded tars, and hot coke.

Claim 13

The method of claim 10, wherein: a. the coal has an average particle size of less than about 1/2 inch; b. the hydrogen/coal weight ratio of the reaction mixture in each reaction zone varies from about 0.005 to about 4; c. The reaction temperature varies from about 500° C. to about 1500° C.; d. the total residence time of hydrogen and coal in each reaction zone is not more than about 1 second; e. the cold hydrogen quenched stream has a temperature of below about 1200° C; and f. the separated liquid hydrocarbon stream is further processed.

Claim 14

The method of claim 10, wherein said coal tars having compound which include between about 10 and 80 carbon atoms.