Char separator

Claim 2

A fluidized-bed furnace system, comprising: a. a fluidized-bed furnace in which carbonaceous fuel particles are burned in the presence of inert particles, gaseous combustion products thereby being produced, which combustion products entrain particulates including inert particles and char particles; b. means for removing the particulates from the gaseous combustion products; c. conduit means connected to the furnace and the removal means to conduct the gaseous combustion products from the furnace to the removal means; d. means for receiving the particulates removed by the removal means and separating them into portions of relatively high and low densities, whereby the char particles are concentrated in the portion of relatively low density and the inert particles are concentrated in the portion of relatively high density; e. a char-burning furnace, connected to the separating means to receive the portion of relatively low density, for burning the low-density portion of the particulates; and f. conduit means connected to the separating means for removing the portion of relatively high density from the fluidized-bed furnace system.

Claim 3

An apparatus as recited in claim 1, wherein the separating means comprises: a. a perforated table having first and second ends; b. means for conducting the particulates from the removal means and depositing them on the perforated table at its first end, thereby allowing them to migrate towards the second end; c. means for causing a stream of air to flow up through the perforated table, the stream being sufficiently strong above the first end to fluidize substantially all the particulates occupying the table at the first end, the strength being gradually reduced towards the second end so that substantially all particulates above a predetermined density are no longer fluidized at the second end, the particulates thereby being stratified during migration from the first end to the second end so that denser particulates at the second end lie on the table below less dense particulates; d. a scoop positioned at the second end of the table at such a height as to remove only those particulates that are more than a predetermined height above the table at the second end; and e. means for conducting from the scoop into the char-burning furnace the particulates removed by the scoop.

Claim 4

An apparatus as recited in claim 2, wherein the table comprises an endless perforated belt and the separating means further comprises means for driving the endless belt from the first end of the table to the second end of the table.

Claim 5

An apparatus as recited in claim 3, wherein the endless belt is inclined so that the second end of the table is lower than the first end of the table, migration of the particulates thereby being facilitated.

Claim 6

An apparatus as recited in claim 4, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 7

An apparatus as recited in claim 3, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 8

An apparatus as recited in claim 2, wherein the table is inclined so that its second end is lower than its first end, migration of the particulates thereby being facilitated.

Claim 9

An apparatus as recited in claim 7, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 10

An apparatus as recited in claim 1, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 13

A method as recited in claim 10, wherein the separation step comprises the steps of: a. depositing the removed particulates on the first end of a perforated table having first and second ends and allowing them to migrate to the second end; b. blowing a stream of air up through the perforated table, the stream being strong enough above the first end to fluidize substantially all of the particulates occupying the first end, the strength being gradually reduced toward the second end so that essentially all particulates above a predetermined density are no longer fluidized at the second end, the particulates thereby being stratified during migration from the first end to the second end so that denser particles at the second end lie on the table below less dense particles; and c. scooping up the particles at the second end that are more than a predetermined height above the table, thereby separating the particulates into a low-density portion and a high-density portion.

Claim 14

A method as recited in claim 11, wherein the step of burning the low-density portion comprises the step of feeding the low-density portion into the fluidized-bed furnace in which the step of burning the fluidized mixture is taking place, the low-density portion thereby being burned with the fluidized mixture.

Claim 15

A method as recited in claim 10, wherein the step of burning the low-density portion comprises the step of feeding the low-density portion into the fluidized-bed furnace in which the step of burning the fluidized mixture is taking place, the low-density portion thereby being burned with the fluidized mixture.

Claim 16

A fluidized-bed furnace system, comprising: a. a fluidized-bed furnace including a bed region; b. means for supplying a mixture of carbonaceous fuel and inerts to the bed region; c. means connected to the furnace for withdrawing part of the contents of the bed region; d. means for receiving said part of the contents of the bed region withdrawn by the withdrawal means and separating it into portions of relatively high and low densities, whereby the char particles are concentrated in the portion of relatively low density and the inert particles are concentrated in the portion of relatively high density; e. a char-burning furnace, connected to the separating means to receive the portion of relatively low density, for burning the low-density portion; and f. conduit means connected to the separating means for removing the portion of relatively high density from the fluidized-bed furnace system.

Claim 17

A fluidized-bed furnace system, comprising: a. a fluidized-bed furnace including a bed region; b. means for supplying a mixture of carbonaceous fuel and inerts to the bed region; c. means connected to the furnace for withdrawing part of the contents of the bed region; d. means for receiving said part of the contents of the bed region withdrawn by the withdrawal means and separating it into portions of relatively high and low densities, whereby the char particles are concentrated in the portion of relatively low density and the inert particles are concentrated in the portion of relatively high density; e. a char-burning furnace, connected to the separating means to receive the portion of relatively low density, for burning the low-density portion; and f. conduit means connected to the separating means for removing the portion of relatively high density from the fluidized-bed furnace system.

Claim 18

An apparatus as recited in claim 14, wherein the separating means comprises: a. a perforated table having first and second ends; b. means for conducting particulates from the withdrawal means, depositing them on the perforated table at the first end, and allowing them to migrate toward the second end; c. means for causing a stream of air to flow up through the perforated table, the stream being sufficiently strong above the first end to fluidize substantially all the particulates occupying the table at the first end, the strength being gradually reduced toward the second end so that substantially all particulates above a predetermined density are no longer fluidized at the second end, the particulates thereby being stratified during migration from the first end to the second end so that denser particulates at the second end lie on the table below less dense particulates; d. a scoop positioned at the second end of the table at such a height as to remove only those particulates that are more than a predetermined height above the table at the second end; and e. means for feeding the particulates removed by the scoop into the char-burning furnace.

Claim 19

An apparatus as recited in claim 15, wherein the table comprises an endless perforated belt and the separating means further comprises means for driving the endless belt from the first end to the second end.

Claim 20

An apparatus as recited in claim 16, wherein the endless belt is inclined so that its second end is lower than its first end, migration of the particulates thereby being facilitated.

Claim 21

An apparatus as recited in claim 17, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 22

An apparatus as recited in claim 16, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 23

An apparatus as recited in claim 15, wherein the perforated table is inclined so that its second end is lower than its first end, migration of the particulates thereby being facilitated.

Claim 24

An apparatus as recited in claim 20, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 25

An apparatus as recited in claim 14, wherein the char-burning furnace is the fluidized-bed furnace.

Claim 28

A method as recited in claim 23, wherein the separation step comprises the steps of: a. depositing the removed part of the mixture on the first end of a perforated table having first and second ends and allowing the removed part to migrate to the second end; b. blowing a stream of air up through the perforated table, the stream being strong enough above the first end to fluidize substantially all of the particulates occupying the first end, the strength being gradually reduced toward the second end so that substantially all of the particles above a predetermined density are no longer fluidized at the second end, the particles thereby being stratified during migration from the first end to the second end so that the denser particles at the second end lie on the table below the less dense particles; and c. scooping up the particles at the second end that are more than a predetermined height above the table, thereby separating the removed part of the mixture into low-density and high-density portions.

Claim 29

A method as recited in claim 24, wherein the step of burning the low-density portion comprises feeding the low-density portion into the fluidized-bed furnace in which the combustion step is taking place, the low-density portion thereby being burned with the fluidized mixture.

Claim 30

A method as recited in claim 23, wherein the step of burning the low-density portion comprises feeding the low-density portion into the fluidized-bed furnace in which the step of burning the fluidized mixture is taking place, the low-density portion thereby being burned with the fluidized mixture.