Subsonic-velocity entrained-bed gasification of coal

Claim 2

A process for the gasification of solid carbonaceous fuel comprising: (a) combusting carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and hot products of combustion including hot combustion gas are formed; (b) introducing steam into said combustion stage to provide an ingredient of said combustion gas; (c) introducing said combustion gas into a mixing stage through which said combustion gas flows at subsonic velocity and at a predetermined level of turbulence; (d) introducing and dispersing finely divided solid carbonaceous fuel in said combustion gas in said mixing stage to form a mixed flow of particles of dispersed solid carbonaceous fuel entrained in surrounding hot combustion gas; (e) introducing said mixed flow into a gasification stage having a duct and through which said mixed flow flows at subsonic velocity with a mean gas flow rate of 10-500 m/sec.; (f) providing one or a plurality of fluid-dynamic bulk gas accelerations and decelerations to said mixed flow whereby said particles are strongly moved with respect to said surrounding hot gas by forcing a velocity differential between said particles and said gas using the inertia of said particles and accelerations of said gas, said mixed flow having accelerations and decelerations and said hot gas having an initial temperature sufficient that said particles are subjected to an average heating rate of at least about 10 5 degrees Kelvin per second, said particles are at least partially gasified and reduced to char and a product gas is formed; (g) withdrawing from said gasification stage a product stream comprising said char and product gas; (h) separating said char from said product stream; and (i) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.

Claim 3

A process for the gasification of carbonaceous fuel according to claim 1 wherein said combustion gas, introduced into said gasification stage, has a temperature of 1900° to 2800° Kelvin, a pressure of 1 to 100 atmospheres and a velocity of 10 to 500 meters per second, and the Reynolds number of the flow of said hot combustion gas around said particles is in the range of 1 to 1000.

Claim 4

A process for the gasification of carbonaceous fuel according to claim 1 wherein said fluid-dynamic accelerations to said mixed flow are provided by a sequence of variations of contour of said duct of said gasification stage.

Claim 5

A process for the gasification of carbonaceous fuel according to claim 3 wherein said sequence of variations of contour is a sequence of variations of area, whereby said duct comprises a sequence of subsonic convergent nozzles and subsonic diffusers.

Claim 6

A process for the gasification of carbonaceous fuel according to claim 3 wherein said sequence of variations of contour is a sequence of variations of direction, whereby said duct comprises a sequence of bent duct segments.

Claim 7

A process for the gasification of carbonaceous fuel according to claim 2 wherein said product stream drops in temperature at rate sufficient to substantially prevent attaining equilibrium among the gas stream components.

Claim 8

A process for the gasification of solid carbonaceous fuel comprising: (a) combusting finely divided carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a mixing stage through which said combustion gas and steam pass at subsonic velocity and a predetermined high level of turbulence; (d) introducing and dispersing finely divided solid fuel in said turbulent combustion gas in said mixing stage; (e) introducing said turbulent combustion gas and steam containing said dispersed solid fuel to a gasification stage through which said combustion gas and steam containing said dispersed fuel flow at subsonic velocity and wherein said particles of dispersed fuel are strongly moved with respect to said combustion gas and steam by forcing a velocity differential between said particles and said gas using the inertia of said particles and bulk gas acceleration and deceleration, said combustion gas and steam upon introduction into said gasification stage having a temperature of 1900°-2800° Kelvin, a pressure of 1-100 atmospheres and a velocity of 20-500 meters per second and the Reynolds number of gas flow around the particles of said fuel is 1-1000 to provide with said bulk gas acceleration and deceleration an average heating rate of at least about 10 5 degrees Kelvin per second whereby said fuel is at least partially gasified and reduced to char and a product gas is formed; (f) withdrawing from said gasification stage a product stream comprising said char and product gas; (g) separating said char from said product stream; and (h) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.

Claim 9

A process for the gasification of solid carbonaceous fuel comprising: (a) combusting finely divided carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a mixing stage through which said combustion gas and steam pass at subsonic velocity and a predetermined high level of turbulence; (d) introducing and dispersing finely divided solid fuel in said turbulent combustion gas in said mixing stage; (e) introducing said turbulent combustion gas and steam containing said dispersed solid fuel to a gasification stage through which said combustion gas and steam containing said dispersed fuel flow at subsonic velocity and wherein said particles of dispersed fuel are strongly moved with respect to said combustion gas and steam by forcing a velocity differential between said particles and said gas using the inertia of said particles and bulk gas acceleration and deceleration, said combustion gas and steam upon introduction into said gasification stage having a temperature of 1900°-2800° Kelvin, a pressure of 1-100 atmospheres and a velocity of 20-500 meters per second and the Reynolds number of gas flow around the particles of said fuel is 1-1000 to provide with said bulk gas acceleration and deceleration an average heating rate of at least about 10 5 degrees Kelvin per second whereby said fuel is at least partially gasified and reduced to char and a product gas is formed; (f) withdrawing from said gasification stage a product stream comprising said char and product gas; (g) separating said char from said product stream; and (h) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.

Claim 10

A process for the gasification of solid carbonaceous fuel comprising: (a) combusting finely divided carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and hot products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a mixing stage through which said combustion gas and steam pass at subsonic velocity and high turbulence; (d) introducing and dispersing finely divided solid fuel as particles in said turbulent combustion gas and steam in said mixing stage; (e) introducing said turbulent combustion gas and steam containing said particles of dispersed solid fuel to a gasification stage through which said combustion gas and steam containing said dispersed solid fuel flow at subsonic velocity with a mean gas flow rate of 10-500 m/sec. and wherein said particles of dispersed fuel are strongly moved with respect to said combustion gas and steam by forcing a velocity differential between said particles and said gas using the inertia of said particles and bulk gas acceleration and deceleration; (f) providing a sequence of subsonic gaseous accelerations and decelerations in said gasification stage augmenting the turbulence of said combustion gas and steam entering said gasification stage, said combustion gas and steam having an initial temperature, initial turbulence and augmented turbulence to provide an average heating rate of at least about 10 5 degrees Kelvin per second whereby said fuel is at least partially gasified and reduced to char and a product gas is formed; (g) withdrawing from said gasification stage a product stream comprising said char and product gas; (h) separating said char from said product stream; and (i) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.

Claim 11

A process for the gasification of solid carbonaceous fuel comprising: (a) combusting finely divided carbonaceous matter and an oxidizer in a combustion stage whereby said carbonaceous matter and oxidizer are reacted and hot products of combustion including combustion gas are formed; (b) introducing steam into said combustion stage; (c) introducing said combustion gas and steam under pressure to a mixing stage through which said combustion gas and steam pass at subsonic velocity and high turbulence; (d) introducing and dispersing finely divided solid fuel as particles in said turbulent combustion gas and steam in said mixing stage; (e) introducing said turbulent combustion gas and steam containing said particles of dispersed solid fuel to a gasification stage through which said combustion gas and steam containing said dispersed solid fuel flow at subsonic velocity with a mean gas flow rate of 10-500 m/sec. and wherein said particles of dispersed fuel are strongly moved with respect to said combustion gas and steam by forcing a velocity differential between said particles and said gas using the inertia of said particles and bulk gas acceleration and deceleration; (f) providing a sequence of subsonic gaseous accelerations and decelerations in said gasification stage augmenting the turbulence of said combustion gas and steam entering said gasification stage, said combustion gas and steam having an initial temperature, initial turbulence and augmented turbulence to provide an average heating rate of at least about 10 5 degrees Kelvin per second whereby said fuel is at least partially gasified and reduced to char and a product gas is formed; (g) withdrawing from said gasification stage a product stream comprising said char and product gas; (h) separating said char from said product stream; and (i) returning at least part of said separated char to said combustion stage to provide carbonaceous matter for combustion.

Claim 12

The process as set forth in claim 8 wherein said product stream drops in temperature at a rate sufficient to substantially prevent attaining equilibrium among the gas stream constituents.

Claim 13

The process as set forth in claim 8 wherein the cross sectional area of said gasification stage is varied to define a sequence of subsonic nozzles and subsonic diffusers.

Claim 14

The process as set forth in claim 8 wherein gaseous products flowing through said gasification stage generally follow a longer course than said fuel as it flows through said gasification stage.

Claim 15

The process as set forth in claim 11 wherein the said variations in the walls of the gasification stage are caused to define a sequence of curved duct segments.