Production of H2 and co-containing gas stream and power

Claim 2

A process for the production of an H 2 and CO-containing gas stream along with power comprising: (1) producing a raw process gas stream comprising H 2 , and CO and at least one member of the group CO 2 , H 2 O, H 2 S, COS, CH 4 , N 2 , A, and entrained particulate solids in the reaction zone of a free-flow gas generator by the partial oxidation of a hydrocarbonaceous fuel with a heated stream of free-oxygen containing gas and in the presence of a temperature moderator, at a temperature in the range of about 1800 to 3000° F and a pressure in the range of about 10 to 200 atmospheres; (2) removing entrained solids if any, cooling, cleaning, and dewatering, said H 2 and CO-containing gas stream; (3) dividing at least a portion of said H 2 and CO-containing gas stream from (2) into a first gas stream which is reacted in the combustion chamber of a pressurized heater as fuel producing a stream of flue gas, and into a second gas stream which is burned as fuel in the combustor of a gas turbine comprising said combustor and an expansion turbine thereby producing a stream of exhaust gas, and passing said stream of exhaust gas through said expansion turbine as the working fluid; and (4) compressing a stream of free-oxygen containing gas in gas compression means powered by said expansion turbine, heating at least a portion of the compressed free-oxygen containing gas in said pressurized heater, and introducing the heated compressed free-oxygen containing gas into the gas generator in step (1).

Claim 3

The process of claim 1 where in step (3) at least a portion of the flue gas from said pressurized heater is introduced into said expansion turbine in admixture with the exhaust gas stream from said combustor.

Claim 4

The process of claim 1 where in step (3) at least a portion of said flue gas is introduced into said combustor.

Claim 5

The process of claim 3 where in step (3) said flue gas is introduced into said combustor in admixture with said second gas stream.

Claim 6

The process of claim 1 wherein the free-oxygen containing gas in step (4) is compressed to a pressure in the range of about 10 to 200 atmospheres and slightly above that in the gas generator.

Claim 7

The process of claim 1 with the additional steps of passing the exhaust gas leaving said turbine in step (3) in indirect heat exchange with saturated steam to produce superheated steam; and introducing said superheated steam into a turboelectric generator as the working fluid.

Claim 8

The process of claim 1 with the additional steps of passing the exhaust gas leaving said turbine in step (3) in indirect heat exchange with saturated steam to produce superheated steam; and introducing said superheated steam into a turbocompressor as the working fluid for compressing to a higher pressure the stream of free-oxygen containing gas compressed in step (4).

Claim 9

The process of claim 1 provided with the added step of producing electrical energy by means of an electric generator powered by said expansion turbine.

Claim 10

The process of claim 1 wherein all of the flue gas from said pressurized heater in step (3) and all of said exhaust gas stream from step (3) are separately introduced into said expansion turbine.

Claim 11

The process of claim 1 where said reaction takes place in said pressurized heater at a pressure in the range of about 10 to 200 atmospheres.

Claim 12

The process of claim 1 wherein said portion of H 2 and CO-containing gas stream from (2) is introduced into said pressurized heater at substantially the same pressure as that in the gas generator less ordinary pressure drop in the lines and equipment.

Claim 13

The process of claim 1 wherein substantially all of the acid-gases are removed from the raw process gas stream from (1) in an absorption zone.

Claim 14

The process of claim 1 wherein the free-oxygen containing gas is selected from the group consisting of air, oxygen-enriched air (more than 21 mole % O 2 ) and substantially pure oxygen (more than 95 mole % O 2 ).

Claim 15

The process of claim 1 wherein said hydrocarbonaceous fuel is a liquid hydrocarbon selected from the group consisting of liquefied petroleum gas, petroleum distillates and residues, gasoline, naphtha, kerosine, crude petroleum, asphalt, gas oil, residual oil, tar-sand oil, shale oil, coal derived oil, aromatic hydrocarbons such as benzene, toluene, xylene fraction, coal tar, cycle gas oil from fluid-catalytic-cracking operation, furfural extract of coker gas oil, and mixtures thereof.

Claim 16

The process of claim 1 wherein said hydrocarbonaceous fuel is a gaseous hydrocarbon.

Claim 17

The process of claim 1 wherein said hydrocarbonaceous fuel is an oxygenated hydrocarbonaceous organic material selected from the group consisting of carbohydrates, cellulosic materials, aldehydes, organic acids, alcohols, ketones, oxygenated fuel oil, waste liquids and by-products from chemical processes containing oxygenated hydrocarbonaceous organic materials, and mixtures thereof.

Claim 18

The process of claim 1 where in step (2) at least a portion of said entrained solids are separated in a slag pot and in a carbon separation zone and said solids are selected from the group consisting of particulate carbon, ash, slag, scale, refractory, metal constituents, and mixtures thereof.

Claim 19

The process of claim 1 wherein said hydrocarbonaceous fuel is a pumpable slurry of solid carbonaceous fuel selected from the group consisting of coal, lignite, particulate carbon, petroleum coke, and concentrated sewer sludge and mixtures thereof, in a vaporizable carrier such as water, liquid hydrocarbon and mixtures thereof.

Claim 20

The process of claim 1 wherein said free-oxygen containing gas in step (1) is compressed air which has been preheated in the pressurized heater in step (4) to a temperature in the range of about 400 to 1800° F.

Claim 21

The process of claim 19 provided with the step of introducing separate portions of said compressed air before being heated in said pressurized heater into the combustor of said gas turbine and into the combustion chamber of said pressurized heater.

Claim 22

The process of claim 19 provided with the steps of introducing a separate portion of said compressed air before being heated in said pressurized heater into the combustor of said gas turbine, and introducing a separate portion of said compressed air after being heated in said pressurized heater into said combustion chamber of said pressurized heater.

Claim 23

The process of claim 1 wherein said free-oxygen containing gas in step (1) is substantially pure oxygen and said oxygen is heated in the pressurized heater in step (4) to a temperature in the range of about 400 to 1800° F prior to introduction into said gas generator; and provided with the additional steps of compressing a stream of air in a separate compressor powered by said expansion turbine and introducing separate portions of said compressed air into the combustor of said gas turbine, and into the combustion chamber of said pressurized heater.

Claim 24

The process of claim 1 where in step (3) said first gas stream is reacted with air in the combustion chamber of said pressurized heater by partial oxidation.

Claim 25

A process for the production of an H 2 and CO-containing fuel gas stream along with power comprising: (1) producing a raw process gas stream comprising H 2 and CO and at least one member of the group CO 2 , H 2 O, H 2 S, COS, CH 4 , N 2 , A, and entrained particulate solids in the reaction zone of a free-flow gas generator by the partial oxidation of a hydrocarbonaceous fuel with a heated stream of air and in the presence of a temperature moderator, at a temperature in the range of about 1800 to 3000° F and a pressure in the range of about 10 to 200 atmospheres; (2) removing entrained solids if any, cooling, cleaning, dewatering and purifying the raw process gas stream from (1) to produce said H 2 and CO-containing fuel gas stream; (3) dividing at least a portion of said H 2 and CO-containing gas stream from (2) into first and second fuel gas streams; (4) reacting said first fuel gas stream with air in a pressurized heater to produce heat and a stream of flue gas, and introducing said flue gas into a power-producing gas turbine comprising a combustor and an expansion turbine; (5) burning said second fuel gas stream with air in said combustor, producing a stream of clean exhaust gas, and introducing said exhaust gas through said expansion turbine as the working fluid; and (6) compressing a stream of air in a compressor powered by a portion of the power produced by said expansion turbine, heating a first portion of the compressed air in said pressurized heater in (4) and introducing the heated compressed air into the gas generator in (1) as said air, and introducing a second portion of said compressed air into the pressurized heater in (4) as said air, and introducing a third portion of said compressed air into the combustor in (5) as said air.

Claim 26

A process for the production of an H 2 and CO-containing fuel gas stream along with power comprising: (1) producing a raw process gas stream comprising H 2 and CO and at least one member of the group CO 2 , H 2 O, H 2 S, COS, CH 4 , N 2 , A, and entrained particulate solids in the reaction zone of a free-flow gas generator by the partial oxidation of a hydrocarbonaceous fuel with a heated stream of air and in the presence of a temperature moderator, at a temperature in the range of about 1800 to 3000° F and a pressure in the range of about 10 to 200 atmospheres; (2) removing entrained solids if any, cooling, cleaning, dewatering and purifying the raw process gas stream from (1) to produce said H 2 and CO-containing fuel gas stream; (3) dividing at least a portion of said H 2 and CO-containing gas stream from (2) into first and second fuel gas streams; (4) reacting said first fuel gas stream with air in a pressurized heater to produce heat and a stream of flue gas, and introducing said flue gas into a power-producing gas turbine comprising a combustor and an expansion turbine; (5) burning said second fuel gas stream with air in said combustor, producing a stream of clean exhaust gas, and introducing said exhaust gas through said expansion turbine as the working fluid; and (6) compressing a stream of air in a compressor powered by a portion of the power produced by said expansion turbine, heating a first portion of the compressed air in said pressurized heater in (4) and introducing the heated compressed air into the gas generator in (1) as said air, and introducing a second portion of said compressed air into the pressurized heater in (4) as said air, and introducing a third portion of said compressed air into the combustor in (5) as said air.

Claim 27

The process of claim 24 wherein at least a portion of the flue gas in step (4) is introduced into said expansion turbine in step (5) along with said clean exhaust gas from the combustor.

Claim 28

The process of claim 24 wherein at least a portion of the flue gas in step (4) is introduced into the combustor in step (5) along with said second fuel gas stream.

Claim 29

The process of claim 24 wherein the cooling in step (2) is effected by indirect heat exchange between the process gas stream from (1) and water thereby producing saturated steam, and provided with the additional steps of superheating said saturated steam by indirect heat exchange with clean exhaust gas from the turbine in step (5), introducing at least a portion of said superheated steam into a turbocompressor as the working fluid, and compressing to a greater pressure the compressed air in step (6) prior to introduction into said pressurized heater.

Claim 30

The process of claim 27 wherein a portion of said superheated steam is introduced into a turboelectric generator as the working fluid.

Claim 31

The process of claim 27 provided with the step of preheating the twice compressed air by indirect heat exchange with a portion of the turbine exhaust gas prior to introduction into said pressurized heater.

Claim 32

The process of claim 1 provided with the step of preheating said stream of compressed free-oxygen containing gas prior to introduction into said pressurized heater in step (4) by indirect heat exchange with a portion of the exhaust gas leaving said expansion turbine in step (3).

Claim 33

The process of claim 1 wherein said hydrocarbonaceous fuel is a gaseous hydrocarbon fuel and said partial oxidation reaction in step (1) takes place in the absence of a temperature moderator.

Claim 34

The process of claim 1 wherein the gas stream from step (2) is purified prior to step (3).