Low temperature carbonization and desulfurization of coal under elevated pressures

Claim 1

A method of coal conversion and subsequent product recovery comprising: (i) a first step of conducting a coal carbonization and desulphurization by contacting a mixture of finely divided particles of char and coal with a gas having at least about 20 mol percent hydrogen and at a temperature of between about 950° to about 1500° F and a pressure of 30-300 psi, said gas containing no more than about 2% by volume of hydrogen sulphide and being substantially free of oxygen, said process yielding a char containing no more than about 1% by weight of sulphur, said char being suitable for the production of a metallurgical grade coking material, and (ii) a second step of recovering individual components including a pure carbon dioxide from the gaseous products of said carbonization and desulphurization step by the use of the gas pressures from said carbonization and desulphurization step which carbon dioxide is recovered by reacting a gas stream containing hydrogen, methane and carbon monoxide with steam and removing carbon dioxide from the reaction products, and wherein this second step includes low temperature condensation of individual components from said gaseous products.

Claim 2

A method of coal conversion and subsequent product recovery comprising: (i) a first step of conducting a coal carbonization and desulphurization by contacting a mixture of finely divided particles of char and coal with a gas having at least about 20 mol percent hydrogen and at a temperature of between about 950° to about 1500° F and a pressure of 30-300 psi, said gas containing no more than about 2% by volume of hydrogen sulphide and being substantially free of oxygen, said process yielding a char containing no more than about 1% by weight of sulphur, said char being suitable for the production of a metallurgical grade coking material, and (ii) a second step of recovering individual components including a pure carbon dioxide from the gaseous products of said carbonization and desulphurization step by the use of the gas pressures from said carbonization and desulphurization step which carbon dioxide is recovered by reacting a gas stream containing hydrogen, methane and carbon monoxide with steam and removing carbon dioxide from the reaction products, and wherein this second step includes low temperature condensation of individual components from said gaseous products.

Claim 6

A method for the conversion of high sulphur coal into a low sulphur char and hydrogen-rich gases and for subsequent product recovery, comprising: (i) carbonizing and desulphurizing a high sulphur coal by contacting a mixture of finely divided particles of said coal and char with a hydrogen-rich fluidizing gas to provide a fluidized bed of said mixture, said contact being at a temperature of from 950° to about 1500° F and at a pressure of 30-300 psia, said fluidizing gas containing at least about 20 mol percent of hydrogen and no more than about 2% by volume of hydrogen sulphide, said contact being maintained until said coal is converted to a char containing no more than about 1% by weight of sulphur and to hydrogen-rich gas having a volume at least equal to said fluidizing gas, and (ii) recovering individual components from the gaseous products of said carbonization and desulphurization by maintaining the pressure from carbonization and desulphurization upon said gases while subjecting said gases to cryogenic conditions until vapor/liquid equilibrium cause condensation of liquids from said gases, yielding a residual gas stream including hydrogen, methane and carbon monoxide, and wherein hydrogen and pure carbon dioxide are recovered by reacting said residual gas stream with steam and removing carbon dioxide from the reaction products.

Claim 7

A method for the conversion of high sulphur coal into a low sulphur char and hydrogen-rich gases and for subsequent product recovery, comprising: (i) carbonizing and desulphurizing a high sulphur coal by contacting a mixture of finely divided particles of said coal and char with a hydrogen-rich fluidizing gas to provide a fluidized bed of said mixture, said contact being at a temperature of from 950° to about 1500° F and at a pressure of 30-300 psia, said fluidizing gas containing at least about 20 mol percent of hydrogen and no more than about 2% by volume of hydrogen sulphide, said contact being maintained until said coal is converted to a char containing no more than about 1% by weight of sulphur and to hydrogen-rich gas having a volume at least equal to said fluidizing gas, and (ii) recovering individual components from the gaseous products of said carbonization and desulphurization by maintaining the pressure from carbonization and desulphurization upon said gases while subjecting said gases to cryogenic conditions until vapor/liquid equilibrium cause condensation of liquids from said gases, yielding a residual gas stream including hydrogen, methane and carbon monoxide, and wherein hydrogen and pure carbon dioxide are recovered by reacting said residual gas stream with steam and removing carbon dioxide from the reaction products.

Claim 8

A method for the conversion of high ash and high sulphur coal into a low sulphur char and hydrogen-rich gases, and for subsequent product recovery, comprising: I. (a) carbonizing and desulphurizing a high ash and high sulfur coal by contacting a mixture of finely divided particles of said coal and char with a hydrogen-rich fluidizing gas to provide a fluidized bed of said mixture, said contact being at a temperature of from 950° to about 1500° F and at a pressure of 30-300 psia, said fluidizing gas containing at least about 20 mol percent of hydrogen and no more than about 2% by volume of hydrogen sulphide and being substantially free of oxygen, said contact being maintained until said coal is converted to a char containing no more than about 1% by weight of sulphur and to hydrogen-rich gas having a volume at least equal to said fluidizing gas, (b) removing hydrogen sulphide from said hydrogen-rich gas and recycling a portion to the carbonizing and desulphurizing of I(a) as fluidization gases therein, and Ii. recovering individual components from the remaining portions of said gas by maintaining the pressure from carbonization and desulphurization upon said gases while subjecting said gases to cryogenic conditions until vapor/liquid equilibrium cause condensation of liquids from said gases, the condensation yielding a residual gas stream including hydrogen, methane and carbon monoxide, and Iii. recovering the separated components, and wherein hydrogen and pure carbon dioxide are recovered by reacting said residual gas stream with steam and removing carbon dioxide from the reaction products.

Claim 9

A method for the conversion of high ash and high sulphur coal into a low sulphur char and hydrogen-rich gases, and for subsequent product recovery, comprising: I. (a) carbonizing and desulphurizing a high ash and high sulfur coal by contacting a mixture of finely divided particles of said coal and char with a hydrogen-rich fluidizing gas to provide a fluidized bed of said mixture, said contact being at a temperature of from 950° to about 1500° F and at a pressure of 30-300 psia, said fluidizing gas containing at least about 20 mol percent of hydrogen and no more than about 2% by volume of hydrogen sulphide and being substantially free of oxygen, said contact being maintained until said coal is converted to a char containing no more than about 1% by weight of sulphur and to hydrogen-rich gas having a volume at least equal to said fluidizing gas, (b) removing hydrogen sulphide from said hydrogen-rich gas and recycling a portion to the carbonizing and desulphurizing of I(a) as fluidization gases therein, and Ii. recovering individual components from the remaining portions of said gas by maintaining the pressure from carbonization and desulphurization upon said gases while subjecting said gases to cryogenic conditions until vapor/liquid equilibrium cause condensation of liquids from said gases, the condensation yielding a residual gas stream including hydrogen, methane and carbon monoxide, and Iii. recovering the separated components, and wherein hydrogen and pure carbon dioxide are recovered by reacting said residual gas stream with steam and removing carbon dioxide from the reaction products.