Integrated gasification iron-air electrical system

Claim 2

An integrated, gasification, iron-air electrical system, capable of generating electrical energy from a carbonaceous material, comprising: (A) a gasification means for carbonaceous material comprising at least one gasification reactor, where a carbonaceous material is contacted and reacted with a gaseous medium containing steam and air, at a temperature and for a time effective to gasify the carbonaceous material and produce a hot gaseous reaction product comprising CO and H 2 ; (B) an iron-air cell containing at least one discharged iron electrode (C) means to remove the discharged iron electrode from the cell of (B), and contact it with the gaseous reaction product produced in (A); (D) the discharged iron electrode removed from the cell of (B), containing material consisting essentially of Fe and Fe(OH) 2 , which electrode is contacted with the hot gaseous reaction product produced in the gasification reactor of (A), directly, at a temperature of from about 450° C. to about 700° C., for a time effective to convert, by reduction, discharged iron compounds consisting essentially of Fe and Fe(OH) 2 to charge iron compounds in the electrode and provide a recharged iron electrode; (E) an iron-air cell into which the recharged iron electrode provided in (D) is placed; (F) means to transport the recharged iron electrode provided in (D) to the iron-air cell of (E); and (G) electrical connection means attached to the iron-air cell of (E), providing the cell with capability of generating electrical energy.

Claim 3

The system of claim 1, where the carbonaceous material is coal, the recharged iron electrode contains elemental iron, the iron electrode comprises active material disposed within a porous fiber metal current collector and the hot gaseous reaction product contacting the electrode contains over 55 volume % of H 2 .

Claim 4

An integrated, coal gasification, iron-air electrical system, capable of generating electrical energy from coal, comprising: (A) a coal gasification means comprising at least one coal gasification reactor, where coal is contacted and reacted with a gaseous medium containing steam and air, at a temperature and for a time effective to gasify coal and produce a hot gaseous reaction product comprising CO and H 2 ; (B) a plurality of iron-air cells, each containing at least one discharged iron electrode having a fiber metal structure; (C) means to remove the discharged iron electrodes from the cells of (B), and contact them with the gaseous reaction product produced in (A); (D) the discharged iron electrodes removed from the cells of (B), containing material consisting essentially of Fe and Fe(OH) 2 , which electrodes are contacted with the hot gaseous reaction product in the gasification reactor of (A), directly at a temperature of from about 450° C. to about 700° C., for a time effective to convert, by reduction, discharged iron compounds consisting essentially of Fe and Fe(OH) 2 to charged iron compounds in the electrodes and provide a plurality of recharged iron electrodes; (E) a plurality of iron-air cells into which the recharged iron electrodes provided in (D) are placed; (F) means to transport the recharged iron electrodes provided in (D) to the iron-air cells of (E); and (G) electrical interconnection means attached to the iron-air cells of (E), and to an inverter, providing the cells with capability of generating electrical energy.

Claim 5

An integrated, coal gasification, iron-air electrical system, capable of generating electrical energy from coal, comprising: (A) a coal gasification means comprising at least one coal gasification reactor, where coal is contacted and reacted with a gaseous medium containing steam and air, at a temperature and for a time effective to gasify coal and produce a hot gaseous reaction product comprising CO and H 2 ; (B) a plurality of iron-air cells, each containing at least one discharged iron electrode having a fiber metal structure; (C) means to remove the discharged iron electrodes from the cells of (B), and contact them with the gaseous reaction product produced in (A); (D) the discharged iron electrodes removed from the cells of (B), containing material consisting essentially of Fe and Fe(OH) 2 , which electrodes are contacted with the hot gaseous reaction product in the gasification reactor of (A), directly at a temperature of from about 450° C. to about 700° C., for a time effective to convert, by reduction, discharged iron compounds consisting essentially of Fe and Fe(OH) 2 to charged iron compounds in the electrodes and provide a plurality of recharged iron electrodes; (E) a plurality of iron-air cells into which the recharged iron electrodes provided in (D) are placed; (F) means to transport the recharged iron electrodes provided in (D) to the iron-air cells of (E); and (G) electrical interconnection means attached to the iron-air cells of (E), and to an inverter, providing the cells with capability of generating electrical energy.

Claim 6

The system of claim 3, where the discharged iron electrodes contain iron and, iron hydroxide compounds substantially as Fe and Fe(OH) 2 , and are heated at from about 550° C. to about 700° C.

Claim 7

The system of claim 3, where the recharged iron electrode contains elemental iron, and the hot gaseous reaction product contacting the electrodes contain over 55 volume % of H 2 .

Claim 8

The system of claim 3, where the coal gasification means is a fluidized bed coal gasification furnace utilizing a downward flow of coal and an upward flow of gases, operating at a reaction coal gasification temperature of from about 850° C. to about 1250° C.

Claim 9

The system of claim 3, where the iron-air cells comprise an iron electrode disposed in alkali electrolyte between two air electrodes, all contained in a casing having air inlet means.

Claim 10

The system of claim 7, where the alkali electrolyte is an alkali hydroxide, the iron electrodes are removably attached to a removable support plate, the iron electrode comprises active material disposed within a porous fiber metal current collector, and the air electrode comprises an active material hydrophilic layer containing a current collector disposed next to electrolyte and bonded to a hydrophobic layer.

Claim 11

The system of claim 1, where the discharged iron electrodes contain iron, and iron hydroxide compounds substantially as Fe and Fe(OH) 2 , and are heated at from about 550° C. to about 700° C.