Coal Compositions for Catalytic Gasification

• US 20090165379A1
• Filed: 12/23/2008
• Published: 07/02/2009
• Est. Priority Date: 12/28/2007
• Status: Abandoned Application

• Current Assignee: Sure Champion Investments Limited
• Original Assignee: GreatPoint Energy, Inc.
• Inventors: Rappas, Alkis S.
• Application Number:
  US12/342,578
• Publication Number:
  US 20090165379A1
• Time in Patent Office: Days
• US Class Current: 48/127.700
• CPC Class Codes: C10J 2300/0903 Feed preparation
• CPC Class Codes: C10J 2300/093 Coal
• CPC Class Codes: C10J 2300/0973 Water
• CPC Class Codes: C10J 2300/0986 Catalysts
• CPC Class Codes: C10J 2300/1662 to methane (SNG) production of synthetic natural gas C10L3/08
• CPC Class Codes: C10J 2300/1807 Recycle loops, e.g. gas, solids, heating medium, water
• CPC Class Codes: C10J 2300/1823 for synthesis gas
• CPC Class Codes: C10J 2300/1853 Steam reforming, i.e. injection of steam only
• CPC Class Codes: C10J 3/00 Production of combustible gases containing carbon monoxide from solid carbonaceous fuels destructive distillation processes C10B
• CPC Class Codes: C10J 3/463 in stationary fluidised beds
• CPC Class Codes: C10L 5/00 Solid fuels produced by solidifying fluid fuels C10L7/00
• CPC Class Codes: C10L 5/366 Powders
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion
• CPC Class Codes: C10L 9/10 by using additives

Abstract

Particulate compositions are described comprising an intimate mixture of a coal and a gasification catalyst in the presence of steam to yield a plurality of gases including methane and at least one or more of hydrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, ammonia and other higher hydrocarbons are formed. Processes are also provided for the preparation of the particulate compositions and converting the particulate composition into a plurality of gaseous products.

Claims

1. A particulate composition comprising an intimate mixture of (a) a coal particulate having a size distribution suitable for gasification in a fluidized bed zone;

(b) a transition metal gasification catalyst;

(c) an alkaline earth metal source; and

(d) an alkali metal gasification catalyst, wherein;

(i) in the presence of steam and under suitable temperature and pressure, the catalysts exhibit gasification activity whereby a plurality of gases including methane and at least one or more of hydrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, ammonia and other higher hydrocarbons are formed;

(ii) the transition metal gasification catalyst is present in an amount sufficient to provide, in the particulate composition, a ratio of transition metal atoms to carbon atoms ranging from 0.001 to about 0.10;

(iii) the alkaline earth metal source is present in an amount sufficient to provide, in the particulate composition, from about 0.1 to about 3.0 wt % alkaline earth metal atoms on a dry basis; and

(iv) the alkali metal gasification catalyst is present in an amount sufficient to provide, in the particulate composition, a ratio of alkali metal atoms to carbon atoms ranging from 0.01 to about 0.08.

2. The particulate composition according to claim 1, wherein the alkali metal gasification catalyst comprises potassium and/or sodium.

3. The particulate composition according to claim 1, wherein the alkaline earth metal source comprises a source of calcium, magnesium or barium.

4. The particulate composition according to claim 2, wherein the alkaline earth metal source comprises a source of calcium, magnesium or barium.

5. The particulate composition according to claim 1, wherein the transition metal gasification catalyst comprises V, Cr, Mn, Fe, Co, Ni, Cu, Mo, or mixtures thereof.

6. The particulate composition according to claim 1, wherein the transition metal gasification catalyst comprises Fe, Mn, or mixtures thereof.

7. The particulate composition according to claim 2, wherein the transition metal gasification catalyst comprises Fe, Mn, or mixtures thereof.

8. The particulate composition according to claim 4, wherein the transition metal gasification catalyst comprises Fe, Mn, or mixtures thereof.

9. The particulate composition according to claim 1, having a particle size ranging from about 25 microns to about 2500 microns.

10. The particulate composition according to claim 1, having a residual moisture content of less than about 6 wt %.

11. A process for converting a particulate composition into a plurality of gaseous products comprising the steps of:

(a) supplying a particulate composition according to claim 1 to a gasifying reactor;

(b) reacting the particulate composition in the gasifying reactor in the presence of steam and under suitable temperature and pressure to form a plurality of gaseous including methane and at least one or more of hydrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, ammonia and other higher hydrocarbons; and

(c) at least partially separating the plurality of gaseous products to produce a stream comprising a predominant amount of one of the gaseous products.

12. The process according to claim 11, wherein the stream comprises a predominant amount of methane.

13. A process for preparing a particulate composition, comprising the steps of:

(a) providing a particulate of a coal feedstock;

(b) contacting the particulate with an aqueous solution comprising a transition metal source to form a first slurry;

(c) dewatering the first slurry to form a first wet cake;

(d) contacting the first wet cake with an aqueous solution comprising an alkaline earth metal source to form a second slurry;

(e) dewatering the second slurry to form a second wet cake;

(f) contacting the second wet cake with an alkali metal gasification catalyst to form a third wet cake; and

(g) drying the third wet cake to provide a particulate composition having a residual moisture content of less than about 6 wt %.

14. The process according to claim 13, wherein the contacting the second wet cake with an alkali metal gasification catalyst to form a third wet cake comprises the steps of:

(i) contacting the second wet cake with an aqueous solution comprising an alkali metal source to provide a third slurry; and

(ii) dewatering the third slurry to form the third wet cake.

15. The process according to claim 13, wherein the alkali metal gasification catalyst comprises potassium and/or sodium.

16. The process according to claim 13, wherein the alkaline earth metal source comprises a source of calcium, magnesium or barium.

17. The process according to claim 15, wherein the alkaline earth metal source comprises a source of calcium, magnesium or barium.

18. The process according to claim 13, wherein the transition metal gasification catalyst comprises Fe, Mn, or mixtures thereof.

19. The process according to claim 17, wherein the transition metal gasification catalyst comprises Fe, Mn, or mixtures thereof.