Petroleum Coke Compositions for Catalytic Gasification

• US 20090165380A1
• 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: Robinson, Earl T., Lau, Francis S.
• Application Number:
  US12/342,608
• Publication Number:
  US 20090165380A1
• Time in Patent Office: Days
• US Class Current: 48/127.700
• CPC Class Codes: C10J 2300/0903 Feed preparation
• CPC Class Codes: C10J 2300/0943 Coke
• CPC Class Codes: C10J 2300/0973 Water
• CPC Class Codes: C10J 2300/0986 Catalysts
• 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 1/1225 halogen containing compounds
• CPC Class Codes: C10L 1/1233 oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
• CPC Class Codes: C10L 1/1266 nitrogen containing compounds, (e.g. NH3)
• CPC Class Codes: C10L 1/1275 sulfur, tellurium, selenium containing compounds
• CPC Class Codes: C10L 1/1881 carboxylic group attached to an aliphatic carbon atom
• CPC Class Codes: C10L 1/1883 polycarboxylic acid
• CPC Class Codes: C10L 5/00 Solid fuels produced by solidifying fluid fuels C10L7/00
• CPC Class Codes: C10L 5/04 Raw material of mineral origin to be used; Pretreatment thereof pretreatment of fuels of non-mineral origin C10L5/40
• CPC Class Codes: C10L 9/00 Treating solid fuels to improve their combustion
• CPC Class Codes: C10L 9/10 by using additives
• CPC Class Codes: Y02P 20/52 using catalysts, e.g. selective catalysts

Abstract

Particulate compositions are described comprising an intimate mixture of a petroleum coke and an alkali metal gasification catalyst, where the alkali metal gasification catalyst comprises a combination of an alkali metal hydroxide and one or more other alkali metal compounds are loaded onto coke for gasification in the presence of steam to yield a plurality of gases including methane and at least one or more of hydrogen, carbon monoxide, 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 having a particle distribution size suitable for gasification in a fluidized bed zone, the particulate composition comprising an intimate mixture of (a) a petroleum coke;

and (b) an alkali metal gasification catalyst which, in the presence of steam and under suitable temperature and pressure, exhibits 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, wherein;

(i) the alkali metal gasification catalyst comprises a combination of an alkali metal hydroxide with one or more other alkali metal compounds selected from the group consisting of an alkali metal carbonate, alkali metal bicarbonate, alkali metal formate, alkali metal oxalate, alkali metal amide, alkali metal acetate, alkali metal sulfide, alkali metal halide, and alkali metal nitrate;

(ii) the weight ratio of the alkali metal hydroxide to the other alkali metal compounds, in the alkali metal gasification catalyst, ranges from about 0.01 to about 0.5;

(iii) 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 about 0.01 to about 0.08; and

(iv) the particulate composition has a moisture content of less than about 6 wt % based on the weight of the particulate composition.

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

3. The particulate composition according to claim 1, wherein the alkali metal gasification catalyst comprises a potassium compound.

4. The particulate composition according to claim 1, wherein the one or more other alkali metal compounds comprises potassium carbonate.

5. The particulate composition according to claim 1, wherein the alkali metal hydroxide comprises potassium hydroxide.

6. The particulate composition according to claim 1, wherein the particulate composition comprises about 20 wt % or less overall ash content.

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

8. The particulate composition according to claim 1, wherein the alkali metal hydroxide is at least about 1 wt % based on the combined weight of the petroleum coke and the alkali metal gasification catalyst.

9. The particulate composition according to claim 1, wherein the alkali metal gasification catalyst comprises a potassium compound, a sodium compound or both;

the particulate composition comprises about 20 wt % or less overall ash content; and

the particulate composition has a particle size ranging from about 25 microns to about 2500 microns.

10. A process for converting a particulate composition into a plurality of gaseous products, the process 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.

11. The process according to claim 10, wherein the stream comprises a predominant amount of methane.

12. The process according to claim 10, wherein a char is formed in step (b), and the char is removed from the gasifying reactor and sent to a catalyst recovery and recycle process.

13. The process according to claim 12, wherein alkali metal catalyst is recovered and recycled.

14. A process for preparing the particulate composition of claim 1, the process comprising the steps of:

(a) providing petroleum coke particulates and an alkali metal gasification catalyst having a combination of an alkali metal hydroxide and one or more other alkali metal compounds, wherein the alkali metal hydroxide is at least about 1 weight percent of the combined weight of the petroleum coke particulates and the alkali metal gasification catalyst;

(b) contacting the coke particulates with an aqueous solution comprising the alkali metal gasification catalyst to form a slurry;

(c) dewatering the slurry to form a wet coke cake loaded with the alkali metal gasification catalyst; and

(d) drying the wet coke cake to produce a particulate composition having a moisture content of less than about 6 weight percent.