PROCESSES FOR HYDROMETHANATION OF A CARBONACEOUS FEEDSTOCK

• US 20110062012A1
• Filed: 09/15/2010
• Published: 03/17/2011
• Est. Priority Date: 09/16/2009
• Status: Abandoned Application

• Current Assignee: Sure Champion Investments Limited
• Original Assignee: GreatPoint Energy, Inc.
• Inventors: Robinson, Earl T.
• Application Number:
  US12/882,415
• Publication Number:
  US 20110062012A1
• Time in Patent Office: Days
• US Class Current: 201/2.5
• CPC Class Codes: C10J 2300/093 Coal
• CPC Class Codes: C10J 2300/0959 Oxygen
• 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 3/00 Production of combustible gases containing carbon monoxide from solid carbonaceous fuels destructive distillation processes C10B
• CPC Class Codes: C10J 3/721 Multistage gasification, e.g. plural parallel or serial gasification stages
• CPC Class Codes: C10J 3/86 combined with waste-heat boilers
• CPC Class Codes: C10K 3/00 Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
• CPC Class Codes: C10L 3/08 Production of synthetic natural gas
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

The present invention relates to processes for preparing gaseous products, and in particular methane and/other value added gases such as hydrogen, via the catalytic hydromethanation of a carbonaceous feedstock in the presence of steam and syngas, wherein a hydromethanation reactor is combined with a syngas generator in a particular combination.

Claims

1. A process for generating a methane-enriched raw product stream and a syngas raw product stream from one or more carbonaceous feedstocks, the process comprising the steps of:

(a) supplying a first carbonaceous feedstock, a first oxygen-rich gas stream, and optionally an aqueous stream comprising one or both of water and steam, to a syngas generator;

(b) reacting the first carbonaceous feedstock in the presence of oxygen and optionally the aqueous stream, in the syngas generator to produce a first gas stream at a first temperature and a first pressure, the first gas stream comprising hydrogen, carbon monoxide, heat energy and optionally steam;

(c) introducing the first gas stream into a first heat exchanger unit, optionally with a quench stream comprising one or both of water and steam, to remove heat energy and generate a cooled first gas stream at a second temperature and a second pressure, the cooled first gas stream comprising hydrogen, carbon monoxide and optionally steam;

(d) separating the cooled first gas stream into a hydromethanation gas feed stream and the syngas raw product stream, the syngas raw product stream comprising carbon monoxide, hydrogen and optionally steam;

(e) optionally adding one or both of steam and heat energy to the hydromethanation gas feed stream such that the resulting hydromethanation gas feed stream comprises hydrogen, carbon monoxide and steam at a third temperature and a third pressure;

(f) introducing a second carbonaceous feedstock, a hydromethanation catalyst, the hydromethanation gas feed stream and optionally a second oxygen-rich gas stream, to a hydromethanation reactor;

(g) reacting the second carbonaceous feedstock in the hydromethanation reactor in the presence of carbon monoxide, hydrogen, steam, hydromethanation catalyst and optionally oxygen, at a fourth temperature and a fourth pressure, to produce the methane-enriched raw product stream, wherein the methane-enriched raw product stream comprises methane, carbon monoxide, hydrogen, carbon dioxide, hydrogen sulfide and heat energy; and

(h) withdrawing the methane-enriched product stream from the hydromethanation reactor,

wherein;

the reaction in step (g) has a syngas demand, a steam demand and a heat demand;

the amount of carbon monoxide and hydrogen in the hydromethanation gas feed stream (or the superheated hydromethanation gas feed stream if present) is sufficient to at least meet the syngas demand of the reaction in step (g);

if the amount of steam in the hydromethanation gas feed stream from step (d) is insufficient to meet the steam demand of the reaction in step (g), then step (e) is present and steam is added to the hydromethanation gas feed stream in an amount that is sufficient to at least meet the steam demand of the reaction in step (g);

if the second temperature is insufficient to meet the heat demand of the reaction in step (g), then step (e) is present and heat energy is added to the hydromethanation gas feed stream in an amount that is at least sufficient to meet the heat demand of the reaction in step (g).

2. The process of claim 1, wherein the methane-enriched raw product stream comprises at least about 20 mol % methane (based on the moles of methane, carbon dioxide, carbon monoxide and hydrogen in the methane-enriched raw product stream).

3. The process of claim 2, wherein the methane-enriched raw product stream comprises at least 50 mol % methane plus carbon dioxide (based on the moles of methane, carbon dioxide, carbon monoxide and hydrogen in the methane-enriched raw product stream).

4. The process of claim 1, wherein steam is supplied to the syngas generator, and the first gas stream further comprises steam.

5. The process of claim 1, wherein the second carbonaceous feedstock is loaded with hydromethanation catalyst prior to being supplied to the hydromethanation reactor.

6. The process of claim 1, wherein the hydromethanation catalyst comprises an alkali metal.

7. The process of claim 1, wherein a char by-product is generated in step (g), and is continuously or periodically withdrawn from the hydromethanation reactor.

8. The process of claim 7, wherein the hydromethanation catalyst comprises an alkali metal, the char by-product comprises an alkali metal content from the hydromethanation catalyst, at least a portion of the char by-product is treated to recover at least a portion of the alkali metal content, and at least a portion of the recovered alkali metal content is recycled for use as hydromethanation catalyst.

9. The process of claim 8, wherein the second carbonaceous feedstock is impregnated with hydromethanation catalyst prior to being supplied to the hydromethanation reactor, and the hydromethanation catalyst used to impregnate the second carbonaceous feedstock comprises recycled hydromethanation catalyst and a make-up hydromethanation catalyst.

10. The process of claim 1, wherein the first and second carbonaceous feedstocks derive from the same carbonaceous material.

11. The process of claim 1, which is a continuous process in which steps (a), (b), (c), (d), (g) and (h), and when present step (e), are performed in a continuous manner.

12. The process of claim 1, further comprising the step of processing the methane-enriched raw product stream to generate a pipeline-quality natural gas product.

13. The process of claim 1, wherein the methane-enriched raw product stream and at least a portion of the syngas raw product stream are treated in a gas processing system to produce a sweetened gas stream.

14. The process of claim 13, wherein the sweetened gas stream is further processed to produce a methane product stream and/or a hydrogen product stream.

15. The process of claim 1, wherein the first carbonaceous feedstock comprises an ash content, the first gas stream comprises a residue from the ash content, and the residue from the ash content is substantially removed prior to introduction of the hydromethanation gas feed stream into the hydromethanation reactor.

17. A process for generating a sweetened gas stream from one or more carbonaceous feedstocks, the sweetened gas stream comprising methane, hydrogen and optionally carbon monoxide with substantially no carbon dioxide and hydrogen sulfide, the process comprising the steps of:

(A) providing an existing facility comprising (i) a syngas generator that produces a first gas stream comprising carbon monoxide and hydrogen, and optionally carbon dioxide, hydrogen sulfide and steam, at a first temperature and pressure, and (ii) a gas processing system comprising an acid gas removal unit for removing substantially all of the carbon dioxide and hydrogen sulfide that may be present in the first gas stream, wherein the syngas generator comprises an exhaust line for the first gas stream that ties into the gas processing system;

(B) modifying the existing facility to produce a modified facility comprising the following modifications;

(1) if the exhaust line does not comprise a cooling zone for cooling the first gas stream to produce a cooled first gas stream at a second temperature and second pressure, inserting such a cooling zone into the exhaust line prior to the gas processing system;

(2) inserting a gas stream splitting mechanism between the cooling zone and the gas processing system, the gas stream splitting mechanism configured to split the cooled first gas stream into a syngas raw product stream and a hydromethanation gas feed stream;

(3) optionally inserting a superheater for the hydromethanation gas feed stream in communication with the gas stream splitting mechanism, the superheater configured to generate a superheated hydromethanation gas feed stream at a third temperature and pressure;

(4) inserting a hydromethanation reactor in communication with the gas stream splitting mechanism (or the superheater if present), wherein the hydromethanation reactor is configured (i) to receive a second carbonaceous feedstock, a hydromethanation catalyst, the hydromethanation gas feed stream and, optionally, an oxygen-rich gas stream;

(ii) to contain a reaction of the second carbonaceous feedstock in the presence of carbon monoxide, hydrogen, steam, hydromethanation catalyst and optionally oxygen, at a fourth temperature and a fourth pressure, that produces a methane-enriched raw product stream, the methane-enriched raw product stream comprising methane, carbon monoxide, hydrogen, carbon dioxide, hydrogen sulfide and heat energy; and

(iii) to exhaust the methane-enriched raw product stream; and

(5) inserting a line to feed the methane-enriched product stream into the gas processing system;

(C) operating the process according to claim 1 in the modified facility; and

(D) processing the methane-enriched product stream and, optionally, at least a portion of the syngas raw product stream to produce the sweetened gas stream.

16. A gasifier apparatus for generating a methane-enriched raw product stream and a syngas raw product stream from one or more carbonaceous feedstocks, the gasifier apparatus comprising:

(a) a syngas generator configured (1) to receive a first carbonaceous feedstock, a first oxygen-rich gas stream and, optionally an aqueous stream comprising one or both of water and steam;

(2) to contain a reaction of the first carbonaceous feedstock in the presence of oxygen and optionally the aqueous stream, that produces a first gas stream comprising hydrogen, carbon monoxide and optionally steam, at a first temperature and a first pressure, and (3) to exhaust the first gas stream;

(b) a cooling zone configured to (1) receive the first gas stream and, optionally, a quench stream comprising one or both of steam and water, and (2) generate a cooled first gas stream comprising hydrogen, carbon monoxide and, optionally, steam at a second temperature and a second pressure;

(c) a separation zone configured to (1) receive the cooled first gas stream, and (2) separate the cooled first gas stream into a hydromethanation gas feed stream and the syngas raw product stream, the syngas raw product stream comprising carbon monoxide, hydrogen and optionally steam;

(d) an optional superheater zone configured to (1) receive the hydromethanation gas feed stream from the separation zone, (2) optionally receive a steam feed stream, and (3) generate a superheated hydromethanation gas feed stream comprising carbon monoxide, hydrogen and steam at a third temperature and a third pressure; and

(e) a hydromethanation reactor configured (1) to receive a second carbonaceous feedstock, a hydromethanation catalyst, the hydromethanation gas feed stream and, optionally, a second oxygen-rich gas stream, the second carbonaceous feedstock comprising a carbon content;

(2) to contain a reaction of the second carbonaceous feedstock in the presence of carbon monoxide, hydrogen, steam, hydromethanation catalyst and optionally oxygen, at a fourth temperature and a fourth pressure, that produces a methane-enriched raw product stream, the methane-enriched raw product stream comprising methane, carbon monoxide, hydrogen and carbon dioxide; and

(3) to exhaust the methane-enriched raw product stream.