Method of producing a cooled syngas of improved quality

1. A method of producing a cooled syngas of improved quality, comprising:

(a) steam reforming biomass to generate unconditioned syngas comprising at least hydrogen, carbon monoxide, and hydrocarbons;

(b) hydrocarbon reforming the unconditioned syngas in a hydrocarbon reformer in the presence of an oxidant, to generate additional hydrogen and additional carbon monoxide from the hydrocarbons, and thereby produce a syngas of improved quality which is at least partially depleted of said hydrocarbons; and

(c) indirectly removing heat from the syngas of improved quality to generate steam by using a heat recovery steam generator (HRSG) to thereby produce said cooled syngas of improved quality, the heat being indirectly removed by:

(c1) providing a steam drum containing water therein;

(c2) transferring the water from the steam drum to the HRSG;

(c3) indirectly transferring heat from the syngas of improved quality to the water within the HRSG to generate the steam and produce the cooled syngas of improved quality;

(c4) transferring the steam from the HRSG back to the steam drum;

(c5) maintaining a predetermined pressure within the steam drum, by measuring a pressure within the steam drum, and adjusting a flow of steam discharged from the steam drum and through a pressure control valve to maintain the predetermined pressure within the steam drum;

(c6) maintaining a predetermined level of the water within the steam drum, by measuring a level of the water within the steam drum, and adjusting a flow of additional water that passes through a level control valve, and into the steam drum, to maintain the predetermined level within the steam drum.

2. The method according to claim 1 , wherein:

the hydrocarbons within the unconditioned syngas includes methane and one or more volatile organic compounds (VOCs) selected from the group consisting of benzene, toluene, phenol, styrene, xylene, and cresol.

3. The method according to claim 1 , further comprising:

(c7) outputting a purge flow of water from the steam drum to regulate a concentration of suspended and total dissolved solids within the steam drum.

4. The method according to claim 1 , wherein:

in step (a), the biomass is steam reformed at a pressure ranging from between 15 psig to 50 psig.

5. The method according to claim 1 , wherein:

in step (b), hydrocarbon reforming is performed in the presence of a catalyst.

6. The method according to claim 1 , further comprising:

(d) scrubbing the cooled syngas of improved quality in a scrubber to produce a scrubbed syngas;

(e) compressing the scrubbed syngas to a pressure between 100 to 2000 psig, to form a compressed syngas; and

(f) cleaning up the compressed syngas to form a conditioned syngas.

7. The method according to claim 6 , further comprising:

(g) providing a syngas processing technology configured to accept the conditioned syngas and produce hydrogen therefrom;

(h) after step (g), introducing the conditioned syngas to the syngas processing technology; and

(i) after step (h), producing said hydrogen from said conditioned syngas.

8. The method according to claim 6 , wherein:

the compressed syngas comprises sulfur, and the method further comprises:

removing sulfur from the compressed syngas to produce said conditioned syngas with a sulfur removal system selected from the group consisting of:

a Claus processing system, a solvent based sulfur removal process, a high temperature sorbent, glycol ether, diethylene glycol methyl ether, a regenerable sorbent, a non-regenerable sorbent, molecular sieve zeolites, calcium based sorbents, FeO-based sorbents, a MgO-based sorbent, a ZnO-based sorbent, a FeO-based catalyst, a MgO-based catalyst, a ZnO-based catalyst, iron sponge, a potassium-hydroxide-impregnated activated-carbon system, impregnated activated alumina, a titanium dioxide catalyst, a vanadium pentoxide catalyst, a tungsten trioxide catalyst, a sodium biphosphate solution, an aqueous ferric iron chelate solution, a potassium carbonate solution, sulfur crystallization, a bio-catalyzed scrubbing process, and a hydrodesulphurization catalyst.

9. The method according to claim 6 , wherein:

the compressed syngas comprises sulfur, and the method further comprises:

removing sulfur from the compressed syngas to produce said conditioned syngas using an amine-based sulfur removal system.

10. The method according to claim 6 , wherein:

the compressed syngas comprises carbon dioxide, and the method further comprises:

removing the carbon dioxide from the compressed syngas to produce said conditioned syngas.

11. The method according to claim 10 , further comprising:

recycling at least a portion of the carbon dioxide removed from said compressed syngas promote steam reforming of biomass in step (a).

12. A method of making Fischer-Tropsch products, comprising:

(i) producing a conditioned syngas in accordance with claim 6 ; and

(ii) introducing the conditioned syngas to Fischer-Tropsch catalytic synthesis processing technology to produce Fischer-Tropsch products including at least naphtha, diesel and wax.

13. The method according to claim 12 , wherein:

the Fischer-Tropsch catalytic synthesis processing technology includes a cobalt catalyst, and the method comprises:

in step (f), removing sulfur from the compressed syngas to form the conditioned syngas.

14. A method of making a product, comprising:

(i) producing a conditioned syngas in accordance with claim 6 ; and

(ii) introducing the conditioned syngas to syngas processing technology to produce one or more products from the group consisting of synthetic natural gas, methanol, ethanol, mixed alcohols, and dimethyl ether.

15. A method of making producing power, comprising:

(i) producing a conditioned syngas in accordance with claim 1 ;

(ii) scrubbing the cooled syngas of improved quality in a scrubber to produce a scrubbed syngas; and

(iii) introducing the scrubbed syngas to a power production system to produce power from the scrubbed syngas.

16. A method of producing a cooled syngas of improved quality, comprising:

(a) steam reforming biomass at a pressure ranging from between 15 pounds per square inch to 50 pounds per square inch to generate unconditioned syngas comprising at least hydrogen, carbon monoxide and at least one hydrocarbon, wherein the hydrocarbon within the unconditioned syngas includes methane;

(b) hydrocarbon reforming the unconditioned syngas in a hydrocarbon reformer in the presence of an oxidant to generate additional hydrogen and additional carbon monoxide from the hydrocarbons, and thereby produce a syngas of improved quality which is at least partially depleted of said hydrocarbons; and

(c) indirectly removing heat from the syngas of improved quality to generate steam by using a heat recovery steam generator (HRSG) to thereby produce said cooled syngas of improved quality, the heat being indirectly removed by:

(c1) providing a steam drum containing water therein;

(c2) transferring the water from the steam drum to the HRSG;

(c3) indirectly transferring heat from the syngas of improved quality to the water within the HRSG to generate the steam and produce the cooled syngas of improved quality;

(c4) transferring the steam from the HRSG back to the steam drum;

(c5) maintaining a predetermined pressure within the steam drum, by measuring a pressure within the steam drum, and adjusting a flow of steam discharged from the steam drum and through a pressure control valve to maintain the predetermined pressure within the steam drum;

(c6) maintaining a predetermined level of the water within the steam drum, by measuring a level of the water within the steam drum, and adjusting a flow of additional water that passes through a level control valve, and into the steam drum, to maintain the predetermined level within the steam drum; and

(c7) outputting a purge flow of water from the steam drum to regulate a concentration of suspended and total dissolved solids within the steam drum.

17. The method according to claim 16 , wherein:

in step (b), hydrocarbon reforming is performed in the presence of a catalyst.

18. The method according to claim 16 , further comprising:

(d) scrubbing the cooled syngas of improved quality in a scrubber to produce a scrubbed syngas; and

(e) compressing the scrubbed syngas to a pressure between 100 to 2000 psig, to form a compressed syngas; and

(f) cleaning up the compressed syngas to form a conditioned syngas.

19. The method according to claim 18 , wherein:

(g) providing a syngas processing technology configured to accept the conditioned syngas and produce hydrogen therefrom;

(h) after step (g), introducing the conditioned syngas to the syngas processing technology; and

(i) after step (h), producing said hydrogen from said conditioned syngas.

20. A method of making Fischer-Tropsch products, comprising;

(i) producing a conditioned syngas in accordance with claim 18 ; and

(ii) introducing the conditioned syngas to Fischer-Tropsch catalytic synthesis processing technology to produce Fischer-Tropsch products including at least naphtha, diesel and wax.

21. The method according to claim 20 , wherein:

the Fischer-Tropsch catalytic synthesis processing technology includes a cobalt catalyst, and the method comprises:

in step (f), removing sulfur from the compressed syngas to form the conditioned syngas.

22. A method of producing a cooled syngas of improved quality, comprising:

(a) steam reforming biomass to generate unconditioned syngas comprising at least hydrogen, carbon monoxide and at least one hydrocarbon, wherein the hydrocarbon within the unconditioned syngas includes methane;

(b) hydrocarbon reforming the unconditioned syngas in a catalytic hydrocarbon reformer in the presence of an oxidant to generate additional hydrogen and additional carbon monoxide from the hydrocarbons, and thereby produce a syngas of improved quality which is at least partially depleted of said hydrocarbons; and

(c) indirectly removing heat from the syngas of improved quality to generate steam by using a heat recovery steam generator (HRSG) to thereby produce said cooled syngas of improved quality, the heat being indirectly removed by:

(c1) providing a steam drum containing water therein;

(c2) transferring the water from the steam drum to the HRSG;

(c3) indirectly transferring heat from the syngas of improved quality to the water within the HRSG to generate the steam and produce the cooled syngas of improved quality;

(c4) transferring the steam from the HRSG back to the steam drum;

(c5) maintaining a predetermined pressure within the steam drum, by measuring a pressure within the steam drum, and adjusting a flow of steam discharged from the steam drum and through a pressure control valve to maintain the predetermined pressure within the steam drum;

(c6) maintaining a predetermined level of the water within the steam drum, by measuring a level of the water within the steam drum, and adjusting a flow of additional water that passes through a level control valve, and into the steam drum, to maintain the predetermined level within the steam drum.

23. The method according to claim 22 , comprising:

(d) scrubbing the cooled syngas of improved quality in a scrubber to produce a scrubbed syngas; and

(e) compressing the scrubbed syngas to a pressure between 100 to 2000 psig, to form a compressed syngas; and

(f) cleaning up the compressed syngas to form a conditioned syngas.

24. A method of making Fischer-Tropsch products, comprising:

(i) producing a conditioned syngas in accordance with claim 23 ; and

(ii) introducing the conditioned syngas to Fischer-Tropsch catalytic synthesis processing technology to produce Fischer-Tropsch products including at least naphtha, diesel and wax.

25. The method according to claim 24 , wherein:

the Fischer-Tropsch catalytic synthesis processing technology includes a cobalt catalyst, and the method comprises:

in step (f), removing sulfur from the compressed syngas to form the conditioned syngas.