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A process and apparatus for producing a synthesis gas for use as a gaseous fuel or as feed into a Fischer-Tropsch reactor to produce a liquid fuel in a substantially self-sustaining process. In one embodiment, a slurry of carbonaceous material in water, and hydrogen from an internal source, are fed

A process and apparatus for producing a synthesis gas for use as a gaseous fuel or as feed into a Fischer-Tropsch reactor to produce a liquid fuel in a substantially self-sustaining process. In one embodiment, a slurry of carbonaceous material in water, and hydrogen from an internal source, are fed into a hydro-gasification reactor to generate methane rich producer gases which are fed into a steam pyrolytic reformer to generate synthesis gas comprising hydrogen and carbon monoxide. A portion of the hydrogen is used as the internal hydrogen source. The remaining synthesis gas is either used as fuel to produce electricity and/or process heat or is fed into a Fischer-Tropsch reactor to produce liquid fuel. In another embodiment of the invention, carbonaceous material can be heated simultaneously in the presence of both hydrogen and steam to undergo steam pyrolysis and hydro-gasification in a single step.

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What is claimed is: 1. A process for converting carbonaceous material to energetic gases, the process comprising a) forming a liquid suspension slurry of particles of carbonaceous material in water; and b) feeding hydrogen and the suspension slurry into a hydro-gasification reactor without a reacti

What is claimed is: 1. A process for converting carbonaceous material to energetic gases, the process comprising a) forming a liquid suspension slurry of particles of carbonaceous material in water; and b) feeding hydrogen and the suspension slurry into a hydro-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1. 2. The process of claim 1 wherein the temperature in step b) is about 580�� C. to 790�� C. 3. The process of claim 1 wherein the pressure in step b) is about 132 psi to 560 psi. 4. The process of claim 1 wherein the carbonaceous material has a nominal particle size of about 1 mm in diameter. 5. The process of claim 1 wherein the carbonaceous material comprises municipal waste, biomass, wood, coal, or a natural or synthetic polymer. 6. The process of claim 5 wherein the carbonaceous material comprises biomass. 7. The process of claim 5 wherein the carbonaceous material comprises municipal waste which comprises wood or a natural or synthetic polymer. 8. A process for converting carbonaceous material to energetic gases, the process comprising: a) forming a liquid suspension slurry of particles of carbonaceous material in water, and b) feeding hydrogen and the Suspension slurry into a hydro-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1, wherein the carbonaceous material comprises wood or a natural or synthetic polymer. 9. A process for producing a synthesis gas, the process comprising: a) forming a liquid suspension slurry of particles of carbonaceous material in water; b) feeding hydrogen and the suspension slurry into a hydro-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1, and c) subjecting the methane and carbon monoxide rich producer gases to steam reforming reactions under conditions whereby synthesis gas comprising hydrogen and carbon monoxide is generated. 10. The process of claim 9 wherein the carbonaceous material is non-pyrolyzed carbonaceous material. 11. The process of claim 9 wherein the carbonaceous material comprises municipal waste, biomass, wood, coal, or a natural or synthetic polymer. 12. The process of claim 11 wherein the carbonaceous material comprises biomass. 13. The process of claim 11 wherein the carbonaceous material comprises municipal waste which comprises wood or a natural or synthetic polymer. 14. A process for producing a synthesis gas, the process comprising: a) forming a liquid suspension slurry of particles of carbonaceous material in water; b) feeding hydrogen and the suspension slurry into a hydra-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the carbonaceous material comprises wood or a natural or synthetic polymer, wherein the ratio of water to dry carbonaceous material in the hydrogasifleation reactor is at least 2:1, and c) subjecting the methane and carbon monoxide rich producer gases to steam reforming reactions under conditions whereby synthesis gas comprising hydrogen and carbon monoxide is generated. 15. A process for producing a liquid fuel, the process comprising: a) forming a liquid suspension slurry of particles of carbonaceous material in water; b) feeding hydrogen and the suspension slurry into a hydro-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1; c) subjecting the methane and carbon monoxide rich producer gases to steam reforming reactions under conditions whereby synthesis gas comprising hydrogen and carbon monoxide is generated; and d) subjecting the synthesis gas to Fischer-Tropsch type reactions under conditions whereby a liquid fuel is produced. 16. The process of claim 15 wherein the carbonaceous material is non-pyrolyzed carbonaceous material. 17. The process of claim 15 wherein the carbonaceous material comprises municipal waste, biomass, wood, coal, or natural or synthetic polymer. 18. The process of claim 17 wherein the carbonaceous material comprises biomass. 19. The process of claim 17 wherein the carbonaceous material comprises municipal waste which comprises wood or a natural or synthetic polymer. 20. A process for producing a synthesis gas for use as a gaseous fuel or as feed into a Fischer-Tropsch type reactor to produce a liquid fuel, the process comprising: a) forming a liquid suspension slurry of particles of carbonaceous material in water to produce a slurry of carbonaceous materials; b) feeding hydrogen and the suspension slurry into a hydro-gasification reactor without a reaction catalyst at a temperature and pressure sufficient to generate methane and carbon monoxide rich producer gases, wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1; c) feeding the methane and carbon monoxide rich producer gases from the hydro-gasification reactor into a steam methane reformer under conditions whereby synthesis gas comprising hydrogen and carbon monoxide is generated; d) feeding a portion of the hydrogen generated by the steam methane reformer into the hydro-gasification reactor as said hydrogen from an internal source; and e) either utilizing said synthesis gas generated by the steam methane reformer for process heat or as fuel for an engine to produce electricity, or feeding said synthesis gas into the Fischer-Tropsch type reactor under conditions whereby a liquid fuel is produced. 21. The process of claim 20 in which said slurry is formed by grinding said carbonaceous material in water. 22. The process of claim 20 in which said carbonaceous material comprises municipal waste, biomass, wood, coal, or a natural or synthetic polymer. 23. The process of claim 22 wherein the carbonaceous material comprises biomass. 24. The process of claim 22 wherein the carbonaceous material comprises municipal waste which comprises wood or a natural or synthetic polymer. 25. The process of claim 20 in which synthesis gas generated by the steam methane reformer is fed into a Fischer-Tropsch type reactor under conditions whereby a liquid fuel is produced. 26. The process of claim 25 wherein said conditions and the relative amounts of hydrogen and carbon monoxide in the Fischer-Tropsch type reactor are such that said liquid fuel is produced exothermally. 27. The process of claim 26 comprising transferring exothermic heat from one or both of the hydro-gasification reactor and Fischer-Tropsch type reactor to the steam methane reformer. 28. The process of claim 26 comprising transferring exothermic heat from the hydro-gasification reactor and Fischer-Tropsch type reactor to the steam methane reformer. 29. The process of claim 28 in which molten salt loops or water-steam loops are used to transfer said exothermic heat. 30. The process of claim 25 in which the relative amounts of hydrogen and carbon monoxide in the synthesis gas fed into the Fischer-Tropsch type reactor are such that said liquid fuel is substantially cetane. 31. A substantially self-sustaining process for producing a liquid fuel from carbonaceous feed, comprising: a) fanning a liquid suspension slurry of particles of carbonaceous material in Water; b) feeding hydrogen from an internal source and the suspension shiny into a hydro-gasification reactor without a reaction catalyst in amounts whereby methane and carbon monoxide rich producer gases are generated exothermally under super-atmospheric pressure; wherein the ratio of water to dry carbonaceous material in the hydrogasification reactor is at least 2:1; c) feeding the methane and carbon monoxide rich producer gases from the hydro-gasification reactor into a steam methane reformer under conditions whereby synthesis gas comprising hydrogen and carbon monoxide are generated; d) feeding a portion of the hydrogen generated by the steam methane reformer, through a hydrogen purification filter, into the hydra-gasification reactor, the hydrogen therefrom constituting said hydrogen from an internal source; e) feeding the remainder of the synthesis gas generated by the steam methane reformer into the Fischer-Tropsch type reactor under conditions whereby a liquid fuel is produced exothermally; and f) transferring exothermic heat from the hydra-gasification reactor and Fischer-Tropsch type reactor to the steam methane reformer, whereby said process is substantially self-sustaining. 32. The process of claim 31 in which molten salt loops or water-steam loops are used to transfer said exothermic heat. 33. The process of claim 31 in which said carbonaceous material comprises municipal waste, biomass, wood, coal, or a natural or synthetic polymer. 34. The process of claim 33 wherein the carbonaceous material comprises biomass. 35. The process of claim 33 wherein the carbonaceous material comprises municipal waste which comprises wood or a natural or synthetic polymer. 36. The process of claim 20, wherein step a) further comprises feeding superheated steam from a steam generator into the hydro-gasification reactor. 37. The process of claim 36, further comprising transferring exothermic heat from one or both of the hydro-gasification reactor and Fischer-Tropsch type reactor to the steam generator.