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A method for controlling the synthesis gas composition obtained from a steam methane reformer (SMR) that obtains its feedstock as product gas directly from a steam hydro-gasification reactor SHR). The method allows control of the H2/CO syngas ratio by adjusting the hydrogen feed and the water conten

A method for controlling the synthesis gas composition obtained from a steam methane reformer (SMR) that obtains its feedstock as product gas directly from a steam hydro-gasification reactor SHR). The method allows control of the H2/CO syngas ratio by adjusting the hydrogen feed and the water content of feedstock into a steam hydro-gasification reactor that supplies the SMR. The steam and methane rich product gas of the SHR is generated by means of hydro-gasification of a slurry of carbonaceous material and water. The mass percentages of the product stream at each stage of the process are calculated using a modeling program, such as the ASPEN PLUS™ equilibrium process. By varying the parameters of solid to water ratio and hydrogen to carbon ratio, a sensitivity analysis can be performed that enables one determine the optimum composition of the slurry feedstock to the SHR to obtain a desired syngas ratio output of the SMR. Thus one can adjust the hydrogen feed and the water content of feedstock into the SHR that supplies the SMR to determine the syngas ratio output of the SMR.

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1. A process for converting carbonaceous feed material to synthesis gas and controlling a desired ratio of hydrogen to carbon monoxide in the synthesis gas, comprising: providing to a steam hydrogasification reactor (a) hydrogen in a first quantity and (b) a slurry formed from a second quantity of w

1. A process for converting carbonaceous feed material to synthesis gas and controlling a desired ratio of hydrogen to carbon monoxide in the synthesis gas, comprising: providing to a steam hydrogasification reactor (a) hydrogen in a first quantity and (b) a slurry formed from a second quantity of water and carbonaceous material;wherein the first quantity is determined by a first ratio of hydrogen to carbon content in the carbonaceous material, wherein the second quantity is determined by a second ratio of water to solid content in the carbonaceous material;generating in a steam hydro-gasification reaction a quantity of steam by superheating the water in the slurry and reacting in the steam hydro-gasification reaction the slurry with the hydrogen at a temperature and pressure sufficient to generate a product gas comprising methane, carbon monoxide, and steam;removing impurities from the product gas;subjecting the resultant product gas in a steam methane reformer to steam methane reforming with the quantity of steam, wherein the quantity of steam is effective to produce the desired ratio of hydrogen to carbon monoxide in the synthesis gas;wherein the steam methane reformer obtains the product gas from the steam hydrogasification reactor; andwherein the first and second ratios are adjusted such as to achieve the desired ratio of hydrogen to carbon monoxide in the synthesis gas effluent of the steam methane reformer. 2. The process of claim 1 wherein the hydrogen is obtained by diverting a portion of hydrogen separated from the synthesis gas to the slurry water. 3. The process of claim 1 wherein the hydrogen is obtained by diverting a portion of the synthesis gas to the slurry water, without separation of hydrogen from the synthesis gas. 4. The process of claim 1 wherein at least part of said water is provided in the form of steam. 5. The process of claim 1 wherein the step of adjusting first and second ratios is performed using a sensitivity analysis that relates a ratio of hydrogen to carbon monoxide in synthesis gas to conversion ratios of the carbon content of the carbonaceous material. 6. The process of claim 5 wherein the sensitivity analysis uses a computer-based modeling program. 7. The process of claim 6 wherein the program uses the ASPEN PLUS™ equilibrium process. 8. The process of claim 1 wherein the desired ratio of hydrogen to carbon monoxide in the synthesis gas effluent of the steam methane reformer is between steam methane reforming is conducted under conditions whereby the composition of synthesis gas produced has a H2:CO mole ratio range of 1:1 to 6:1. 9. The process of claim 1 wherein the carbonaceous material comprises municipal waste, biomass, wood, coal, or a natural or synthetic polymer. 10. The process of claim 1 in which synthesis gas generated by the steam methane reforming is fed into a Fischer-Tropsch type reactor under conditions whereby a liquid fuel is produced. 11. A process for converting municipal waste, biomass, wood, coal, or a natural or synthetic polymer, in a water containing slurry to synthesis gas, comprising: providing hydrogen and water to a steam hydro-gasification reactor, at a predetermined ratio of hydrogen to water, the ratio of hydrogen to water being determined by analysis of the effect on a H2:CO mole ratio in the synthesis gas effluent from a steam methane reformer of (a) the ratio of solid content of the carbonaceous material to the slurry water and (b) the ratio of the hydrogen to carbon content of the carbonaceous material that would produce synthesis gas comprising hydrogen and carbon monoxide at a H2:CO mole ratio range of 1:1 to 6:1;generating in a steam hydro-gasification reaction a quantity of steam by superheating the water and reacting in the steam hydro-gasification reaction carbonaceous material in the presence of both said hydrogen and water, at a temperature of about 700° C. to about 900° C. and pressure about 132 psi to 560 psi, whereby to generate a product gas comprising steam, methane, and carbon monoxide;removing impurities from the product gas stream substantially at said temperature and pressure;subjecting the resultant product gas to steam methane reforming with the quantity of steam under conditions whereby to generate synthesis gas comprising hydrogen and carbon monoxide at a H2:CO mole ratio range of 1:1 to 6:1; andfeeding synthesis gas generated by the steam methane reforming into a Fischer-Tropsch type reactor under conditions whereby a liquid fuel is produced;wherein the steam methane reformer obtains the product gas from the steam hydrogasification reactor. 12. The process of claim 11 wherein the hydrogen is obtained by diverting a portion of hydrogen separated from the synthesis gas to the slurry water. 13. The process of claim 11 wherein the hydrogen is obtained by diverting a portion of the synthesis gas to the slurry water, without separation of hydrogen from the synthesis gas. 14. The process of claim 11 comprising transferring exothermic heat from the Fischer-Tropsch type reaction to the hydro-gasification reaction and/or steam methane reforming reaction. 15. The process of claim 1, wherein the product gas is generated by a process consisting essentially of said simultaneously heating the slurry in the presence of both said hydrogen and water in the hydrogasifier.