초록 ▼

Organic matter, i.e., biomass, fibrous plant matter, organic chemicals or organic waste, or other carbon-based matter is converted to synthesis fuel gas by reactive contact with superheated steam at a temperature of about 200 to 2000 degrees C., typically 500 to 1700 degrees. A reactor has a general

Organic matter, i.e., biomass, fibrous plant matter, organic chemicals or organic waste, or other carbon-based matter is converted to synthesis fuel gas by reactive contact with superheated steam at a temperature of about 200 to 2000 degrees C., typically 500 to 1700 degrees. A reactor has a generally tubular envelope, a rotor within the envelope, and hot reaction spaces disposed annularly within the wall of the tubular envelope. The steam and biomass particles can be heated to the required temperatures by RF induction. The product gases include H2, CO, and CO2 in ratios controlled by a programmable controller. Control of temperature, biomass feed rate and water flow preselects the output synthesis gas mix. The synthesis gas may be processed into portable liquid fuels, or can be used directly in a fuel cell.

대표청구항 ▼

We claim: 1. A process for converting biomass and any other organic material to useful energy gases, comprising supplying a feed of said biomass as dried, pre-heated particles to a reactor wherein said reactor is formed of a quartz glass or other refractory non-corrosible material; generating super

We claim: 1. A process for converting biomass and any other organic material to useful energy gases, comprising supplying a feed of said biomass as dried, pre-heated particles to a reactor wherein said reactor is formed of a quartz glass or other refractory non-corrosible material; generating superheated steam within said reactor; subjecting the biomass particles in a primary reaction zone in the reactor to a stream of said superheated steam having a temperature in a temperature range of sufficient temperature to cause pyrolysis of the biomass and steam under anaerobic conditions to produce production gases; passing said steam and said production gases through a secondary reforming zone within the reactor to convert any residual volatile organic compounds and said superheated steam to said energy gases, the latter including one or more of hydrogen and carbon monoxide; and adding thermal energy to said superheated steam while the superheated steam is in said secondary reaction zone. 2. The process of claim 1 wherein said superheated steam is contacted with the biomass particles at a temperature of 300° C. to 1700° C. 3. The process of claim 1 wherein said superheated steam is applied to the biomass particles while in a temperature range of 700° C. to 1700° C. 4. The process of claim 1 comprising producing said superheated steam by RF inductive heating of a susceptor in thermal contact with water vapor used to generate said superheated steam. 5. The process of claim 1 wherein the energy gases produced in the reactor exit the reactor at an elevated temperature, and such exiting energy gases are placed in thermal contact with entering water that is introduced into the reactor to produce said superheated steam. 6. The process of claim 1 comprising thermally contacting exiting energy gases with the incoming water to preheat the water by sending the exiting energy gases into a regenerative heat exchanger. 7. The process of claim 1 comprising reducing the biomass particle to energy gases and a mineral ash. 8. The process of claim 7 wherein said ash includes a salt or hydroxide of potassium. 9. The process of claim 8 further comprising processing said ash to adapt the ash to be utilized as a fertilizer. 10. The process of claim 1 comprising regulating the relative amounts of hydrogen and carbon monoxide in said energy gases by controlling the rate or water vapor input; controlling the temperature of the superheated steam; and controlling the feed rate of said biomass particles. 11. The process of claim 10 including maintaining temperature of the superheated steam, rate of water vapor input, and feed rate of said biomass particles such that volatile complex components produced in said reaction are prevented from producing high-molecular-weight pyrolysis oils. 12. The process of claim 1 comprising passing said superheated steam and said energy gases together with other product gases produced in said reactor through a counterflow stage for continued energy injection to convert said other gases into simple product gases. 13. The process of claim 1 wherein said biomass comprises a mixture of waste materials of vegetable origin. 14. The process of claim 1, wherein the process of conversion of said biomass particles and said superheated steam to said energy gases free of pyrolysis oils takes place entirely within a single reactor.