Garbage in power out (GIPO) thermal conversion process
A system for gasifying a carbonaceous feedstock, such as municipal waste, to generate power includes a devolatilization reactor that creates char from the feedstock and a gasifier that creates a product gas from both the char and from volatiles released when devolatilizing the feedstock. The product gas is reacted in a fuel cell to create electrical energy and process heat. The process heat is used to heat the devolatilization reactor and the gasifier. The gasifier comprises a plurality of configurable circuits that can each be tuned to meet the individual needs of the char material being gasified.
1. A method for processing a carbonaceous feedstock, the method comprising the steps of:
(a) providing a carbonaceous feedstock;
(b) preparing a feedstock slurry from said carbonaceous feedstock, wherein said feedstock slurry comprises between 40% and 80% water;
(c) optionally pre-heating said feedstock slurry prior to devolatilizing;
(d) devolatilizing said feedstock slurry at a pressure between 300 and 900 psia such that the water in the slurry does not flash to steam while heating at a temperature between 300 and 600 degrees F. for between 5 and 30 minutes, to generate a char slurry comprising char and between 40% and 80% water;
(e) introducing a pressure decrease in the flow of said char slurry from the devolatilization step to the gasification step, such that at least a portion of the water flashes to steam to produce a steam char slurry;
(f) subjecting said steam char slurry to gasification at a temperature between 1500 and 2000 degrees Fahrenheit, to generate a product gas comprising methane;
(g) supplying said product gas to a primary energy generator to generate mechanical or electrical power, wherein a heated fluid, either gas or liquid, is exhausted; and
(h) indirectly heating at least one of said feedstock slurry and said char slurry, utilizing said exhausted heated fluid;
wherein steps (d), (e) and (f) directly follow one another.
2. The method of claim 1 wherein indirectly heating said feedstock slurry comprises generating steam or hot water, and utilizing said steam or hot water to heat a devolatilization reactor adapted to accept the feedstock slurry.
3. The method of claim 1 wherein indirectly heating said char slurry comprises heating a gasification reactor adapted to accept said char slurry.
4. The method of claim 1 wherein indirectly heating said char slurry comprises inputting the exhaust gas into to a process air temperature booster and utilizing an output of said process air temperature booster to heat a gasification reactor adapted to accept said char slurry.
5. The method of claim 4 further comprising combusting said product gas in said process air temperature booster to heat the exhaust gas.
6. The method of claim 1 further comprising scavenging heat from said product gas, and pre-heating said feedstock slurry utilizing the scavenged heat, prior to devolatilizing said feedstock slurry.
7. The method of claim 1 wherein said primary energy generator is a fuel cell.
8. The method of claim 1 wherein said primary energy generator is selected from the group consisting of an internal combustion engine, a gas turbine and a boiler.
9. The method of claim 1 wherein said carbonaceous feedstock comprises waste selected from the group consisting of municipal waste, farm waste, food processing waste and combinations of two or more thereof.
10. The method of claim 1 , without the further addition of reagents or fluids to the process stream, with the exception of steam pressurization, and without the venting of fluids from the process stream.
11. A method for processing a carbonaceous feedstock, the method consisting of:
(a) providing a carbonaceous feedstock;
(b) preparing a feedstock slurry from said carbonaceous feedstock, wherein said feedstock slurry comprises between 40% and 80% water;
(c) optionally pre-heating said feedstock slurry prior to devolatilizing;
(d) devolatilizing said feedstock slurry at a pressure between 300 and 900 psia such that the water in the slurry does not flash to steam while heating at a temperature between 300 and 600 degrees F. for between 5 and 30 minutes, to generate a char slurry comprising char and between 40% and 80% water;
(e) introducing a pressure decrease in the flow of said char slurry from the devolatilization step to the gasification step, such that at least a portion of the water flashes to steam to produce a steam char slurry; and
(f) subjecting said steam char slurry to gasification at a temperature between 1500 and 2000 degrees Fahrenheit, to generate a product gas comprising methane.