Low temperature gasification facility with a horizontally oriented gasifier
A low-temperature gasification system comprising a horizontally oriented gasifier is provided that optimizes the extraction of gaseous molecules from carbonaceous feedstock while minimizing waste heat. The system comprises a plurality of integrated subsystems that work together to convert municipal solid waste (MSW) into electricity. The subsystems comprised by the low-temperature gasification system are: a Municipal Solid Waste Handling System; a Plastics Handling System; a Horizontally Oriented Gasifier with Lateral Transfer Units System; a Gas Reformulating System; a Heat Recycling System; a Gas Conditioning System; a Residue Conditioning System; a Gas Homogenization System and a Control System.
1. A method for the conversion of carbonaceous feedstock into gas comprising plasma reformulated gas of a defined composition, the method comprising the steps of:
a) feeding the feedstock to a first zone of a gasifier, the gasifier comprising two or more substantially laterally distributed processing zones and configured to promote, in succession, drying, volatilization and char-to-ash conversion;
b) laterally transferring the feedstock through each zone of the gasifier as a reactant material and processing the reactant material, thereby sequentially promoting drying, volatilization, char-to-ash conversion, to provide raw offgas and/or syngas; and
c) reformulating the raw off-gas and/or syngas into a gas comprising plasma reformulated gas by the application of plasma heat, the gas comprising plasma reformulated gas containing higher levels of CO and H 2 than the raw off-gas and/or syngas.
2. The method of claim 1 , comprising the step of monitoring lateral transfer of the reactant material being processed in step (b) and adjusting the rate of lateral transfer of the reactant material in response thereto.
3. The method of claim 2 , wherein monitoring the lateral transfer of the reactant material is via feedstock height sensors operatively associated with the gasifier.
4. The method of claim 1 , wherein the carbonaceous feedstock comprises a feedstock additive to adjust the amount of carbon in the reactant material.
5. The method of claim 1 , comprising imparting turbulence, countercurrent, radial, tangential, or other flow direction to the raw offgas and/or syngas gas during step c).
6. The method of claim 1 , comprising recovering heat generated in one or more of steps a) to c).
7. The method of claim 6 , comprising transferring the recovered heat to one or more of the processing zones of the gasifier.