Feedstock Processing Systems And Methods For Producing Fischer-Tropsch Liquids And Transportation Fuels

Abstract

A method for processing feedstock is described, characterized in that incoming feedstock is processed to selectively recover biogenic carbon material from the incoming feedstock. In some embodiments the incoming feedstock is comprised of mixed solid waste, such as municipal solid waste (MSW). In other embodiments the incoming feedstock is comprised of woody biomass. In some instances, the incoming feedstock is processed to selectively recover biogenic carbon material from the incoming feedstock to produce a processed feedstock having biogenic carbon content of 50% and greater suitable for conversion into biogenic carbon Fischer Tropsch liquids. The high biogenic carbon Fischer Tropsch liquids may be upgraded to biogenic carbon liquid fuels. Alternatively, the incoming feedstock is processed to selectively recover plastic material from the incoming feedstock to produce a processed feedstock having biogenic carbon content of 50% or less.

1 . A system for producing syngas from processed feedstock, comprising:
 a feedstock processing system configured to process incoming feedstock to selectively recover carbon material from the incoming feedstock, the feedstock processing system comprising:
 a sorting station configured to separate the incoming feedstock into a first stream containing mixed solid waste material having a predetermined size and larger, and a second stream containing mixed solid waste material having the predetermined size and smaller; 
 a first commination unit in communication with the sorting station and configured to comminute the first stream to produce an output stream containing mixed solid waste having the predetermined size and smaller, and combine the output stream and the second stream to produce a combined stream; 
 a fractionation unit in communication with the commination unit and configured to fractionate the combined stream by size to remove small size, low carbon content material having a size of 2 inches and smaller from high carbon content material; 
 a fine fractionation density unit in communication with the fractionation unit and configured to further fractionate the high carbon content material to remove inert material to produce a carbonaceous material stream; 
 a ferrous removal unit in communication with the fine fractionation density unit configured to remove ferrous material from the carbonaceous material stream; 
 a non-ferrous removal unit in communication with the ferrous removal unit and configured to remove non-ferrous material from the carbonaceous material stream; 
 a plastic removal unit in communication with the non-ferrous removal unit and configured to remove plastic material from the carbonaceous material stream; 
 a second commination unit in communication with the plastic removal unit and configured to comminute the carbonaceous material stream to produce an output stream containing carbonaceous material having a size of 1 inch and smaller; and 
 a drying unit in communication with the second commination unit and configured to dry the output stream to produce a processed feedstock containing carbonaceous material and a moisture content in the range of 8% to 15%; and 
 a bio-refinery including a gasification island configured to receive the processed feedstock from the feedstock processing system and convert the processed feedstock to syngas. 
   
     
     
         2 . The system of  claim 1 , wherein the incoming feedstock is comprised of mixed solid waste. 
     
     
         3 . The system of  claim 1 , wherein in the incoming feedstock is comprised of woody biomass. 
     
     
         4 . The system of  claim 1 , wherein the mixed solid waste is municipal solid waste (MSW). 
     
     
         5 . The system of  claim 1 , wherein the at least a portion of non-biogenic carbons and non-carbonaceous materials comprises dirt, glass, wet organics, and other inerts. 
     
     
         6 . The system of  claim 1 , wherein the incoming feedstock is processed to selectively recovery biogenic carbon material from the incoming feedstock to produce a processed feedstock having high biogenic carbon content suitable for conversion into high biogenic carbon Fischer Tropsch liquids. 
     
     
         7 . The system of  claim 6 , wherein the high biogenic carbon Fischer Tropsch liquids are upgraded to high biogenic carbon liquid fuels. 
     
     
         8 . The system of  claim 1 , wherein the ferrous removal unit comprises magnetic separators. 
     
     
         9 . The system of  claim 1 , further comprising an anaerobic digester station comprising one or more anaerobic digesters, used to digest sewage biosolids, low solids or screened animal manure, and low suspended solids or high soluble solids as in anaerobic filters or upflow sludge blanket digesters. 
     
     
         10 . The system of  claim 1 , wherein the processed feedstock contains up to 50% biogenic carbon content. 
     
     
         11 . The system of  claim 1 , wherein the processed feedstock contains biogenic carbon content in a range of 50% to 100%. 
     
     
         12 . The system of  claim 1 , wherein the processed feedstock contains 51% and greater biogenic carbon content. 
     
     
         13 . The system of  claim 1 , wherein the sorting station comprises a trommel. 
     
     
         14 . The system of  claim 1 , wherein the first commination unit comprises a shredder with a shredder opening in a range of 6-15 inches. 
     
     
         15 . The system of  claim 1 , wherein the fractionation unit comprises a vibratory screen, and where the 2 inch and smaller fraction is removed for further fractionation into an inert low biogenic carbon material and a high biogenic content material. 
     
     
         16 . The system of  claim 1 , wherein the fractionation unit further comprises an air separator wherein a heavy fraction is separated from a light fraction by differences in density. 
     
     
         17 . The system of  claim 16 , wherein the heavy fraction from the air separator is further fractionated in another air separator wherein the heavy fraction is further separated into a medium fraction and a heavy-heavy fraction by differences in density. 
     
     
         18 . The system of  claim 17 , wherein the heavy-heavy fraction is removed as inert low biogenic material. 
     
     
         19 . The system of  claim 18 , wherein the light fraction is combined with the medium fraction and the combined stream is sent to the ferrous removal unit. 
     
     
         20 . The system of  claim 19 , wherein the fine fractionation density unit is configured to fractionate the heavy fraction through a vibratory screen to remove non-carbonaceous (i.e. inert) material having a size of 1 inch and smaller. 
     
     
         21 . The system of  claim 20 , wherein the light fraction, medium fraction and heavy fraction are combined to produce a combined fraction stream and then passed to the non-ferrous removal unit, the non-ferrous removal unit comprising an eddy current configured to remove non-ferrous material. 
     
     
         22 . The system of  claim 21 , wherein the combined fraction stream is passed to the plastic removal unit, the plastic removal unit comprising an optical sorter configured to remove at least a portion of plastic content in the combined fraction stream, to produce a processed feedstock. 
     
     
         23 . The system of  claim 22 , wherein the plastic content in the combined fraction stream is selectively removed such that processed feedstock has a biogenic carbon content of up to 95%. 
     
     
         24 . The system of  claim 22 , wherein the plastic content in the combined fraction stream is selectively removed such that processed feedstock has a biogenic carbon content of up to 50%. 
     
     
         25 . The system of  claim 22 , wherein the plastic content in the combined fraction stream is selectively removed such that processed feedstock has a biogenic carbon content of 51% and greater. 
     
     
         26 . The system of  claim 22 , wherein the plastic content in the combined fraction stream is selectively removed such that processed feedstock has a biogenic carbon content between 50% and to 100%. 
     
     
         27 . The system of  claim 1 , wherein the bio-refinery further comprises:
 a Fischer-Tropsch reactor configured to receive the syngas from the gasification island and convert the syngas into Fischer-Tropsch liquids.   
     
     
         28 . The system of  claim 1 , further comprising:
 an upgrading system configured to upgrade the Fischer-Tropsch liquids to transportation fuels.