Systems and methods for gasification of carbonaceous materials

Abstract

Carbonaceous-containing material including biomass, municipal solid waste, and/or coal and/or contaminated soil, and/or other carbonaceous materials may be gasified at low temperatures utilizing a reactor designed to generate shockwaves in a supersonic gaseous vortex. Preprocessed waste may be introduced into the reactor. A gas stream may be introduced substantially tangentially to an inner surface of a chamber of the reactor to generate a gaseous vortex rotating about a longitudinal axis within the chamber. The gas stream may be introduced using a nozzle that accelerates the gas stream to a supersonic velocity, and may impinge on an impactor positioned within the reactor chamber. A frequency of shockwaves emitted from the nozzle into the gaseous vortex may be controlled. The processed waste discharged from the reactor, which may include a gas component and at least a solid component, can be subjected to separation, and at least some of the gas component and at least one solid component (i.e., tars) may be fed back to the feeding device so that the solids from the processed waste condense on preprocessed waste contained in the feeding device and are reprocessed within the reactor. The gas component from the feeding device may be cleaned after the solids have been condensed out in the feeding device.

1 . A system configured for carbonaceous-containing material gasification at low temperatures utilizing a reactor designed to generate shockwaves in a supersonic gaseous vortex, the system comprising:
 a feeding device configured to introduce carbonaceous-containing material into a higher-pressure region from a lower-pressure region;   a reactor configured to pulverize and gasify carbonaceous-containing material received from the feeding device, the reactor including:   a chamber having an internal surface that is substantially axially symmetrical about a longitudinal axis;   a material inlet disposed at a first end of the chamber and configured to introduce carbonaceous-containing material into the chamber configured to introduce carbonaceous-containing material into the chamber;   a gas inlet disposed proximate to the material inlet and arranged to introduce a gas stream substantially tangentially to the internal surface of the chamber to generate a gaseous vortex rotating about the longitudinal axis within the chamber, the gas inlet comprising a nozzle configured to accelerate the gas stream to a supersonic velocity to thereby generate shockwaves in the stream of gas from the nozzle, and to introduce the gas stream to the chamber at a temperature of less than about 700° C.; and   an outlet disposed on the longitudinal axis at a second end of the chamber substantially opposite the first end, the outlet configured to discharge processed material from the chamber, the processed material comprising at least a gas component and at least one solid component;   a gas/solid separator configured to receive the processed material from the reactor and separate the gas component and at least one solid component, and   a gas cleanup unit configured to receive the gas component of the processed material, clean the gas component, and output clean gas.   
     
     
         2 . The system of  claim 1 , wherein the carbonaceous-containing material is preprocessed biomass selected from the group consisting of wood, wood products, wood waste, paper, cardboard, cellulose-based materials, and mixtures thereof. 
     
     
         3 . The system of  claim 2 , wherein the preprocessed biomass is contaminated with one or more of glass, stone, brick, ceramic material, or metals. 
     
     
         4 . The system of  claim 1 , wherein the carbonaceous-containing material is municipal solid waste selected from the group consisting of biodegradable waste, recyclable material, inert waste, electrical and electronic waste, composite waste, hazardous waste, toxic waste, medical waste, and mixtures thereof. 
     
     
         5 . The system of  claim 1 , wherein the nozzle is configured to adjustably control a frequency of shockwaves emitted from the nozzle into the gaseous vortex to optimize pulverization and/or gasification of the carbonaceous-containing material introduced into the chamber of the reactor. 
     
     
         6 . (canceled) 
     
     
         7 . (canceled) 
     
     
         8 . (canceled) 
     
     
         9 . (canceled) 
     
     
         10 . (canceled) 
     
     
         11 . The system of  claim 1 , wherein the gas stream introduced by the gas inlet into the chamber of the reactor has a temperature of less than about 500° C. 
     
     
         12 . The system of  claim 11 , wherein the system is configured to completely gasify of the carbonaceous-containing material with the gas stream introduced by the gas inlet into the chamber of the reactor at a temperature of less than about 500° C. 
     
     
         13 . The system of  claim 1 , wherein the gas stream introduced by the gas inlet into the chamber of the reactor has a temperature that is low enough such that any glass contaminants in the carbonaceous-containing material will not soften. 
     
     
         14 . The system of  claim 1 , wherein the carbonaceous-containing material is biomass, wherein the outlet of the reactor is configured to discharge dirty syngas from the chamber, the dirty syngas including a gas component, tars, and biochar, wherein the gas/solid separator is configured to receive the dirty syngas from the reactor and separate the gas component and tars from the biochar of the dirty syngas, wherein the gas component and tars are fed back to the feeding device so that the tars from the syngas condense on preprocessed biomass contained in the feeding device and are reprocessed within the reactor; and wherein the gas cleanup unit is configured to receive the gas component of the syngas from the feeding device after the tars have been condensed out in the feeding device, the gas cleanup unit being further configured to clean the gas component and output clean gas. 
     
     
         15 . The system of  claim 14 , wherein the gas component and tars are fed back to the feeding device via a heated conduit to prevent condensation of the tars prior to reaching the feeding device. 
     
     
         16 . The system of  claim 14 , wherein the gas/solid separator is selected from the group consisting of a cyclone, a bag house, a spray tower, a venturi scrubber, or mixtures thereof. 
     
     
         17 . (canceled) 
     
     
         18 . The system of  claim 14 , wherein the gas cleanup unit cleans the gas component of the syngas passed through the feeding device by one or more processes selected from the group consisting of dust collection; a dry and wet process for removing gaseous pollutants; separating heavy metals; abating acid gases, dioxins and/or furans; abating carbonyls and/or other related byproducts, and mixtures thereof. 
     
     
         19 . The system of  claim 1 , wherein the carbonaceous-containing material is municipal solid waste, wherein the system further comprises: (a) a sorting apparatus configured to facilitate sorting of municipal solid waste to remove metal components from the municipal solid waste; (b) a preprocessing unit configured to preprocess the sorted municipal solid waste by reducing a size of individual pieces of the sorted municipal solid waste; and (c) a conveying chamber configured to introduce preprocessed municipal solid waste into a reactor, the conveying chamber being pressurized with waste gas or process gas to a pressure compatible with the reactor, wherein the outlet of the reactor is configured to discharge a mixture of gas and ash from the reactor, wherein the gas/solid separator is configured to receive the gas and ash from the reactor and separate product gas from the ash, and wherein the gas cleanup unit is configured to receive the receive the product gas, clean the product gas and output clean gas. 
     
     
         20 . The system of  claim 19 , wherein the product gas is fed back to the feeding device so that any tars in the product gas are condensed on preprocessed municipal solid waste contained in the feeding device and are reprocessed within the reactor. 
     
     
         21 . The system of  claim 20 , wherein the product gas is fed back to the feeding device via a heated conduit to prevent condensation of any tars prior to reaching the feeding device. 
     
     
         22 . The system of  claim 19 , wherein the gas/solid separator is selected from the group consisting of a cyclone, a bag house, a spray tower, a venturi scrubber, or mixtures thereof. 
     
     
         23 . The system of  claim 19 , wherein the gas cleanup unit cleans the product gas by one or more processes selected from the group consisting of dust collection; a dry and wet process for removing gaseous pollutants; separating heavy metals; abating acid gases, dioxins and/or furans; abating carbonyls and/or other related byproducts, and mixtures thereof. 
     
     
         24 . A method for waste gasification at low temperatures utilizing the system of  claim 1 , the method comprising:
 introducing carbonaceous-containing material using a feeding device into the reactor;   introducing a gas stream at a temperature of less than about 700° C. substantially tangentially to the internal surface of the chamber to generate a gaseous vortex rotating about the longitudinal axis within the chamber, the gas stream being introduced via the gas inlet disposed proximate to the material inlet, the gas inlet comprising a nozzle that accelerates the gas stream to a supersonic velocity;   controlling a frequency of shockwaves emitted from the nozzle into the gaseous vortex;   discharging processed material from the chamber of the reactor via the outlet;   separating the gas component and at least one solid component using the gas/solid separator;   cleaning the gas component; and   outputting clean gas.   
     
     
         25 . (canceled) 
     
     
         26 . (canceled) 
     
     
         27 . The method of  claim 24 , further comprising heating the gas stream to a temperature of less than about 500° C. prior to introducing the gas steam to the chamber of the reactor. 
     
     
         28 . The method of  claim 24 , wherein the carbonaceous-containing material is biomass, and wherein the discharging, separating, and cleaning processes comprise:
 discharging dirty syngas from the chamber of the reactor via an outlet disposed on the longitudinal axis at a second end of the chamber opposite from the first end, the dirty syngas including a gas component, tars, and biochar;   separating the gas component and tars from the biochar of the dirty syngas using a gas/solid separator;   feeding back the gas component and tars to the feeding device so that the tars from the syngas condense on preprocessed biomass contained in the feeding device and are reprocessed within the reactor; and   cleaning the gas component of the syngas from the feeding device after the tars have been condensed out in the feeding device.   
     
     
         29 . (canceled)