Orange County NC Website
Figure B-9~ EnTechU»rocess <br />As shown in Figure B-9, 4SN is classified by combination bag breaker and gravity <br />separator process, termed a Kinetic Streamer. Oversize materials, which are <br />basically inorganic,are directed either to a plastics pecyder or a non-plastics etics <br />recycling station, while the majority of waste (presumably organic) is directed to <br />dryer to remove entrained moisture. The dryer utilizes the latent heat inherent in <br />and <br />the organic content of the waste to produce the heat necessary for to drive the <br />nn <br />gasification process. The syngas can be fired in e waste heat boiler r e <br />subsequent electric power production. <br />1~2.2 Pyrolysis <br />In pyrolysis, an organic waste (MSW) is heated without <br />oxygen (or air), similar to <br />the generation of coke from coal orcharcoal from wood. Both a char and a gas are <br />generated. The gas isburned out in e gaseous phase, requiring much less oxygen <br />than incineration. The char will usually melt at the temperatures within the pyrolysis <br />chamber and ||| b discharged along with a black gravel-like substance, termed frit' <br />n i the |ao� of air entering the chamber and the <br />Advantages of this process one <br />resulting smaller size of system components. Without air ' there is little nitrogen <br />have a h�en many <br />oxide generation and low particulate /sooO formation. . There e <br />attempts to develop this technology outside ^ 'a laboratory or a pilot plant. In full- <br />scale demonstrations in the 1870s, it Was difficult to maintain a sealed chamber to <br />keep air out and waste variability creates problems in maintaining consistent <br />operation, ~~ When the pyrolysis gas is fired in a combustion chamber that is part of <br />the system, the system is classified as an incinerator. <br />As shown in Figure B-10" MSVV is shred into a uniform size capable of feeding into the thermal converter, or pyrolysis chamber. The pyrolysis gas generated is fired in <br />a secondary combustion chamber, or th e ma| oxidizer, and passes through a waste <br />heat boiler for heat recovery. Char drops out the bottom of the pyrolysis chamber <br />for disposal or further processing for recovery of metals and other constituents. <br />Although this system is marketed as a pyrolysis system, a combustion chamber is <br />necessary for its operation (for destroying organics in the off-gas) and the presence <br />of this chamber classifies the system asanincinerator. <br />`1Souroe: Entach. <br />GBB/C08027-01 B-12 August 15, 2008 <br />Water <br />Dried <br />organic <br />organic <br />< <br />6[ <br />R si <br />si u <br />Syngas <br />Kinetic <br />Dryer <br />Gasifier <br />Streamer <br />Solid <br />Residue <br />Figure B-9~ EnTechU»rocess <br />As shown in Figure B-9, 4SN is classified by combination bag breaker and gravity <br />separator process, termed a Kinetic Streamer. Oversize materials, which are <br />basically inorganic,are directed either to a plastics pecyder or a non-plastics etics <br />recycling station, while the majority of waste (presumably organic) is directed to <br />dryer to remove entrained moisture. The dryer utilizes the latent heat inherent in <br />and <br />the organic content of the waste to produce the heat necessary for to drive the <br />nn <br />gasification process. The syngas can be fired in e waste heat boiler r e <br />subsequent electric power production. <br />1~2.2 Pyrolysis <br />In pyrolysis, an organic waste (MSW) is heated without <br />oxygen (or air), similar to <br />the generation of coke from coal orcharcoal from wood. Both a char and a gas are <br />generated. The gas isburned out in e gaseous phase, requiring much less oxygen <br />than incineration. The char will usually melt at the temperatures within the pyrolysis <br />chamber and ||| b discharged along with a black gravel-like substance, termed frit' <br />n i the |ao� of air entering the chamber and the <br />Advantages of this process one <br />resulting smaller size of system components. Without air ' there is little nitrogen <br />have a h�en many <br />oxide generation and low particulate /sooO formation. . There e <br />attempts to develop this technology outside ^ 'a laboratory or a pilot plant. In full- <br />scale demonstrations in the 1870s, it Was difficult to maintain a sealed chamber to <br />keep air out and waste variability creates problems in maintaining consistent <br />operation, ~~ When the pyrolysis gas is fired in a combustion chamber that is part of <br />the system, the system is classified as an incinerator. <br />As shown in Figure B-10" MSVV is shred into a uniform size capable of feeding into the thermal converter, or pyrolysis chamber. The pyrolysis gas generated is fired in <br />a secondary combustion chamber, or th e ma| oxidizer, and passes through a waste <br />heat boiler for heat recovery. Char drops out the bottom of the pyrolysis chamber <br />for disposal or further processing for recovery of metals and other constituents. <br />Although this system is marketed as a pyrolysis system, a combustion chamber is <br />necessary for its operation (for destroying organics in the off-gas) and the presence <br />of this chamber classifies the system asanincinerator. <br />`1Souroe: Entach. <br />GBB/C08027-01 B-12 August 15, 2008 <br />