Patent ID: 9599337
Date: 2017-03-21
CPC Classifications: B09B,C10B,C10K,F23G,Y02E

Claim:
1. A process for the treatment of solid waste provided to a processing system, said processing system comprising a reactor ( 1 ) configured to operate at a negative pressure, and having first and second chambers ( 2 and 3 ) namely a pyrolysis chamber ( 2 ) and a fusion chamber ( 3 ) for ash and inert material, respectively, said reactor ( 1 ) configured to achieve a temperature gradient of between 900° C. to 1600° C. between said first and second chambers ( 2 , 3 ), said temperature gradient provided by first and second power controlled thermal sources ( 4 and 5 ), said first power controlled thermal source ( 4 ) coupled to said pyrolysis chamber ( 2 ) and serving as a controlled thermal source for said pyrolysis chamber ( 2 ), and said second power controlled thermal source ( 5 ) coupled to said fusion chamber ( 3 ) and serving as a controlled thermal source for said fusion chamber ( 3 ), said process for the treatment of said solid waste provided to said processing system comprising: initiating the treatment of solid waste by said processing system, said step of initiating the treatment of solid waste comprising providing the solid waste to the pyrolysis chamber ( subjecting said solid waste to be treated in said pyrolysis chamber ( establishing a temperature gradient in said primary reactor ( removing said quantity of gases from the pyrolysis chamber ( directing said removed gases to a heat exchanger ( cooling said removed gases utilizing a water circulating via a pump ( condensing oil and water from said removed gases utilizing said heat exchanger ( directing said condensed oil and water by gravity to a tank ( injecting said cooled and removed gases into an alkaline water containing tank ( removing effluent gases from the alkaline water containing tank ( directing said effluent gases removed from said alkaline water containing tank ( directing said effluent gases from said activated charcoal filter ( after said fuel gases contained in said effluent gases are oxidized in said combustor (