An oxidizer head assembly includes a head body defining an inlet flange, an outlet flange, and a wall, where the inlet flange, the outlet flange, and the wall define a cavity positioned between the inlet flange and the outlet flange, a plurality of nozzles extending through the cavity, a fuel inlet in communication with the plurality of nozzles, where a fuel passes through the fuel inlet and the plurality of nozzles, a shield gas inlet in communication with the cavity, and a porous diffuser plate extending across the outlet opening, the porous diffuser plate including apertures for the plurality of nozzles and a plurality of pores, where a shield gas passes through the shield gas inlet, through the cavity, and through the plurality of pores of the porous diffuser plate around the plurality of nozzles.

A waste incinerator, in a vertical structure and including from the top down: a drying section, a destructive distillation section, a reduction section, and a combustion section. The combustion section includes: two layers of grate bars, a first combustion layer, a second combustion layer, and a third combustion layer. The heat produced from the combustion in the combustion section is used to heat the carbide in the reduction section. The heated carbide reduces CO.sub.2 produced in the combustion into CO (coal gas). The coal gas ascends to the destructive distillation section through the ambient coal gas chamber to heat and destructively distillate the waste to produce the pyrogenic coal gas and the carbide. The carbide drops to the combustion section for combustion, and the pyrogenic coal gas and the coal gas are collected by the draft fan.

A nonflammable burner includes a can with holes in its sidewalls and bottom. Hollow legs are coupled to the bottom of the can. Each hollow leg has an open end in fluid communication with an interior of the can with perforations in each hollow leg providing fluid communication with an interior of the hollow leg such that each hollow leg provides fluid communication between an ambient environment and the interior of the can. A tray is positioned on a ground surface and engages with the hollow legs wherein the bottom of the can is spaced apart from the tray. Open-ended conduits extend between the sidewalls of the can to provide a fluid flow path there through. Each conduit admits the ambient environment therein, and includes perforations for providing fluid communication between the fluid flow path and the interior of the can.

A combustion chamber has an internally hollow tank containing biomass to be combusted and gasified, an air supply to supply air inside the tank, a gas supply connected to a gas source to supply gas inside the tank, and valve or valves electrically connected to the control to control the air flow and the gas flow inside the tank.

An oxidizer head assembly includes a head body defining an inlet flange, an outlet flange, and a wall, where the inlet flange, the outlet flange, and the wall define a cavity positioned between the inlet flange and the outlet flange, a plurality of nozzles extending through the cavity, a fuel inlet in communication with the plurality of nozzles, where a fuel passes through the fuel inlet and the plurality of nozzles, a shield gas inlet in communication with the cavity, and a porous diffuser plate extending across the outlet opening, the porous diffuser plate including apertures for the plurality of nozzles and a plurality of pores, where a shield gas passes through the shield gas inlet, through the cavity, and through the plurality of pores of the porous diffuser plate around the plurality of nozzles.

A process for carbonization and pyrolyzation of hydrocarbons containing, non-fluid materials is characterized by a continuous plug stream in shafts within a refractory structure. Within the shafts, the materials are heated by the hot inner surface of the shafts without air admitted to enter the shafts. Furthermore, the developing pyrolyze gas is led directly to combustion channels around the carbonization shafts within the refractory structure where a controlled amount of air or oxygen is added, partially combusting the gas, providing the heat for the process. Aim of the process is to convert different waste streams into reusable elements without CO2 emissions, to take away hazardous materials, to produce syngas, to extract hydrogen and to create a carbon rich residue fit for mining of, among others, metals, CaO and phosphor.

Disclosed is an apparatus for combusting recyclable or waste material. The apparatus comprises a cylindrical combustion chamber. The chamber comprises a first inlet in a side wall. The first inlet is in communication with a blower and an ignition means. The chamber also comprises a second inlet in a first end wall or a side wall. The second inlet is in communication with a source of recyclable or waste material. The chamber also comprises an outlet in a second end wall on a central axis of the chamber. The longitudinal axis of the first inlet is offset from the central axis of the chamber. In use, the blower forces the recyclable or waste material to circulate around the inside of the chamber.

A combustion chamber has an internally hollow tank containing biomass to be combusted and gasified, an air supply to supply air inside the tank, a gas supply connected to a gas source to supply gas inside the tank, and valve or valves electrically connected to the control to control the air flow and the gas flow inside the tank.

A method and system for the conversion of waste into energy in a sealed system where combustion does not take place and the operating pressure prior to the inlet of the steam or power generating equipment is maintained below atmospheric pressure. Destruction of the RDF (refuse derived fuel) is accomplished by subjecting the RDF to a high temperature environment under controlled conditions in a purpose designed and built reactor. The high temperature environment, <5000 C., is achieved through the use of one or more non-transferred plasma torches for generation of plasma gas. The plasma gas exiting the torch and provides the thermal energy for the continual gasification of metallurgic coke configured as a carbon bed in the lower part of the reactor, which acts as a thermal catalyst and this provides the thermal energy for the gasification process.

Briefly, the invention provides an incinerator comprising a housing suspended above the ground. The housing is without a top or bottom, but includes an elongated member supporting the housing and a grate intermediate of the housing and the elongated member. Also provided is a device for aiding combustion reactions. The device includes a vertically disposed stanchion, a housing, a first open end and a second open end. The housing is supported at the second open end by the stanchion. The device also include a grid with a cross section identical to the cross section of the housing. The diameter of the cross section of the grid is less than the diameter of the cross section of the housing and the grid in rotates around the stanchion.