A system and process for producing synthetic gas from solid fuel comprising waste material, municipal solid waste or biomass, and for upgrading the synthetic gas produced. The system and process utilizes a first thermal chamber having a gasification zone in which a fuel stream is gasified by thermal oxidation to produce a first synthetic gas stream and heat; a pyrolysis reactor housed within the first thermal chamber where fuel undergoes pyrolysis to produce a second synthetic gas stream; and a thermal catalytic reactor comprising a second thermal chamber having a catalyst chamber within with a selected catalyst. The first synthetic gas stream is completely thermally oxidized to produce high temperature flue gas that imparts heat to the catalyst chamber in which the second synthetic gas stream is thermally cracked and directed over the catalyst to yield a finished gas or liquid product having a desired chemical composition as determined by the selected catalyst.

A method for the treatment of polymeric and/or organic waste using a heat-resistant process container provided with a valve and filled with prepared waste and which is closed in a gas-tight manner. The container is moved with the waste into a process furnace for thermal treatment. The waste is degassed therein via the valve during the thermal treatment, and immediately after degassing, the heated process container is moved from the process furnace into a cooling chamber in which the residual heat is removed from the process container and stored in a thermal storage. After cooling, the process container is removed from the cooling chamber and the contents of the process container are emptied into a separating device.

A method for the treatment of polymeric and/or organic waste using a heat-resistant process container provided with a valve and filled with prepared waste and which is closed in a gas-tight manner. The container is moved with the waste into a process furnace for thermal treatment. The waste is degassed therein via the valve during the thermal treatment, and immediately after degassing, the heated process container is moved from the process furnace into a cooling chamber in which the residual heat is removed from the process container and stored in a thermal storage. After cooling, the process container is removed from the cooling chamber and the contents of the process container are emptied into a separating device.

The pyrolysis reactor system for the conversion and analysis of organic solid waste is a dual gas-liquid separation system, allowing for the conversion of organic solid waste, as well as analysis of the conversion products. A pyrolysis reactor is provided for converting the organic solid waste into a solid product and a gas-liquid product mixture through pyrolysis. A source of carrier gas is in fluid communication with the pyrolysis reactor for degrading the organic solid waste. A first gas-liquid separator is in fluid communication with the pyrolysis reactor and receives the gas-liquid product mixture therefrom, separating a portion of gas therefrom. A second gas-liquid separator is in fluid communication with the first gas-liquid separator and receives the gas-liquid product mixture therefrom and separates the remainder of the gas therefrom. The remainder of the gas and the separated liquid are each collected separately from one another, in addition to the char.

The pyrolysis reactor system for the conversion and analysis of organic solid waste is a dual gas-liquid separation system, allowing for the conversion of organic solid waste, as well as analysis of the conversion products. A pyrolysis reactor is provided for converting the organic solid waste into a solid product and a gas-liquid product mixture through pyrolysis. A source of carrier gas is in fluid communication with the pyrolysis reactor for degrading the organic solid waste. A first gas-liquid separator is in fluid communication with the pyrolysis reactor and receives the gas-liquid product mixture therefrom, separating a portion of gas therefrom. A second gas-liquid separator is in fluid communication with the first gas-liquid separator and receives the gas-liquid product mixture therefrom and separates the remainder of the gas therefrom. The remainder of the gas and the separated liquid are each collected separately from one another, in addition to the char.

Systems and methods for heating material through cogeneration of thermal and electrical energy can include a heat source and an electric generator configured to produce hot exhaust gas and electricity. One or more heating conduits can carry the hot exhaust gas to one or more bodies of material. The electric generator can at least partially power one or more electric heaters configured to reheat the hot exhaust gas after a portion of heat has been transferred from the hot exhaust gas to the one or more bodies of material.

Processes and systems for olefin and diluent recovery utilizing one or more side columns, including a side rectifier column and/or a side degassing column, in combination with a heavies column.

Processes and systems for olefin and diluent recovery utilizing one or more side columns, including a side rectifier column and/or a side degassing column, in combination with a heavies column.

System and method for processing pyrolyzable materials in order to recover usable end products are disclosed. The pyrolysis process comprises a number of stages. First pre-treating is to reduce moisture content to approximately 15%. Second is to optimize the volatile organic under the heat and vacuum. This treatment stage is carried out at the temperature between 350 to 400 C. Next, the material is treated with heat and vacuum to produce hot gas and solid carbon residue. This stage is carried out at the temperature up to 800 C. The solid carbon residue can be separated from the hot gas, the volatile organic materials condensed to produce liquid hydrocarbon and gas products. Pyrolysis processes and system according to the present invention are able to thermally decompose carbon-containing materials, including, but not limited to, tires and other rubber-containing materials, hydrocarbon-containing products including pyrolysis oil, used oil and lubricants, organic wastes and alike, carbon containing minerals like brown and bituminous coal, oil shale and oil bearing schists. System and pyrolysis methods according to aspects of the present invention may be successful on a commercial scale.

A method of gasifying carbonaceous material is described. The method comprises a first step of pyrolyzing and partially gasifying the carbonaceous material to produce volatiles and char. The volatiles and the char are then separated and, subsequently, the char is gasified and the volatiles are reformed. The raw product gas is then finally cleaned with char or char-supported catalysts or other catalysts.