Method of producing high value chemicals from feedstock, wherein the feedstock is waste material or comprises waste material. A fluidised reactor system is provided comprising a pyrolysis chamber (2) and combustion chamber (12). The feedstock is input into the pyrolysis chamber and a pyrolysis process is executed at a temperature in the range of from 650 to 850 C. to obtain a product gas comprising high value chemicals.

Method of producing high value chemicals from feedstock, wherein the feedstock is waste material or comprises waste material. A fluidised reactor system is provided comprising a pyrolysis chamber (2) and combustion chamber (12). The feedstock is input into the pyrolysis chamber and a pyrolysis process is executed at a temperature in the range of from 650 to 850 C. to obtain a product gas comprising high value chemicals.

A carbonized solid agglomerate for use in a blast furnace, comprising in its composition: at least one source of carbon (10); at least one source of calcium (11); and at least one binder (12); wherein, after mechanical shaping (200) of the solid agglomerate, the agglomerate is subjected to a pyrolyzing step (400) at a temperature greater than or equal to 600 C. and less than 800 C.; wherein the solid agglomerate comprises 25 to 35% by mass of the at least one source of calcium (11). A method for manufacturing the proposed solid agglomerate.

A carbonized solid agglomerate for use in a blast furnace, comprising in its composition: at least one source of carbon (10); at least one source of calcium (11); and at least one binder (12); wherein, after mechanical shaping (200) of the solid agglomerate, the agglomerate is subjected to a pyrolyzing step (400) at a temperature greater than or equal to 600 C. and less than 800 C.; wherein the solid agglomerate comprises 25 to 35% by mass of the at least one source of calcium (11). A method for manufacturing the proposed solid agglomerate.

Mixture products containing charred products and coal or coke, and associated systems, devices and methods are disclosed herein. The charred product components of the mixture products can be made by receiving an input material in an oven, and heating the oven containing the input material to a predetermined temperature of at least 900 F. for a predetermined time of no more than 48 hours to produce a charred product. Advantageously, embodiments of the present technology can enable a more efficient mixture product production process. The resulting mixture products can also have higher quality in terms of desired Coke Strength After Reaction (CSR), Coke Reactivity Index (CRI), volatile matter content, ash content, sulfur content, grain size, etc.

Mixture products containing charred products and coal or coke, and associated systems, devices and methods are disclosed herein. The charred product components of the mixture products can be made by receiving an input material in an oven, and heating the oven containing the input material to a predetermined temperature of at least 900 F. for a predetermined time of no more than 48 hours to produce a charred product. Advantageously, embodiments of the present technology can enable a more efficient mixture product production process. The resulting mixture products can also have higher quality in terms of desired Coke Strength After Reaction (CSR), Coke Reactivity Index (CRI), volatile matter content, ash content, sulfur content, grain size, etc.

A system and process for the resultant gas constituent-controlled gasification of a carbonaceous feedstock uses feedback loop-controlled pyrolysis to produce a stable and predictable gas product from a variable or unknown feedstock, such as MSW, that may include methane, ethane, and other desirable hydrocarbon gases, and a solid product, that includes activated Carbon or Carbon.

A system and process for the resultant gas constituent-controlled gasification of a carbonaceous feedstock uses feedback loop-controlled pyrolysis to produce a stable and predictable gas product from a variable or unknown feedstock, such as MSW, that may include methane, ethane, and other desirable hydrocarbon gases, and a solid product, that includes activated Carbon or Carbon.

A method for processing a plastic-derived oil may comprise contacting the plastic-derived oil with a catalyst to crack the plastic-derived oil to form a hydrocarbon product. The catalyst may comprise a metal oxide-loaded ZSM-5 zeolite comprising: ZSM-5 particles having a size of less than 100 nm, and one or more metal oxides chosen from iron oxide, lanthanum oxide, and cerium oxide. The one or more metal oxides may be disposed on the ZSM-5 particles.

A method for processing a plastic-derived oil may comprise contacting the plastic-derived oil with a catalyst to crack the plastic-derived oil to form a hydrocarbon product. The catalyst may comprise a metal oxide-loaded ZSM-5 zeolite comprising: ZSM-5 particles having a size of less than 100 nm, and one or more metal oxides chosen from iron oxide, lanthanum oxide, and cerium oxide. The one or more metal oxides may be disposed on the ZSM-5 particles.