A pyrolysis method and a pyrolysis reactor for recovering silica from a polymer waste material containing silica, particularly a rubber or plastics waste material containing silica, using thermal decomposition for separating silica from at least one non-silica component of the polymer waste material, are disclosed. The waste material is delivered to a pyrolytic chamber, and heated to a decomposition temperature of at least one non-silica component of the waste materiel by microwave radiation. The decomposition temperature is selected such that the at least one non-silica component includes a higher microwave absorptivity than silica.

A pyrolysis method and a pyrolysis reactor for recovering silica from a polymer waste material containing silica, particularly a rubber or plastics waste material containing silica, using thermal decomposition for separating silica from at least one non-silica component of the polymer waste material, are disclosed. The waste material is delivered to a pyrolytic chamber, and heated to a decomposition temperature of at least one non-silica component of the waste materiel by microwave radiation. The decomposition temperature is selected such that the at least one non-silica component includes a higher microwave absorptivity than silica.

Methods and apparatus for compact and easily maintainable waste reformation. Some embodiments include a rotary oven reformer adapted and configured to provide synthesis gas from organic waste. Some embodiments include a rotary oven with simplified operation both as to reformation of the waste, usage of the synthesized gas and other products, and easy removal of the finished waste products, preferably in a unit of compact size for use in austere settings. Yet other embodiments include Fischer-Tropsch reactors of synthesized gas. Some of these reactors include heat exchanging assemblies that provide self-cleaning effects, efficient utilization of waste heat, and ease of cleaning.

Methods and apparatus for compact and easily maintainable waste reformation. Some embodiments include a rotary oven reformer adapted and configured to provide synthesis gas from organic waste. Some embodiments include a rotary oven with simplified operation both as to reformation of the waste, usage of the synthesized gas and other products, and easy removal of the finished waste products, preferably in a unit of compact size for use in austere settings. Yet other embodiments include Fischer-Tropsch reactors of synthesized gas. Some of these reactors include heat exchanging assemblies that provide self-cleaning effects, efficient utilization of waste heat, and ease of cleaning.

An organic matter degradation device has a reaction chamber which sidewall includes at least one energy resonance/reflection/storage unit made of an infrared material. An excess heat energy of each degradation is reflected by the infrared material, and the excess heat energy and a heat energy radiated from the infrared material propagate to the non-degraded organic matter in the housing space of the reaction chamber, again, so as to continue the degradation of the organic matter. The organic matter degradation device has active heat radiation to present main advantages of uniform heat effect, low energy consumption and fast degradation time. The heat energy is accumulated after several times, and thus the degradation of the organic matter continues without using the initial heating device to continuously provide the subsequent heat energy. The present disclosure further provides an organic matter degradation method.

An organic matter degradation device has a reaction chamber which sidewall includes at least one energy resonance/reflection/storage unit made of an infrared material. An excess heat energy of each degradation is reflected by the infrared material, and the excess heat energy and a heat energy radiated from the infrared material propagate to the non-degraded organic matter in the housing space of the reaction chamber, again, so as to continue the degradation of the organic matter. The organic matter degradation device has active heat radiation to present main advantages of uniform heat effect, low energy consumption and fast degradation time. The heat energy is accumulated after several times, and thus the degradation of the organic matter continues without using the initial heating device to continuously provide the subsequent heat energy. The present disclosure further provides an organic matter degradation method.

The present disclosure relates to a method of producing metallurgical coke from a combination of non-coking and non-metallic carbon-based microwave susceptor. The method is energy efficient, economical, and environmentally friendly. The present disclosure also relates to metallurgical coke having improved coke quality, such as improved coke strength after reaction.

The present disclosure relates to a method of producing metallurgical coke from a combination of non-coking and non-metallic carbon-based microwave susceptor. The method is energy efficient, economical, and environmentally friendly. The present disclosure also relates to metallurgical coke having improved coke quality, such as improved coke strength after reaction.

A system for processing rubber material pre-heats the material and then applies microwave energy to process the system The system comprising a rubber material receiver for accepting the rubber material which passes the material to a pre-heating unit adapted for the rubber material passing through comprising a plurality of heating elements that heat the rubber material to between about 100 to about 350 C in an oxygen depleted atmosphere. Once pre-heated, the material is conveyed to a microwave unit adapted for receiving the pre-heated rubber material comprising microwave magnetrons, which radiate the pre-heated rubber material and external heat sources in an oxygen depleted environment until the pre-heated rubber is substantially reduced to a carbonaceous material having a volatile content of below 5% and more preferably below 2%. After being processed by microwave energy, the processed material exits on a cooling conveyor that receives processed rubber material from the microwave unit and cools the material in an oxygen depleted environment. One or more conveyors are used to transport the rubber material from the rubber material receiver into and through the pre-heating unit and into and through the microwave unit to the cooling conveyor.

The procedure (1) for obtaining raw materials resulting from waste material comprises: the supply (A) of harmonic steel resulting from waste material and prepared in a skein to be treated (3); a heat treatment (B) of the skein to be treated (3) for obtaining a treated skein (3a);—a post-treatment (E) of the treated skein (3a) for obtaining steel reusable as raw material; where the heat treatment (B) comprises an inductive exposure step (B1) of the skein to be treated (3) to at least an alternate magnetic field for the induction in the skein to be treated (3) of alternate eddy currents adapted to raise the temperature of same.