The present invention provides a system for producing mesophase coke from an isotropic pitch. The system includes a reactor having a first heating zone to carry out pretreating of the isotropic pitch by operating at a temperature of 250° C.-350° C. under atmospheric pressure. The reactor further includes a second heating zone to carry out heating of the pretreated isotropic pitch by maintaining the temperature of 350° C.-500° C. under the atmospheric pressure to obtain mesophase pitch. The reactor includes a third heating zone to carry out heating of the said mesophase pitch by maintaining the temperature of 500° C.-800° C. under the atmospheric pressure to obtain mesophase coke. The system further includes a pusher unit adapted to physically move the container from the entry zone to the exit zone to obtain the mesophase coke.

A system for producing oil is disclosed. The system may comprise a container for a naturally occurring or synthetically produced hydrocarbon source material. The system may also comprise a material preparation device to physically degrade the hydrocarbon source material into small pieces. The system may further comprise a heat source to heat the hydrocarbon source material indirectly by heating the container, the hydrocarbon source material being heated to a temperature sufficient to gasify hydrocarbons in the hydrocarbon source material and release the hydrocarbons therefrom. The system may still further comprise a fractionation device fluidly coupled to the container to receive the hydrocarbons and separate the hydrocarbons into like components. Additionally, the system may comprise a collection container to receive the like components.

A system for producing oil is disclosed. The system may comprise a container for a naturally occurring or synthetically produced hydrocarbon source material. The system may also comprise a material preparation device to physically degrade the hydrocarbon source material into small pieces. The system may further comprise a heat source to heat the hydrocarbon source material indirectly by heating the container, the hydrocarbon source material being heated to a temperature sufficient to gasify hydrocarbons in the hydrocarbon source material and release the hydrocarbons therefrom. The system may still further comprise a fractionation device fluidly coupled to the container to receive the hydrocarbons and separate the hydrocarbons into like components. Additionally, the system may comprise a collection container to receive the like components.

The invention relates to an apparatus for the material treatment of raw materials. The apparatus has a heating system, a distillation unit and a reaction unit to be loaded with the raw materials for treatment. The heating system can be opened and closed to be fitted with the reaction unit. The heating system comprises a top element and a jacket element firmly connected to the top element, and supporting elements. The length of the support elements can be varied in the vertical direction, between two end positions, the heating system can be opened and closed in the vertical direction of movement. The invention further relates to a method for operating an apparatus for the material treatment of raw materials.

The invention relates to an apparatus for the material treatment of raw materials. The apparatus has a heating system, a distillation unit and a reaction unit to be loaded with the raw materials for treatment. The heating system can be opened and closed to be fitted with the reaction unit. The heating system comprises a top element and a jacket element firmly connected to the top element, and supporting elements. The length of the support elements can be varied in the vertical direction, between two end positions, the heating system can be opened and closed in the vertical direction of movement. The invention further relates to a method for operating an apparatus for the material treatment of raw materials.

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.

Pressure vessels containing a charge are preheated at pressure of 2 to 5 kPa with liquid heat carrier to maximally 120 C. They are afterheated in another place to maximally 550 C. The pressure vessels are continually added and/or replaced and generated gasses are continuously drawn off, cooled to maximally 60 C. and separated oily condensate. Residual gasses and solid residues are burned after treatment in a cogeneration unit.

Pressure vessels containing a charge are preheated at pressure of 2 to 5 kPa with liquid heat carrier to maximally 120 C. They are afterheated in another place to maximally 550 C. The pressure vessels are continually added and/or replaced and generated gasses are continuously drawn off, cooled to maximally 60 C. and separated oily condensate. Residual gasses and solid residues are burned after treatment in a cogeneration unit.

A continuous solid organic matter pyrolysis polygeneration system and method for using the system is disclosed. The pyrolysis polygeneration system mainly includes a processing system, a drying furnace, a pyrolysis furnace, a cooling furnace, a tail gas treatment system, and a gas treatment system and a protective gas circulation system cooperate with each other to realize the multi-level rational utilization of energy, and are suitable for the continuous and rapid pyrolysis and carbonization of various solid organic matter in the actual production. While realizing the polygeneration of coke, wood vinegar and tar, the maximum utilization of overall heat is realized through process optimization.

A continuous solid organic matter pyrolysis polygeneration system and method for using the system is disclosed. The pyrolysis polygeneration system mainly includes a processing system, a drying furnace, a pyrolysis furnace, a cooling furnace, a tail gas treatment system, and a gas treatment system and a protective gas circulation system cooperate with each other to realize the multi-level rational utilization of energy, and are suitable for the continuous and rapid pyrolysis and carbonization of various solid organic matter in the actual production. While realizing the polygeneration of coke, wood vinegar and tar, the maximum utilization of overall heat is realized through process optimization.