Provided herein is a method for devolatizing a solid feedstock. The solid feedstock is treated to a produce a particle size laying between 1 cm.sup.3 and 100 cm.sup.3. The solid feedstock is passed into a device connected to an outlet of a compaction screw auger comprising an assembly including a solid feedstock injector, a retort, a side arm for injecting a heated gas comprising hydrogen, and a process auger. The solid feedstock is contacted with the heated gas at a temperature of 500 C. to 1000 C. for a time of 60 seconds to 120 seconds, whereby the solid feedstock is converted into a gas stream and a solid stream.

The invention relates to shipbuilding and can be used in reconditioning in order to economize fuel and to increase speed. The technical problem is solved by the shipboard installation of air compressors, air receiver tanks, pass valves, air conduits, air separating conduits, air intakes and air injectors, which are interconnected by air ducts. An air separating conduit is mechanically secured in the bow of the ship and has air injectors secured along the centre thereof up to the stern. The injectors direct a jet of air backwards so that the jet of air thrusts the ship forwards, then the air rises along the sides of the ship, maintaining a layer of air between the ship and the water, thus reducing water resistance. The injectors in the bow direct a jet of air such that the ship is constantly sailing into an air space.

The invention relates to shipbuilding and can be used in reconditioning in order to economize fuel and to increase speed. The technical problem is solved by the shipboard installation of air compressors, air receiver tanks, pass valves, air conduits, air separating conduits, air intakes and air injectors, which are interconnected by air ducts. An air separating conduit is mechanically secured in the bow of the ship and has air injectors secured along the centre thereof up to the stern. The injectors direct a jet of air backwards so that the jet of air thrusts the ship forwards, then the air rises along the sides of the ship, maintaining a layer of air between the ship and the water, thus reducing water resistance. The injectors in the bow direct a jet of air such that the ship is constantly sailing into an air space.

A continuous flow pyrolytic reactor (200) equipped with one or more pyrolysis chamber assemblies (204) is disclosed. A positive pressure waste feeder hopper (100) for the pyrolytic reactor and its respective furnace, in addition to a pyrolysis system for the use of waste. The pyrolytic reactor (200) having a plurality of cylindrical pyrolysis chambers (201) provided, within it, with an endless screw conveyor (202) arranged longitudinally. The worm conveyor screw (202) is provided with a shaft (203), the shaft (203) being coupled to the bases of the pyrolysis chamber (201). The shaft (203) is further coupled to a rotation device that transfers torque to the shaft (203) by rotating the worm conveyor screw (202). The cylindrical pyrolysis chambers (201) are housed in an insulating housing (300) having within it two or more assemblies (204). The assemblies (204) are fed by a hopper (100) forming a pyrolysis system.

A continuous flow pyrolytic reactor (200) equipped with one or more pyrolysis chamber assemblies (204) is disclosed. A positive pressure waste feeder hopper (100) for the pyrolytic reactor and its respective furnace, in addition to a pyrolysis system for the use of waste. The pyrolytic reactor (200) having a plurality of cylindrical pyrolysis chambers (201) provided, within it, with an endless screw conveyor (202) arranged longitudinally. The worm conveyor screw (202) is provided with a shaft (203), the shaft (203) being coupled to the bases of the pyrolysis chamber (201). The shaft (203) is further coupled to a rotation device that transfers torque to the shaft (203) by rotating the worm conveyor screw (202). The cylindrical pyrolysis chambers (201) are housed in an insulating housing (300) having within it two or more assemblies (204). The assemblies (204) are fed by a hopper (100) forming a pyrolysis system.

Provided herein is a method for devolatizing a solid feedstock. The solid feedstock is treated to a produce a particle size laying between 1 cm.sup.3 and 100 cm.sup.3. The solid feedstock is passed into a device connected to an outlet of a compaction screw auger comprising an assembly including a solid feedstock injector, a retort, a side arm for injecting a heated gas comprising hydrogen, and a process auger. The solid feedstock is contacted with the heated gas at a temperature of 500 C. to 1000 C. for a time of 60 seconds to 120 seconds, whereby the solid feedstock is converted into a gas stream and a solid stream.

Provided herein is a method for devolatizing a solid feedstock. The solid feedstock is treated to a produce a particle size laying between 1 cm.sup.3 and 100 cm.sup.3. The solid feedstock is passed into a device connected to an outlet of a compaction screw auger comprising an assembly including a solid feedstock injector, a retort, a side arm for injecting a heated gas comprising hydrogen, and a process auger. The solid feedstock is contacted with the heated gas at a temperature of 500 C. to 1000 C. for a time of 60 seconds to 120 seconds, whereby the solid feedstock is converted into a gas stream and a solid stream.

Systems and methods of dynamically charging coal in coke ovens related to the operation and output of coke plants including methods of automatically charging a coke oven using a charging ram in communication with a control system to increase the coke output and coke quality from coke plants. In some embodiments, the control system is capable of moving the charging ram in a horizontal first direction, a horizontal second direction and a vertical third direction while charging coal into the oven. In some embodiments, the coal charging system also includes a scanning system configured to scan an oven floor to generate an oven floor profile and/or oven capacity. The scanning system used in combination with the control system allows for dynamic leveling of the charging ram throughout the charging process. In some embodiments, the charging ram includes stiffener plates and support members to increase the mechanical strength of the charging ram and decrease the sag of the charging ram at a distal end.

Systems and methods of dynamically charging coal in coke ovens related to the operation and output of coke plants including methods of automatically charging a coke oven using a charging ram in communication with a control system to increase the coke output and coke quality from coke plants. In some embodiments, the control system is capable of moving the charging ram in a horizontal first direction, a horizontal second direction and a vertical third direction while charging coal into the oven. In some embodiments, the coal charging system also includes a scanning system configured to scan an oven floor to generate an oven floor profile and/or oven capacity. The scanning system used in combination with the control system allows for dynamic leveling of the charging ram throughout the charging process. In some embodiments, the charging ram includes stiffener plates and support members to increase the mechanical strength of the charging ram and decrease the sag of the charging ram at a distal end.

Embodiments described herein relate to retorts for separating materials or substances (e.g., based on volatility thereof) and forming a base or waste material (e.g., basic sediment and water, inorganic materials, char, organic waste materials, and other solids) and a target material (e.g., shale oil or other oils), contained in feed-stock.