A heat shield bladder includes first and second sheets of insulating material that form a bladder between the first and second sheets. At least one reflective foil is disposed within the bladder and a plurality of spacers are disposed within the bladder and positioned to space the at least one reflective foil from the first and second sheets of insulating material. Multiple reflective foils may be disposed within the bladder with spacers between each reflective foil. The heat shield bladder may be rolled into a tube shaped and used inside a pipe or formed into panels that may be used to line a vessel.

There is disclosed a system and method for processing diesel fuel from petroleum-based waste oil on a small scale compared to conventional methods for re-refining waste oil to a valuable product. In an embodiment, the method comprises dehydrating waste oil to remove water from the waste oil, and operating a vertical cylindrical reactor to induce pyrolysis of the dehydrated waste oil and convert it into a hydrocarbon vapor phase. The hydrocarbon vapor derived from pyrolysis is condensed and distilled using a distillation tower to produce diesel fuel, heavy liquid hydrocarbon, light liquid hydrocarbon and light hydrocarbon vapor. A filtering step cleans the processed diesel fuel to obtain a clean diesel fuel product.

A device (110) comprising a multitude of hollow cylinder pipes is proposed. At least one of the hollow cylinder pipes is set up as a fluid cylinder (112) to receive at least one feedstock. At least one further hollow cylinder pipe is configured as a current-conducting heating cylinder (129). The device (110) has at least one power source or voltage source (126) set up to generate an electrical current in the heating cylinder (129) that heats the fluid cylinder (112) by means of Joule heat that arises on passage of the electrical current through the heating cylinder (129).

A high-temperature decomposition reactor is provided. The reactor includes a reaction vessel, a furnace, and an insulation layer. The reaction vessel includes an inner volume configured to contain a quantity of carbonated medium while the quantity of carbonated medium transitions to a quantity of carbonation medium. The furnace is disposed around the reaction vessel and includes a furnace material. The furnace material is configured to simultaneously absorb heat and transmit heat. In some instances, the furnace material transmits heat to the inner volume to heat the carbonated medium. The insulation layer is disposed around the furnace and configured to prevent thermal losses from the reactor.

A reactor system and a process for carrying out reverse water gas shift reaction of a feedstock comprising CO.sub.2 and H.sub.2 to a first product gas comprising CO are provided, where a methanation reaction take place in parallel to the reverse water gas shift reaction, and where the heat for the endothermic reverse water gas shift reaction is provided by resistance heating.

A reactor system for carrying out an endothermic reaction of a feed gas, including: a structured catalyst arranged for catalyzing the endothermic reaction of a feed gas, the structured catalyst including a macroscopic structure of electrically conductive material, the macroscopic structure supporting a ceramic coating, wherein the ceramic coating supports a catalytically active material; a pressure shell housing the structured catalyst; heat insulation layer between the structured catalyst and the pressure shell; at least two conductors electrically connected to the electrically conductive material and to an electrical power supply placed outside the pressure shell, wherein the electrical power supply is dimensioned to heat at least part of said structured catalyst to a temperature of at least 200 C. by passing an electrical current through the electrically conductive material. Also, a process for performing an endothermic reaction of a feed gas.

The present disclosure relates to reactor components and their use, e.g., in regenerative reactors. A process and apparatus for utilizing different wetted areas along the flow path of a fluid in a pyrolysis reactor, e.g., a thermally regenerating reactor, such as a regenerative, reverse-flow reactor, is described.

A two step process for the destruction of a precursor material using a steam plasma in a three zone reactor wherein the precursor material is hydrolyzed as a first step in the high temperature zone of the reactor, followed by a second step of medium temperature oxidation of the reactant stream in the combustion zone of the reactor where combustion oxygen or air is injected and immediate quenching of the resulting gas stream to avoid the formation of unwanted by-products. A related apparatus includes a non transferred direct current steam plasma torch, an externally cooled three zone steam plasma reactor means for introducing the precursor material into the plasma plume of the plasma torch, means for introducing the combustion air or oxygen into the combustion zone, means for exiting the reactant mixture from the reactor and means for quenching the reactant mixture located at the exit end of the reactor.

A hydrogen generator and a fuel cell system including the hydrogen generator are disclosed. The hydrogen generator includes a fuel composition including a hydrogen containing material that releases hydrogen gas to produce hydrogen when heated. A biasing member working in cooperation with a heating element and retainer, all of which are disposed within a unitary container, facilitate and control the release of hydrogen gas. The fuel composition can be segregated into individual quantities.

The present invention discloses a hydrogen sulfide reactor vessel with an external heating system that is conductively and removably attached to an exterior portion of the reactor vessel. Also disclosed are processes for producing hydrogen sulfide utilizing the reactor vessel.