A body of heat transfer fluid circulates in a first loop through an indirect screw-type thermal processor, a rundown tank, a pump, a heater and a fill tank, continuously heating the processor. With the pump operating, a first vertical distance between the fill tank bottom and the processor under the influence of gravity sets a minimum fluid pressure at the processor; a stem pipe opening in the fill tank at a second vertical distance above the processor sets a maximum pressure. With the pump inactive, the entire body of fluid passively drains to the rundown tank. Supplying the fluid may entail melting a salt, hydrating a salt, or both; such may be done in the rundown tank before circulation through the processor begins. A hydrated salt may be circulated, then heated and dehydrated, to gradually warm the processor. A dehydrated salt may be rehydrated and then stored; this may be done in the rundown tank after ceasing circulation through the processor. Also described: misting hydration and variable-speed-pump pressure regulation.

A heat exchanging system includes a tank including a fluid inlet and a fluid outlet, which encloses (envelopes) a heat exchanger including a manifold tube and one or more one heat exchanging plates, extending from the manifold tube. The manifold tube includes a fluid intake and the fluid outlet, as well as a manifold barrier, which divides the interior of the manifold tube (for example, which is hollow), so as to define within the manifold tube an intake region and an outlet region. The heat exchanging system also has at least one heat exchanging plate extending from the manifold tube, the at least one heat exchanging plate with at least one plate barrier, such that the heat exchanging plate is configured to define a fluid flow path within the heat exchanging plate such that fluid flows from the intake region of the manifold tube.

A reaction device is provided with a first wall that defines an interior in which a stirring mechanism is located. A heat exchanger is at least partly provided on the first outer wall surface facing away from the interior and/or on the stirring mechanism, wherein the heat exchanger has a grate structure, and at least two layers are provided which have a grate structure. Thus, it is possible to transfer heat in a precise and efficient manner primarily by means of thermal radiation in endothermic processes at different temperature levels, in particular pyrolysis, gassing, and reforming processes, and thereby use the exhaust heat for other processes.

A reaction device is provided with a first wall that defines an interior in which a stirring mechanism is located. A heat exchanger is at least partly provided on the first outer wall surface facing away from the interior and/or on the stirring mechanism, wherein the heat exchanger has a grate structure, and at least two layers are provided which have a grate structure. Thus, it is possible to transfer heat in a precise and efficient manner primarily by means of thermal radiation in endothermic processes at different temperature levels, in particular pyrolysis, gassing, and reforming processes, and thereby use the exhaust heat for other processes.

Disclosed is a heat exchanger for a thermal management system of an aircraft assembly, the heat exchanger including: a core including a first side with a first core inlet, a second side opposing the first side and includes a first core outlet, the first core inlet is in fluid communication with the first core outlet, a third side having a second core inlet and a fourth side opposing the third side and includes a second core outlet, the second core inlet is in fluid communication with the second core outlet, and a screen wrapped around the core, the screen covering the first core inlet and the first core outlet, and a plurality of rollers disposed between the core and the screen for movably securing the screen to the core, the rollers engaging the screen and movement of at least one of the rollers moves the screen about the core.

There is provided a heat exchanger adapted to exchange heat between a first fluid and a second fluid. The heat exchanger comprises an outer tubular body, an inner body, a first inlet, a first outlet, a second inlet and a second outlet. The outer tubular body has an inner surface. The inner body is arranged inside the outer tubular body and has an outer surface facing the inner surface of the outer tubular body, leaving free a gap between the inner surface of the outer tubular body and the outer surface of the inner body. The first inlet and the first outlet are arranged to provide a first flow path for the first fluid from the first inlet to the first outlet via a first channel and via a second channel. The second inlet and the second outlet are arranged to provide a second flow path from the second inlet to the second outlet for the second fluid in the gap between the inner surface of the outer tubular body and the outer surface of the inner body. The outer tubular body comprises the first channel. The inner body comprises the second channel. The inner body and the second channel are rotatable relative to the outer tubular body and the first channel.

There is provided a heat exchanger adapted to exchange heat between a first fluid and a second fluid. The heat exchanger comprises an outer tubular body, an inner body, a first inlet, a first outlet, a second inlet and a second outlet. The outer tubular body has an inner surface. The inner body is arranged inside the outer tubular body and has an outer surface facing the inner surface of the outer tubular body, leaving free a gap between the inner surface of the outer tubular body and the outer surface of the inner body. The first inlet and the first outlet are arranged to provide a first flow path for the first fluid from the first inlet to the first outlet via a first channel and via a second channel. The second inlet and the second outlet are arranged to provide a second flow path from the second inlet to the second outlet for the second fluid in the gap between the inner surface of the outer tubular body and the outer surface of the inner body. The outer tubular body comprises the first channel. The inner body comprises the second channel. The inner body and the second channel are rotatable relative to the outer tubular body and the first channel.

The disclosure relates to a heat transfer assembly for a rotary regenerative heat exchanger. The assembly includes a rotor arranged between at least two separated fluid flow passages passing flow axially through the rotor, where each flow passage is connected to a sector part of the rotor. The assembly further includes a plurality of channels in the rotor for flowing a fluid through the rotor, each of the channels is enclosed by heat transfer and heat accumulating surfaces in the rotor, and the heat transfer and heat accumulating surfaces of the channels are made in a material providing an average axial thermal conductivity less than 100 W/mK arranged to reduce the Longitudinal Heat Conductivity of the rotor.

The disclosure relates to a heat transfer assembly for a rotary regenerative heat exchanger. The assembly includes a rotor arranged between at least two separated fluid flow passages passing flow axially through the rotor, where each flow passage is connected to a sector part of the rotor. The assembly further includes a plurality of channels in the rotor for flowing a fluid through the rotor, each of the channels is enclosed by heat transfer and heat accumulating surfaces in the rotor, and the heat transfer and heat accumulating surfaces of the channels are made in a material providing an average axial thermal conductivity less than 100 W/mK arranged to reduce the Longitudinal Heat Conductivity of the rotor.

Embodiments disclosed herein relate to devices, systems, and methods for cooling and/or heating a medium as well as cooling and/or heating an environment containing the medium. More specifically, at least one embodiment includes a heat pump that may heat and/or cool a medium and, in some instances, may transfer heat from one location to another location.