The invention provides a powder-gas heat exchanger for exchanging heat between a powder stream and a gas stream in counter-current flow comprising a powder stream mass flow rate substantially equal to a gas stream mass flow rate in a vertical shaft heat exchanger. A hot gas stream may be adapted for use in heating a cool solids stream, or a cool gas stream may be adapted for use in cooling a hot solids stream.

The invention provides a powder-gas heat exchanger for exchanging heat between a powder stream and a gas stream in counter-current flow comprising a powder stream mass flow rate substantially equal to a gas stream mass flow rate in a vertical shaft heat exchanger. A hot gas stream may be adapted for use in heating a cool solids stream, or a cool gas stream may be adapted for use in cooling a hot solids stream.

A sorption module for a sorption temperature-control device may include a housing enclosing a working chamber. A sorption zone and a phase change zone may be arranged in the working chamber where a working medium is displaceable reversibly between the sorption zone and the phase change zone. A sorption structure may be arranged in the sorption zone, and a phase change structure may be arranged in the phase change zone. An outer wall of the housing may include a double-walled section that may provide a cavity between an outer wall part and an inner wall part of the double-walled section, and the phase change zone may be arranged on an inner side of the inner wall part.

Devices and methods of recycling cement waste. A cement waste recycling device (1) comprising a heater (2) with an inlet (3) for cement waste and an outlet (4) for processed cement waste, wherein the heater (2) is configured for transporting cement waste in a cement waste transportation direction from the inlet (3) to the outlet (4) while transporting heated gas in countercurrent with the cement waste transportation direction.

A heater, especially an oilseed heater (15) comprising an insulated jacket (2) which contains a material inlet (3), a material outlet (4), a heating medium inlet (5) and an air outlet (6) and where at least one exchanger (7) for condensation of evaporation residues is arranged inside the insulated jacket (2) and connected with the source (1) of the evaporation residues.

A heater, especially an oilseed heater (15) comprising an insulated jacket (2) which contains a material inlet (3), a material outlet (4), a heating medium inlet (5) and an air outlet (6) and where at least one exchanger (7) for condensation of evaporation residues is arranged inside the insulated jacket (2) and connected with the source (1) of the evaporation residues.

A heater, especially an oilseed heater (15) comprising an insulated jacket (2) which contains a material inlet (3), a material outlet (4), a heating medium inlet (5) and an air outlet (6) and where at least one exchanger (7) for condensation of evaporation residues is arranged inside the insulated jacket (2) and connected with the source (1) of the evaporation residues.

A heater, especially an oilseed heater (15) comprising an insulated jacket (2) which contains a material inlet (3), a material outlet (4), a heating medium inlet (5) and an air outlet (6) and where at least one exchanger (7) for condensation of evaporation residues is arranged inside the insulated jacket (2) and connected with the source (1) of the evaporation residues.

A pumped heat energy storage system (11) is provided. A thermodynamic charging assembly (11) may be configured to compress a working fluid and generate thermal energy. A thermal storage assembly (32) is coupled to charging assembly to store at atmospheric pressure by way of a conveyable bulk solid thermal storage media thermal energy generated by the charging assembly. A thermodynamic discharging assembly (11) is coupled to the thermal storage assembly to extract thermal energy from the thermal storage assembly and convert extracted thermal energy to electrical energy. A heat exchanger assembly (34) is coupled to the thermal storage assembly. The heat exchanger assembly is arranged to directly thermally couple the conveyable bulk solid thermal storage media that is conveyed to the heat exchanger assembly with a flow of the working fluid that passes through the heat exchanger assembly. Disclosed embodiments can make use of immersed-particle heat exchanger technology and can offer similar roundtrip efficiency and pressure ratio characteristics comparable to those of a recuperated cycle without involving a recuperator and concomitant piping.

A pumped heat energy storage system (11) is provided. A thermodynamic charging assembly (11) may be configured to compress a working fluid and generate thermal energy. A thermal storage assembly (32) is coupled to charging assembly to store at atmospheric pressure by way of a conveyable bulk solid thermal storage media thermal energy generated by the charging assembly. A thermodynamic discharging assembly (11) is coupled to the thermal storage assembly to extract thermal energy from the thermal storage assembly and convert extracted thermal energy to electrical energy. A heat exchanger assembly (34) is coupled to the thermal storage assembly. The heat exchanger assembly is arranged to directly thermally couple the conveyable bulk solid thermal storage media that is conveyed to the heat exchanger assembly with a flow of the working fluid that passes through the heat exchanger assembly. Disclosed embodiments can make use of immersed-particle heat exchanger technology and can offer similar roundtrip efficiency and pressure ratio characteristics comparable to those of a recuperated cycle without involving a recuperator and concomitant piping.