Barocaloric heat transfer systems and related methods are generally described. In some embodiments, a heat transfer system may include a barocaloric material which may generate heat upon compression and may cool down upon decompression. The barocaloric material may be pressurized using high pressure and low pressure fluids, which may, in some embodiments, also transfer heat to/from the barocaloric material. The heat transfer system may also include a hot heat exchanger to dissipate heat from the heat transfer system to a first environment and a cold heat exchanger to absorb heat from a second environment, effectively cooling the second environment. In some embodiments, the barocaloric material may be in particulate form.

Barocaloric heat transfer systems and related methods are generally described. In some embodiments, a heat transfer system may include a barocaloric material which may generate heat upon compression and may cool down upon decompression. The barocaloric material may be pressurized using high pressure and low pressure fluids, which may, in some embodiments, also transfer heat to/from the barocaloric material. The heat transfer system may also include a hot heat exchanger to dissipate heat from the heat transfer system to a first environment and a cold heat exchanger to absorb heat from a second environment, effectively cooling the second environment. In some embodiments, the barocaloric material may be in particulate form.

A system including: a pumped-heat energy storage system (“PHES system”), wherein the PHES system is operable in a charge mode to convert electricity into stored thermal energy, wherein the PHES system comprises a working fluid path circulating a working fluid through, in sequence, at least a compressor system, a hot-side heat exchanger system, a turbine system, a cold-side heat exchanger system, and back to the compressor system; and (ii) a fluid path directing a hot fluid from a heat source external to the PHES system through a reheater, wherein a portion of the working fluid path through the turbine system comprises circulating the working fluid through a first turbine, the reheater, and a second turbine, and wherein the working fluid thermally contacts the hot fluid in the reheater, thereby transferring heat from the hot fluid to the working fluid.

A system including: a pumped-heat energy storage system (“PHES system”), wherein the PHES system is operable in a charge mode to convert electricity into stored thermal energy, wherein the PHES system comprises a working fluid path circulating a working fluid through, in sequence, at least a compressor system, a hot-side heat exchanger system, a turbine system, a cold-side heat exchanger system, and back to the compressor system; and (ii) a fluid path directing a hot fluid from a heat source external to the PHES system through a reheater, wherein a portion of the working fluid path through the turbine system comprises circulating the working fluid through a first turbine, the reheater, and a second turbine, and wherein the working fluid thermally contacts the hot fluid in the reheater, thereby transferring heat from the hot fluid to the working fluid.

Provided is a heat accumulator including a heat exchange chamber having a lower portion and an upper portion and being configured to accommodate therein heat storage elements for storing thermal energy, wherein the heat exchange chamber includes an inlet which is configured to supply a working fluid into the heat exchange chamber. A passively controlled first pressure loss regulating device is arranged within the flow of the working fluid in the heat exchange chamber and configured to pass the working fluid through, wherein the first pressure loss regulating device is configured to form a first flow resistance for a flow of the working fluid in the first pressure loss regulating device being different to a flow resistance for a flow of the working fluid in the heat exchange chamber adjacent and outside the first pressure loss regulating device.

A system including: a pumped-heat energy storage system (“PHES system”), wherein the PHES system is operable in a charge mode to convert electricity into stored thermal energy, wherein the PHES system comprises a working fluid path circulating a working fluid through, in sequence, at least a compressor system, a hot-side heat exchanger system, a turbine system, a cold-side heat exchanger system, and back to the compressor system; and (ii) a fluid path directing a hot fluid from a heat source external to the PHES system through a reheater, wherein a portion of the working fluid path through the turbine system comprises circulating the working fluid through a first turbine, the reheater, and a second turbine, and wherein the working fluid thermally contacts the hot fluid in the reheater, thereby transferring heat from the hot fluid to the working fluid.

A system including: a pumped-heat energy storage system (“PHES system”), wherein the PHES system is operable in a charge mode to convert electricity into stored thermal energy, wherein the PHES system comprises a working fluid path circulating a working fluid through, in sequence, at least a compressor system, a hot-side heat exchanger system, a turbine system, a cold-side heat exchanger system, and back to the compressor system; and (ii) a fluid path directing a hot fluid from a heat source external to the PHES system through a reheater, wherein a portion of the working fluid path through the turbine system comprises circulating the working fluid through a first turbine, the reheater, and a second turbine, and wherein the working fluid thermally contacts the hot fluid in the reheater, thereby transferring heat from the hot fluid to the working fluid.

A rotary counter-current solid/fluid contact apparatus is developed to enhance the efficiency of adsorption, ion exchange and regenerative heat exchange. The counter-current apparatus uses a rotor to direct fluids to multiple stationary columns. By the action of the rotor, counter-current flows of a fluid phase and a solid phase can be achieved for a combined adsorption and desorption cycle, or a combined heating and cooling cycle. The apparatus allows not only countercurrent solid-fluid flows based on columns in series, but also countercurrent solid-fluid flows in the length of each individual column. A method is also disclosed.

A rotary counter-current solid/fluid contact apparatus is developed to enhance the efficiency of adsorption, ion exchange and regenerative heat exchange. The counter-current apparatus uses a rotor to direct fluids to multiple stationary columns. By the action of the rotor, counter-current flows of a fluid phase and a solid phase can be achieved for a combined adsorption and desorption cycle, or a combined heating and cooling cycle. The apparatus allows not only countercurrent solid-fluid flows based on columns in series, but also countercurrent solid-fluid flows in the length of each individual column. A method is also disclosed.

A rotary counter-current solid/fluid contact apparatus is developed to enhance the efficiency of adsorption, ion exchange and regenerative heat exchange. The counter-current apparatus uses a rotor to direct fluids to multiple stationary columns. By the action of the rotor, counter-current flows of a fluid phase and a solid phase can be achieved for a combined adsorption and desorption cycle, or a combined heating and cooling cycle. The apparatus allows not only countercurrent solid-fluid flows based on columns in series, but also countercurrent solid-fluid flows in the length of each individual column. A method is also disclosed.