F28C3/12

A Powder-Gas Heat Exchanger and Applications Thereof

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.

Method for cooling a solid and system for carrying out the method

The present disclosure relates to a method and a device for cooling a solid, in particular a hygroscopic bulk material, in a more energy-efficient manner. For this purpose, an air flow is, if needed, cooled and/or dehumidified and/or subsequently heated in order to reduce the relative humidity of the air flow. The cooling air flow conditioned in this manner is then used in a contact device for cooling the solid, and a heated exhaust air flow is drawn from the contact device. According to the invention, a part of the exhaust air flow is mixed with the air flow in order to pre-heat the air flow and thus reduce the relative humidity of the air flow. In addition, a second part of the exhaust air flow can be mixed with feed air and used in a separate second contact device in order to pre-cool the solid.

Method for cooling a solid and system for carrying out the method

The present disclosure relates to a method and a device for cooling a solid, in particular a hygroscopic bulk material, in a more energy-efficient manner. For this purpose, an air flow is, if needed, cooled and/or dehumidified and/or subsequently heated in order to reduce the relative humidity of the air flow. The cooling air flow conditioned in this manner is then used in a contact device for cooling the solid, and a heated exhaust air flow is drawn from the contact device. According to the invention, a part of the exhaust air flow is mixed with the air flow in order to pre-heat the air flow and thus reduce the relative humidity of the air flow. In addition, a second part of the exhaust air flow can be mixed with feed air and used in a separate second contact device in order to pre-cool the solid.

HEAT EXCHANGER

A heat exchanger according to one embodiment includes: a cyclone flow path into which a first fluid is introduced along a tangential direction, the first fluid flowing downward in the cyclone flow path; a lower case located below the cyclone flow path and forming a lower space having a flow path area larger than that of the cyclone flow path; a first outlet flow path located on an outer peripheral side of the cyclone flow path, the first outlet flow path communicating with the lower space; a second inlet flow path into which a second fluid is introduced, the second inlet flow path being located on the outer peripheral side of the cyclone flow path; a second outlet flow path located on an inner peripheral side of the cyclone flow path; and a second intermediate flow path connecting the second inlet flow path and the second outlet flow path.

HEAT EXCHANGER

A heat exchanger according to one embodiment includes: a cyclone flow path into which a first fluid is introduced along a tangential direction, the first fluid flowing downward in the cyclone flow path; a lower case located below the cyclone flow path and forming a lower space having a flow path area larger than that of the cyclone flow path; a first outlet flow path located on an outer peripheral side of the cyclone flow path, the first outlet flow path communicating with the lower space; a second inlet flow path into which a second fluid is introduced, the second inlet flow path being located on the outer peripheral side of the cyclone flow path; a second outlet flow path located on an inner peripheral side of the cyclone flow path; and a second intermediate flow path connecting the second inlet flow path and the second outlet flow path.

Heat transfer system

A system for heat transfer including a compressor, a regolith inlet, a first storage hopper, and a load. The compressor is in fluid communication with a closed loop system. The regolith inlet is in fluid communication with the closed loop system. The first storage hopper is adapted to carry an amount of regolith and is in fluid communication with the regolith inlet. The load is in fluid communication with the closed loop system between a compressor inlet a compressor outlet.

Compact Dual Chamber Heat Exchange Unit
20200278155 · 2020-09-03 ·

An environmentally friendly compact dual chamber heat exchange unit that is integrated into the heating and cooling system of a building that can be fabricated and assembled off site, transported to the site, installed and then filled with matrix and/or slurry, as well as a method of installation of the compact dual chamber heat exchange unit. The compact dual chamber heat exchange unit is designed to fit in most residential back yards.

Compact Dual Chamber Heat Exchange Unit
20200278155 · 2020-09-03 ·

An environmentally friendly compact dual chamber heat exchange unit that is integrated into the heating and cooling system of a building that can be fabricated and assembled off site, transported to the site, installed and then filled with matrix and/or slurry, as well as a method of installation of the compact dual chamber heat exchange unit. The compact dual chamber heat exchange unit is designed to fit in most residential back yards.

Slurry droplet melting heat exchange
10533812 · 2020-01-14 · ·

Devices, systems, and methods for cooling a gas is disclosed. A slurry is passed through a droplet generating device to produce droplets of the slurry. The slurry comprises a contact liquid and solids. A melting point of the solids is higher than a vaporization point of the contact liquid. A carrier gas is passed across the droplets to exchange heat between the carrier gas and the droplets. At least a portion of the heat transferred to the droplets melts the solids.

Slurry droplet melting heat exchange
10533812 · 2020-01-14 · ·

Devices, systems, and methods for cooling a gas is disclosed. A slurry is passed through a droplet generating device to produce droplets of the slurry. The slurry comprises a contact liquid and solids. A melting point of the solids is higher than a vaporization point of the contact liquid. A carrier gas is passed across the droplets to exchange heat between the carrier gas and the droplets. At least a portion of the heat transferred to the droplets melts the solids.