Water generation systems and related methods of generating water from air are disclosed herein. In various embodiments, water generation systems and related methods comprise a solar unit or layer to convert solar radiation into heat and/or electrical energy, a sorption unit or layer comprising a hygroscopic material to capture water vapor from ambient air, a regeneration gas to accumulate water vapor from the sorption unit or layer, and a heat exchange assembly to condense water vapor from the regeneration gas to produce liquid water. Disclosed heat exchange assemblies can comprise a vapor-compression cycle or refrigeration circuit configured to circulate a refrigerant. A refrigerant evaporator can transfer heat from condensation of water vapor in the regeneration gas to the refrigerant and/or a refrigerant condenser can transfer heat from condensation of refrigerant vapor to the sorption unit or layer. Various embodiments include a controller to adjust a system operational setpoint based on a system operational state and/or an environmental condition.

Provided herein are water and carbon dioxide harvesting systems, as well as methods using such systems, for capturing water and carbon dioxide from surrounding air. The systems and methods use water capture materials to adsorb water from the air and carbon dioxide capture materials to adsorb carbon dioxide from the air. For example, the water and carbon dioxide capture materials may be metal-organic-frameworks. The systems and methods desorb the water in the form of water vapor and the carbon dioxide. The water vapor is then condensed into liquid water. The water and carbon dioxide generated can be used in farming systems, including hydroponics and vertical farming systems.

A method is provided for a combination of CO.sub.2-capture and storage from the ambient air and fast charging of electric vehicles. A charging station for electric vehicles is also provided.

System (2) for CO.sub.2 capture from a combustion engine (1) comprising an exhaust gas flow circuit (6) having an inlet end fluidly connected to an exhaust of the combustion engine, a heat exchanger circuit (12), a primary exhaust gas heat exchanger (H1) for transferring heat from exhaust gas to fluid in the heat exchanger circuit, at least one compressor (10) for compressing fluid in a section of the heat exchanger circuit, the compressor driven by thermal expansion of heat exchanger circuit fluid from the primary exhaust gas heat exchanger (H1), and a CO.sub.2 temperature swing adsorption (TSA) reactor (4) fluidly connected to an outlet end of the exhaust gas flow circuit. The TSA reactor includes at least an adsorption reactor unit (D4) and a desorption reactor unit (D2), the heat exchanger circuit comprising a heating section (12b) for heating the desorption unit (D2) and a cooling section (12a) for cooling the adsorption unit (D4).

Devices, systems, facilities, and methods for direct air capture using adsorbent beds are disclosed. A exemplary system may include water adsorbent beds in fluid communication with an air cooled heat exchanger, and the water adsorbent beds adsorb water from a CO.sub.2 containing gas stream from the air cooled heat exchanger. The system may include CO.sub.2 adsorbent beds in fluid communication with the air cooled heat exchanger, and the CO.sub.2 adsorbent beds adsorb the CO.sub.2 from the CO.sub.2 containing gas stream. A heat source provides heat energy to the water adsorbent beds and the CO.sub.2 adsorbent beds to regenerate these adsorbent beds. A sequestration compression unit then compresses the saturated CO.sub.2 from the CO.sub.2 adsorbent beds.

The invention provides a process of purifying a fluid useful in a manufacturing process, particularly in the manufacture of silicon wafers, by removing one or more impurities; and apparatus for use in the process.

A device for reducing a carbon dioxide and water content in an enclosed air volume has first and second sorption units for sorbing carbon dioxide and water. The first and second sorption units can be transferred from a sorption mode into a desorption mode and vice versa. In the sorption mode, the first and second sorption units sorb carbon dioxide and water from raw air of the enclosed air volume. In the desorption mode, the first and second desorption units desorb carbon dioxide and water to supplied regeneration air. An air distribution device can switch the first and second sorption units, based on the carbon dioxide and water content, alternately from sorption mode into desorption mode such that, in at least one operating state of the device, one of the first and second sorption units is in sorption mode while the other is in desorption mode.

A water collecting apparatus (100) includes a moisture-absorbing material (10) and a heat-conducting member (20). The moisture-absorbing material (10) includes a polymer compound having a property in which a degree of hydrophilicity changes with temperature. The heat-conducting member (20) is disposed facing a portion of an outer surface of the moisture-absorbing material (10) and has thermal conductivity. The heat-conducting member (20) is preferably disposed so that another portion of the outer surface of the moisture-absorbing material (10) is left exposed. The portion of the outer surface of the moisture-absorbing material (10) and the other portion of the outer surface of the moisture-absorbing material (10) are collinearly positioned.

A continuous desulfurization process and process system are described for removal of reduced sulfur species at gas stream concentrations in a range of from about 5 to about 5000 ppmv, using fixed beds containing regenerable sorbents, and for regeneration of such regenerable sorbents. The desulfurization removes the reduced sulfur species of hydrogen sulfide, carbonyl sulfide, carbon disulfide, and/or thiols and disulfides with four or less carbon atoms, to ppbv concentrations. In specific disclosed implementations, regenerable metal oxide-based sorbents are integrated along with a functional and effective process to control the regeneration reaction and process while maintaining a stable dynamic sulfur capacity. A membrane-based process and system is described for producing regeneration and purge gas for the desulfurization.

System (2) for CO.sub.2 capture from a combustion engine (1) comprising an exhaust gas flow circuit (6) having an inlet end fluidly connected to an exhaust of the combustion engine, a heat exchanger circuit (12), a primary exhaust gas heat exchanger (H1) for transferring heat from exhaust gas to fluid in the heat exchanger circuit, at least one compressor (10) for compressing fluid in a section of the heat exchanger circuit, the compressor driven by thermal expansion of heat exchanger circuit fluid from the primary exhaust gas heat exchanger (H1), and a CO.sub.2 temperature swing adsorption (TSA) reactor (4) fluidly connected to an outlet end of the exhaust gas flow circuit. The TSA reactor includes at least an adsorption reactor unit (D4) and a desorption reactor unit (D2), the heat exchanger circuit comprising a heating section (12b) for heating the desorption unit (D2) and a cooling section (12a) for cooling the adsorption unit (D4).