A device, method, and system for CO.sub.2 capture is disclosed. The method includes receiving a process vapor including water and CO.sub.2 into a vessel at an intake pressure, the vessel having a desiccant and a CO.sub.2 sorbent material. The method includes passing the process vapor through the desiccant and sorbent, the desiccant absorbing the water resulting in a dry vapor, the sorbent absorbing CO.sub.2 from the dry vapor resulting in a CO.sub.2-lean dry vapor. The method includes discontinuing the process vapor, desorbing the water from the desiccant by at least one of reducing pressure downstream from the desiccant to below the intake pressure and increasing a temperature of the desiccant, desorbing the CO.sub.2 from the sorbent by placing the desorbed water in contact with the sorbent, removing the desorbed CO.sub.2 through the product outlet as a product stream, and desorbing a remaining water from the desiccant and the sorbent.

A system for collecting a sorbate gas from a sorbent is disclosed, including a regeneration vessel enclosing a sorbent having a sorbate gas, a liquid water supply heated to a first temperature, and a heat pump with a condenser. The heat pump is also in contact with the water supply. Heat is removed from the condenser and used to heat the water supply to the first temperature. The system includes a compressor coupled to the condenser. The sorbent within the vessel is placed in contact with water vapor at the first temperature. The water vapor coming into contact with the sorbent causes sorbate gas to be released, forming a mixture including sorbate and water gases, raising the pressure. The vapor mixture is removed and cooled by the condenser, where a portion is condensed into water that is returned to the supply. The remaining mixture is compressed into a product gas.

An installation for separating carbon dioxide from ambient air is disclosed. The installation includes an adsorption chamber configured to bind carbon dioxide from ambient air to a sorbent, a desorption chamber configured to release carbon dioxide from the sorbent, and a cooling chamber configured to cool the sorbent after desorption. A heating mechanism is disposed within the desorption chamber to facilitate the release of carbon dioxide. The installation further includes a continuous belt configured to support or contain the sorbent and a drive element configured to transport the continuous belt through the adsorption chamber, the desorption chamber, and the cooling chamber. Also disclosed is a method for separating carbon dioxide from ambient air using the installation.

A vapor recovery system comprises an inlet located at a first end of a fluid path configured to receive a fluid vapor to the vapor recovery system. The vapor recovery system comprises a condenser located on the fluid path and a scrubber located on the fluid path. The vapor recovery system comprises a composition sensor located on the fluid path between the scrubber and a second end of the fluid path. The composition sensor is configured to measure a composition of the fluid vapor. The vapor recovery system comprises an exhaust located at the second end of the fluid path configured to exhaust at least a portion of the fluid vapor from the fluid path at a composition having an amount of a working fluid below a working fluid threshold.