An LED lighting fixture powered by a Metal-Organic Framework heat battery. The heat battery is formed of a canister, a MOF container comprised of a plurality of MOF tunnels, each MOF tunnel containing a powdered MOF material, a gate, and a plurality of thermoelectric devices.

Below a certain adsorption activation temperature, the MOF material adsorbs a gas from the atmosphere. Above a certain desorption activation temperature, the MOF desorbs the gas. The heat from the adsorption is used to generate electrical current. The desorbed gas is captured to remove it from the atmosphere.

Pressure swing adsorption process for reducing fluctuations in the flow rate of tail gas from the adsorption unit and reducing fluctuations in the stoichiometric oxidant flow rate required to completely combust the tail gas in a reformer furnace. Constant flow rate and constant fuel property can be obtained by intelligent mixing designs.

An installation and method for recovering gaseous substances from gas flows comprising a first gas-treatment module (module 1) to receive a first inlet gas flow (1) in which the temperature and pressure are controlled in order to dry said flow by removing water, nitrogen and sulfur oxides, unburned substances and other solids in suspension, a second CO.sub.2 separation module (module 2) in which the first outlet flow (13) from module 1 is treated using a PSA adsorption/desorption process to separate the gases selected, thereby enriching the third outlet flow (27), and a third, optional module (module 3) in which the CO.sub.2 purification process is carried out and in which the third outlet flow (27) from module 2 is treated using a PSA adsorption/desorption process to separate the gases selected, thereby enriching the fifth outlet flow (44) from module 3.

An installation and method for recovering gaseous substances from gas flows comprising a first gas-treatment module (module 1) to receive a first inlet gas flow (1) in which the temperature and pressure are controlled in order to dry said flow by removing water, nitrogen and sulfur oxides, unburned substances and other solids in suspension, a second CO.sub.2 separation module (module 2) in which the first outlet flow (13) from module 1 is treated using a PSA adsorption/desorption process to separate the gases selected, thereby enriching the third outlet flow (27), and a third, optional module (module 3) in which the CO.sub.2 purification process is carried out and in which the third outlet flow (27) from module 2 is treated using a PSA adsorption/desorption process to separate the gases selected, thereby enriching the fifth outlet flow (44) from module 3.

Provided is an oxygen concentration device, a control method, and a control program with which a start-up interval until a desired high-concentration oxygen gas can be supplied can be reduced. The oxygen concentration device includes a pressurized air supply unit for supplying pressurized air, an adsorption tube which concentrates oxygen in the pressurized air by adsorbing nitrogen in the supplied pressurized air to generate oxygen gas, an oxygen gas tank for storing oxygen gas, a flow rate adjustment unit which adjusts an oxygen gas flow rate to be output to the exterior from the oxygen gas tank, and a control unit which controls the flow rate adjustment unit so that the oxygen gas flow rate becomes a set flow rate and controls the pressurized air supply unit so that the pressurized air achieves a supply amount corresponding to the set flow rate.

A portable oxygen concentrator designed for medical use where the adsorbent beds, are designed to be replaced by a patient. The concentrator is designed so that the power supply and adsorbent bed mount is one module and the compressor and air filter are part of another module configured to provide a unitary cooling and air supply system. Replacement beds may be installed easily by patients, and all gas seals will function properly after installation.

A portable gas separator assembly utilizing carbon molecular sieve absorbents or elements to separate a compressed air stream to extract nitrogen and oxygen molecules. Components of the assembly include at least two charging towers so that one tower can be charged with compressed gas while the other of the at least two towers is purged.

The present invention discloses methods for extracting and recycling ammonia in MOCVD processes by FTrPSA. Through pretreatment, medium-shallow temperature PSA concentration, condensation and freezing, liquid ammonia vaporization, PSA ammonia extraction, and ammonia gas purification procedures, ammonia-containing exhaust gases from MOCVD processes are purified to meet the electronic-level ammonia gas standard required by the MOCVD processes, so as to implement recycling and reuse of the exhaust gases, where the ammonia gas yield is greater than or equal to 70-85%. The present invention solves the technical problem that atmospheric-pressure or low-pressure ammonia-containing exhaust gases in MOCVD processes cannot be returned to the MOCVD processes for use after being recycled, and fills the gap in green and circular economy development of the LED industry.

A carbon dioxide recovery system includes: an adsorber configured to adsorb and desorb carbon dioxide; a supply channel through which supply gas passes; a storage section configured to store carbon dioxide desorbed from the adsorber; and a gas supply section supplying carbon dioxide stored in the storage section to the adsorber. The carbon dioxide recovery system is operated in an adsorption mode, a desorption mode or in a desorption preparation mode. In the adsorption mode, the adsorber adsorbs CO.sub.2 contained in the supply gas supplied through the supply channel. In the desorption mode, the adsorber desorbs the adsorbed CO.sub.2, and the storage section stores CO.sub.2 desorbed from the adsorber. In the desorption preparation mode, the gas supply section supplies CO.sub.2 stored in the storage section to the adsorber during a time from an end of the adsorption mode to a start of the desorption mode.

A carbon dioxide recovery system includes: an adsorber configured to adsorb and desorb carbon dioxide; a supply channel through which supply gas passes; a storage section configured to store carbon dioxide desorbed from the adsorber; and a gas supply section supplying carbon dioxide stored in the storage section to the adsorber. The carbon dioxide recovery system is operated in an adsorption mode, a desorption mode or in a desorption preparation mode. In the adsorption mode, the adsorber adsorbs CO.sub.2 contained in the supply gas supplied through the supply channel. In the desorption mode, the adsorber desorbs the adsorbed CO.sub.2, and the storage section stores CO.sub.2 desorbed from the adsorber. In the desorption preparation mode, the gas supply section supplies CO.sub.2 stored in the storage section to the adsorber during a time from an end of the adsorption mode to a start of the desorption mode.