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IIR document
Production of stable neon isotope by the method of low temperature rectification.
Desorber and rectifier geometries for ammonia-water absorption systems; Part II: Mass transfer, flooding, and component performance.
Parameter optimization of successive stages of the technology for obtaining 3He isotope from natural helium.
Universal research cryogenic unit for xenon production.
Comparison of refrigeration cycles used for production of pure neon and its isotopic components.
Theoretical and experimental study of improved cycle for large temperature lifts application in ammonia water absorption system.
Heat and mass transfer in microscale diabatic distillation columns for ammonia–water desorption and rectification.
Modelling and experimental analysis of the desorber of a gas-fired absorption heat pump.
Experimental study on improving the performance of dry evaporator with rectifying nozzle type critical distributor.
Desorber and rectifier geometries for ammonia-water absorption systems; Part I: Experimental approach and heat transfer.
Separation of binary mixtures based on helium and heavy inert gases.
Low-temperature natural helium separation processes for obtaining 3Helium isotope.
Design and modeling of a microscale diabatic distillation column for small capacity ammonia–water absorption systems.
Low-temperature application adsorption method for separation of rare inert gas isotope mixture.
Experimental investigation of an absorption refrigerator working with ionic liquid and ethanol.
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Activities of the IIR’s Commission A2 on Liquefaction and Separation of Gases
The problems related to thermodynamic optimization and new technologies in liquefaction and separation of gases are actual and critical for many branches of modern industry, power generation and medicine.