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The paper presents the results of ground and flight (on OSS Mir) tests of an updated purification assembly of the WRS-C system outfitted with a filter-reactor. The tests have proved that the filter-reactor oxidizes effectively basic organic contaminants in humidity condensate including ethyleneglycol to ones that easily undergo sorption, enables the operation of the recovery system in the event of an off-design increase in organic contaminants in condensate and significantly improves the lifetime of the purification assembly. The data obtained confirm a wise selection of the purification assembly hardware for the system for water recovery from humidity condensate WRS-CM for the ISS service module.

The paper deals with possible performance enhancement of the system for water reclamation from urine based on a principle of atmospheric distillation. It is shown by way of example using the system operating on Mir that the introduction of heat energy recuperation, an increase in heat-and-mass transfer efficiency on evaporation and the optimization of the air flowrate in the distillation cycle allow a rise in the capacity of the distillation assembly and a reduction in specific energy. The system outfitted with a rotary evaporator/separator and a thermoelectric heat pump is reviewed. The design and experimental data verify the feasibility and benefits of the system updating.

The paper analyzes and summarizes experience in developing and flight operation of the system for potable water recovery from humidity condensate. The system schematic and its hardware are reviewed. The system performance data on Salut and Mir space stations are presented. Succession to the development of a similar system for the International Space Station (ISS) service module is shown.

The paper deals with description and results of long-term operation of separation and heat-and-mass transfer hardware incorporated in Mir's water recovery systems. Static separators outfitted with hydrophilic capillary/ porous elements, a rotary separator, a through-flow condenser/static separator combination, a membrane evaporator as well as separation and distillation schematics are reviewed. Operational and life performance data are discussed and recommendations for hardware use on ISS are made.