The invention relates to an arrangement for providing sterile water for injection purposes. A device for heating drinking water above the boiling point, a device for maintaining a chamber inner pressure which lies below the atmospheric pressure, and an electronic controller are provided, and the chamber is equipped with at least one membrane which is impermeable for liquids and a film or plate at a distance from the membrane, wherein steam which is permeated through the membrane is condensed on the film of plate. The membrane and the film or plate form a module, and the condensed water can be removed from the chamber via an outlet as sterile water for injection purposes.

Embodiments provide methods and structures for purification or volume reduction of a brine by an advanced vacuum distillation process (AVMD) to achieve higher flux by passage of vapors through an AVMD distillation unit. In one example, brine is circulated in a tank. The tank may include one or more membrane pouches that are submerged in the circulating brine or placed above the water level of the hot circulating brine. In other embodiments the membrane pouches are outside of the tank that includes the hot circulating brine but still in communication with it. The circulating brine is heated, allowing creation of water vapor. Using a vacuum, the water vapor is drawn through the membrane, where it may be condensed and subjected to further beneficial use. This process can concentrate to levels to generate crystals or solids, which can be separated and utilized.

A filter flow management system includes a cartridge having an inlet through which fluid flow can be introduced to the cartridge, a plurality of channels situated within the cartridge and designed to remove particulates from the fluid flow, at least one channel being in fluid communication with the inlet to receive the fluid flow, and a reservoir into which fluid flow flowing through the at least one channel can be directed and subsequently redirected into at least one other channel.

Apparatus for energy-efficient conductive-gap membrane distillation includes a feed-liquid source and a distillation module. The distillation module includes a feed-liquid chamber in fluid communication with the feed-liquid source. The feed-liquid chamber includes a selectively porous material that allows a component of the feed liquid to pass through the selectively porous material and exit the feed-liquid chamber in vapor form but not in liquid form. The distillation module also includes a conductive-gap chamber adjacent to the selectively porous material on an opposite side of the selectively porous material from the feed-liquid chamber; a heat-transfer surface maintained at a lower temperature than the feed liquid in the feed-liquid chamber, wherein the heat-transfer surface is in thermal contact with the conductive-gap chamber; and a thermally conductive material extending across the conductive-gap chamber.

A replaceable membrane distillation module has a membrane distillation plate with an upper portion and a lower portion at two ends respectively. Two upper holes and two lower holes are defined through the upper portion and the lower portion at two ends respectively. A distillation portion is recessed in at least one side of the membrane distillation plate, and a distillation membrane covers on the distillation portion that a distillation space forms between the distillation portions and the distillation membrane. Multiple channels are disposed in the membrane distillation plate to communicate one of the upper holes, the distillation space and one of the lower flow holes. A blocking element is selectively combined with one of the upper holes or one of the lower flow holes.

A system for regeneration of acidic gas solvent, the system comprising; a regeneration cell having a solvent chamber arranged to receive a solvent flow, and an internal chamber arranged to receive a steam flow; said regeneration cell including a gas permeable membrane separating the solvent chamber and internal chamber; wherein the regeneration cell is arranged to vent acidic gas stripped from the solvent by the steam.

A human waste processing system adapted to process both human solid and liquid waste deposited into a toilet or similar vessel and to process the waste for further use and/or convenient disposal. The present system is specifically configured for use with low-water-volume flush toilets and dry toilets. In particular, the present system is configured to separate solid waste and liquid waste with liquid waste being processed via a plurality of sequential filtration stages and with the solid waste being processed by thermal decomposition such as pyrolysis/torrefaction processing.

A water purification system utilizes an ionomer membrane and mild vacuum to draw water from source water through the membrane. A water source may be salt water or a contaminated water source. The water drawn through the membrane passes across the condenser chamber to a condenser surface where it is condensed into purified water. The condenser surface may be metal or any other suitable surface and may be flat or pleated. In addition, the condenser surface may be maintained at a lower temperature than the water on the water source side of the membrane. The ionomer membrane may be configured in a cartridge, a pleated or flat plate configuration. A latent heat loop may be configured to carry the latent heat of vaporization from the condenser back to the water source side of the ionomer membrane. The source water may be heated by a solar water heater.

The invention relates to a distillation apparatus for producing water for injection, comprising: at least one membrane distillation module (500, 600), the module being configured to be flowed through by a liquid to be concentrated, wherein: the module (500, 600) comprises at least one condensation/evaporation stage (50, 60), the condensation/evaporation stage (50, 60) comprises at least one condensation/evaporation element (101, 102), and the condensation/evaporation element comprises at least one condensation unit (101) and at least one evaporation unit (102), the apparatus further comprising: a heating stage (300) configured to generate steam and to provide the steam to the at least one condensation/evaporation stage (50, 60) of the at least one module, and a droplet elimination device (320) comprising a membrane (321) configured to separate droplets from the steam generated by the heating stage.

A desalination system employs vacuum to evaporate heated water through a separator material. The evaporated water is then passed through a heat exchanger wherein the heat is exchanged with an inflow of water to the system to heat the incoming water and greatly increase the overall system efficiency. The incoming water heated in the heat exchanger may then be passed to a heater to further heat the water before being provided to an evaporator. A vacuum is drawn across a separator material in the evaporator to produce evaporated water vapor that is purified. This water vapor is then provided to the heat exchanger, wherein the water vapor is condensed and the incoming water is heated. An ozone disinfecting system may produce ozone that is mixed with the condensed water to produce a purified and disinfected water that is suitable for consumption.