The present disclosure relates to an apparatus and a method of delivering a liquid to a downstream process. The apparatus can include a vessel configured to retain a liquid, a bellow in fluid communication with the vessel to receive the liquid from the vessel and in fluid communication with the downstream process to deliver the liquid. The bellow can be exposed to a constant external pressure and configured to deliver the liquid under the constant external pressure when the bellow stops receiving the liquid from the vessel. In some embodiments, the constant external pressure is atmospheric pressure. The bellow can include a pressure deformable material. The apparatus can further include a vaporizer configured to receive the liquid and to produce a vapor, one or more chemical vapor deposition chambers configured to receive the vapor and to hold a substrate for deposition of a component of the vapor on a substrate.

A flow resistant part having a rod shape is disposed in a raw liquid introduction path in a manner such that the raw liquid is sprayed onto a vaporization plate to reduce the conductance of the raw liquid introduction path with respect to the raw liquid. Because the pressure on an outlet side of the liquid mass flow controller is increased, and the pressure difference from the pressure on the inlet side of the liquid mass flow controller is reduced, the occurrence of cavitation can be prevented. A plurality of the flow resistant parts can be provided.

A plant oil extractor includes a food grade tray with a removable lid that together define an evaporation chamber. A gaseous fluid pump has an inlet fluidly connected to the evaporation chamber and an outlet fluidly connected to an area outside of the evaporation chamber, which may be positioned in a freezer to recover condensed solvent leaving previously dissolved plant essential oil on the food grade tray. A vacuum sublimation freeze drying apparatus includes a container, which defines a drying chamber, is positioned in a freezer. A gaseous fluid pump has an inlet fluidly connected to the drying chamber and an outlet that opens outside the container. Water in fresh herbs positioned in the drying chamber initially freezes and then sublimates leaving behind freeze dried herbs.

A system and method for separating bitumen and condensate extracted from separating bitumen from oil sands material is disclosed. The method includes passing the mixture of bitumen and condensate through a flash evaporator to separate them. In the flash evaporator the mixture is heated at high pressure after which it is sprayed into a tank where the pressure is much lower, allowing the condensate to vaporize and the bitumen to settle to the bottom of the tank. The vapors are then passed through a condenser unit, causing them to cool and liquefy.

A hot water and distillation apparatus configured to simultaneously produce distilled water and hot water is disclosed. The hot water and distillation apparatus comprises a hot water tank, a condensation and evaporation chamber, an (feed water) evaporation tray provided in the condensation and evaporation chamber, a heat source thermally connected to the evaporation tray. The hot water and distillation apparatus is configured to condensate evaporated feed water from the evaporation tray by means of heat exchange between the hot water tank and a condensation surface. The condensation surface is provided at the outside surface of the hot water tank. The heat source is thermally connected to the evaporation tray. The hot water and distillation apparatus comprises a distillate collection member configured to collect distillate. The hot water tank, the evaporation tray and the distillate collection member are provided in the condensation and evaporation chamber.

A system of fluid sterilization of fluid of vessel is provided, such as sterilization of ballast water for a water vessel. The system incorporates a heating section to heat pressurized fluid above prescribed thresholds for temperature, pressure, and duration (e.g., dwell time) to achieve desired levels of sterilization, including a heat exchanger to both (a) preheat fluid prior to entering the heating section and (b) cool outflow of the heating apparatus, in which fluid travels through the apparatus by operating valves forward and aft of the heating section in a controlled sequence to facilitate flow through the system while maintaining prescribed pressure and temperature profiles. The system operates within prescribed ranges of pressure and temperature to achieve the desired level of sterilization without need of maintaining a fixed temperature or a fixed pressure within any portion of the system, including the heating section.

Water purification may occur by introducing sufficient heat into a standing fluid wave produced by supplying impure water into a supersonic gas stream. At least partially purified water may be recovered in the form of steam and undergo condensation into liquid water thereafter. Such water purification methods may comprise: generating a supersonic gas stream by feeding a gas through a shockwave nozzle under conditions sufficient to achieve a supersonic velocity, supplying impure water into the supersonic gas stream to produce a standing fluid wave comprising atomized water droplets downstream from an exit end of the shockwave nozzle, introducing sufficient heat into the standing fluid wave to cause at least a portion of the atomized water droplets to phase change into steam, and obtaining the steam as an overhead stream separated from an effluent stream containing one or more contaminants.

A system for condensing vapor product is provided. The system includes a first duct configured to receive a vapor product having a first humidity level, the first duct having a first charge in response to application of a first voltage to the first duct so as to ionize the vapor product. A second duct is configured to allow the ionized vapor product to pass therethrough and configured with a second charge in response to application of a second volt age to thereby allow collection of at least a portion of liquid particles present in the ionized vapor product and form a first modified vapor product. A chamber is configured to receive the first modified vapor product and includes at least one cooling plate configured to reduce a temperature of the first modified vapor product, and at least one first mesh plate configured to collect at least a portion of liquid particles. Methods for condensing vapor are also provided.

A drying apparatus includes a body and a rotatable foot pad located on the lower part of the body to dry a user's feet. An air inlet is provided, and a flow generator to receive inlet air from the air inlet and generate an airflow to the top surface of the foot pad.

The invention relates to a water purification system and distillation unit.

The water purification system (3) comprises an input section (31) for providing water (21), in particular tap water, to a distillation unit (1), and said distillation unit (1) for producing distilled water. Said distillation unit comprises an evaporation section (12) for evaporating said water (21) and producing steam (23), and a condensation section (14) for at least partly condensing said steam (23), producing distilled water. The system further comprises a first admixing unit (32), in particular a cartridge, which is arranged and configured in such a way that it is enabled for admixing compounds, in particular minerals, to said distilled water, producing enriched distilled water, and an output section (33) for dispensing said enriched distilled water. Said evaporation section (12) is provided by a heatable side (101) of a first Peltier effect device (10) and said condensation section (14) is provided by a coolable side (102) of said first Peltier effect device (10).