Abstract: Apparatus comprising a solar still and a wind powered generator. Sea water is preheated in a condenser and is supplied to the still where it is heated further either by solar radiation, or by a heated pipe containing brine, or both. The still supplies warm humid air and vapor to the condenser to provide a distilled water condensate, which condensate is supplemented by water collected from the sloping parts of the still roof. The brine in the heated pipe in the still is supplied from a brine pit which is heated by electrodes connected to the wind powered generator. The generator also charges batteries and supplies electrical power to brine pumps and to a ventilator in the still.

Abstract: There is disclosed a water distiller, primarily for producing water for human consumption which includes a boiler, a distillation tower extending about two or more feet above the boiler, and a steam conduit exiting from near the top of the tower leading into a helically grooved condensation tube with a water-cooled jacket. The boiler and tower are of uniform cross-section to facilitate cleaning. The water jacket has a water inlet located in the bottom and an exit orifice for preheated input water at the top. A conduit from the orifice leads to an evaporator for volatile impurities on top of the tower, and a conduit for preheated input water leads to the bottommost part of the boiler from the evaporator. An overflow conduit with an intermittent siphon is provided connected to the bottom of the boiler; the highest and lowest points of the siphon serve to automatically regulate the maximum and minimum depths of water in the boiler.

Abstract: A solar still apparatus having a condensation chamber is disclosed. A plurality of hollow columns are connected to the chamber at the open upper ends of the hollow columns and the lower ends of the hollow columns are adapted to engage a support surface for the still apparatus. The hollow columns also function to contain distilland liquid and to support parabolic solar collectors for heating the liquid to form vapor at the upper end of the hollow columns. The vapor is introduced into the condensation chamber for condensing to form a distillate liquid. Means including a shield and an evaporative surface layer are disclosed to aid the cooling of the condensation chamber relative to the vapor to facilitate the condensation of the vapor in the chamber.

Abstract: An apparatus and method for removing contaminants from water having solid contaminants dissolved therein. Contaminated water flows across a grid and into a storage tank. The grid utilizes solar energy to heat that water to a predetermined temperature. A heat transfer structure which is dome-shaped and receives water from the storage tank and a preheater means utilizing solar energy heats the water to a further predetermined temperature. An evaporator means receives the heated water and exposes it to a vacuum condition so that the temperature of the water is above the saturation temperature. The water is thus vaporized, and solid contaminants dissolved therein are separated therefrom. The solids are deposited on a plurality of moving belts and are then moved into a solids removal system. The solids removal system comprises a plurality of trap door pairs upon which the solids are deposited and which are sequentially opened so that the vacuum conditions existing in the evaporator are not disturbed.

Abstract: An apparatus and method for removing contaminants from water having solid contaminants dissolved therein. Contaminated water flows across a grid and into a storage tank. The grid utilizes solar energy to heat that water to a predetermined temperature. A heat transfer structure which is dome-shaped and receives water from the storage tank and a preheater means utilizing solar energy heats the water to a further predetermined temperature. An evaporator means receives the heated water and exposes it to a vacuum condition so that the temperature of the water is above the saturation temperature. The water is thus vaporized, and solid contaminants dissolved therein are separated therefrom. The solids are deposited on a plurality of moving belts and are then moved into a solids removal system. The solids removal system comprises a plurality of trap door pairs upon which the solids are deposited and which are sequentially opened so that the vacuum conditions existing in the evaporator are not disturbed.

Abstract: According to one aspect of the invention, a system is disclosed for substantially continuous distillation of water which comprises a plurality of parallel distillation units each comprising series of fluid and preferably also Fresnel-type lenses. Water to be distilled is preheated by circulating it through the fluid lenses on which evaporated water vapor is condensed to produce distilled water. The quantity of water circulated in the lenses is many more times the quantity of water evaporated by the solar energy concentrated by the lenses and condensed per unit of time to allow the circulated water to carry off heat recuperated within the lenses and the system. The preheated water circulated through the lenses is discharged into a central container in which the foci of the fluid and Fresnel-type lenses are located. Secondary containers are provided to receive overflow from the central container since preheated water may be discharged into the central container faster than it is being evaporated.

Abstract: A method and closed system for high volume distillation of impure liquids comprises evaporating the impure liquid in an evaporator to form a vapor at a temperature above the freezing point and below the critical point, preferably the boiling point, of the liquid at ambient pressure and at a pressure not exceeding a pressure corresponding to the evaporation temperature under saturated conditions; compressing the vapor in compression means which preferably has a compression ratio variable in the range 1.

Abstract: A method and apparatus for high volume distillation of impure liquid comprises evaporating the impure liquid in an evaporator to form a vapor at a temperature above the freezing point and below the boiling point of said liquid at atmospheric pressure and at a pressure not exceeding a pressure corresponding to the evaporation temperature under saturated conditions; compressing the vapor; passing a portion of the compressed vapor through an expansion engine to do work upon and motivate the engine and to produce shaft energy, whereby the vapor expands and cools; bypassing the expansion engine with the remainder of the compressed vapor and admixing the remainder directly with the expanded vapor from the expansion engine in a mixing chamber; adding work to the expansion engine to supplement the work done by the vapor expanding therethrough to make up for work lost when the remainder of the compressed vapor bypassed the expansion engine and for other work lost; cooling the admixed vapor in heat transfer relation wi

Abstract: An impure liquid is continuously distilled in a deaerated conduit arranged in a coil to present adjacent loops in heat exchange relationship. The conduit is divided by a partial partition into a distilland trough and a distillate trough, the latter being on the outside of each loop. The impure liquid is introduced into the distilland trough for flow therealong and vaporization, and the resultant vapor crosses over to the distillate trough due to centrifugal force and condensation within the distillate trough. As the vapor condenses in the distillate trough, the heat of condensation is transferred to the distilland trough of the adjacent downstream loop and to the incoming liquid flowing in a feed tube lying in the distillate trough. Spaced obstructions to vapor flow in the distillate trough and flow guide fins are employed to increase efficiency. A number of coils may be stacked to provide a multi-unit distillation system.

Abstract: The double effect floating solar still uses a partly immersed corrugated metal plate to heat the upper layer of a body of water in order to establish a temperature difference between the upper and lower sections of the still. The difference in temperature creates a difference in vapor pressures, forcing the vapor produced in the hot section of the still to flow into a submerged condenser, giving up the heat of condensation to the surrounding water, preheating it before it reaches the stage of evaporation.

Abstract: The invention provides unusally efficient distillation apparatus configured into a compact structure which conserves material in its construction and power consumption in its operation. The present structure particularly provides horizontally disposed flash effect distillation chambers coupled "back-to-back" across a common wall, the chambers being operable as a distillation system for water purification and/or solute concentration or as a sub-system in multi-effect distillation systems.

Abstract: Desalination apparatus utilizing solar heating of metal member(s) such as balls, rollers, or metal endless belt(s) in a heating chamber and vaporizing saline water with the latent heat in said metal member(s) by spraying saline water thereon in a vaporizing chamber, a water-cooled condenser to condense the vapors, a trough to collect the condensate, a rinse tank to remove salt deposits and/or saline water from the metal member(s), and means for returning the rinsed metal member(s) for solar reheating.

Abstract: A process for simultaneously generating power and recovering potable water from a source of salinous water -- e.g. sea water. Salinous water, from a locus which is proximate to the surface thereof and at a relatively high temperature -- e.g. about 85.degree. F. -- is increased in temperature via indirect contact with a vaporous phase, derived from the surface water at an elevated temperature and a subatmospheric pressure. The preheated salinous water is exposed to radiant solar energy, in a solar radiation heat sink, to further increase the temperature thereof. Thus-heated salinous water is introduced into a first flash separation zone, maintained at subatmospheric pressure, to provide a first substantially non-salinous vaporous phase and a first salinous liquid phase. The first vaporous phase is passed into and through a turbine, from the resulting motion of which power is generated.

Abstract: A home water distiller which provides for an efficient distillation process wherein the inlet water supply is controlled as a function of the temperature of the output of the distiller, and which inlet water is preheated by introducing it into a chamber surrounding the condensor coils. After preheating, the water flows into the boiling chamber. The unit is provided with a flowthrough or constant-flush drainage system to keep mineral buildup to a minimum, and to provide for automatic control of the input water.

Abstract: A flash evaporator to be used for purposes such as distilling sea water has a series of evaporator stages in which vapor derived from liquid flowing through the successive evaporator stages is condensed to form a distillate. A wall structure situated in each evaporated stage defines therein an elongated narrow gap the length of which is substantially greater than the width of each evaporator stage with this gap forming an orifice through which the liquid is compelled to issue while flowing from an inlet to an outlet of each evaporator stage. Between the inlet and the gap in each evaporator stage the wall structure defines an upstream flow path the cross section of which decreases from the inlet toward the gap. From the gap toward the outlet of each stage the wall structure defines a downstream flow path the cross section of which increases from the gap toward the outlet.

Abstract: A municipal water supply system for providing potable water under pressure from sea water including a nuclear reactor heated boiler for raising the temperature of sea water to at least 250.degree. F and at superatmospheric pressure means for conveying the superheated steam to an expansion turbine, whereby the superheated steam drives the turbine while the temperature of the steam is reduced to about the boiling point of water at atmospheric pressure, a heat exchanger for condensing the exhaust from the turbine while simultaneously preheating incoming sea water to the system, and liquid pumping means driven by the expansion turbine for conveying the condensed water under pressure to a municipal distribution system. Additionally, means are provided for controlling the temperature within the boiler chamber by controlling the volume of incoming sea water.

Abstract: Vapor degreasing apparatus comprising a tank having in its lower part a heatable reservoir for a solvent for fats, oils, lubricants or the like, and having, above said reservoir, a vapor space adapted for introducing therein metal articles or machine parts to be degreased. Cooling water piping is provided in the upper part of the tank, said piping comprising a section which functions as a heat exchanger for incoming heat released during the vapor-liquid conversion of the solvent while forming a vapor escape barrier for retaining, through condensation, the solvent vapor, said piping also comprising a section which functions as a heat exchanger for outgoing heat to the ambient air.

Abstract: A water distiller arrangement which provides for an efficient distillation process wherein the inlet water supply is controlled as a function of the temperature of the output of the distiller, and inlet water is preheated in an interior chamber surrounded by a passageway through which the water vapor passes after leaving the boiling chamber and while it condenses.

Abstract: A method and apparatus for high volume distillation of impure liquid comprises evaporating the impure liquid in an evaporator to form a vapor at a temperature above the freezing point and at or below the boiling point of said liquid at atmospheric pressure and at a pressure corresponding to the evaporation temperature under saturated conditions; compressing said vapor adiabatically; admixing in a mixing chamber the compressed vapor under substantially isobaric conditions directly with hot gases having a temperature sufficiently greater than the temperature of the compressed vapor that the resulting vapor-gas mixture temperature is greater than the temperature of the compressed vapor prior to the mixing; passing the vapor-gas mixture through an expansion engine to motivate the engine and to produce shaft energy, whereby the vapor-gas mixture adiabatically expands and cools; compressing the expanded vapor-gas mixture adiabatically in an independently powered compressor to a predetermined pressure corresponding

Abstract: A system for optimal pressure control in a multistage evaporation unit comprising two or more series connected evaporation stages with at least one of the stages preceded by a heat source, where the fresh or feed solution is passed through heat exchangers in which it is heated by means of the vapors from the subsequent evaporation stages, and where a heat exchanger adapted to permit free flow of the vapor condensate through the heat exchanger inner portion or tube portion is arranged in the line through which the vapor leaves the higher-pressure evaporation stage.

Abstract: A float valve arrangement is disposed in a mixing condenser that is arranged intermediate the first and second stage of a two-stage evaporation installation suitable for purifying radio-active liquids. In normal operation, vapor evaporated in the first stage extends via a first conduit into the mixing condenser where such vapor is condensed by contact with a portion of the liquid in the second stage that is circulated back to the mixing condenser via a pump. The normal vapor pressure generated in the first stage keeps the float valve open and permits the steam to displace, into the second stage, liquid present in the mixing condenser. During start-up and shutdown of the installation wherein vapor from the first stage is no longer present, the resulting rise in liquid level in the mixing condenser causes the float valve to close and to prevent any backflow of liquid into the first stage via the first conduit.

Abstract: A water distillation unit is disclosed herein. The unit preferably comprises an upper boiler container and a lower condensation container which are rigidly maintained in spaced apart relationship by a molded coupling member containing a plurality of water passageways and fittings. The coupling member is integral with the condensation container and is removably and threadably attached to the upper boiler container so that same may be easily removed when desired for cleaning. The boiler container receives raw liquid which is vaporized by an interiorly disposed heater element. The condensation container houses a condenser tube which receives steam from the boiler container and conducts distillate exteriorly of the apparatus. To improve thermal efficiency the condenser tube is cooled by raw liquid which is routed through the condensing container.

Abstract: A vapor compression distillation system utilizing a two stage vapor compressor comprising a rotary positive displacement first stage compressor backed by a second stage liquid ring compressor.

Abstract: An automatic water distiller has an insulated evaporator to which water is supplied after being preheated by cooling the steam, which is produced by the evaporator, in a condensing chamber with which the water is in heat exchange relation. Air also flows in heat exchange relation with the condensing chamber to aid in condensing the steam. A storage chamber is disposed above the evaporator and beneath the condensing chamber to receive the condensed steam and the air, which flows over the condensing chamber to cool the steam therein, is first passed in heat exchange relation with the distilled water in the storage chamber. The vapors in the condensing chamber are vented to the chamber in which the water is in heat exchange relation with the condensing chamber.