Abstract: Method and apparatus for desalinizing water. Salt water in an evaporation zone is provided with heat of vaporization by a heat pump which transfers heat to the water from a thermal sink. The evaporation zone is maintained at subatmospheric pressure so that the salt water boils at a temperature at least about 10 degrees above the ambient dew point. The pressure in the evaporation zone is maintained at a low level by a vacuum pump and by condensing the vapor in a condensation zone from which fresh water is collected. The heat of condensation is dissipated into a "cold" sink if available or by a heat dissipating means such as an evaporative cooling apparatus. Energy efficiency results from the ability of the heat pump or pumps in the system to operate at a high coefficient of performance.

Abstract: A process for the concentration of spent brine from the membrane electrolytic cell which comprises removing spent brine containing dissolved chlorine from the membrane electrolytic cell, feeding the spent brine to a concentration zone, applying microwave energy to the spent brine to produce concentrated brine and a gaseous mixture of chlorine and steam, feeding the concentrated brine and the gaseous mixture to a separation zone, separating the gaseous mixture from the concentrated brine, and returning the concentrated brine to the membrane electrolytic cell.Process reduces the operating and equipment costs while effectively recovering chlorine and brine values.

Abstract: Water containing dissolved compounds is preheated, and is then pressurized in stages of water pressure, while receiving a quantum of steam. Scale-forming compounds in the water are thermally precipitated, and clarified post-thermal water is formed. This is flash vaporized in stages corresponding to the stages of water pressure, and the flashed vapors are compressed to form each said quantum of steam. Alternately, the flashed vapors themselves comprise each said quantum of steam, by being induced into the water as it flows through an eductor means. Flash-cooled, post-thermal water, substantially devoid of scale-forming compounds, is employed as such, or more generally is evaporated to form fresh water and an end concentrate of dissolved compounds.

Abstract: A process and system for obtaining fresh water from salt water such as sea water, by direct contact heat transfer using staged evaporator-condenser units operating with a low boiling water-immiscible liquid hydrocarbon. Each stage comprises a closed vessel divided into two compartments, an evaporator and a condenser, by a bubble cap tray similar in construction to those used in distillation. Relatively hot fresh water is introduced into the liquid hydrocarbon contained in the lower compartment of each stage, causing boiling of the hydrocarbon at a temperature difference of 2.degree.-4.degree. F. Hydrocarbon vapors pass from the evaporator compartment through the bubble caps to the upper condenser compartment where they are condensed in contact with a colder saline stream, and the condensed hydrocarbon is returned to the lower compartment.

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: A low pressure, low temperature, solar powered evaporating-condensation system to provide relatively large scale conversion of brackish and seawater to fresh water, utilizes a solar radiation frequency selective material covered evaporation chamber, a throat connected elevated condenser containing energy transferring devices for vapor volume reduction to form a condensate which flows through a water-locked barometric leg to maintain the system at the sub-atmospheric pressure. The system is regenerative and includes means whereby the energy removed from the vapor during condensation is returned to the evaporating chamber and is again utilized in the cycle. Egress valves and locks are provided to maintain balanced flower of raw water, condensate and ejection of residuals. Suitable elevation of the condenser above the evaporator would provide for power generation.

Abstract: A continuous distillation apparatus and method, the apparatus including separate stripping and rectifying sections in tandem, each of which are segregated into a plurality of vapor/liquid contact stages. The rectifying section is operated at a higher temperature than the stripping section by compressing vapor from the stripping section prior to introducing the vapor into the rectifying section. Thermal energy is conserved during the distillation process by transferring thermal energy from the rectifying section to the stripping section with a plurality of heat pipes.

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: Aqueous saline solutions are converted in part to potable water by passing a compressed aqueous saline solution through one or more beds of contained pellets of higher temperature to heat the aqueous solution to a flash vaporization temperature, then passing the solution to one or more flash vaporization zones. Vaporized potable water from each vaporization zone is separately passed to contained bed of pellets where water is condensed and pellets heated. Simultaneously, a bed of pelletized solids is heated to supplant the highest temperature bed in the system used for heating. By selective switching of beds, the system is kept in continuous operation with a heated bed of pellets replacing the highest temperature bed previously used to heat the aqueous saline solution. The bed used for water condensation is transferred to the heating cycle for subsequent introduction to the system.

Abstract: Minerals are recovered from warm geothermal brines by installing a brine eductor device such as a venturi at the end of a thermally insulated drill casing. The geothermal brine is recovered by flowing a warm, low saline carrier solution at high flow rate through the device to pick up a selected flow of brine. On entering the device the geothermal brine is diluted in an amount sufficient to preclude precipitation and scaling as the mixture flows to the surface. The flow velocity is adequate to entrain any non-dissolved solids without settlement. Thermal losses to the surrounding strata are minimized by the thermal insulation surrounding the casing. The mineral values are recovered from the mixture by flashing, evaporation, and filtration. Clarified solution, filter liquor and make-up water as necessary are combined to form the low salinity carrier solution which is heated in heat exchangers before recycling to the eductor device.

Abstract: The water is heated to convert it into steam; the steam is passed from a container into a superheating zone and then condensed in the form of purified water. The superheating zone contains at least in part, a packing of a material inert with respect to steam and impurities possibly present in the latter. The steam is superheated in said zone by means of supplementary heating to a temperature exceeding 300.degree. C., and reaching notably from 400.degree. to 700.degree. C., preferably from 500.degree. to 700.degree. C. Highly purified apyrogenic water freed from undesired organic substances, useful in research in physical chemistry, physics, biochemistry or molecular biology or in the medical field is, produced by this process.

Abstract: A method and a device for controlling the flow through a distillation apparatus for separating components of a mixture, particularly a dissolved substance, such as an oil, a wax, a polishing agent or alike, from a liquid mixture, particlularly containing a chlorinated solvent, such as tri- or perchlorethylene. According to the present invention, the feeding of new liquid mixture or solution into the boiling vessel of the distillation apparatus is controlled in response to the liquid level in the boiling vessel, whereas the draining of substance-enriched liquid or separated substance from the boiling vessel is controlled in response to the distillation temperature, or to a variable being co-variant therewith, so as to maintain the distillation temperature within predetermined limits and the flow through the apparatus at an optimal, high level.

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: 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 solar energy device comprising a body having a plurality of spaced focusing lenses to concentrate direct and reflected rays from the sun. A heat receiving member is inside of said body. One of the body and the member is expansible and contractible so as to direct the member into exact convergence with the focal points of said lenses. The member is supported within said body and fed fluid to be heated. The heated fluid is then removed from the member. The heat receiving member that is expansible and contractible may be employed separately and used as a prime mover.

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: 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 method and apparatus is disclosed where aqueous solutions of chemicals are added to fused non-aqueous baths. This is done by spraying the aqueous solution of the chemicals onto the surface of the fused bath in a fine spray, causing the evaporation of the water.

Abstract: A process for simultaneously generating power and recovering potable water from a source of salinous water-- e.g. ocean and/or sea water. A first portion of salinous water, from the surface of the source, or from a colder, deeper depth, is increased in temperature via indirect contact with a plurality of non-salinous vaporous phases (i) derived from the salinous water and, (ii) obtained therefrom at an elevated temperature and a subatmospheric pressure. The warmed salinous water is further increased in temperature by being maintained in a solar radiation heat sink and exposed therein to radiant solar energy to increase its temperature to a level within the range of about 135.degree. F. to about 210.degree. F. Heated salinous water is introduced into a plurality of vacuum flash separation zones, each succeeding one of which is maintained at a lower absolute pressure. At least one of the resulting vaporous phases is passed into and through a turbine, from the resulting motion of which power is generated.

Abstract: There is described a solar still comprising a pair of juxtaposed corrugated sheets which in a preferred embodiment are positioned at an angle to one another whereby the upper sheet rests on the raised portions of the lower sheet. A thermally insulating, solar energy transmitting window overlies the upper sheet. The upper sheet is made of solar energy absorbent material and the lower portions of the sheet are adapted to contain water to be distilled. A plurality of vents are provided in the uppermost portions of the upper sheet and the lower sheet and are adapted to be placed on the ground or a body of water for cooling and act as a condenser for vapor passing through the vents into the space below the upper sheet.

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: Method and apparatus for implementing the same to provide fresh potable water and electric power from a source of natural brine by the use of energy derived from a geothermal source of pressurized fluid that is of a temperature of greater than 212.degree. F, and which fluid may contain numerous minerals and extraneous material entrained and/or dissolved therein, together with apparatus for carrying out the method. In addition, the invention encompasses a method of providing a clean source of heat for energy conversion from a geothermal source together with an apparatus for carrying out the method.

Abstract: Phosphorus is recovered from phosphorus mud by introducing a skip of phosphorus mud into a furnace, closing the furnace and contacting the skip inside the furnace with a pool of molten lead. Phosphorus vapour is distilled from the mud and recovered.

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: Preheated saline water, typically sea or brackish water, is further heated by quanta of steam, passed to it at differential temperatures and pressures and condensed in the saline water. Scale compounds are precipitated and scale-forming bicarbonates decomposed, with the evolution of carbon dioxide, which is gathered and expelled by steam accessory to the quanta of steam. Post-thermal saline water, which is formed, is multistage flash vaporized while self-cooling. The flashed vapors are compressed to form said quanta of steam. After being further cooled while preheating saline water, post-thermal saline water is evaporated in a multistage vapor compression evaporator, producing brine at a high concentration factor. Relative to equilibrium in scale-compound precipitation between 302.degree. F and 347.degree. F, the recovery of fresh water is 70% to 80% for sea water, and 80% to 90% for brackish waters over a wide range of salinity.

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: In a fractional distillation process and apparatus two columns are intercoupled to provide variable reboil in one and variable reflux in the other so as to approach closely to thermodynamically ideal fractionation. The variable reboil column has a series of heat transfer assemblies at different levels up its height and these are fed with vapor withdrawn from respective different levels of the variable reflux column. Partial condensation of each withdrawn stream takes place in the respective heat transfer assembly, after which the partially condensed stream is returned to the variable reflux column at a level close to the level at which the corresponding vapor was withdrawn. The variable reflux column will ordinarily be at a higher pressure, and mounted at a lower level than the variable reboil column.

Abstract: 2,5 DIOXO-1-OXA-2-PHOSPHOLANES OF THE GENERAL FORMULA: ##STR1## in which R.sup.1 stands for an alkyl radical having from 1 to 4 carbon atoms, or a phenyl radical, and R.sup.2 and R.sup.3 each stand for hydrogen or CH.sub.3, are distillatively purified. To this end the respective crude compound is preheated to 120.degree. to 160.degree. C and fed to the head of a distilling column provided with a plurality of individually heatable trays maintained at temperatures increasing from the upper-most tray to the lowermost, the uppermost tray in the column being maintained at 120.degree. to 160.degree. C and the lowermost tray being maintained at 160.degree. to 200.degree. C, the pressure at the head of the column being 20 to 200 mm Hg, preferably 50 to 120 mm Hg; an inert gas preheated to 160.degree. to 200.degree.

Abstract: A vapor generating and recovering apparatus for separating one component from a second component of a liquid solution and recovering the first component including at least one chamber for generating vapor from the liquid solution and recovering the vapor in a liquid form, the vapor generating portion of the chamber being in heat emitting relation with a heat emitting means and the vapor recovering portion chamber being in heat absorbing relation with a heat absorbing means. A preferred system for providing heat to the vapor generating portion of the chamber and removing heat from the vapor recovering portion of the chamber is a refrigerating system which includes condensing coils and evaporating coils in heat transfer relation with the vapor generating and vapor recovery chamber.

Abstract: A low boiling water immiscible fluid containing two or more molecular species and having a variable boiling point is contacted in the liquid state with relatively hot or warm water such as surface sea water or geothermal water, thereby generating vapor of immiscible fluid (together with a certain amount of water vapor) which is used to drive a prime mover such as a gas turbine and thereby produce mechanical energy; the exhaust vapor from the prime mover is condensed by direct contact with a relatively cool or cold liquid aqueous phase such as deep sea water or water from a lake or stream or cooling tower to condense the vapor; and the condensate is recycled. Provision is made for ridding water discharged from the system of entrained and dissolved immiscible fluid. By countercurrent flow of the liquid phases and by suitable matching techniques greater efficiency is obtained. The invention is also applicable to heat pumps.

Abstract: A more economical method of removing materials adsorbed on solid adsorbents used to treat hydrocarbon streams is presented. The method comprises removing a liquid hydrocarbon stream from a distillation column, vaporizing the liquid stream and superheating the vapors which are formed, passing the superheated vapor through the adsorbent and effecting the removal of the adsorbed material, and then returning the vapor to the fractionation column and utilizing the vapor as stripping media within the column. In the preferred embodiment, water is removed from alumina.

Abstract: A vapor generating and recovering apparatus for separating one component from a second component of a liquid solution and recovering the first component including at least one chamber for generating vapor from the liquid solution and recovering the vapor in a liquid form, the vapor generating portion of the chamber being in heat emitting relation with a heat emitting means and the vapor recovering portion chamber being in heat absorbing relation with a heat absorbing means. A preferred system for providing heat to the vapor generating portion of the chamber and removing heat from the vapor recovering portion of the chamber is a refrigerating system which includes condensing coils and evaporating coils in heat transfer relation with the vapor generating and vapor recovery chamber.

Abstract: Apparatus for manufacturing fresh water which utilizes the energy of surface waves in an ocean, and comprises a buoyant helical member mounted for rotation about an axis. The pitch of the helical member approximates the length of the expected waves and the member is floated on the surface with its axis oriented so that each wave traverses the helix lengthwise and buoyantly supports successive sections thereof causing it to rotate about its axis. The helix is coupled with transducer means for using the rotational energy of the helix to distill the sea water. The ocean is used also as a cooling medium in the distillation process.

Abstract: Saline water, typically sea water or brackish water, after deaeration and deoxygenation is preheated, then further heated by steam condensing with the preheated saline water. By the further heating, bicarbonates are thermally decomposed, forming carbon dioxide, while scale compounds, comprising magnesium hydroxide, anhydrite and minor compounds containing silica, iron, alumina, phosphate, etc., are thermally precipitated. Some of the steam is uncondensed and issues from the further heated saline water with included, evolved carbon dioxide. It is condensed in preheating saline water; evolved carbon dioxide is separated from the condensate and recycled to the saline water to prevent alkaline scale in preheating, while condensate is combined with the further heated saline water, forming post-thermal saline water. This is flash vaporized while cooling and the steam is regenerated by compressing the flashed vapors.

Abstract: Water containing dissolved salt, e.g., sea water, is desalinized by vaporng a part thereof by direct contact with a flame within a closed vessel, e.g., by introducing the water as a spray into a closed vessel onto the flame, removing a gaseous mixture of vaporized water and combustion products, and condensing the water in the mixture within a condenser, while withdrawing unvaporized residual water, enriched in salt, from the bottom of the vessel at a rate to maintain a pool thereof in the vessel.