Abstract: Solar distillation apparatus are disclosed in which a substantial part of the heat of condensation of the condensing liquid is recovered. A conduit having an inclined smooth lower surface is disposed above the liquid to be distilled and on which the evaporated liquid condenses and releases its heat of condensation. A fluid is circulated through the conduit in a heat exchanging relationship with the lower surface thereof, the fluid absorbing a substantial part of the released heat of condensation. The condensed liquid flows along the bottom of the inclined lower surface and is discharged from the lower end thereof and collected. The conduit in the preferred embodiments is flat and transparent and the spacing between the upper and lower walls of the conduit is selected so that only a small part of the solar energy is absorbed in the conduit while the fluid in the conduit recovers a substantial part of the released heat of condensation.

Abstract: A method and apparatus are disclosed relating to the recovery and reuse of heat during fractionation of liquids in a tray-type fractionating tower. According to this method, a portion of the feed to the tower is directed through heat exchange tubing positioned on the trays in such a way that the tubing is in contact with liquid there present so as to bring about an indirect exchange of heat between the said liquid on the trays and the liquid in the tubing, at the same time that there is occurring the normal transfer of heat by direct contact between the vapor and the liquid on the trays and the normal interchange of material components by direct contact between vapor and liquid on the trays, the said heat exchange tubing being serially connected so as to carry liquid from tray to tray.

Abstract: In recovering the multi-solvent portion of the oil solvent mixture in a solvent dewaxing process, decomposition of a thermally unstable, lower boiling solvent component is substantially avoided by recovering the solvent in a series of controlled evaporations whereby the major portion of the lower boiling solvent component is removed from the mixture prior to the removal of the remaining portion of the solvent. The solvent removal may be conducted in a high pressure evaporator having an upper section and a lower section separated by an annular tray.

Abstract: A process is described for the removal of acid gases and ammonia from dilute aqueous solutions. This is achieved by two separate and successive distillations. In the first distillation, substantially all of the acid gases and free ammonia are removed. In the second distillation, substantially all of the fixed ammonia is removed. Exemplary aqueous solutions are waste waters from coke oven and coal conversion plants.

Abstract: A water distillation apparatus having a feed water pre-heater, an evaporator tank, and a storage tank. The storage tank has an upper surface and depending walls, the pre-heater and evaporator tank being on the upper surface, and extending, with the other components, to approximately the same height, all components being within the periphery of the walls. A mixing vessel including a level controlling overflow pipe receives water from the pre-heater, and a short, straight, large diameter conduit connects the mixing vessel and evaporator tank. The mixing vessel contains a valve to drain it and the evaporator tank. The pre-heater comprises two dished elements in facing relation, with a divider plate between them, the elements being joined at their peripheries. A serpentine path is provided in each of the two spaces of the pre-heater, formed by a pair of L-shaped separators extending linearly from one end of the space to a point spaced from the other end.

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: 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: 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 improved solvent recovery process comprising distilling soiled solvent in a main still and conducting hot solvent vapor through a heat exchanger associated with a tank in which an azeotropic mixture of water and soiled solvent is maintained, which mixture boils at a temperature lower than the boiling point of the solvent alone. A series of tanks feed soiled solvent to the azeotropic mixture tank and then to the main still, and heat exchangers fed by the vapor from the main still and the vapor from the azeotropic mixture tank pre-heat the soiled solvent. Automatic control of water injection into the azeotropic mixture tank in dependence upon the temperature of conductivity of the tank contents maintains the composition of the azeotropic mixture, the injected water being taken from separators which separate water from condensate of the main still and azeotropic mixture tank vapors.

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: Purified methanol is produced by distilling a water methanol mixture in (a) a first column from which is taken a product methanol stream at an upper level, weakly aqueous methanol as a side stream and water as bottoms and (b) a second column in which that weakly aqueous methanol is separated into an overhead product stream and aqueous methanol bottoms. The first column may be preceded by a preliminary volatiles-removal column. The process is economical in heat consumption, especially when methanol vapor from the second column is heat-exchanged with the feed or bottoms of the first column.

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: 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: A solar energy collector floating on water is supported by fluid cushion and comprises elements each of them consist of a solar energy absorbing layer arranged between two heat insulating layers.

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 using solar energy comprises a main insulated container with a subsidiary preheating container next to it; the main container is covered with a transparent cover serving as a selective filter to provide "the greenhouse effect" and also as a condensation surface for water vapor, and this transparent cover incorporates a hollow space, for example by making the cover double skinned. The hollow space forms part of a syphon which automatically regulates the water levels, transferring salt water from a preheating container to the main container as the level in the main container falls due to loss by evaporation leading to condensation and withdrawal of the desalinated water. The hollow part of the transparent cover thus serves also to preheat the incoming salt water with the heat lost upon condensation by the vapor within the main container.

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: 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: An integrated system for converting ocean thermal energy to electrical power for use in synthesis of anhydrous ammonia and a mariculture operation for raising a selected species of marine fauna. The mariculture operation is carried out in a lagoon located adjacent to a deep ocean region where the surface water temperature is at least 21.degree. C and the deep nutrient-rich water temperature is no more than about 10.degree. C. A separate working fluid, such as ammonia, operates in a Rankine cycle between the warm and cold seawater temperatures. The deep ocean water is used to condense the working fluid and is then mixed with warm surface water that has been used to evaporate the same working fluid in a closed power cycle. The resulting mixture is directed to the lagoon, where the nutrient-rich component contributes to the growth rate of a selected mariculture species.

Abstract: In dual temperature systems utilizing different fluid materials in liquid and gas phases separable from each other (for example H.sub.2 O and H.sub.2 S), the phases are contacted with each other at a relatively hot temperature. Herein combinations of method and means are provided by which the gas is conditioned by raising its temperature and humidity principally by heat derived from the cooling and dehumidification of said gas. Special provisions are made in the combinations for transferring said heat and for the conditioning of the gas with high efficiency; and for economically controlling the temperature of the condensate resulting from the dehumidification of the gas to adapt it for particular uses in the system. Method and means are provided for such liquid gas contacting systems for efficiently stripping or separating dissolved gas from the effluent liquid and returning one of the so separated materials to the system.

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: 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.