Abstract: Solar distillation apparatus is disclosed in which the released heat of condensation of the condensing liquid is recovered in a transparent conduit disposed over the liquid to be distilled. Solar energy passes through the transparent conduit and is received on an undulated plate system over which the liquid to be distilled is conducted. A cooling fluid is circulated through the conduit to absorb heat released by the condensing liquid. In one embodiment, the conduit does not concentrate the solar energy. The conduit is preferably disposed at an angle of up to about 25.degree. with the horizontal so that the system is subjected to minimal pressure. In another embodiment the conduit defines a fluid lens system which concentrates the solar energy on the plate system. Provision is also made to recover heat from the condensate and a concentrate of the liquid to be distilled.

Abstract: A method for removing vinyl chloride monomer rapidly from a large amount of slurry of vinyl chloride resin to give waste water separated from said slurry, exhaust gas used in the drying of separated resin and resin product which are not objectionable from the environmental sanitation or to produce such a treated slurry which can give waste water separated from said slurry, exhaust gas used in the drying of separated resin and resin product which are not objectionable from the environmental sanitation by the repetition of said method. In said method a slurry of vinyl chloride resin is caused to flow down a plate column in which flow of slurry on the trays in each step of plates is treated with steam in a combination of specified plates and specified conditions of treatment.

Abstract: Apparatus is provided for converting sea or other undrinkable waters to drinkable water without the use of driven or moving parts. Reliance upon gradient effects is made to effect the vaporization of, for example, sea water, followed by the condensation of the vapor to form distilled water. Gradient effects are achieved through the provision of differentials in the thermal conductivity, capillary activity, adsorptive, absorptive and/or pressure characteristics of particulate materials, or combinations of such physicals. For example, a column is packed with material graded as to its conductivity, the least thermally conductive material being nearest the cold or ambient water that is to be purified. In packing the column each successive layer of material has a greater thermal conductivity than the layer beneath it with the most conductive being at the top near the outlet arm of the column.

Abstract: A method and an apparatus is disclosed in which solar heated air is drawn down a hole in the earth by a draft from a solar heated convection column located above the surface of the earth, the hot air being initially drawn downwards to a depth at which damp, moist earth is encountered with the hot air thereby evaporating water from the damp earth and producing water vapor and increasing the moisture content of the heated air and as this damp air is subsequently drawn back to the surface by the draft from the same solar heated convection column, it is allowed to contact cooled plates near the surface, the water vapor thereby condensing on the plates from which it is collected for irrigation or other purposes. In various embodiments either vertical or horizontal porous tubes in the ground contact the moist earth to bring the moisture of the earth into contact with the heated air flowing through the tube.

Abstract: A solar fermentation process and distillation system for the manufacture of ethanol product suitable for blending with motor gasoline or as a substitute fuel for gasoline. Fermentation of starches or sugars is carried out in situ in solar collector tubes. The raw beer product emanating from the solar tubes is purified into a high quality ethanol fuel product by passing the beer product through a series of distillation columns whose internal reboil vapor is generated in whole or in substantial part through direct application of solar heat energy. The use of solar energy as heating source in the fermentation and distillation steps markedly reduces the need for external utilities such as steam and fuel to run the plant thereby greatly reducing the operating costs of the plant.

Abstract: Individually useable wave-powered pumping means, solar distillation means, and cyclonic wind generating means, together with a system which employs each of them for harnessing natural energy sources are disclosed. Wave and solar energy, together with Coriolis acceleration are employed in the system which includes a basin for water situated near an ocean, or othe such body of water, having a surface subject to wave action. A solar energy transmitting cover is provided over the basin for solar heating, and evaporation of water contained therein. Vapor condensing means are located adjacent the bottom of the basin, and an upwardly extending inlet conduit, or passageway, connects the condenser to a source of water vapor above the water surface of the covered basin. Cooled air, and distilled water, are discharged from the condenser to a location outside the covered basin.

Abstract: Solar apparatus for producing alcohol including a frame portion, a heating portion, a slurry-forming portion, a fermentation portion, a distillation portion, a condensation portion and a drying portion; the heating portion including a plurality of solar panel members, the slurry-forming portion including a hammer mill and a frustoconical section thereunder, the frustoconical section including a tangential liquid inlet opening and a tangential slurry outlet opening, the fermentation portion including a fermentation chamber, a pump disposed adjacent the chamber, inlet and outlet conduits extending between the pump and the bottom of the chamber, the distillation portion including a base section and a face section, the face section including a conduit having a circuitous path, the condensation portion including a first chamber, a second chamber extending downwardly within the first chamber partway down from the top, a spiral conduit disposed within the first chamber, the drying portion including a solar air heati

Abstract: A continuous trickle-down distillation unit for producing hydrated alcohol having a compact, elongated distillation tube through which a fluid mixture including alcohol as one of its constituents passes. Within the distillation tube only the alcohol-predominant portion of the fluid mixture is vaporized while the remaining constituents of the fluid mixture are removed. The vaporized alcohol-predominant portion is condensed within a chamber which communicates with the distillation tube and is removed therefrom by a collection plate which extends partially into the chamber.

Abstract: Apparatus and a method for upgrading low pressure steam or brine, such as from a geothermal well, to prepare the steam or brine for any one of a number of uses, such as for conversion to pure, high pressure, high temperature steam for driving turbines. The system operates in a degasification phase in which a small amount of superheated steam is applied to the brine to scrub the same to cause the removal of concentrated gases therefrom. The degasified product is then pumped to a high pressure, heated countercurrently, and directed through a demineralized phase to remove the salts and solids in a liquid phase and convert the bulk of the water into pure, high pressure saturated steam. The steam output from the demineralizing phase can then be used to produce useful work, such as driving a turbine. In addition to forming saturated steam from geothermal brine, the system can be used to form pure saturated steam from impure water from any suitable source.

Abstract: A highly efficient and economic solar distillation unit comprising a plurality of angled trays in a frame, each tray including a vaned absorber element on the bottom surface. The trays are extruded in plastic and cut to size, as are the absorber elements and frame sidewalls. Frame endwalls are cut from flat extrusions. A transparent glass removable cover completes the basic assembly, but many variations are possible, including means to monitor and control water level within the unit from a storage tank. With the exception of an optional check valve there are no moving parts. There are no metal parts, and the basic unit is glued together from plastic extrusions and flat plates.

Abstract: Water degasification and distillation apparatus having a container for water to be degasified and distilled, a relatively small boiler adjoining said container and having a first conduit extending into the container so that a selected water level in the container will fill said boiler to a selected height, a condenser within the container and immersed in the water contained therein, a second conduit extending from the space above the water in said boiler to the inlet of the condenser, an outlet on the condenser extending through a container wall for discharging degasified and distilled water and heating means in said boiler for heating the water therein at a rate greater than the capacity of the second conduit to handle the steam generated in the boiler.

Abstract: A water distillation apparatus which produces distilled water by means of solar energy. The water to be distilled is confined within an internal chamber and subjected to solar energy through a transparent lid. The water that is distilled collects on the interior surface of the lid. The lid is located at an inclined position with respect to gravity. The droplets of distilled water which adhere to the interior surface of the lid flow to the lowest elevation of the lid. These accumulated droplets of distilled water are to be removed and collected within a collecting container. A water inlet valve assembly is connected to supply water within the internal chamber.

Abstract: A multiple effect diffusion distillation system includes a plurality of parallel plates for continuous recovery of heat having opposed evaporation and condensation faces for alternately evaporating and condensing phases of a liquid fed on to the upper end of the plates in a thin film for gravity flow along the evaporator face of the plates with vapor condensing on the condensation faces and with means for collecting and recovering the condensed product from the system. Alternate embodiments including a solar heat input system and others include multiple modular systems.

Abstract: An apparatus for the distillation of vaporizable liquids, for example alcohol, solvents used for the degreasing of metal and the like, comprises a distillation chamber, a heating unit in the region of the bottom of the distillation chamber, a cooling and condensation unit at an upper portion of the distillation chamber and a cold-generating unit. According to the invention, the cold-generating unit is formed as a heat pump with a circulating refrigerant and has a compressor, a cold branch and a hot branch. The cold branch is connected to the cooling and condensation unit of the distillation chamber while the hot branch transfers heat via a heat exchanger to a heat storage device, e.g. a utility water reservoir from which hot water is drawn to heat the heating unit of the distillation chamber.

Abstract: A steam generation apparatus includes a primary source of hot water supplied to an enclosed hot water receptacle maintained at a pressure of approximately 300 psi. Supply and return lines pump the hot water in a recirculating manner through a serially connected supplemental heating device until the hot water has reached a temperature of substantially 400.degree. F. whereupon a thermal valve associated with the supplemental heating device opens to deliver the heated water to an expansion tank. Steam formed within the expansion tank is transmitted through a steam outlet line to appropriate using apparatus. The initial hot water source may alternately include industrial by-product heated waste water on a primary heating station serially connected between a water supply and the enclosed hot water receptacle. Water condensed in the expansion tank is recycled to either the hot water receptacle or primary heating station.

Abstract: A device for desalting sea or brackish water by means of solar energy essentially comprises two adjacent canals or equivalent systems fed with seawater or brackish water and a greenhouse-type structure placed over one of the canals for evaporating the water. A fresh-water condensing and collecting structure is adapted to communicate with the greenhouse structure and is largely immersed in the water of the other canal which performs the function of a cold source for the condensing structure.

Abstract: A water distillation system which includes a storage tank for impure water and a storage tank for distilled water. Impure water is pumped through a heater to an evaporator. Impure water is also pumped through an impure water jet ejector. Distilled water is pumped through a distilled water jet ejector. The impure water jet ejector withdraws water from the bottom of the evaporator. The distilled water jet ejector withdraws water vapor from the top of the evaporator. Distilled water from the distilled water jet ejector passes through a heat exchanger in the impure water tank to heat input water. Impure water from the impure water jet ejector passes through a heat exchanger in the distilled water tank to cool the distilled water.

Abstract: An alcohol still having a boiler with a valve for maintaining the amount of liquor constant. The boiler mounts a distilling column having a temperature controlled inlet for liquor to be distilled which assists in maintaining the operation at a constant optimum operating temperature.

Abstract: A method and apparatus for recovering and simultaneously partially refining hydrocarbon products such as liquid oil, oil vapor and combustible and noncombustible gases from oil shale, by subjecting the oil shale ore, in fragments between 5 and 10 cm, or larger, to microwave energy at frequencies between 300 MHz and 3000 MHz. The apparatus includes kiln structures closed to air and microwave leakage, and associated microwave generators for both continuous discrete and batch processes. The microwave energy may also be applied in situ to beds and deposits of the oil shale.

Abstract: Distillation method and apparatus for separation of alcohol from an alcohol-water mixture are disclosed which include use of a fluid-tight vacuum tank within which a surface condenser is located adjacent the tank bottom. The condenser has a vapor inlet above the condenser, and a condenser outlet which communicates with a first pump having a pump discharge outside the tank. A second pump is provided for removal of mixture from the bottom of the tank. In operation, an alcohol-water mixture is fed into the tank to completely fill the same while air is vented therefrom. The vent is closed, and mixture then is pumped from the tank and condenser to empty the condenser and to lower the level of mixture in the tank beneath the vapor inlet to the condenser. With the removal of mixture, a vacuum is created whereupon alcohol rapidly evaporates from the mixture surface to rapidly reduce the temperature of remaining mixture.

Abstract: Method and apparatus for distillation of liquids such as sea water, brackish water, waste water, or the like, which also may be used for cooling purposes, are disclosed. The apparatus includes a vacuum tank, or vessel, into which liquid to be distilled, such as saline water, is fed to partially fill the tank. If desired, heating means may be included for heating the liquid adjacent the surface thereof to promote evaporation thereof. Vapor from the region above the liquid surface is fed to vapor condensing means adjacent the bottom of the tank for condensing the same. A condensate discharge tube extends downwardly from the condensing means for discharge of condensate therefrom. Means including a pressure head of condensate within the condensate discharge tube maintains a subatmospheric pressure within the tank to promote evaporation of liquid contained therein.

Abstract: An electrically and/or solar heated distillation and fractionation system for separating ethanol-water mixtures comprised with an insulated inclined vaporization chamber divided into an upper solar absorbent vaporization section and a lower pre-heating section by a vaporization floor, float means to automatically control the ethanol-water feed to the lower portion of the preheating section when distillation is taking place, means to evenly distribute the ethanol-water mixture on the vaporization floor, means to heat the ethanol-water mixture in the distillation chamber, a packed fractionation column through which the vapors from the distillation chamber must pass, means to control the temperature at the top of the fractionation column-condensing means to recover and/or recycle distillate exiting to the upper portion of the distillation column and means to remove or recycle residual aqueous liquid from the lower end of the vaporization section.

Abstract: A solar energy desalination process utilizing solar radiation directly for the evaporation of salt water is described. Ambient air takes on water vapor as the air passes through an evaporative medium. It is then directed between a saline water-covered, solar absorbing surface and a solar collecting housing. The resulting heated and moisture-saturated air is cooled in a heat exchange means where condensation of fresh water occurs. Simultaneously, cool salt water is utilized as the cooling water in the heat exchange means, and takes on the heat of condensation given up by the condensing vapor. The heated salt water from the heat exchange means is partially directed over the solar absorbing surface, and at least a portion of it is also directed to wet the evaporative medium. Several optional sub-processes are described for operation of the system during periods of reduced insolation, and an alternative process is described for operation of the process on a floating platform.

Abstract: A method of desalinating water resides in evaporating water from an aqueous salt solution upon contact of the latter with air, the water vapor being subsequently retrieved by condensing. The evaporation of water from the aqueous salt solution through contact thereof with the air is conducted by using two air flows, that is, primary and secondary flows. The primary air flow is supplied to a cooling zone, while the secondary air flow and the aqueous salt solution are delivered to an evaporation zone wherein the secondary flow is moistened by the water evaporating from the aqueous salt solution by virture of the psychrometric temperature difference until the moisture content in the secondary air flow is increased, as compared with the initial moisture content therein, by from 3.5 to 116 g/kg. During the course of absorbing the moisture, the secondary air flow acts to cool the primary air flow passing through the cooling zone.

Abstract: Solar apparatus for producing alcohol including a fermentation section and a distillation section; the fermentation section including a shallow pan with a large top opening inclined at an angle to the horizontal, a transparent sealing member disposed over the top opening of the fermentation pan, a cover for the fermentation pan; mechanism for introducing fermentable material into the fermentation pan, mechanism for removing liquid from the fermentation pan, solar heating mechanism for the liquid, mechanism for transferring the heated liquid to the distillation pan; the distillation section including a shallow pan with a large top opening inclined at an angle to the horizontal, the distillation pan including a bottom section with a plurality of spaced rib members, the rib members being disposed in a substantially horizontal, parallel orientation, a transparent sealing member disposed over the top opening of the distillation pan, mechanism for selectively reducing the solar exposure of the distillation pan, liq

Abstract: The disclosed invention is a solar still utilizing recirculating air driven by natural convection to evaporate pure water from saline water. The pure water evaporated into the air is removed by a condenser and the condenser also cools the air thereby causing its density to increase. The air density difference within the still, due to temperature differences, causes the air to flow in the desired pattern. This natural convection may be augmented by a fan or fans, if desired, to increase the output of the still. The same air is continuously circulated thereby reducing the thermal losses that occur when moist air is removed from the still. A recirculating pump is the only mechanical device required when the still is in the natural convection mode of operation.

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: Apparatus usable to heat fluid comprises:(a) a steam vessel having an inlet for water and an outlet for steam,(b) heating means associated with the vessel to heat water received therein and produce steam, and(c) a condenser connected with the vessel outlet to receive steam, the condenser adapted to extend in heat transfer relation with the fluid to heat that fluid in response to condensation of steam in said condenser, the condenser having a condensate outlet, and(d) other means to remove solid particles from the vessel.

Abstract: An apparatus and method is disclosed for direct absorption of solar energy by material being processed whereby it is not necessary to first convert the solar energy to sensible heat in an intermediate heat exchange medium or apparatus. The material to be processed is dispersed downwardly in a chamber, or reaction vessel, in the form of small droplets, or particles, of controlled size. Solar energy entering the vessel through an elongated vertically disposed window impinges directly upon the dispersed material and energy that is not absorbed but is scattered by the dispersed material is generally intercepted by surrounding droplets or particles. Energy not so absorbed by the dispersed droplets or particles is absorbed by the vessel walls and is re-radiated to the dispersed droplets or particles. The vessel is sized so as to absorb the energy whereby the energy is re-radiated from the walls at wave lengths essentially absent from the solar spectrum at sea level due to atmospheric attenuation.

Abstract: The apparatus includes a housing enclosing a boiler in the lower portion and a water-filled condenser in the upper portion with an insulated partition between them. The entry of boiler feed water is controlled by a float valve in the boiler, and steam from the boiler is conveyed through the partition and thus through a condenser coil substantially immersed in the water in the condenser.

Abstract: A still for the distillation of water or other liquids, the still having a boiling chamber with a heater, a vapor condenser chamber, and a vapor separator chamber all supported by a frame having a catch basin below the chambers and a distilled liquid sump below the catch basin into which the condenser discharges. The chambers telescopically plug together in position on the frame and are easily separated and knocked-down for cleaning without requiring tools. The chambers are tubes having their ends removably plugged, and one of the plugs in the boiling chamber carries the heater with it, the heater coils supporting a convection sleeve which is easily separated therefrom for cleaning. The water level in the boiling chamber is controlled by connection with a separate tank having a float valve setting its own level, and the unit has automatic electrical shut-off switches operative when the sump is full or in case of overheating.

Abstract: A solar desalting method and apparatus includes a storage tank for receiving heated sea water at a first rate from a solar collector during daylight hours and for delivering the same to a flash evaporator a second rate. The flash evaporator is connected for delivery of the evaporated and unevaporated portions of the feed water as the heating vapor and feed liquid, respectively, to a serially connected multi-effect film evaporator. Sea water is used to condense the vapor from the last evaporator effect as the distillate product of the system. The storage tank permits nighttime operation with the brine from the last effect and a portion of the cooling water being fed to the solar collector during the daytime and discharged at night.

Abstract: A multiple effect diffusion distillation system includes a plurality of parallel plates for continuous recovery of heat having opposed evaporation and condensation faces for alternately evaporating and condensing phases of a liquid fed on to the upper end of the plates in a thin film for gravity flow along the evaporator face of the plates with vapor condensing on the condensation faces and with means for collecting and recovering the condensed product from the system. Alternate embodiments including a solar heat input system and others include multiple modular systems.

Abstract: A process and an apparatus for distilling water in which a heat receiving plate member and a plurality of cooling plate members have a means for holding water to be treated on each reverse side thereof and are arranged in parallel spaced relationship with each other, and the water vapor produced by heating the heat receiving surface of the heat receiving plate member is condensed on the condensing surface of the adjacent cooling plate member, while giving the latent heat of the condensation to the cooling plate member and heating a water held on its back to produce the water vapor which is condensed on the condensing surface of the next cooling plate member, such evaporation by the latent heat and condensation being conducted according the number of rooms partitioned by adjacent two cooling plate members. There are apparatuses of two types, i.e.

Abstract: A distillation/evaporation/drying apparatus wherein alcohol is removed by a dry, warm carrier gas from an alcohol-containing slurry from a fermenter. Carbon dioxide from the fermenter is used as the carrier gas and is suitably dried, warmed and recycled into contact with the slurry to assist in removing alcohol therefrom. The apparatus includes a reflux section to upgrade the alcohol content of the carrier gas.

Abstract: Apparatus is provided for converting sea or other undrinkable waters to drinkable water without the use of driven or moving parts. Reliance upon gradient effects is made to effect the vaporization of, for example, sea water, followed by the condensation of the vapor to form distilled water. Gradient effects are achieved through the provision of differentials in the thermal conductivity, capillary activity, adsorptive, absorptive and/or pressure characteristics of particulate materials, or combinations of such physicals. For example, a column is packed with material graded as to its conductivity, the least thermally conductive material being nearest the cold or ambient water that is to be purified. In packing the column each successive layer of material has a greater thermal conductivity than the layer beneath it with the most conductive being at the top near the outlet arm of the column.

Abstract: A solar distillation unit is disclosed capable of operating entirely off solar radiation and intended for large scale industrial use offshore. A lens focusing system housed within an enclosed shell focuses the incident radiation from the sun on a heating element. Saltwater or contaminated fresh water is ejected toward the heating element at a predetermined rate resulting in the immediate evaporation of the water. The water vapor migrates and condenses on the cooler inner surface of the shell running to the bottom where it is collected and removed as fresh water.

Abstract: A spent solvent purification apparatus for treating spent acetone includes an evaporation unit, a condensing unit, and a housing for the units which has upper and lower sections and a panel section that divides the housing interior into separate compartments for the respective units. The evaporating unit is housed by the upper section and it includes a container with an interior wall that divides the interior into upper and lower chambers. The lower chamber has a heater for heating a heat exchange fluid that is contained therein and the upper chamber is for containing the spent solvent during the batch distillation procedure to which it is subjected. Both chambers have temperature sensors which are designed to break the control circuit when the temperature in either chamber exceeds a temperature that is predetermined and set for each sensor.

Abstract: A desalinazation apparatus has the bulk of its piping circuitry composed of black iron pipe, or similar pipe, which is normally subject to corrosion by sea water. Heat transfer to a salt water still includes indirect heat transfer by a thermal oil which is contained in the black iron pipe. A solar collector heat source is used to heat the heat transfer oil. The heat transfer rate from the heat transfer oil is maintained by using turbulence inducing fins in the interior of the heat transfer tubes in the salt water still and by directing high pressure gas at the exterior of the heat transfer tubes in the salt water still. A manifold of jets placed beneath the heat transfer tubes in the salt water still projects the high pressure gas, such as high pressure high temperature steam, onto the exterior of the heat exchange tubes.

Abstract: Direct contact heat transfer process and system for recovery of energy from geothermal brines or other hot aqueous solutions of a non-volatile solute, or for desalination, 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. In one embodiment, hot geothermal brine or other hot aqueous liquid is introduced into the liquid hydrocarbon contained in the lower compartment of each stage, causing boiling of the hydrocarbon. Hydrocarbon vapors pass from the evaporator compartment through the bubble caps to the upper condenser compartment where they are condensed in contact with a cooler water stream. The heated water stream under substantial pressure is fed to an expander or turbine to produce work.

Abstract: Reconcentration of moist glycol, which has been used to dry natural gas, by heating the moist glycol with flue gas from a reboiler and by thereafter stripping water from the moist glycol with the dried flue gas or with a hydrocarbon gas by-product of the natural gas being dried.

Abstract: A distiller that includes a micro-wave generating unit in a housing, a water holding chamber for vaporizing water by micro-wave energy and means for conducting water vapor outwardly through the housing while preventing the passage of micro-waves, a condenser for the vapor and a distilled water reservoir. The distiller is automatically operated by sensor operated valves. The heat from the condenser may be used to preheat the feed water.

Abstract: Apparatus and methods for concentrating and collecting solar energy are disclosed. In accordance with the invention, solar energy is concentrated by economical refringent lenses or lens systems including fluid lenses and/or Fresnel-type lenses. The lenses concentrate the solar energy preferably along lines in continuous linear foci or in discrete foci at an elongated collector comprising one or more fluid-carrying conduits and one or more fluids therein. In one embodiment, a plurality of photoelectric cells are located in or on the collector along the linear foci or at the discrete foci and operate at increased efficiency with heat being removed by the collector. A first fluid in the collector is heated by the concentrated solar energy and in a preferred embodiment is used to heat a second fluid contiguous to the first fluid, the first fluid having a boiling point exceeding that of the second fluid.

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 differnce 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: A process and apparatus especially suited for distilling alcohol from aqueous fermentation liquors wherein liquid vapors from a body of a liquid mixture (4) which is to be distilled pass from a container (2) holding the liquid mixture to a vapor heating chamber (8) disposed above the container where the vapors are heated by solar radiation and/or heat exchange with a source of process heat. The vapors are then withdrawn from the vapor heating chamber, compressed, passed in heat exchange relation with the liquid mixture and introduced into a reflux column (15) disposed in the interior of the body of liquid to be distilled near the center of the container. An aqueous fraction (24) is collected from the bottom of the reflux column, and an alcohol vapor fraction is withdrawn from the top of the reflux column and further condensed in heat exchange contact with the liquid mixture to produce an alcohol fraction (32).

Abstract: This invention relates to a distillation column for removing vinyl chloride monomer or other volatile material from an emulsion, suspension or dispersion containing such material. The apparatus comprises a column in which a series of inverted cones are mounted. The dispersion or emulsion is pulled downwardly over the cones and steam is fed into the column through sparges and flows upwardly against the descending stream of material. The low boiling materials are distilled out and recovered for reuse. The strips emulsion or dispersion are collected at the bottom of the column.

Abstract: An energy efficient design of fractionation column in which the liquid at the column bottom must be cooled to prevent thermal degradation, the column being provided with a perforated annular baffle through which liquid from the lowermost tray is channeled to the outlet of the column bottom, while a body of cooler recycled liquid is maintained in the column bottom outside of said baffle.

Abstract: A device for desalting sea or brackish water using solar energy, characterized by the fact that it includes two adjacent canals or equivalent structures fed with the sea or brackish water, a green house type structure over one of the canals to vaporize water from it and a structure for condensation of water and for collecting softwater, the structure being in communication with the greenhouse structure and largely immersed in the other canal, which acts as the cold source for the condensating unit.

Abstract: An apparatus for continuously producing concentrated alcohol from beer comprises a plurality of concentrator cells and a plurality of salvage cells arranged in a line in side-by-side relation. Liquid beer, supplied to the first upstream concentrator cell through a supply conduit, flows through passages between adjacent cells in response to the volume of beer reaching a predetermined level in the adjacent upstream cell. A microwave ignition bulb is positioned in each cell to heat the liquid beer and boil or vaporize the alcohol content thereof. The gaseous alcohol is serially bubbled through a fluid passage from each concentrator cell to the next adjacent upstream cell until the gaseous alcohol reaches the first concentrator cell where the gaseous alcohol is concentrated and condensed in a column to a liquid solution containing approximately 95% alcohol and approximately 5% water.

Abstract: The fouling of ammonia stills which results from the clogging, particularly of the lower plates of the stills, with sludge and precipitates is eliminated by use of combined apparatus in which a calcium compound precipitation step followed by a clarification step prior to initiation of actual distillation can be effected.