Abstract: A method for evaporating a starting solution to produce an end solution by spraying the starting solution into a gaseous medium under the conditions that the heat content of the starting solution in contact with the gaseous medium is smaller than the heat content of the gaseous medium; the duration of contact is such that most of the evaporation of solution takes place under conditions of constant enthalpy; and the vapor pressure of the gaseous medium is less than the vapor pressure of the liquid/gas interface of the end solution including the step of spraying the starting solution supplied by delivering devices using a pump through spray heads, each spray head includes a member having a plurality of holes the radii of which are not less than 0.025 mm and the distance between them is at least 0.3 mm for producing a shower of starting solution droplets of substantially constant radius substantially independent of spray head operating pressure. An apparatus for evaporating a starting solution is also provided.

Abstract: Weather in the vicinity of a land mass such as a continental arid zone near, and usually eastward of a body of water is modified by preferably propelling a ship pulling a submerged body having plurality of vertically displaced foils having an angle of attack that effects an upward displacement to the water in response to the surface displacement of the ship. The upward displacement of the water moves cooler sub-surface water toward the surface thereby cooling the surface water and reducing its heat loss in the summer. As a result, the heat capacity of the water is increased and additional heat will be stored in the water as a consequence of the greater absorption of solar radiation thereby increasing winter storms and the amount of rainfall over the land mass during the winter.

Abstract: A method for controlling the condition of air in an enclosure, such as a greenhouse, containing growing plants involves reducing the heat load on the enclosure by reducing the rate of convective heat flow of air across the canopy of the plants. This is achieved by heating and dehumidifying the air in the greenhouse during periods of low light levels such as at night in a manner that minimizes ventilation for controlling humidity. Apparatus is also provided for controlling the condition of air in an enclosure using an air-brine-vapor direct contact heat exchanger. Regeneration of the brine from the heat exchanger can be achieved by heating the brine using heated air from the enclosure or hot flue gases such that latent heat and/or sensible heat contained in the air, gases, and/or vapor exiting the regenerator can be transferred to the sir in the enclosure.

Abstract: Apparatus for conditioning air in an enclosure includes a direct contact air/brine heat exchanger with which air in the enclosure is exchanged, and a reservoir of brine. A first brine loop is established by which brine from the reservoir is exchanged with the direct contact heat exchanger for condensing water vapor in the enclosure air onto the brine to form dilute brine that flows into the reservoir. The apparatus also includes a brine concentrator for evaporating water from the dilute brine in the first loop to produce concentrated brine that is supplied to the reservoir. The brine concentrator is preferably constructed and arranged such that a thin film of dilute brine in the first loop flows over a heat transfer surface that is heated by flue gases from a burner.

Abstract: The air in a greenhouse is dehumidified using a direct-contact heat exchanger utilizing concentrated brine. The diluted brine produced when water vapor in the greenhouse condenses on the concentrated brine is regenerated in a fuel-fired boiler whose products of combustion, carbon dioxide and water vapor, are passed into the greenhouse. The products of combustion provide the desired level of carbon dioxide in the greenhouse; and the excess water vapor in the products of combustion as well as a significant portion of the water vapor produced by plants, growing in the greenhouse are removed by the hygroscopic concentrated brine.

Abstract: A heat exchanger according to the present invention comprises a housing for containing an upper and a lower layer of fluid, means for preventing intermixing of the two fluids, and heat transfer means for enhancing the transfer of heat between the layers. Specifically, the heat exchanger means is in form of a plurality of elongated cylinders extending into both layers, each of said cylinders containing a convective fluid. Preferably, the convective fluid is a liquid; and the preferred liquid includes water. Where the fluid in each of said upper and lower layers is a gas, the preferred orientation of the cylinders is vertical. The hotter fluid should be beneath the cooler fluid so that heat from the hotter fluid is first transferred to the liquid in the lower ends of each cylinder. The buoyancy of the heated liquid sets up convection currents which carry the heated liquid upwardly in the vertical cylinders where the heat is given up to the cooler fluid.

Abstract: Apparatus for conditioning air in an enclosure includes a reservoir of brine, a direct contact air-brine-vapor heat exchanger, a brine evaporator, and a brine circulation system for exchanging brine between the reservoir and heat exchanger, and between the reservoir and the evaporation. The apparatus also includes a condenser operatively associated with the evaporator, a primary air circulation system constructed and arranged to exchange air between the heat exchanger and the enclosure for drying the air in the heat exchanger, and a secondary air circulation system constructed and arranged to exchange air between the evaporator and the condenser for evaporating water from the brine in the evaporator. Water vapor produced by the brine evaporator is condensed in the condenser which is constructed and arranged to transfer the heat released by condensation, which is the same as the latent heat of vaporization of water evaporated from the brine by the vaporizer, to the air in the enclosure.

Abstract: Apparatus for conditioning air in an enclosure includes a direct contact air/brine heat exchanger with which air in the enclosure is exchanged, and a reservoir of brine. A first brine loop is established by which brine from the reservoir is exchanged with the direct contact heat exchanger for condensing water vapor in the enclosure air onto the brine to form dilute brine that flows into the reservoir. The apparatus also includes a brine concentrator for evaporating water from the dilute brine in the first loop to produce concentrated brine that is supplied to the reservoir. The brine concentrator is preferably constructed and arranged such that a thin film of dilute brine in the first loop flows over a heat transfer surface that is heated by flue gases from a burner.

Abstract: A method of and apparatus for controlling precipitation in evaporation ponds containing brine is provided wherein brine to be concentrated is introduced into a pond at at least one brine entrance, this brine being mixed in the vicinity of the entrance with bine present in the pond by enhanced brine mixing apparatus such that precipitation of salts occurs and salt deposits form in the vicinity of the entrance. This salt deposits collect in a collection basin at the floor of the pond. Brine present in the pond can be close to saturation or even saturated with respect to at least one of the salts contained therein. Deposits present in the collection basin can be removed to a location external to the pond by removal apparatus preferably including a mechanical scapper and conveying or transporting apparatus. A submerged source of compressed air producing bubbles or a motorized propellor mixer may be used to enhance the mixing of the brines near the brine entrance.

Abstract: A centrifugal heat engine comprises a first member rotatably mounted on a second member. The first member has an annular chamber on its periphery containing a vaporizable working fluid, and a central chamber separated from the annular chamber by a bulkhead. The central chamber contains an operating liquid and an hydraulic turbine mounted on the second member which projects into the central compartment and divides the same into two axially displaced compartments each of which contains operating liquid. The working fluid in the annular chamber is heated and vaporized. A conduit conducts vaporized working fluid in the annular chamber into one of the compartments wherein the vaporized working fluid expands in the operating liquid producing a liquid/gas mixture in the one compartment. Rotation of the first member creates a pressure differential between the two compartments that is related to the rotational speed of the first member and the density distribution of the fluids in the two compartments.

Abstract: A heat exchanger according to the present invention comprises a housing for containing an upper and a lower layer of fluid, means for preventing intermixing of the two fluid, and heat transfer means for enhancing the transfer of heat between the layers. Specifically, the heat exchanger means is in form of a plurality of elongated cylinders extending into both layers, each of said cylinders containing a convective fluid. Preferably, the convective fluid is a liquid; and the preferred liquid includes water. Where the fluid in each of said upper and lower layers is a gas, the preferred orientation of the cylinders is vertical. The hotter fluid should be beneath the cooler fluid so that heat from the hotter fluid is first transferred to the liquid in the lower ends of each cylinder. The buoyancy of the heated liquid sets up convection currents which carry the heated liquid upwardly in the vertical cylinders where the heat is given up to the cooler fluid.

Abstract: A heat exchanger comprises a housing containing upper and lower layers of fluid, the upper layer being less dense than the lower layer. The large and sharp density gradient at the interface between the upper and lower layers acts to prevent mixing of the two layers. A plurality of vertically oriented tubular sleeves that are closed at each end and filled with fresh water are located in the housing such that the axial ends of each tubular sleeve are in different ones of the layers. Heat added to the liquid in the lower layer is transferred to the liquid in the upper layer through the medium of the water contained in the tubular sleeves.

Abstract: Apparatus for conditioning the air in an enclosure utilizes a primary direct contact air/brine heat exchanger in which enclosure air is contacted with brine from a reservoir for condensing water vapor in the enclosure air onto the brine to form dilute brine. A brine concentrator is provided in the form of a secondary direct contact air/brine heat exchanger in which segregated air, separate from enclosure air, is contacted with heated dilute brine from the reservoir for evaporating water from the heated dilute brine into the segregated air to form concentrated brine. The secondary heat exchanger operates to heat the brine while it is being contacted with the segregated air.

Abstract: Apparatus for conditioning air in an enclosure includes a direct contact air/brine heat exchanger constructed to exchange air in the enclosure with the direct contact heat exchanger, and a reservoir of brine. A first brine loop is established by which brine from the reservoir is exchanged with the direct contact heat exchanger for condensing water vapor in the enclosure air onto the brine to form dilute brine that flow into the reservoir. The apparatus also includes a brine boiler constructed and arranged for establishing a second brine loop in which dilute brine from the first loop is exchanged with the boiler for evaporating water from the dilute brine and producing steam. Finally, a flow control is provided for maintaining a smaller flow rate in the second loop than in the first loop.

Abstract: The air in a greenhouse is dehumidified using a direct-contact heat exchanger utilizing concentrated brine. The diluted brine produced when water vapor in the greenhouse condenses on the concentrated brine is regenerated in a fuel-fired boiler whose products of combustion, carbon dioxide and water vapor, are passed into the greenhouse. The products of combustion provide the desired level of carbon dioxide in the greenhouse; and the excess water vapor in the products of combustion as well as a significant portion of the water vapor produced by plants, growing in the greenhouse are removed by the hygroscopic concentrated brine.

Abstract: Apparatus for conditioning air in an enclosure includes a reservoir of brine, a direct contact air-brine-vapor heat exchanger, a brine evaporator, and a brine circulation system for exchanging brine between the reservoir and heat exchanger, and between the reservoir and the evaporator. The apparatus also includes a condenser operatively associated with the evaporator, a primary air circulation system constructed and arranged to exchange air between the heat exchanger and the enclosure for drying the air in the heat exchanger, and a secondary air circulation system constructed and arranged to exchange air between the evaporator and the condenser for evaporating water from the brine in the evaporator. Water vapor produced by the brine evaporator is condensed in the condenser which is constructed and arranged to transfer the heat released by condensation, which is the same as the latent heat of vaporization of water evaporated from the brine by the vaporizer, to the air in the enclosure.

Abstract: A heat exchanger comprises a housing containing upper and lower layers of fluid, the upper layer being less dense than the lower layer. The large and sharp density gradient at the interface between the upper and lower layers acts to prevent mixing of the two layers. A plurality of vertically oriented tubular sleeves that are closed at each end and filled with fresh water are located in the housing such that the axial ends of each tubular sleeve are in different ones of the layers. Heat added to the liquid in the lower layer is transferred to the liquid in the upper layer through the medium of the water contained in the tubular sleeves.

Abstract: Apparatus for humidity and temperature control of the air in an enclosure comprising brine-vapor-air direct heat exchanger apparatus disposed in communication with an enclosure and a brine reservoir arranged to store brine and to be exposed to naturally occuring temperature gradients for desired conditioning of the brine. The temperature gradients may be relatively short term, such as day-night or may be longer term, such as summer-winter.

Abstract: A power plant includes a source of water, a heat exchanger having an evaporator side maintained below atmospheric pressure for converting the water to steam, and a turbine responsive to said steam for producing work and heat depleted steam. The heat exchanger also has a condenser side for receiving and condensing the heat depleted steam. The evaporator side of the heat exchanger is separated by a barrier from the condenser side. Concentrated brine from a source thereof is caused to fall in a film on the condenser side of the barrier, and water from the water source is caused to fall in a film on the evaporator side of the barrier. The heat of dilution of the film of concentrated brine, as it is directly contacted by the heat depleted steam in the condenser side of the heat exchanger, is transferred through the barrier from the condenser side to the evaporator side raising the temperature of the film of water on the evaporator side which evaporates in the reduced pressure in the evaporator.

Abstract: A starting solution is concentrated to a desired end solution by contacting the starting solution with a gaseous medium under the conditions that the heat content of the starting solution in contact with the gaseous medium is smaller than the heat content of the medium, and the duration of contacting is such that most of the solution that evaporates does so under conditions of constant enthalpy. When the starting solution is a brine, and the gaseous medium is air whose relative humidity is less than the relative humidity at the air/brine interface, the brine can be sprayed into the air to form a shower of droplets within which heat and vapor transfer take place during the transit time of the droplets in the air. When the ratio of droplets to air is sufficiently small, the heat content of the droplets is much smaller than the heat content of the air.