Abstract: A method of implementing a thermodynamic cycle by expanding a gaseous working stream to transform its energy into a useful form and produce an expanded gaseous stream, removing from the expanded gaseous stream an extracted stream, absorbing the extracted stream into a lean stream having a higher content of higher-boiling component than is contained in the extracted stream to form a combined extracted/lean stream, at least partially condensing the combined extracted/lean stream, combining at least part of the combined extracted/lean stream in condensed form with an oncoming working stream including a rich stream having a lower content of higher-boiling component than is contained in the extracted stream to provide a combined working stream, and heating the combined working stream with external heat to provide the gaseous working stream.

Abstract: Converting heat in a primary fluid (e.g., steam) to useful energy by multistage expansion of the primary fluid, heating of a multicomponent working fluid in a separate closed loop using heat of the primary fluid, and expansion of the multicomponent working fluid. The primary fluid in a vapor state is expanded in a first stage expander to obtain useful energy and to produce a partially expanded primary fluid. The partially expanded primary fluid stream is then separated into liquid and vapor components and split into a vapor stream (which is expanded in a second stage expander) and a further primary stream (which used to heat the multicomponent working fluid).

Abstract: Apparatus and a method for forming a gas hydrate for use in the production of pressurised gas due to the decomposition of the gas-hydrate in a storage chamber, and for controlled delivery of the pressurised gas as working medium to a turbine engine which is preferably coupled to a generator for the production of electricity.

Abstract: A power generating system is powered by a circulating working fluid that is heated by heat of condensation deposited in a concentrated brine solution. A condenser transfers heat from working fluid vapor exhaust from the turbine to cooling water to form a condensed working fluid and heat the cooling water to a first vapor pressure. A heat transfer chamber has a concentrated brine solution in vapor communication with the cooling water so that vapor from the cooling water at the first vapor pressure will condense on the brine solution for diluting and heating the brine solution. For efficient heat and vapor transfer, the cooling water and the brine solution are caused to flow along opposed surfaces. A boiler is placed in heat transfer communication with the brine solution for receiving heat from the brine solution and heating the condensed working fluid to a vapor for input to the turbine.

Abstract: The disclosed power plant can attain an extremely high thermal efficiency, as compared with that of the conventional power plant. The power plant comprises a steam system and a mixed medium system. The steam system comprises a heat source (1) for generating steam; a steam turbine (3) driven by the steam generated by the heat source; a steam condenser (81) for forming condensed water by condensing exhaust of the steam turbine; and a condensed water feeding pump (9) for feeding the water condensed by the steam condenser to the heat source.

Abstract: An externally fired gas turbine system according to the present invention has a compressor for compressing ambient air and producing compressed air, an air heat exchanger for heating the compressed air to produce heated compressed air, a turbine for expanding the heated compressed air to produce heat depleted expanded air, and a generator connected to the turbine for generating electricity. According to the present invention, the system also includes combustible products producing apparatus for processing fuel to produce combustible products that include combustible gases and an external combustion chamber for burning the combustible products and transferring heat to the air heat exchanger and producing heat depleted combustion products. The system also includes a closed Rankine cycle steam power plant having a water heat exchanger for vaporizing water and producing steam using heat contained in the heat depleted combustion products.

Abstract: A method and apparatus for implementing a thermodynamic cycle. A heated gaseous working stream including a low boiling point component and a higher boiling point component is expanded to transform the energy of the stream into useable form and to provide an expanded working stream. The expanded working stream is then split into two streams, one of which is expanded further to obtain further energy, resulting in a spent stream, the other of which is extracted. The spent stream is fed into a distillation/condensation subsystem, which converts the spent stream into a lean stream that is lean with respect to the low boiling point component and a rich stream that is enriched with respect to the low boiling point component. The lean stream and the rich stream are then combined in a regenerating subsystem with the portion of the expanded stream that was extracted to provide the working stream, which is then efficiently heated in a heater to provide the heated gaseous working stream that is expanded.

Abstract: An apparatus for a method using hydrogen-occluded alloy for recovering power from waste heat includes first and second heat exchangers containing hydrogen-occluded alloy, a first selector valve for alternating introduction of waste heat fluid between the first and second heat exchangers, a second selector valve for alternating introduction of cooling fluid between the first and second heat exchangers, a turbine associated with the heat exchangers, and a power generator connected to the turbine. The hydrogen-occluded alloy in the first and second heat exchangers is in the form of a multiplicity of stages that release the hydrogen gas at different temperatures, with the hydrogen gas being produced at a prescribed pressure by contact with waste heat fluid.

Abstract: A process and apparatus are disclosed for generating hydrogen gas from a charge of fuel selected from the group consisting of lithium and alloys of lithium and aluminum. The charge of fuel is placed into an enclosed vessel, then heated until it is molten. A reactant consisting of water is introduced into the vessel, as by spraying from a nozzle, for reaction with the charge of fuel resulting in the production of hydrogen gas and heat which are withdrawn from the vessel. Prior to initiation of the process, an inert gas atmosphere, such as argon, may be imparted to the interior of the vessel. A sufficiently large mass flow of the reactant through the nozzle is maintained to assure that there be no diminution of flow resulting from the formation on the nozzle of fuel and chemical compounds of the fuel. Optimum charges of the fuel are application specific and the ranges of the constituents are dependent upon the particular use of the system.

Abstract: An encagement vessel contains water and a working gas capable of forming hydrate with the water. A heat exchange arrangement is associated with the encagement vessel for removing heat from the working gas and water in the encagement vessel to form gas hydrate at an initial temperature. A working gas supply continues to add working gas to the encagement vessel as heat is removed in order to maintain the equilibrium pressure of the gas hydrate at the equilibrium pressure associated with the initial temperature as the hydrate is formed. An equilibrium pressure shifting arrangement increases the equilibrium pressure of the gas hydrate to an end pressure. A dissociating heat exchanger is included for adding heat to the hydrate at the end equilibrium pressure to dissociate the gas hydrate into water and working gas at the end pressure.

Abstract: A thermal power generator includes a high heat source pump, and cold working fluid pumps. An evaporator heat exchanges a high heat source fluid and a warmed working fluid. A liquid-vapor separator is connected to the evaporator. A first stage turbine is connected to the liquid-vapor separator. A second stage turbine is connected to the first stage turbine. A heater is connected to the first stage turbine, and receives remaining vapor working fluid, and the cold-working fluid to heat exchange the fluids. A tank stores and mixes the working fluids discharged from the heater, and supplies the stored working fluid to the first cold working fluid pump. A regenerator receives the liquid working fluid from the separator, and the cold working fluid, and forms a regenerated working fluid, and a warmed working fluid discharged to the evaporator. An absorber is connected to the second stage turbine and the regenerator. A reducing valve is located between the absorber and regenerator.

Abstract: Method and apparatus for implementing a thermodynamic cycle in which a gaseous working fluid is expanded to transform its energy into useable form, thereby generating a spent stream which is then condensed to produce a condensed stream. From the condensed stream the following streams are generated: a first stream having a higher percentage of a low boiling component than is included in the condensed stream, a second stream having a lower percentage of a low boiling component than is included in the condensed stream, and a third stream having the same percentage of a low boiling component as is included in the condensed stream. The first, second, and third streams are subjected to multiple distillation operations to generate a liquid working fluid which is then evaporated to generate the gaseous working fluid.

Abstract: A Rankine cycle power plant has a vaporizer member responsive to heat input for vaporizing a working fluid and producing vaporized working fluid, a turbogenerator responsive to vaporized working fluid for generating power and producing heat depleted working fluid, a condenser member responsive to said heat depleted working fluid for condensing the same and producing condensate, and suitable piping for returning said condensate to the vaporizer. The working fluid is in the form of a liquid having a plurality of fractions; at least one fraction is distilled from said liquid to produce a distillated fluid. It is this distillated fluid that is supplied to the power plant as the working fluid.

Abstract: A low temperature engine system has an elevated temperature recuperator in the form of a heat exchanger (12) having a first inlet connected to an extraction point (45) at an intermediate position between the high temperature inlet and low temperature outlet (14) of a turbine heat engine (8, 10) and an outlet connected by a conduit (47) to a second inlet to the turbine between the high and low temperature ends thereof and downstream of the extraction point (45). In the recuperator (12) thermodynamic medium vapor from extraction point (45) is in heat exchange relationship with thermodynamic medium conducted from the low temperature exhaust end (14) of the turbine unit (8, 10) through a water cooled condenser (6) and in heat exchange relationship in a refrigerant condenser (2) with a refrigerant flowing in an absorption-refrigeration subsystem.

Abstract: A method and apparatus is disclosed to provide a fuel efficient source of readily converted energy to an isolated or remote energy consumption facility. External heat from any of a large variety of sources is converted to an electrical, mechanical, heat or cooling form of energy. A polyatomic working fluid energized by external heat sources is dissociated to a higher gaseous energy state for expansion through a turbine prime mover. The working fluid discharge from the turbine prime mover is routed to a recouperative heat exchanger for exothermic recombination reaction heat transfer to working fluid discharged from the compressor segment of the thermodynaic cycle discharge. The heated compressor discharge fluid is thereafter further heated by the external heat source to the initial higher energy state.

Abstract: The present invention relates to an energy conversion system and more particularly tot he related apparatus and process. A reactor chamber is positioned with respect to a means for collecting and focussing. The focussed beam of radiation is employed to induce a reversible reaction in which the reaction products are converted into work in a work output means. Following that conversion, the reaction materials are passed through a heat sink and are recycled so that the process can be continuously operated.

Abstract: Disclosed are an apparatus and method used to preheat a working fluid for a subsequent solar-driven dissociation reaction. The working fluid is first passed through a blackbody receiver where it absorbs thermal energy, and is subsequently exposed to direct solar radiation. The present invention allows the working fluid to absorb relatively large amounts of solar energy at elevated temperatures, while the blackbody absorber remains at a relatively low temperature, thus minimizing energy losses through reradiation and enhancing the efficiency of the overall energy exchange.

Abstract: A thermodynamic cyclic process with a gaseous working medium, which is alternately compressed and expanded, in which process a working medium is employed, which experiences a volume expansion due to chemical processes at the higher temperature after the compression and a corresponding volume contraction at the lower temperature after the expansion, is to be improved so that a higher efficiency is achieved. This is achieved in that the volume contraction is endothermic. In this case, the cyclic process can increase the efficiency both in heat engines and also in heat pumps.

Abstract: A method and apparatus for converting thermal energy into electric power. A high pressure gaseous working stream is expanded, producing a spent stream. The spent stream is condensed, producing a condensed stream. The condensed stream forms first and second partially evaporated streams, which in turn form first and second vapor streams and first and second liquid streams. A rich stream is generated from the first vapor stream. A lean stream is generated from combining the second vapor stream with a mixing stream. The resulting rich and lean streams are passed through a boiler where they are evaporated. After exiting the boiler, the evaporated rich stream is combined with the evaporated lean stream generating the high pressure gaseous working stream, completing the cycle.

Abstract: Modifications are made to the standard process for the manufacture of ammonia and related compounds, resulting in lower operating costs through reduced total energy consumption. In one aspect of the invention, this is achieved by directing ammonia gas through one feed line, and carbon dioxide gas and steam through another feed line, into a closed reaction chamber to form ammonium carbonate. The formation of this solid compound results in a reduced pressure in the chamber. This reduced pressure can be used to drive heat engines in the reactant feed lines. In another aspect of the invention, the cost of running the potassium carbonate loop while the rest of the system is down is reduced by constructing an alternate pathway along part of the loop. The carbon dioxide gas and water vapor formed by the heating of the potassium bicarbonate flow through a heat engine and are cooled. The cooled water vapor and carbon dioxide gas are then recycled.

Abstract: A mechanochemical engine cpaable of desalinating sea water or brackish water by the conversion of mechanical work to chemical work, which comprises: a) a housing containing an elastomeric material capable of being stretched, to thereby allow salt-diminished water to move into the elastomeric material, while substantially repelling solvated salt ions from entry thereto, b) means for stretching and relaxing said elastomeric material in said housing, in connection with said elastomeric material; and c) means for uptake of said sea water or brackish water into said housing, means for draining concentrated salt water from said housing, and means for draining desalinated water from said housing.

Abstract: A method and apparatus for implementing a thermodynamic cycle which may be used to convert low temperature heat to electric power.

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 hybrid Rankine cycle system comprises a boiler in which water steam is generated, a steam turbine which is worked by the water steam from the boiler to drive a generator to obtain an electric power, an absorber condenser for introducing thereinto strong absorbent solution to absorb the water steam from the steam turbine to produce weak absorbent solution, and a pump for delivering the weak absorbent solution from the absorber condenser to the boiler. The weak absorbent solution is heated in the boiler to produce the strong absorbent solution to be fed to the absorber condenser and the water steam to be fed to the steam turbine.

Abstract: Motor apparatus which converts hydraulic energy and change of state heat energy to mechanical energy. The motor includes a main chamber divided by a piston into first and second portions. During a first half cycle or hydraulic power stroke, a valve places the first portion of the chamber in fluid communication with a source of pressurized, saturated liquid and the second portion of the chamber in fluid communication with a drain port. A switch senses the end of the hydraulic power stroke and causes the valve to move to a second position wherein the first and second portions of the chamber are placed in fluid communication with one another to form a common motor chamber and drive the piston in an expansion power stroke. Power is derived from the working fluid during the piston stroke in each direction. The motor finds particular application for energy recovery in an absorption refrigeration system.

Abstract: A method and apparatus for implementing a thermodynamic cycle, which includes the use of a composite stream, having a higher content of a high-boiling component than a working stream, to provide heat needed to partially evaporate the working stream. After being partially evaporated, the working stream is evaporated completely with heat provided by returning gaseous working streams and heat from an auxiliary steam cycle. After being superheated, the working stream is expanded in a turbine. Thereafter, the expanded stream is separated into a spent stream and a withdrawal stream. The withdrawal stream is combined with a lean stream to produce the composite stream. The composite stream partially evaporates the working stream and preheats the working stream and the lean stream. A first portion of the composite stream is fed into a distillation tower. A liquid stream flowing from the distillation tower forms the lean stream that is combined with the withdrawal stream.

Abstract: An open cycle latent heat engine has an elevator (10) rising preferably several thousand feet from a lower level entrance (12) to a higher level exit (13). Warm water vapor is input at the lower level of the elevator passageway (10) to cause moist air to rise, and a condensate remover (17) in an upper region of the elevator passageway removes condensate from the adiabatically expanded air. A compressor passageway (20) descending from exit (13) of the elevator passageway to the region of elevator passageway entrance (12) receives a portion of the air discharged from the exit and adiabatically and gravitationally compresses the dry air descending in the compressor passageway. An ejector arranged in the lower region of the compressor passageway has a nozzle (15) receiving ambient atmosphere flowing into the entrance of elevator passageway (10), where subatmospheric pressure air from compressor passageway (20) merges to help sustain the flow through ejector nozzle (15).

Abstract: A solar cooling process is described in which tapwater is injected into an adiabatic flash chamber. A portion of the tapwater vaporizes to steam chilling the remainder. A special brine absorbs the water vapor in an absorber chamber. Then the brine is pumped over an open air evaporator where excess water picked up by the brine is driven off using solar or waste heat.

Abstract: The present invention relates to process and apparatus for regenerating low temperature, low pressure energy from the vaporization of a primary fluid having a high boiling point and a large latent heat of vaporization to high pressure, high temperature energy which can then either be fed back to that same primary fluid or put to other uses. The process comprises interacting the primary fluid with a heat recycling fluid consisting of a solution of two basic fluids, a solute and a solvent. The solvent has a low boiling point and a large latent heat of vaporization, while the solvent has a high boiling point. The solute and the solvent have a high affinity for one another. The heat recycling fluid takes up the latent heat of vaporization of the primary fluid to separate the solute from the solution and thereby produce an endothermic reaction.

Abstract: Heat engines having improved efficiencies are provided. In accordance with preferred embodiments, topping cycle engines are provided employing ejectors. Use of ejectors in accordance with the invention permits higher high side temperatures while permitting work extraction devices to be operated at standard temperatures. A preferred sodium-helium system is described in detail.

Abstract: A solar energy collection system utilizing a fluid, e.g. ammonia, which dissociates endothermically and recombines exothermically and in which work output is obtained directly from the thermochemical fluid stream by expanding the fluid through turbines subsequent to the endothermic reaction. Undissociated fluid is introduced at an elevated temperature into an absorber-reaction vessel which is exposed to solar radiation and subsequently the dissociated fluid is conducted from the vessel to expansion turbines and through a counterflow heat exchanger to allow cooling. A second reaction chamber effects partial recombination of the dissociated products and a separator separates the undissociated and dissociated fluids with the undissociated fluid being returned via the heat exchanger where it is heated prior to entry to the absorber-reaction vessel .

Abstract: A method is provided for converting sensible heat energy of a heating fluid supplied by a high-temperature heat source to work, by means of a thermodynamic cycle employing a multi-component working fluid, wherein a "rich solution" having a higher concentration of lower boiling component, or components, is heated in a vapor generator in counter-current heat exchange with the heating fluid to produce a vapor-liquid mixture which is introduced into a lower zone of a rectifier and separated therein into a "lean solution" having a higher concentration of said lower boiling component, or components, and a vapor mixture; the enthalpy of the vapor mixture is increased by passing it through a superheater in counter-current heat exchange with said heating fluid at its highest temperature; the vapor mixture is then expanded in a first turbine to an intermediate pressure level thereby to generate work and subsequently in a second turbine to a low pressure level to generate additional work; the spent vapor mixture is then

Abstract: Gas or vapor phase chemical reactions are conducted inside an open loop Stirling cycle apparatus which may operate as a heat engine or as a heat pump. Adsorbent surfaces are associated with the thermal regenerators of the Stirling cycle apparatus, so that pressure swing adsorption separation of reactant and product gas species may be achieved in response to cyclic variations of flow and pressure within the apparatus. Flow control means are provided to introduce the feed gas into the working space of the apparatus and to remove separated product fractions. The feed gas is chemically reactive in a reaction zone of the working space, with reactant and product species separated by the apparatus to remove desired product(s) from the reaction zone while retaining reactant(s) in the reaction zone, so that conversion and selectivity objectives can be achieved.

Abstract: A nuclear excited power system includes a gaseous core nuclear reactor through the core of which helium is passed. The helium is excited by the high energy radiation from the nuclear reactor and is coupled to a reaction chamber wherein the high energy helium mixes with hydrogen and a halogen, such as, chlorine. The energy thus transferred to the hydrogen and chlorine causes the hydrogen and chlorine to combine to form a hydrogen chloride plasma. The high temperature, high pressure hydrogen chloride plasma drives a turbine, magnetohydrodynamic generator or other electromechanical device to form electrical and/or mechanical energy. The helium and hydrogen chloride exhaust products are separated with the helium coupled back to the reactor core. The hydrogen chloride is disassociated and coupled back to the reaction chamber.

Abstract: Pressure swing adsorption separation of a gas mixture containing a more readily adsorbed component and a less readily adsorbed component is performed within an apparatus containing an adsorbent bed with cyclically varied geometry, such that the bed volume can be expanded or contracted. Variable volume displacement means at either end of a flow path through the adsorbent bed are operated cyclically to generate flow of a gas mixture along the flow path, in a first direction when the more readily adsorbed component is preferentially adsorbed during the high pressure portion of the cycle while the bed volume is relatively contracted, and in a second reverse direction during the low pressure portion of the cycle while the bed volume is relatively expanded.

Abstract: A system for converting thermal energy into electrical energy includes a fluid reservoir, a relatively high boiling point fluid such as lead or a lead alloy within the reservoir, a downcomer defining a vertical fluid flow path communicating at its upper end with the reservoir and an upcomer defining a further vertical fluid flow path communicating at its upper end with the reservoir. A variable area nozzle of rectangular section may terminate the upper end of the upcomer and the lower end of the of the downcomer communicates with the lower end of the upcomer. A mixing chamber is located at the lower end portion of the upcomer and receives a second relatively low boiling point fluid such as air, the mixing chamber serving to introduce the low boiling point fluid into the upcomer so as to produce bubbles causing the resultant two-phase fluid to move at high velocity up the upcomer.

Abstract: A closed loop power regeneration system combines chlorine and hydrogen to form hydrogen chloride at high temperatures and pressure. The high temperature, high pressure hydrogen chloride is used to drive a turbine after which the heat from the hydrogen chloride is extracted for use in a regeneration system. The hydrogen chloride is converted to hydrogen and chlorine in the regeneration system. In the regeneration system copper and cuprous chloride react with the hydrogen chloride at a temperature of at least about 200.degree. C. to generate cuprous chloride, cupric chloride and molecular hydrogen. In a second reactor containing cuprous chloride and cupric chloride the extracted thermal energy from the hydrogen chloride is utilized to generate copper, cuprous chloride and molecular chlorine. The molecular chlorine and hydrogen are recombined to form hydrogen chloride in the system. In an alternative embodiment, silver is used as a reagent rather than copper and cuprous chloride.

Abstract: Methods and apparatus for ocean thermal energy conversion using metal hydride heat exchangers to power a turbine by desorbing and absorbing hydrogen gas. Heat exchangers are alternatively floated to the ocean surface to warm the metal hydride bed or sunk to the bottom to cool the bed. The turbine powers an electric generator which produces electricity which may be utilized directly, stored in a superconducting magnet, used to desalinate water, or used to power the electrolysis of water in order to produce hydrogen for use as a fuel.

Abstract: A method and apparatus for implementing a thermodynamic cycle with preheating, involves expanding a gaseous working fluid to a medium pressure to transform its energy into usable form. The expanded gaseous working fluid is split into two different streams. One stream is further expanded to a spent low pressure level to produce further usable energy. This stream is then condensed. The other of the two streams is used to preheat the condensed stream and is mixed with the condensed stream at a point upstream of the point of preheating. This decreases the irreversibilities in the preheating process and enables greater efficiencies to be achieved.

Abstract: Method and system for generating electric power utilizing a coolant circuit, in which a coolant is evaporated at a lower level position, allowed to rise via tubing to a higher level position, liquified at the higher level position, and allowed to flow down to the lower level position in tubing where it impinges a hydraulic turbine connected to a generator. The preferred embodiment includes a vertical tube system of approximately 3000 m length, composed of a long tube for rising vapors and fall tubes for falling liquid coolant. Multiple cooling systems located at the higher level position, including a counterflow cooling system, forced-draught type air cooler, and a step-by-step cooling process, are utilized to liquify the coolant and provide working vapor to power the cooling systems. The coolant is composed to C.sub.3 H.sub.8 and NH.sub.3, which is varied on a percent composition basis to match atmospheric weather conditions.

Abstract: A method is provided for utilizing sensible heat energy supplied by a high-temperature heating fluid, employing a multi-component working fluid thermodynamic cycle, wherein a solution rich in a lower boiling component is heated in a vapor generator in counter-current heat exchange with the heating fluid to produce a vapor-fluid mixture which is separated in a rectifier into a lean solution and a vapor mixture; the enthalpy of the vapor mixture is optionally increased in a superheater by counter-current heat exchange with said heating fluid at its highest temperature; the vapor mixture is then expanded thereby to perform the function of the cycle; and the spent vapor mixture is dissolved in said lean solution in an absorber so as to regenerate the rich solution; characterized in that the rich solution leaving the absorber is compressed and divided into a first and second parts; the first part is heated by counter-current heat exchange with said lean solution drawn from the rectifier, whereafter said first part

Abstract: A method and apparatus for implementing a thermodynamic cycle, which includes the use of a composite stream, having a higher content of a high-boiling component than a working stream, to provide heat needed to evaporate the working stream. After being superheated, the working stream is expanded in a turbine. Thereafter, the expanded stream is separated into a spent stream and a withdrawal stream. The withdrawal stream is combined with a lean stream to produce a composite stream. The composite stream evaporates the working stream and preheats the working stream and the lean stream. The composite stream is then expanded to a reduced pressure. A first portion of this composite stream is fed into a gravity separator. The liquid stream flowing from the gravity separator forms a portion of the lean stream that is combined with the withdrawal stream. The vapor stream flowing from the separator combines with a second portion of the composite stream in a scrubber.

Abstract: The purpose of a thermal induction machine is to put thermal resources and thermal uses (Q.sub.o, Q.sub.1, Q'.sub.1, Q.sub.2) into relation, so as to valorize the energy of the resources, the device operating in very similar fashion to reversibility with a binary working fluid used in diphasic form. It includes a first direct assembly of heat transfer elements inserted serially on the liquid and working fluid vapor flows. The first assembly consists of a first diphasic contact column (Kd) operating at an initial pressure value. It also includes a second assembly of heat transfer elements. The second assembly is reverse to the first and containing the same number of elements and notably a second diphasic contact column (Kg), the second column working at a second pressure value lower than the first value, adventitious flows (m.sub.o, m'.sub.o, m.sub.1, m'.sub.1) being established between the two assemblies on the terminals of the homologous elements.

Abstract: A chemical pump system that utilizes a self-driven compressor to increase the system pressure while obviating the need for a one-way valve and liquid head to provide the driving force for the reactants, thus enhancing long distance transport. The system comprises a chemical heat pipe employing reversible endothermic/exothermic chemical reactions to transfer thermal energy between a heat source and a heat sink. At least one reactant is self-driven substantially unidirectionally through the heat pipe by compressing the reactant(s) with a compressor and heating the reactant(s) to a predetermined pressure and temperature sufficient to form a reaction product having at least a 150% molar increase. The reaction product is expanded with an expander that is linked mechanically to the compressor. The expansion energy is sufficient to compress the reactants to the predetermined pressure while maintaining the self-driven unidirectional flow.

Abstract: Pressure swing adsorption gas separations are conducted inside an open loop Stirling cycle apparatus which may operate as an engine, refrigerator or heat pump. Adsorbent surfaces are associated with the thermal regenerators of the Stirling cycle apparatus, so that a preferentially adsorbed gas fraction is concentrated by parametric pumping into a colder end of an engine or into a warmer end of a refrigerator or heat pump, while a less readily adsorbed gas fraction is concentrated into warmer end of an engine or into colder end of a refrigerator or heat pump. Flow control means are provided to introduce the feed gas into the working space of the apparatus and to remove separated product fractions. Feed gases may be chemically reactive within a portion of the working space, with reactant and product species of the reaction separated by the apparatus to drive the reaction off equilibrium.

Abstract: Disclosed is a steam engine which is used to propel underwater vehicles without exhausting combustion products to the surrounding water. A solid metallic fuel reacts in a first chamber with water to produce hydrogen which is subsequently reacted in a second chamber with oxygen to produce heat and water. The amount of water produced in the second chamber is equal to the amount of water used in the first chamber. Consequently, no excess water is produced.

Abstract: A solar electric power generating process is described which consists of tapwater thermally contacted with special brine. Low pressure characteristics of the brine draw steam through a power generating turbine from the water into the brine. As the brine is pumped over an open air evaporator, excess water picked up by the brine is driven off using solar or waste heat.

Abstract: A dispensing system for use with a wide variety of dispensable products which employs an inflatable pouch positioned within the container containing a pressurizing gas phase. A product gas phase is incorporated in the expelled product to enhance the product appearance, functionally or safety. The weight to weight (w/w) ratio of the product gas phase to the flowable materials should be between about 0.001:1 to about 0.015:1 and preferably, the w/w ratio of the product gas phase to the flowable material is between about 0.001:1 and about 0.07:1.

Abstract: The absorption power generator is similar to a conventional steam power generator. High pressure vapor is produced in a vapor generator and expanded in a prime mover to produce power. Exhaust vapor from the prime mover is collapsed to liquid and pumped back into the vapor generator. The absorption power generator differs in that the temperature of the vapor generator heat source can be much lower. This is because a low boiling point liquid, such as ammonia, is vaporized instead of water. Instead of condensing the exhaust vapor from the prime mover in a condenser, the exhaust vapor is absorbed by an absorbent liquid in an absorber. For ammonia, water is the absorbent liquid. Unused heat is rejected from the process, at normal heat rejection temperatures, by a high pressure condenser, working in parallel with the prime mover.

Abstract: A method and apparatus for combustion of hydrogen to produce heat, for example to generate steam for power generation. Water is electrolyzed and the hydrogen and a fraction of the oxygen products of electrolysis are passed immediately to a first combustion zone where the immediate combustion of the oxygen products and a function of the hydrogen products is effected. The products from this first combustion zone are immediately passed to a second combustion zone where combustion is again effected with the remaining fraction of the oxygen products of the electrolysis and the remaining hydrogen products from the first combustion zone. The heat generated is thereafter applied to the desired use, for example by passing the products of combustion from the second combustion zone through water to boil the water, the steam thereby produced being used for power generation. Apparatus to carry out this method is also described.