WO1981002154A1 - A desalination apparatus with power generation - Google Patents
A desalination apparatus with power generation Download PDFInfo
- Publication number
- WO1981002154A1 WO1981002154A1 PCT/US1980/000081 US8000081W WO8102154A1 WO 1981002154 A1 WO1981002154 A1 WO 1981002154A1 US 8000081 W US8000081 W US 8000081W WO 8102154 A1 WO8102154 A1 WO 8102154A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- evaporator
- condenser
- water
- conduit
- ocean
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/046—Treatment of water, waste water, or sewage by heating by distillation or evaporation under vacuum produced by a barometric column
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Definitions
- This invention relates to a heat pump process and apparatus which is applicable to desalination and power generation, water distillation and power generation, cooling of thermal plant cooling water discharges. More parti ⁇ cularly, this invention relates to a process and apparatus comprising an evaporator ' and a condenser where the heating and cooling sources are both obtained from the ocean waters and the products of the process are distilled or desalinated water and electrical energy in excess of that required to operate the apparatus as a result of the mass flow of vapors between the evaporator and the condenser driving a prime mover coupled to an electrical generator.
- an object of this invention is to provide a process and apparatus using ocean or other waters with high temperature differentials to produce distilled or desali ⁇ nated water with excess electricity as an additional produc
- This invention provides an improvement which is a significant improvement to the advancement of th art of distillation and desalination and the art of thermal energy conversion.
- Another object of this invention is to provide a means whereby the oceans that are warmed by the sun and the cold deep ocean waters can be used directly to evaporate and condense ocean waters for desalinating.
- Another object of this invention is to provide a means for using any sources of water that have large temperature differentials to operate an apparatus that distills or desalinates water and produces electrical energy.
- Another object of this invention is to incorporate in said process and apparatus a means of using the vapors from the evaporating and condensing process to drive a prime mover which is connected to a generator providing the electrical energy to operate the apparatus and additionally to provide excess electrical energy for external usage.
- Another object of this invention is to provide a process and apparatus with a barometric leg to maintain the process and apparatus at the saturation pressure level of the warm ocean water, or other warm water source, in the apparatus while permitting thermal circulation of the warm water to the evaporator.
- Another object of this invention is to provide a process and apparatus with a barometric leg at the condenser to permit removal of condensed vapors from the negative pressure of the system while maintaining this pressure.
- Another object of this invention is to provide a process and apparatus with a vacuum pump to establish the initial saturation, or negative, pressure of the process and apparatus and to remove non-condensable vapors during operation of the process and apparatus.
- Another object of this invention is to provide a process and apparatus with a pump and conduit means to bring deep ocean water, or other cooling water, in contact with the condenser and to return this condensing water to the ocean or other return source.
- Another object of this invention is to provide a process and apparatus with a barometric conduit in contact with the evaporator and located between the evaporator and the ocean surface, or other warm water source, of such sufficient size as to allow thermal circulation of the ocea water, or other warm water source, in the barometric condui to replace the warm water in the evaporator which is cooled when evaporation takes place removing the heat of vapori ⁇ zation from the surface of the warm water in the evaporator.
- Another object of this invention is to provide a process and apparatus with a pump and conduit means to draw in warm surface ocean water, or other warm water source, an direct it upwardly in the barometric conduit between the evaporator and the ocean surface, or surface of any other warm water source, to induce and assist thermal circulation in the barometric conduit.
- Another object of this invention is to provide a process and apparatus with a particle separation chamber located above the evaporator and between the evaporator and the conduit connecting the evaporator and the condenser.
- This particle separation means comprises an enlarged chambe wherein the vapors from the evaporator are reduced in velocity to allow liquid or particles to settle back into the evaporator.
- Another object of this invention is to provide a process and apparatus with a barometric conduit at the condenser, a liquid level control at the top of the baro ⁇ metric conduit and a condensate water out valve at the bottom of the said conduit to maintain the desired height o condensate water in the barometric conduit and the outlet pressure of the condensate water at the outlet valve.
- Another object of this invention is to provide a process and apparatus with an electrical control to direct electrical energy from the above mentioned electrical
- Another object of this invention is to provide a process and an apparatus with a means of using ocean water, or other warm water source, as the refrigerant fluid, eliminating the necessity of additional refrigerants.
- the vapors of the fluid will be at the saturation pressure corresponding to the temperatures in the various portions of the apparatus.
- Another object of this invention is to provide a process and an apparatus with a heat source, a conduit of such sufficient height as to form a barometric leg, a pump and conduit means to induce and direct circulation in the barometic leg, an evaporator means, a particle separation means, a conduit means to connect said evaporator means to a condenser means, a prime mover interposed in said conduit means, a generator means coupled to said prime mover means, an electrical control means, a condenser means, pump and conduit means to pump cooling water to said condenser means and to return the condensing or cooling water to the cooling water source, a conduit from said condenser means of such height as to form a barometric leg and of such additional height as to obtain the desired pressure of condensate water in the barometric conduit means to remove the same from the apparatus, a level control, a condensate water out valve and a vacuum pump means.
- the invention may be incorporated into a distilling or desalination apparatus with power generation comprising conduit connecting an evaporator to the surface of the ocean, or other warm water source and having sufficient height as to form a barometric leg in which the ocean water or other warm water source, will only rise to the level determined by the magnitude of the negative pressure or the saturation pressure which is a function of the temperature of the warm water source in the evaporator section of the apparatus.
- An evaporator means with an attached particle separation chamber is connected by a conduit means to a condenser means.
- a prime mover of the turbine type or the positive displacement type is interposed into the said conduit means.
- a generator means coupled to the prime move means converts the power generated by the prime mover means to electrical energy.
- a pump and conduit means deliver col deep water or other cooling water to a condenser and return the cooling or condensing water to the cooling water source
- a conduit means connected to the condenser means has suffi ⁇ cient height to create a pressure head equal to the sum of the difference between the atmospheric pressure and the pressure within the apparatus, plus the desired head pres ⁇ sure at the condensate water outlet.
- Valve means is connec to the condensate water outlet to allow removal of con ⁇ densate water from the apparatus.
- a liquid level control means is located at the top of the barometric conduit means to control the condensate water out valve means for the purpose of allowing condensate water out of the condensate water out valve in such a manner as to control the desired height of condensate water in the barometric conduit means.
- a vacuum pump means initially reduces the pressure in the apparatus to the saturation pressure of the ocean water, or other warm water source, and then further removes any non-
- An electrical control means connects the output of the elec ⁇ trical generator means to the elements of the apparatus which require power such as the cold water pump, the vacuum pump, and the recirculating pump, thereby making the process self-sustaining with only the differential temperatures in the heating and cooling waters providing the power for the apparatus.
- a pump and conduit means draw in warm surface ocean water, or other warm water source, and directs the warm water upwardly in the barometric conduit between the evaporator means and the ocean surface, or surface of other warm water source, to induce and assist thermal circulation in the barometric conduit means.
- a fundamental characteristic of the heat pump system comprises a closed loop system established between an evaporator means where a fluid, in this case warm water, is evaporated, and'becomes a vapor carrying with it the heat of vaporization, and a condenser means wherein % the vapor is condensed thereby liberating the heat of condensation.
- a fluid in this case warm water
- a condenser means wherein % the vapor is condensed thereby liberating the heat of condensation.
- the heat to the evaporator means is furnished by warm surface ocean water, or other warm water source
- the cooling means for the condenser means is furnished by cold deep ocean water, or other cooling water source.
- the prime mover means interposed in the closed loop provides the power to drive an electrical generator means and supplies power to an electrical control means to direct electrical energy to the elements of the apparatus thereby providing distilled or desalinated water in addition to excess electrical energy for external usage.
- Barometric conduits allow entry and exit of the warm water source and the exit of condensate water, now distilled or desalinated, from the apparatus.
- a vacuum pump establishes the initial negative pressure of the apparatus and during operation removes any non-condensable vapors.
- the practice of the instant invention enables a distillation or desali ⁇ nation apparatus with power generation to utilize the differential temperatures present in the ocean, and such other sources of water in which temperature differentials are present, to produce distilled or desalinated water and electrical energy.
- This invention accordingly comprises a process and an apparatus possessing the features, properties and the relationship of elements which will be exemplified in the article hereinafter described, and the scope of the inventi will be indicated in the claims.
- Fig. 1 illustrates a desalination apparatus with power generation.
- the drawing illustrates a desalination apparatus with power generation 10 including an evaporator 14 and a con ⁇ denser 26.
- the evaporator 14 is connected to the surface o the ocean by means of a conduit 12.
- Said conduit 12 being of sufficient height that the ocean water will rise to the desired level in the evaporator 14 taking into account the variation in the levels of the ocean, when the evaporator 14 is at the saturation pressure for the corresponding temper ⁇ ature of the ocean water.
- Said conduit is also of such sufficient size as to permit thermal circulation of the ocean water in said conduit 12 to allow the warm surface ocean water to rise to the evaporator 14 to replace the ocean water in the evaporator 14 that becomes cooled as ocean water evaporates taking with it the heat of vapori ⁇ zation.
- a pump means 46 draws warm surface ocean water through conduit 44 and discharges it through conduit 48 upwardly in conduit 12 to induce and assist in thermal circulation.
- a particle separation chamber 16 is located above the evaporator 14 of such diameter that the vapors from the evaporator 14 are sufficiently reduced in velocity to prevent particles or liquid from reaching other portions of the system.
- Conduit 18 connects the evaporator 14 and the particle separation chamber 16 to the condenser 26.
- the con ⁇ denser 26 illustrated is a simple serpentine condenser for ease of illustration although more elaborate types of condensers such as plate or tubular could be used on given designs.
- Vapors from the evaporator 14 come in thermal contact with the condenser 26 and condense, liberating the heat of condensation to the condensing water in the con- denser 26.
- a prime mover 20 is interposed in the conduit 18. The prime mover derives power from the mass flow of vapors which flow from the evaporator 14, which is at the saturation pressure for the temperature of the warm surface ocean water, and the condenser 26 which is at the saturation pressure for the temperature of the colder sub-surface ocean water,
- the type of prime mover is, for clarity, shown as a simple axial turbine, although the variety of applications of the invention might dictate other prime movers such as multi-stage turbines, roots type positive displacement prime movers, and others well known and used to derive rotary motion from the flow of vapors.
- An electrical generator 22 is coupled to the prime mover 20 and converts the power of the prime mover 20 to electrical energy.
- An electrical control 28 directs the electrical power from the generator 22 for use to operate the various elements of the apparatus and further to direct such excess electrical power for external usage.
- a conduit 42 is extended deep into the ocean to a depth satisfactory to obtain cold ocean water for input to the inlet of a pump 40 for pumping cold ocean water to the condenser 26 through conduit 34. This cold or condensing water is returned to the ocean from the condenser 26 through a conduit 36.
- Conduit 32 is connected to the condenser 26 and is of such height as to create a head pressure equal to the difference in atmospheric pressure and the pressure in the condenser 26 plus a head sufficient to give the desired head pressure at the condensate water valve 38.
- a liquid level control 30 located at the top conduit 32 controls the condensate water valve 38 and allows the " valve to discharge condensate water while maintaining the desired head in the conduit 32.
- Vacuum pump 24 is connected to the condenser 26 portion of the apparatus and initially reduces the pressure in the apparatus to the initial saturation pressure of the ocean water and subsequently removes any non-condensable vapors from the process during operation.
- the process is instituted initially by the vacuum pump 24 evacuating the air from the closed system.
- the vacuum pump 24 reduces the pressure in the closed system until the pressure in the system reaches the saturation pressure dictated by the temperature of the ocean surface water. In the case of surface ocean water at 80° F the pressure left in the apparatus 10 would be the saturation pressure of water at 80° F or approximately 0.507 psia. With the continued operation of the vacuum pump 24, the closed apparatus 10 then fills with water vapor at the saturation temperature and pressure of 80° F and 0.507 psia.
- the ocean water in conduit 12 rises until the ocean water in conduit 12 has created a head pressure at the ocean surface equal to the atmospheric pressure.
- the difference in pressure between the inside of the closed apparatus 10 and the atmospheric pressure outside the closed apparatus 10 would be approximately 14.193 psi and would therefore cause the ocean water in conduit 12 to rise approximately 31.8 feet above the surface of the ocean.
- the pump 40 is then started to draw cold deep ocean water through conduit 42 and pump the same through conduit 34 to the condenser 26.
- Conduit 36 returns the condensing water to the ocean.
- Heat for continued evaporation in the evaporator 14 is supplied by the thermal circulation of the warm surface ocean water in conduit 12. This thermal circulation is induced and assisted by the pum 46 which draws warm surface ocean water through conduit 44 and discharges this flow through conduit 48 upwardly in conduit 12 thus establishing a non-random thermal circu ⁇ lation. The heat of vaporization lost to the vapors evap ⁇ orated in the evaporator 14 are thus constantly replaced.
- the vapors caused by evaporation in the evaporator 14 are pure water and do not contain the salts or minerals present in the ocean water.
- the evaporator 14 is separated from the condenser 26 by a particle separation chamber 16 and a vapor conduit 18 and the condensate water obtained as a result of the condensation of the vapors in the condenser 26 is desalinated, or distilled, water.
- Condensate water from the condenser 26 collects in the conduit 32 until this condensate water reaches the liquid level control 30 at which time the liquid level control 30 then regulates the action of the condensat.e water valve 38 letting condensate water out of the apparatus 10 sufficient to maintain the condensate water level in the conduit 32 at the liquid level control 30.
- the conduit 32 is of such height that the head of water in the conduit 32 is equal to the difference between the saturation pressure in the condenser 26 and the atmospheric pressure outside of the apparatus plus the desired pressure head at the condensate water valve 38.
- the head of ocean water in th conduit 12 and the head of condensate water in the conduit 32 provides a means of bringing ocean water in contact with the evaporator 14 and removing condensate water from the condenser 26 even though the apparatus 10 is at a pressure considerably lower than that of the atmospheric air outside of the closed apparatus 10.
- An electrical control 28 directs the electrical output of the generator 22 to necessary elements of the apparatus and the excess diverted for external usage.
- the apparatus has thus provided for itself a power source to sustain its own operation and provide external energy for other uses.
- the power to initiate the process and apparatus 10 must be external and most easily could be provided by storage batteries which would be recharged during system operation.
- a desalination apparatus with power generation providing desalinated water and electrical energy has thus been described.
- the temperature differential present at various parts in the ocean waters being the energy necessary to operate the said process and apparatus.
Abstract
Desalination apparatus with power generation comprising an evaporating means (14) and a condensing means (26). Conduit means (18) connect the evaporator means (14) and said condensing means (26) in a closed loop with the vapors of said evaporator (14) being coupled thermally with said condenser means (26). Temperature differential means comprise the temperature of the ocean water at the ocean surface providing heat input into said evaporator means (14) whereas cold ocean water pumped from the depths of the ocean provides the cooling means to said condenser (26). The difference in temperature between this warm ocean water at the ocean surface and the cold water from the depths of the ocean thus provides the heating and cooling means for powering said apparatus. Evaporation in the condenser (26) and condensing in the said condenser (26) when the air has been removed from the apparatus by means of a vacuum pump means (24) leaves only water vapor in the system. This evaporation and subsequent condensing of the vapors from the ocean water, which are essentially low temperature steam, results in a mass flow of vapors from the evaporator means (14) to the condenser means (26) through the conduit means (18) connecting same. These vapors when condensed in the condenser means (26) become distilled or desalinated water since only water vapors are carried through the apparatus and the salt, minerals, etc. are retained in the ocean water in the evaporator (14).
Description
Description
A Desalination Apparatus with Power Generation
Technical Field
This invention relates to a heat pump process and apparatus which is applicable to desalination and power generation, water distillation and power generation, cooling of thermal plant cooling water discharges. More parti¬ cularly, this invention relates to a process and apparatus comprising an evaporator' and a condenser where the heating and cooling sources are both obtained from the ocean waters and the products of the process are distilled or desalinated water and electrical energy in excess of that required to operate the apparatus as a result of the mass flow of vapors between the evaporator and the condenser driving a prime mover coupled to an electrical generator.
Background Art
The shortage of oil and natural gas is rapidly becoming a significant problem for manufacturers and producers in the United States. The increasing price of fossilized fuel presents a very serious problem to producers of electrical energy and to desalination plants in particular. Accord¬ ingly, other sources of energy are being investigated and it is natural that the oceans of the world are being investigated, particularly in those areas of the ocean such as the Gulf of Mexico, the Gulf Stream off Florida, the Carribbean and the equatorial waters in the Atlantic and Pacific oceans where considerable temperature differences exist between the surface waters, say 78° F to 88° F and the deep water several thousand feet deep, say ,40° F. The natural approach to the utilization of these differential temperatures has led to research of various refrigeration cycles using the warm surface water to "boil" a low boiling point refrigerant
such as ammonia or freon and the cold deep water to effect condensing of the refrigerant. A turbine type of device in the refrigerant loop would drive electrical generators to produce electricity and to further operate desalination plants.
In the very areas where the ocean waters provide significant temperature differentials, fossilized fuel is used to operate large desalination plants for the conversio of ocean or salt water to drinking water. The thermal pollution as a result of hot water dis¬ charge from thermal and thermal nuclear generating plants and the usual nearby water cooling sources offer additional opportunities for devices using temperature differentials a energy sources. Therefore an object of this invention is to provide a process and apparatus using ocean or other waters with high temperature differentials to produce distilled or desali¬ nated water with excess electricity as an additional produc The balance of said outputs of distilled or desalinated water and electricity being a function of a particular individual design. This invention provides an improvement which is a significant improvement to the advancement of th art of distillation and desalination and the art of thermal energy conversion.
Another object of this invention is to provide a means whereby the oceans that are warmed by the sun and the cold deep ocean waters can be used directly to evaporate and condense ocean waters for desalinating.
Another object of this invention is to provide a means for using any sources of water that have large temperature differentials to operate an apparatus that distills or desalinates water and produces electrical energy.
Another object of this invention is to incorporate in said process and apparatus a means of using the vapors from the evaporating and condensing process to drive a prime mover which is connected to a generator providing the electrical energy to operate the apparatus and additionally to provide excess electrical energy for external usage.
Another object of this invention is to provide a process and apparatus with a barometric leg to maintain the process and apparatus at the saturation pressure level of the warm ocean water, or other warm water source, in the apparatus while permitting thermal circulation of the warm water to the evaporator.
Another object of this invention is to provide a process and apparatus with a barometric leg at the condenser to permit removal of condensed vapors from the negative pressure of the system while maintaining this pressure.
Another object of this invention is to provide a process and apparatus with a vacuum pump to establish the initial saturation, or negative, pressure of the process and apparatus and to remove non-condensable vapors during operation of the process and apparatus.
Another object of this invention is to provide a process and apparatus with a pump and conduit means to bring deep ocean water, or other cooling water, in contact with the condenser and to return this condensing water to the ocean or other return source.
Another object of this invention is to provide a process and apparatus with an evaporator wherein ocean, or other warm water, is evaporated. Another object of this invention is to provide a process and apparatus, with a condenser wherein the vapors from the evaporator are brought into thermal contact with the condensing water in the condenser.
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Another object of this invention is to provide a process and apparatus with a barometric conduit in contact with the evaporator and located between the evaporator and the ocean surface, or other warm water source, of such sufficient size as to allow thermal circulation of the ocea water, or other warm water source, in the barometric condui to replace the warm water in the evaporator which is cooled when evaporation takes place removing the heat of vapori¬ zation from the surface of the warm water in the evaporator. Another object of this invention is to provide a process and apparatus with a pump and conduit means to draw in warm surface ocean water, or other warm water source, an direct it upwardly in the barometric conduit between the evaporator and the ocean surface, or surface of any other warm water source, to induce and assist thermal circulation in the barometric conduit.
Another object of this invention is to provide a process and apparatus with a particle separation chamber located above the evaporator and between the evaporator and the conduit connecting the evaporator and the condenser.
This particle separation means comprises an enlarged chambe wherein the vapors from the evaporator are reduced in velocity to allow liquid or particles to settle back into the evaporator. Another object of this invention is to provide a process and apparatus with a barometric conduit at the condenser, a liquid level control at the top of the baro¬ metric conduit and a condensate water out valve at the bottom of the said conduit to maintain the desired height o condensate water in the barometric conduit and the outlet pressure of the condensate water at the outlet valve. Another object of this invention is to provide a process and apparatus with an electrical control to direct electrical energy from the above mentioned electrical
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generator to the elements of the apparatus that require power such as the vacuum pump, cooling water pump, and recirculating pump and to further direct any excess elec¬ trical power for external usage. Another object of this invention is to provide a process and an apparatus with a means of using ocean water, or other warm water source, as the refrigerant fluid, eliminating the necessity of additional refrigerants. The vapors of the fluid will be at the saturation pressure corresponding to the temperatures in the various portions of the apparatus.
Another object of this invention is to provide a process and an apparatus with a heat source, a conduit of such sufficient height as to form a barometric leg, a pump and conduit means to induce and direct circulation in the barometic leg, an evaporator means, a particle separation means, a conduit means to connect said evaporator means to a condenser means, a prime mover interposed in said conduit means, a generator means coupled to said prime mover means, an electrical control means, a condenser means, pump and conduit means to pump cooling water to said condenser means and to return the condensing or cooling water to the cooling water source, a conduit from said condenser means of such height as to form a barometric leg and of such additional height as to obtain the desired pressure of condensate water in the barometric conduit means to remove the same from the apparatus, a level control, a condensate water out valve and a vacuum pump means.
Other objects and a fuller understanding of this invention may be had by referring to the summary of the invention, the description and the claims, taken in con¬ junction with the accompanying drawing.
Disclosure of the Invention
The invention may be incorporated into a distilling or desalination apparatus with power generation comprising conduit connecting an evaporator to the surface of the ocean, or other warm water source and having sufficient height as to form a barometric leg in which the ocean water or other warm water source, will only rise to the level determined by the magnitude of the negative pressure or the saturation pressure which is a function of the temperature of the warm water source in the evaporator section of the apparatus. An evaporator means with an attached particle separation chamber is connected by a conduit means to a condenser means. A prime mover of the turbine type or the positive displacement type is interposed into the said conduit means. A generator means coupled to the prime move means converts the power generated by the prime mover means to electrical energy. A pump and conduit means deliver col deep water or other cooling water to a condenser and return the cooling or condensing water to the cooling water source A conduit means connected to the condenser means has suffi¬ cient height to create a pressure head equal to the sum of the difference between the atmospheric pressure and the pressure within the apparatus, plus the desired head pres¬ sure at the condensate water outlet. Valve means is connec to the condensate water outlet to allow removal of con¬ densate water from the apparatus. A liquid level control means is located at the top of the barometric conduit means to control the condensate water out valve means for the purpose of allowing condensate water out of the condensate water out valve in such a manner as to control the desired height of condensate water in the barometric conduit means. A vacuum pump means initially reduces the pressure in the apparatus to the saturation pressure of the ocean water, or other warm water source, and then further removes any non-
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condensable vapors from the apparatus during operation. An electrical control means connects the output of the elec¬ trical generator means to the elements of the apparatus which require power such as the cold water pump, the vacuum pump, and the recirculating pump, thereby making the process self-sustaining with only the differential temperatures in the heating and cooling waters providing the power for the apparatus. A pump and conduit means draw in warm surface ocean water, or other warm water source, and directs the warm water upwardly in the barometric conduit between the evaporator means and the ocean surface, or surface of other warm water source, to induce and assist thermal circulation in the barometric conduit means.
A fundamental characteristic of the heat pump system comprises a closed loop system established between an evaporator means where a fluid, in this case warm water, is evaporated, and'becomes a vapor carrying with it the heat of vaporization, and a condenser means wherein% the vapor is condensed thereby liberating the heat of condensation. In the case of the subject invention, the heat to the evaporator means is furnished by warm surface ocean water, or other warm water source, and the cooling means for the condenser means is furnished by cold deep ocean water, or other cooling water source. The prime mover means interposed in the closed loop provides the power to drive an electrical generator means and supplies power to an electrical control means to direct electrical energy to the elements of the apparatus thereby providing distilled or desalinated water in addition to excess electrical energy for external usage. Barometric conduits allow entry and exit of the warm water source and the exit of condensate water, now distilled or desalinated, from the apparatus. A vacuum pump establishes the initial negative pressure of the apparatus and during
operation removes any non-condensable vapors. The practice of the instant invention enables a distillation or desali¬ nation apparatus with power generation to utilize the differential temperatures present in the ocean, and such other sources of water in which temperature differentials are present, to produce distilled or desalinated water and electrical energy.
This invention accordingly comprises a process and an apparatus possessing the features, properties and the relationship of elements which will be exemplified in the article hereinafter described, and the scope of the inventi will be indicated in the claims.
Brief Description of the Drawing
For a fuller understanding of the nature and objects o the invention, reference should be had to the following detailed description taken in connection with the accom¬ panying drawing in which:
Fig. 1 illustrates a desalination apparatus with power generation.
Best Mode for Carrying Out the Invention
The drawing illustrates a desalination apparatus with power generation 10 including an evaporator 14 and a con¬ denser 26. The evaporator 14 is connected to the surface o the ocean by means of a conduit 12. Said conduit 12 being of sufficient height that the ocean water will rise to the desired level in the evaporator 14 taking into account the variation in the levels of the ocean, when the evaporator 14 is at the saturation pressure for the corresponding temper¬ ature of the ocean water. Said conduit is also of such sufficient size as to permit thermal circulation of the ocean water in said conduit 12 to allow the warm surface
ocean water to rise to the evaporator 14 to replace the ocean water in the evaporator 14 that becomes cooled as ocean water evaporates taking with it the heat of vapori¬ zation. A pump means 46 draws warm surface ocean water through conduit 44 and discharges it through conduit 48 upwardly in conduit 12 to induce and assist in thermal circulation. A particle separation chamber 16 is located above the evaporator 14 of such diameter that the vapors from the evaporator 14 are sufficiently reduced in velocity to prevent particles or liquid from reaching other portions of the system. Conduit 18 connects the evaporator 14 and the particle separation chamber 16 to the condenser 26. Although there are various types of condensers, the con¬ denser 26 illustrated is a simple serpentine condenser for ease of illustration although more elaborate types of condensers such as plate or tubular could be used on given designs. Vapors from the evaporator 14 come in thermal contact with the condenser 26 and condense, liberating the heat of condensation to the condensing water in the con- denser 26. A prime mover 20 is interposed in the conduit 18. The prime mover derives power from the mass flow of vapors which flow from the evaporator 14, which is at the saturation pressure for the temperature of the warm surface ocean water, and the condenser 26 which is at the saturation pressure for the temperature of the colder sub-surface ocean water, The type of prime mover is, for clarity, shown as a simple axial turbine, although the variety of applications of the invention might dictate other prime movers such as multi-stage turbines, roots type positive displacement prime movers, and others well known and used to derive rotary motion from the flow of vapors. An electrical generator 22 is coupled to the prime mover 20 and converts the power of the prime mover 20 to electrical energy. An electrical
control 28 directs the electrical power from the generator 22 for use to operate the various elements of the apparatus and further to direct such excess electrical power for external usage. A conduit 42 is extended deep into the ocean to a depth satisfactory to obtain cold ocean water for input to the inlet of a pump 40 for pumping cold ocean water to the condenser 26 through conduit 34. This cold or condensing water is returned to the ocean from the condenser 26 through a conduit 36. Conduit 32 is connected to the condenser 26 and is of such height as to create a head pressure equal to the difference in atmospheric pressure and the pressure in the condenser 26 plus a head sufficient to give the desired head pressure at the condensate water valve 38. A liquid level control 30 located at the top conduit 32 controls the condensate water valve 38 and allows the" valve to discharge condensate water while maintaining the desired head in the conduit 32. Vacuum pump 24 is connected to the condenser 26 portion of the apparatus and initially reduces the pressure in the apparatus to the initial saturation pressure of the ocean water and subsequently removes any non-condensable vapors from the process during operation.
The process is instituted initially by the vacuum pump 24 evacuating the air from the closed system. The vacuum pump 24 reduces the pressure in the closed system until the pressure in the system reaches the saturation pressure dictated by the temperature of the ocean surface water. In the case of surface ocean water at 80° F the pressure left in the apparatus 10 would be the saturation pressure of water at 80° F or approximately 0.507 psia. With the continued operation of the vacuum pump 24, the closed apparatus 10 then fills with water vapor at the saturation temperature and pressure of 80° F and 0.507 psia.
Because of the difference in the pressure in the closed
apparatus 10 and the pressure of the atmospheric air surroun¬ ding the closed apparatus 10, the ocean water in conduit 12 rises until the ocean water in conduit 12 has created a head pressure at the ocean surface equal to the atmospheric pressure. In the case of atmospheric pressure at 14.7 psia, the difference in pressure between the inside of the closed apparatus 10 and the atmospheric pressure outside the closed apparatus 10 would be approximately 14.193 psi and would therefore cause the ocean water in conduit 12 to rise approximately 31.8 feet above the surface of the ocean. The pump 40 is then started to draw cold deep ocean water through conduit 42 and pump the same through conduit 34 to the condenser 26. Conduit 36 returns the condensing water to the ocean. Cold water flowing through the condenser 26 causes the water vapors in the condenser 26 to condense releasing the heat of condensation to the condensing water. The warmer vapors present in the evaporator 14 then flow to the condenser 26 where they are condensed to a liquid. The rapid flow of vapors then existing from the evaporator 14 to the condenser 26 is caused by the reduction in volume of the vapors in the condenser 26 as they are condensed to a liquid and the difference in the saturation pressure in the evap¬ orator 14 and the lower saturation pressure in the condenser 26 as a result of the lower temperature of the condensing water in the condenser 26. This difference in pressure between the evaporator 14 and the condenser 26 and the mass flow of vapors, low temperature steam, from the evaporator 14 to the condenser 26 drives the prime mover 20 located in the conduit 18 between the evaporator 14 and the condenser 26. Power is thus provided to the electrical generator 22 which is coupled to the prime mover 20. Heat for continued evaporation in the evaporator 14 is supplied by the thermal
circulation of the warm surface ocean water in conduit 12. This thermal circulation is induced and assisted by the pum 46 which draws warm surface ocean water through conduit 44 and discharges this flow through conduit 48 upwardly in conduit 12 thus establishing a non-random thermal circu¬ lation. The heat of vaporization lost to the vapors evap¬ orated in the evaporator 14 are thus constantly replaced.
The vapors caused by evaporation in the evaporator 14 are pure water and do not contain the salts or minerals present in the ocean water. The evaporator 14 is separated from the condenser 26 by a particle separation chamber 16 and a vapor conduit 18 and the condensate water obtained as a result of the condensation of the vapors in the condenser 26 is desalinated, or distilled, water. Condensate water from the condenser 26 collects in the conduit 32 until this condensate water reaches the liquid level control 30 at which time the liquid level control 30 then regulates the action of the condensat.e water valve 38 letting condensate water out of the apparatus 10 sufficient to maintain the condensate water level in the conduit 32 at the liquid level control 30. The conduit 32 is of such height that the head of water in the conduit 32 is equal to the difference between the saturation pressure in the condenser 26 and the atmospheric pressure outside of the apparatus plus the desired pressure head at the condensate water valve 38.
It can thus be seen that the head of ocean water in th conduit 12 and the head of condensate water in the conduit 32 provides a means of bringing ocean water in contact with the evaporator 14 and removing condensate water from the condenser 26 even though the apparatus 10 is at a pressure considerably lower than that of the atmospheric air outside of the closed apparatus 10.
An electrical control 28 directs the electrical output of the generator 22 to necessary elements of the apparatus and the excess diverted for external usage. The apparatus has thus provided for itself a power source to sustain its own operation and provide external energy for other uses. During initial startup of the apparatus 10 , since no elec¬ tricity exists at the electrical control 28, the power to initiate the process and apparatus 10 must be external and most easily could be provided by storage batteries which would be recharged during system operation.
A desalination apparatus with power generation providing desalinated water and electrical energy has thus been described. The temperature differential present at various parts in the ocean waters being the energy necessary to operate the said process and apparatus.
The foregoing process and apparatus has a substantial savings over that of the prior art in that no conventional energy sources are required to operate the apparatus so described. The present disclosure includes that contained in the appended claims, as well as that of the foregoing descrip¬ tion. Although this invention has been described in its preferred form with a certain degree of particularity, it is understood that the present disclosure of the preferred form has been made only by way of example and numerous changes in the details of construction and the combination and arrange¬ ment of parts may be resorted to without departing from the spirit and scope of the invention.
Claims
1. An apparatus for desalinating ocean waters and furnishing electrical power, comprising in combination: an evaporator; a first conduit for connecting said evaporator to the warm surface water of the ocean; said first conduit forming a barometric leg to separate the low internal pressure of the evaporator from the ambient atmospheric pressure during operation of said evaporator; means for circulating the ocean water between sai evaporator and the warm surface water of the ocean to replace the heat of vaporization lost in the evaporator; a condenser comprising condenser cooling means connected by a second conduit to cool ocean water; a first pump interposed in said second conduit to provide a cool condensing source for vapors evaporated from said evaporator; a third conduit connecting said evaporator to sai condenser for directing evaporator vapors into thermal contact with said condenser cooling means; a prime mover interposed in said third conduit to be driven by the mass flow of vapors between said evaporato means and said condenser means resulting from the pressure differential between the saturated vapors in said evaporato and the saturated vapors in said condenser; and a condenser conduit connected to said condenser for providing a barometric leg for the removal of condensed desalinated water from the lower pressure in said condenser to the higher pressure of the atmospheric air.
2. An apparatus as set forth in claim 1 including a third pump and a fourth conduit means for drawing warm surface water of the ocean into said evaporator to assist thermal circulation in said evaporator conduit.
3. An apparatus as set forth in claim 3, incuding an electrical generator coupled to said prime mover for generating electrical power; and an electrical control system for connecting said electrical power for controlling said pumps and said valve.
4. An apparatus as set forth in claim 1, including: a particle separation channel interposed between said evaporator and said condenser for reducing the velocity of vapors from said evaporator to prevent non-vapors from entering said condenser.
5. An apparatus for desalinating ocean waters and furnishing electrical power, comprising in combination: an evaporator; a first conduit for connecting said evaporator to the warm surface water of the ocean; said first conduit forming a barometric leg to separate the low internal pressure of the evaporator from the ambient atmospheric pressure during operation of said evaporator; means for circulating the ocean water between said evaporator and the warm surface water of the ocean to replace the heat of vaporization lost in the evaporator; a condenser comprising condenser cooling means; connected by a second conduit to a cooling source; a third conduit connecting said evaporator to said condenser for directing evaporator vapors into thermal contact with said condenser cooling means; a prime mover interposed in said third conduit to be driven by the mass flow of vapors between said evaporator means and said condenser means resulting from the pressure differential between the saturated vapors in said evaporator and the saturated vapors in said condenser; a particle separation channel interposed between said evaporator and said condenser for reducing the velocity of vapors from said evaporator to prevent non-vapors from entering said condenser; a condenser conduit connected to said condenser for providing a barometric leg for the removal of condensed water from the lower pressure in said condenser to the higher pressure of the atmospheric air; a condensate water output valve located proximate the bottom of said barometric leg; a liquid level control means to sense the level of the condensate water in the barometric leg for controlling said condensate water output valve, and a vacuum pump in fluid communication with said third conduit for initially reducing the internal vapor pressure in.said evaporator for initiating operation of the apparatus.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US1980/000081 WO1981002154A1 (en) | 1980-01-28 | 1980-01-28 | A desalination apparatus with power generation |
| EP19800900843 EP0044294A4 (en) | 1980-01-28 | 1980-01-28 | A desalination apparatus with power generation. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US1980/000081 WO1981002154A1 (en) | 1980-01-28 | 1980-01-28 | A desalination apparatus with power generation |
| WOUS80/00081 | 1980-01-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1981002154A1 true WO1981002154A1 (en) | 1981-08-06 |
Family
ID=22154178
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US1980/000081 WO1981002154A1 (en) | 1980-01-28 | 1980-01-28 | A desalination apparatus with power generation |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0044294A4 (en) |
| WO (1) | WO1981002154A1 (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2534293A1 (en) * | 1982-10-08 | 1984-04-13 | Buchere Jeanne Marie De | Improvements to water desalination units with or without the simultaneous production of electrical power from hot and cold water sources with a small DELTA T used in an open cycle at a subatmospheric pressure |
| FR2561637A1 (en) * | 1984-03-20 | 1985-09-27 | Guiffray Michel | Process and device for producing distilled water from seawater |
| FR2601353A1 (en) * | 1986-07-10 | 1988-01-15 | El Ghaziri Abdel | Method of desalination of seawater by vacuum distillation employing the differences in temperature between surface and deep layers in the sea |
| GB2176714B (en) * | 1985-06-26 | 1989-07-12 | William Masterton | Water evaporating and condensing plant |
| DE3938670C1 (en) * | 1989-11-21 | 1991-02-14 | Pi Praktische Informatik Gmbh, 8000 Muenchen, De | Drinking water from sea water - water is pulled in through vacuum in floating column and passes through to evapn. chamber |
| GB2249968A (en) * | 1990-11-23 | 1992-05-27 | John Hilary Bryant | Vacuum enhanced water extraction system |
| US5248394A (en) * | 1992-03-23 | 1993-09-28 | Fsr Patented Technologies, Ltd. | Liquid purifying/distillation device |
| US5441606A (en) * | 1992-03-23 | 1995-08-15 | Fsr Patented Technologies, Ltd. | Liquid purifying and vacuum distillation process |
| ES2113778A1 (en) * | 1994-03-30 | 1998-05-01 | Santisteban Gonzalez Jose Luis | Low pressure distillation of sea water or effluent |
| US9938162B2 (en) | 2015-02-26 | 2018-04-10 | Shaker A. REDA | System, method, and apparatus for water desalination |
| US9988284B2 (en) | 2015-02-26 | 2018-06-05 | Shaker Ahmed REDA | System, method, and apparatus for water desalination |
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| US1966938A (en) * | 1928-07-14 | 1934-07-17 | Wallace G Stone | Method of distillation |
| US2006985A (en) * | 1926-03-13 | 1935-07-02 | Claude George | Method and apparatus for obtaining power from sea water |
| US2636129A (en) * | 1948-05-08 | 1953-04-21 | Edward A Agnew | Solar engine |
| US3032482A (en) * | 1959-04-02 | 1962-05-01 | Richard W Shoemaker | Process of recovering fresh water from salt water with a hot heavy material |
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| US3158554A (en) * | 1959-10-26 | 1964-11-24 | Phillips Petroleum Co | Method and apparatus for starting up the distillation of a liquid which tends to boil up as a liquid |
| US3269919A (en) * | 1963-06-11 | 1966-08-30 | Steam Sales & Service Co | Automatic still |
| US3468762A (en) * | 1965-06-09 | 1969-09-23 | Max P Klitzsch | Distillation of sea water using steam turbine electric generator and solar still |
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| US3928145A (en) * | 1974-09-16 | 1975-12-23 | Donald F Othmer | Process for producing power, fresh water, and food from the sea and sun |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2503249A1 (en) * | 1975-01-28 | 1976-07-29 | Ralf Horst Krauss | Sea water desalination plant - using solar energy for heating and power and deep water for condensation |
-
1980
- 1980-01-28 EP EP19800900843 patent/EP0044294A4/en not_active Ceased
- 1980-01-28 WO PCT/US1980/000081 patent/WO1981002154A1/en not_active Application Discontinuation
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1445134A (en) * | 1922-03-10 | 1923-02-13 | Otis L Fowler | Device for heating and purifying water |
| US2006985A (en) * | 1926-03-13 | 1935-07-02 | Claude George | Method and apparatus for obtaining power from sea water |
| US1966938A (en) * | 1928-07-14 | 1934-07-17 | Wallace G Stone | Method of distillation |
| US2636129A (en) * | 1948-05-08 | 1953-04-21 | Edward A Agnew | Solar engine |
| US3080302A (en) * | 1958-11-04 | 1963-03-05 | Submerged Comb Inc | Process and apparatus for converting non-potable water to potable water |
| US3032482A (en) * | 1959-04-02 | 1962-05-01 | Richard W Shoemaker | Process of recovering fresh water from salt water with a hot heavy material |
| US3158554A (en) * | 1959-10-26 | 1964-11-24 | Phillips Petroleum Co | Method and apparatus for starting up the distillation of a liquid which tends to boil up as a liquid |
| US3269919A (en) * | 1963-06-11 | 1966-08-30 | Steam Sales & Service Co | Automatic still |
| US3468762A (en) * | 1965-06-09 | 1969-09-23 | Max P Klitzsch | Distillation of sea water using steam turbine electric generator and solar still |
| US3783108A (en) * | 1971-01-18 | 1974-01-01 | R Saari | Method and apparatus for distilling freshwater from seawater |
| US3928145A (en) * | 1974-09-16 | 1975-12-23 | Donald F Othmer | Process for producing power, fresh water, and food from the sea and sun |
Non-Patent Citations (1)
| Title |
|---|
| See also references of EP0044294A4 * |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2534293A1 (en) * | 1982-10-08 | 1984-04-13 | Buchere Jeanne Marie De | Improvements to water desalination units with or without the simultaneous production of electrical power from hot and cold water sources with a small DELTA T used in an open cycle at a subatmospheric pressure |
| FR2561637A1 (en) * | 1984-03-20 | 1985-09-27 | Guiffray Michel | Process and device for producing distilled water from seawater |
| GB2176714B (en) * | 1985-06-26 | 1989-07-12 | William Masterton | Water evaporating and condensing plant |
| FR2601353A1 (en) * | 1986-07-10 | 1988-01-15 | El Ghaziri Abdel | Method of desalination of seawater by vacuum distillation employing the differences in temperature between surface and deep layers in the sea |
| DE3938670C1 (en) * | 1989-11-21 | 1991-02-14 | Pi Praktische Informatik Gmbh, 8000 Muenchen, De | Drinking water from sea water - water is pulled in through vacuum in floating column and passes through to evapn. chamber |
| GB2249968A (en) * | 1990-11-23 | 1992-05-27 | John Hilary Bryant | Vacuum enhanced water extraction system |
| US5248394A (en) * | 1992-03-23 | 1993-09-28 | Fsr Patented Technologies, Ltd. | Liquid purifying/distillation device |
| US5441606A (en) * | 1992-03-23 | 1995-08-15 | Fsr Patented Technologies, Ltd. | Liquid purifying and vacuum distillation process |
| ES2113778A1 (en) * | 1994-03-30 | 1998-05-01 | Santisteban Gonzalez Jose Luis | Low pressure distillation of sea water or effluent |
| US9938162B2 (en) | 2015-02-26 | 2018-04-10 | Shaker A. REDA | System, method, and apparatus for water desalination |
| US9988284B2 (en) | 2015-02-26 | 2018-06-05 | Shaker Ahmed REDA | System, method, and apparatus for water desalination |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0044294A1 (en) | 1982-01-27 |
| EP0044294A4 (en) | 1982-07-12 |
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