Patent Application
20090151368
The present invention relates to method and technology of extracting air humidity in order to supply fresh water. More particularly, the present invention relates to implementation of the method of extracting water from air humidity in hot and dry regions, where infrastructure for fresh water is not available or water supplement or quality is not secured. The present invention allows recovering most of the energy needed to be invested in the process and thereby to minimize energy consumption. In addition, this invention also relates to method of integrating an apparatus for extraction water from air in constructions such as building blocks of buildings, while utilizing, beside water supplement, temperature control and moisture control.
Nowadays, more than 1,500,000,000 people worldwide suffer from inadequate and/or insufficient fresh water. According to Population Action International, by the year 2025 more than 2.8 billion people in 48 countries will face water deficiency ranging from serious water shortages to major life-threatening crises, unless dramatic solutions are introduced. The number of people without access to piped fresh water accounts for more than 25% of the global population, most of them located in Africa, Asia and South America. Every 8 seconds, a child in the developing countries dies from disease caused by unsafe drinking water. The rapid growth of urban and rural populations, industry and agriculture, forces governments to enlarge infrastructures in order to provide fresh water; however, the existing budgets are insufficient for both water treatment (purification or desalination) and installation of pipe-net.
Desalination has long been considered a solution to the world's current and future water problems. Water desalting, or desalination, has long been utilized by water-deficient nations worldwide to produce or augment drinking water supplies. However, water desalting is limited to places where salty water is available and still needs long-distance pipes to transfer water from the production facility to the consumers. In addition, desalination cannot relieve the sea of pollutions, including heavy metals (mainly mercury), radioactive isotopes, etc.
Water evaporation, which is in the basis of the hydrologic cycle, is one of the most powerful physical processes on earth. The natural hydrologic cycle is composed of evaporation of water from bodies of water, earth and vegetation and condensation of air humidity to form precipitations. This process contributes the major part of the water on earth. The equilibrium between the water on earth and air humidity maintains air humidity to be unaffected by human activities.
At any given time, each square kilometer of air, almost everywhere on the globe, contains 10-40 thousands metric tons of water, sufficient to supply at least 100,000 people with all their water consumption or drinking water only for at least 2 million people.
Water extraction from air moisture as an alternative water source is known and reported since bible time. Water from air humidity, an unlimited renewable natural resource, is available to all mankind, except in certain climatic extremes such as temperatures below 4° C. and extreme arid zone. Nature continually recharges the atmosphere with moisture by evaporation from oceans, seas and fresh water bodies and therefore, air humidity is endless water source.
The importance of implementation of technologies for extraction of water from the air stems from four main reasons: 1) In many regions drinking water is unavailable or insufficient; 2) In many regions where water is available the water is polluted; 3) Tens of percentages of the global population have no access to piped fresh water; and 4) Infrastructure expansion cannot overtake rapid population growth, industrial development and developing agricultural needs.
Cost effective adsorption of atmospheric moisture and low dependency on ambient relative humidity and temperature are the breakthrough characteristics of effective method and technology enable utilization of this enormous water resource. Unfortunately, none of the existing methods and technologies to extract water from air overcomes these basic problems to fulfill these demands.
Various methods for extraction of atmospheric moisture for water supplement, as well as for air drying, are known and reported (for example: U.S. Pat. No. 1,816,592, U.S. Pat. No. 2,761,292, U.S. Pat. No. 3,740,959, U.S. Pat. No. 4,315,599, U.S. Pat. No. 4,351,651, U.S. Pat. No. 4,433,552, U.S. Pat. No. 4,726,817, U.S. Pat. No. 6,490,879, U.S. Pat. No. 6,644,060, DE 3,313,711, EP 1,142,835, WO 2004029372, U.S. Pat. No. 6,182,453, U.S. Pat. No. 2,779,172, U.S. Pat. No. 2,919,553, U.S. Pat. No. 2,944,404, U.S. Pat. No. 3,740,959, U.S. Pat. No. 4,315,599, U.S. Pat. No. 4,506,510, US 20050103615). Technologies utilizing cold for condensation, whether by direct cooling the air, and thereby reducing moisture capacity of the air below dew point, or condensation on cold object enable condensation of humidity without cooling the entire air volume, were reported. However, cold-based methods suffer from few disadvantages and technical limitations, including the need to apply electric power, effective at high relative humidity and at moderate temperature range, adsorb air pollutions and contaminates with the humidity and high energy consumption. Moreover, due to the need to cool large volumes of air and the high energy consumption, such technologies are limited for small scale apparatii, while the bigger reported was with daily capacity of 1 to 2 cubic meters of water. Nevertheless, there is no doubt that under extremely high relative humidity (RH), cold condensation is highly effective and the lower energy consumed technology for air drying or for extraction of water from air, especially if natural energy of physical process such as solar energy or night cold are involves. For instance, patent application IL183073, which is based on patent application IL182120, describe a method for extraction water from air combining solar Infrared chilling, night chilling, wind-flow and natural termo isolation.
Different approach suggesting utilization of the dipolar property of the water molecule using electromagnetic technologies and charged electrode to capture humidity (U.S. Pat. No. 4,206,396).
Additional approach claims condense air humidity by applying pressure using compressor or piston (WO/2002/018859, U.S. Pat. No. 6,230,503, WO 01/36885A1, U.S. Pat. No. 6,360,549, U.S. Pat. No. 6,453,684). Condensation of moisture with pressure is ineffective because steam do not act as ideal gas and therefore not well condensed under pressure. Moreover, applying pressure on large volumes of air, consume a lot of energy, which can't be recovered. The present invention makes use of piston to built pressure in isolated cylinder with integral heat exchanger. The combination of humidity adsorbing unit with pressure condenser, as described in the present invention, makes it possible to compress relatively small volume of hot gas with very high water content, instead of compressing large volume of ambient air with low water content. Therefore, much less energy is needed to be invested to compress the small volume of gas (air with steam) and the high temperature of the gas, together with the heat forming due to the pressure, can be recovered and reused for evaporation of water from the desiccant(s).
Additional group of methods involves desiccating materials, including liquid or solid (for example U.S. Pat. No. 2,138,689, U.S. Pat. No. 2,462,952, U.S. Pat. No. 4,146,372, U.S. Pat. No. 4,185,969, U.S. Pat. No. 4,219,341, U.S. Pat. No. 4,285,702, U.S. Pat. No. 4,304,577, U.S. Pat. No. 4,342,569, U.S. Pat. No. 4,345,917, U.S. Pat. No. 4,374,655, FR 2,813,087, WO 09966136, US 20050103615, WO 106649, U.S. Pat. No. 6,588,225). In many of the technologies, solar heat is utilize to desorb the humidity adsorbed by the desiccants, while condensation is made by heat exchanging technique, mainly with cold air or water. The reason for the need to use natural energy source is the high energy required for desorption since water evaporation is required, consume more than 550 kcal per each liter of water and temperature close to 100 deg C. Under such conditions, additional energy is needed to condense the vapors to liquid. Therefore, with integration of energy recovery techniques (U.S. Pat. No. 4,345,917) or without using waste or solar heat, the practical application of such technologies is in doubt.
In order to reduce energy consumption, in WO 09966136A1 it was suggested to integrate pressure-valve enabling desorption under low temperature of about 65 deg C. simultaneously with increasing the pressure in the condenser. This enables condensation without applying cooling. However, condensation is made by air cooling, which cause lose of all energy invested at the desorption stage.
The present invention combines various technologies and methods in order to overcome the drawbacks of the known methods for extracting water from atmospheric air and to enable fresh water production at reasonable energy consumption, low dependency on ambient relative humidity and temperature. The present invention is applicable under conditions that cannot be appropriate in the known methods and technologies and makes it possible to recover most of energy needed to be invested during the process.
The present invention makes it possible to extract water vapors from the atmospheric air in small and medium and large portable devices, as well as extremely large water plants.
There is therefore provided, in accordance with a preferred embodiment of the present invention, a method for extracting water from atmospheric air. The method comprises the steps of:
(a) causing ambient air to be drawn across an air-desiccation material that is adapted to adsorb and/or absorb water vapors;
(b) collecting heat formed of the adsorption process and utilizing it to cool the condenser during the absorption stage using heat pump technology.
(c) contributing the heat energy to cool the condenser and thereby reduce temperature of ambient air pass through the condenser to achieve condensation of the humidity out of the atmospheric air passed. This can be performed by solar heat collector, or any alternative heat source, including waste or residual heat.
(d) flowing cold air formed in the condenser through gas-gas heat exchanger located at the inlet of the desiccant container in order to reduce the temperature of the atmospheric air entering into the desiccant container, and thereby increasing relative humidity and optimize the adsorption conditions and preventing evaporation of the absorbed humidity as a results of combination of dry air and high temperature.
(e) after the desiccant material has been fully or partially saturated with water vapor, sealing the desiccant container from enclosure of fresh air;
(f) circulating hot air in order to evaporate water that adsorbed by the desiccant as vapor;
(g) sucking the gas volume containing the water from the desiccants container and compress it into isolated cylinder;
(h) recover the heat from the cylinder and return the heat into the desiccants container;
(i) collecting the condensed water in water container while still under pressure;
(j) release pressure from the cylinder and the water container and transfer the water to water reservoir container;
(k) return the released air, upon releasing pressure, from the water container into a second desiccants container;
(l) releasing the cooled air from the heat pump, and entering atmospheric air into the desiccants container through one direction valve to compensate the volume air; and
(m) after all the water previously accumulated in the desiccation material was released and steam are condensed, opening the desiccants container and flowing fresh atmospheric air through the desiccants container.
Instead of using cold condensation, a pressure condenser can be applied, combined with heat recovery system and number of desiccants chambers connecting to single air compressor, functioning as condenser (pressure condenser). The pressure condenser, equipped with heat exchanger, makes it possible to return the heat energy applied to evaporate the water that was adsorbed by the desiccants, as well as energy that needed to be invested to generate pressure to condense steam. By using a set of three or more individual adsorbing chambers and heat transfer regime(s), it becomes possible to return more than 85% of the energy invested for desorption and thereby to minimize energy consumption and to overcome the drawbacks of the known methods for the extraction of water from atmospheric air. The possibility to produce fresh water with low energy consumption, low dependency on ambient relative humidity and to use renewable energy such as solar power, waste or residual heat and biomass are all benefits resulting from the low energy consumption as described in the present invention.
By designing the water production unit in flat and narrow dimensions, combined with infrared solar collectors, it is possible to combine a plurality of units together in a frame of wall or ceiling, while the external side of each unit is connected to solar heater and the internal side is exposed to the indoor space. In such design, it is also possible to cool indoor air directly with the cold condensation and/or to circulate the internal air through the condenser in order to remove humidity and to control indoor air temperature, including cooling the cold air by flowing it from the condenser or hot air by flowing it from the absorption/desorption compartment into the building space.
With such configuration, when the water production unit is designed in a compact structure having two sides wherein the absorption/desorption process occurs on one side while condensation occurs on the second side that involves cooling, it is an object of the present invention to provide a construction of walls or ceilings or any part of the building with building blocks that are capable of extracting humidity from atmospheric air, as an alternative source for fresh water supply. In parallel, the construction controls the internal temperature and humidity of close spaces.
It is another object of the present invention to integrate water producing system as a part of a construction with no need to make any significant change in the construction.
Before explaining at least one embodiment of the invention in detail, it is to be understood that the present invention is not limited in its application to the details set forth in the following description or exemplified by the examples. The invention is capable of other embodiments or of being practiced or carried out in various ways. Also, it is to be understood that the phraseology and terminology employed herein is for the purpose of description and should not be regarded as limiting.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the invention belongs. In addition, the descriptions, materials, methods, and examples are illustrative only and not intended to be limiting. Methods and materials similar or equivalent to those described herein can be used in the practice or testing of the present invention.
As used herein, the terms “comprising” and “including” or grammatical variants thereof are to be taken as specifying the stated features, integers, steps or components but do not preclude the addition of one or more additional features, integers, steps, components or groups thereof. This term encompasses the terms “consisting of” and “consisting essentially of”.
The phrase “consisting essentially of” or grammatical variants thereof when used herein are to be taken as specifying the stated features, integers, steps or components but do not preclude the addition of one or more additional features, integers, steps, components or groups thereof but only if the additional features, integers, steps, components or groups thereof do not materially alter the basic and novel characteristics of the claimed composition, device or method.
The term “method” refers to manners, means, techniques and procedures for accomplishing a given task including, but not limited to, those manners, means, techniques and procedures either known to, or readily developed from known manners, means, techniques and procedures by practitioners of the chemical, of engineering, and technological arts. Implementation of the methods of the present invention involves performing or completing selected tasks or steps manually, automatically, or a combination thereof.
The phrase “consisting essentially of” means that the composition or method may include additional ingredients and/or steps, but only if the additional ingredients and/or steps do not materially alter the basic and novel characteristics of the claimed composition or method.
Throughout this disclosure, various aspects of this invention can be presented in a range format. It should be understood that the description in range format is merely for convenience and brevity and should not be construed as an inflexible limitation on the scope of the invention. Accordingly, the description of a range should be considered to have specifically disclosed all the possible sub-ranges as well as individual numerical values within that range. Whenever a numerical range is indicated herein, it is meant to include any cited numeral (fractional or integral) within the indicated range. The phrases “ranging/ranges between” a first indicate number and a second indicate number and “ranging/ranges from” a first indicate number “to” a second indicate number are used herein interchangeably and are meant to include the first and second indicated numbers and all the fractional and integral numerals there between.
As used herein, the singular form “a,” “an,” and “the” include plural references unless the context clearly dictates otherwise. For example, the term “a compound” or “at least.
It is thus provided in accordance with a preferred embodiment of the present invention, an improvement to a method of extracting water from atmospheric air that comprises a first stage in which atmospheric air is passed through a desiccant material and is absorbed so as to saturate the desiccant material with water vapor and a second stage in which hot air is passed through the desiccant material so as to evaporate the water from the desiccant material and pass it through a condenser so as to collect the water that condenses on the condenser, the improvement comprising capturing heat formed by the desiccant material in the first stage and utilizing said heat to cool the condenser or to evaporate water adsorbed by desiccants in another chamber or compartment that connected to the same condenser.
Furthermore and in accordance with a preferred embodiment of the present invention, said capturing heat formed by said desiccant material is combined with capturing heat from desorption stage of another desiccants chamber, and/or heat formed upon compressing air upon condensation, and/or solar heat and or any other heat source, including residual or waste heat.
Furthermore and in accordance with a preferred embodiment of the present invention, the improvement further comprising utilizing cold air released by the condenser during the first stage to reduce temperature and increase relative humidity of the atmospheric air passed through the desiccant material.
Furthermore and in accordance with a preferred embodiment of the present invention, the improvement further comprising recovering heat forming from cooling the condenser and combining said heat with solar heat so as to maintain high temperature in the second stage and thereby reducing heat consumption.
It is therefore also provided in accordance with another preferred embodiment of the present invention an improvement to an apparatus for extracting water from atmospheric air that comprises a container provided with a desiccant material adapted to adsorb water vapor and a condenser adapted to recover water from saturated air, the improvement comprising a heat collector adapted to collect heat and a heat pump adapted to receive said heat and utilizing said heat to cool the condenser.
Furthermore and in accordance with a preferred embodiment of the present invention, the improvement further comprising a solar heat collector that transfers additional heat to said heat pump.
Furthermore and in accordance with a preferred embodiment of the present invention, the use of set of desiccants chambers or compartments, combined with heat recovery element makes it possible to compress small volume of hot gas with very high water content, instead of compressing large volume of ambient air with low water content. Therefore, much less energy is needed to be invested in order to compress the small volume of gas (air with steam) and produce high temperature gas, together with the heat formed due to the pressure. The heat can be recovered and reused for evaporation of water from the desiccant(s). The present invention is therefore the sole technology for extraction of water from air having positive energy balance.
Furthermore and in accordance with a preferred embodiment of the present invention, the improvement further comprising a heat exchanger adapted to utilize cold air released by the condenser in order to reduce the temperature and increase relative humidity of the atmospheric air that is passed through the desiccant material.
Furthermore and in accordance with a preferred embodiment of the present invention, the apparatus comprises at least one blower.
Furthermore and in accordance with a preferred embodiment of the present invention, the apparatus comprises a heating unit.
Therefore and in accordance with yet another preferred embodiment of the present invention, it is provided an integrated construction comprising: a plurality of water extracting building blocks comprising a container provided with a desiccant material adapted to adsorb water vapor and a condenser adapted to recover water from air moisture;
a plurality of solar heat collectors wherein each solar collector is provided to each one of said water extracting building blocks wherein said solar collectors are adapted to utilize solar heat for either or both water release from said desiccant material and cooling said condenser; and
water pipes adapted to transfer the extracted water for accumulation; constructing material adapted to adhere said plurality of building blocks together.
Furthermore and in accordance with a preferred embodiment of the present invention, said plurality of water extracting building blocks are working in a continuous manner.
Furthermore and in accordance with a preferred embodiment of the present invention, said plurality of solar collectors are organized to be in an outer side of the construction while the condensers are organized to be placed in an inner side of the construction.
In addition and according to yet another preferred embodiment of the present invention, there of provided a method of integrating water extraction building blocks and air conditioning in a construction comprising:
providing a plurality of water extracting building blocks comprising a container provided with a desiccant material adapted to adsorb water vapor and a condenser adapted to recover water from saturated air;
structuring said plurality of water extracting building blocks in a wall-like structure;
providing water pipe to each one of said plurality of water extracting building blocks to collect the extracted water; and
providing a plurality of solar collectors for utilizing solar heat for either or both water release from said desiccant material and cooling said condenser.
In order to better understand the present invention and appreciate its practical applications, the following Figures are attached and referenced herein. Like components are denoted by like reference numerals.
It should be noted that the figures are given as examples and preferred embodiments only and in no way limit the scope of the present invention as defined in the appending Description and Claims.
The present invention provides a new and unique apparatus for extracting water out of humid air and using an apparatus and method of as building blocks in buildings in order to cool indoor air in spaces in which the building blocks are combined.
According to one aspect of the present invention, it is provided an improvement to a method of extracting water from atmospheric air that comprises a first stage in which atmospheric air is passed through a desiccant material and is absorbed so as to saturate the desiccant material with water vapor and a second stage in which dry and hot air is passed through the desiccant material so as to evaporate the water from the desiccant material and pass it through a condenser so as to collect the water that condenses on the condenser. The improvement comprises capturing heat formed by the desiccant material in the first stage and utilizing this heat to cool the condenser. The method of the present invention succeeds in utilizing a method that is worthless from energy logistics reasons to a beneficial method that can be up scaled.
Reference is now made to
A main blower 2 that is positioned at an outlet tube of desiccants container 1 is adapted to suck the air into the container through heat exchanger 10. Alternatively, main blower 2 can be positioned at the inlet of desiccant container 1 so as to push the atmospheric air to within the container. The air that is passed through cassette 4 and main blower 2 is flowing through an air circulating container 6 and can be released through an air release damper 7 and a condenser damper 13. Air circulating container 6 is provided with an air heating unit 1 adapted to heat the air circulating in circulating container 6.
While air is passed through the desiccant material in cassette 4, heat is also absorbed and is being collected by heat collector 5 that is adapted to transfer the absorbed heat to a heat pump 8. Optionally, a solar heat collector 12 is provided and positioned at the inlet to heat exchanger 10. The energy supplied by both heat collector 5 and solar heat collector 12 is utilized by heat pump 8 as will be explained herein after.
The apparatus is further provided with a condensing plate 9. Atmospheric air that passes through plate 9 is condensed on the cool plate. The energy from the heat collectors, heat collector 5 and solar heat collector 12 can be used to cool water condensing plate 9. A secondary blower 15 is provided to the apparatus so as to pump the atmospheric air and allow it to pass through condensing plate 9. Water that is condensed on the plate can be released from the apparatus through a water outlet 14.
Reference is now made to
According to the method of the present invention, the process of extracting water from atmospheric air is performed in two stages of operation. The first stage is the absorption process (shown in
The first stage is completed when the desiccation material is saturated with the humidity of the atmospheric air. Then, the second stage of extracting the water is commencing.
In the second stage shown in
When the temperature in desiccants container 1 reaches at least 65° C. the absorbed water in the desiccant material is evaporated as a results of the hot air flowing through.
When the temperature of condensing plate 9 reaches a temperature that enable condensation, or less, secondary blower 15 is being operated again so as to allow a small part of the circulated air (indicated by arrow 202) that is saturated with humidity to diverge into the condenser, so as to condense the moisture on condensing plate 9. The residual air that was passed through the condenser flows through heat exchanger 10 into the atmosphere; the air flow is indicated by arrow 204. In order to prevent vacuum in the apparatus, a one-direction valve 16 enables atmospheric air to be sucked into desiccants container 1. The water is collected from the system through water outlet 14.
When most of the absorbed water is extracted and condensed, the heating of the air by heating unit 11 stops and the system returns to the first absorption stage.
It should be mentioned that the apparatus for extracting water from atmospheric air that is applicable to the method of the present invention is an apparatus that is continuously operated.
It should be noted that the absorption conditions could be optimized in order to maximize the effectiveness of the method. As an example, as much as the ambient temperature is higher or sun irradiation is higher, more solar energy is supplied to heat pump 8, enabling massive reduction of the temperature of the air that passes through the condenser and flows into the inlet heat exchanger 10. In this way, atmospheric air that passes through heat exchanger 10 into desiccant container 1 is getting colder.
The energy loss from the desorption process according to the present invention is minimized by releasing the cooled air after condensation and recovering the heat formed in the condenser to maintain heat of desorption.
Moreover, minimizing absorption-desorption cycle by optimization of absorption conditions and condensation using cooled condenser is used in the apparatus of the present invention to increase the daily capacity of the apparatus.
Reference is now made to
In order to evaporate the water captured by the desiccants, heat is being applied using heat exchanger 607 or a heater and the air circulating through heat exchanger 607 forces the water to evaporate from the desiccants. After typical few minutes of heating, when the gas phase inside the desiccant container is saturated with steam, the air is sucked into a compressor 602 to be condensed into a cylinder 604.
The best option for compressing the gas is a piston 611 connected to an engine using crankshaft 612 or second piston or any other mechanical solution to move piston 611 backward and forward. Any other mechanical or other wise mechanism can be employed in this invention without limiting the scope of the invention. When the piston moves backwardly, the hot air containing steam from the desiccant container is pumped out of the desiccants container through valve 613 and when it moves forward, the steam is pumped through valve 614 into isolated cylinder 604 that contains a heat exchanger 605. Steam being condensed in the cylinder flows into water container 615 while the heat is being transferred from heat exchanger 605 to heat exchanger 607 located inside the desiccant container 600. When water container 615 is full, pressure is released through valve 616 and the water flows out into a water storage container (the storage container is not shown in the figure).
Optionally, hot air saturated with humidity is sacked out from desiccants container 600 into piston 611 and then compressed into isolated cylinder 604 equipped with heat exchanger 605.
Optionally, the condensed water flows into water container 615 and the water inside the water container condensing humidity from the hot air until the water container is full. When the water container is full, the pressure is released while the hot air flows back into the desiccants container and the water is transferred from the cylinder 604 into water container 615. When cylinder 604 is empty, condenser 602 is ready to continue and condensing steam.
Optionally, heat inside isolated cylinder 604 is transferred back to desiccant container 600 with liquid, which can be oil or aqueous solution, being circulated through pipe 606 between isolated cylinder 604 and heat exchanger 607 located inside desiccants container 600. When most of the water from the desiccant is evaporated and transferred to the condenser, the desiccants container is opened and fresh air is allowed to pass through the desiccants.
Reference is now made to
For the chamber in the desorption stage, when the gas phase inside the desiccant container is saturated with steams, the air is sucked from the chamber piston 611 or the steam pump to be compressed into isolated cylinder 604. When using piston 611, the piston is operated with engine using crankshaft 612 or hydraulic piston or other available technology capable of moving the piston forward and backward. When the piston moves backwardly, the hot air containing steam from the desiccant container is pumped out of the desiccants container through valve 613 and when it moves forward, the steam is pumped through valve 614 into a isolated cylinder 604. Valve 617 is open only in the chamber that at the desorption stage, enable to flow the steam into the condenser. Steam that is being condensed in the cylinder flow into water container 615, while the heat is being transferred from the heat exchanger 605 located inside isolated cylinder 604 back to heat exchanger 607 located in the desiccant chamber. When the water container 615 is full, pressure is released through valve 616 and the water flow out into a water storage container (not illustrated). It is an option to flow the released air from the water container 615 back into the container that during heating stage so the hot air will contribute the heating of the desiccants, and humidity of the released air will be adsorbed by the desiccants (not illustrated).
Because most of the energy required to operate the system is heat and because most of the heat invested to produce the water can be recovered and preserved, it is possible to use, for example, biomass as an energy source and even solar heat. Accordingly, by using agriculture/municipal organic wastes, it is possible to supply water for both municipal and agricultural purposes at significant lower price than many alternative water sources, especially other technologies for extraction of water from air.
According to another aspect of the present invention, it provides a method of combining the extraction of water from atmospheric air and air conditioning. According to the method of the present invention, the method comprises a plurality of modular building blocks in which the extraction of water occurs and is further comprising a construction made by the plurality of modular building blocks in order to establish an integrated working unit, structured in a wall, or any other part of buildings or construction.
The method is comprised of the following steps that take place in each building block:
(a) causing ambient air to be drawn across an air-desiccation material that is adapted to adsorb and/or absorb water vapors;
(b) cooling a condenser to temperature below dew point and flowing indoor air through the cold condenser to cool indoor atmosphere and to condensate the indoor humidity for water production;
(c) isolating the desiccants after it is saturated from the external atmosphere, and heating the desiccants by solar heat or any other heating source, including waste or residual heat, with or without involvement of heat pump;
(d) directing small air volume from the desiccants through the condenser into the internal space when the temperature of the desiccants is about 60 deg C. or higher and the temperature of the condenser is below dew point;
(e) collecting condensed water; and
(f) opening the desiccants compartment after the water previously accumulated in the desiccants was released and condensed and allowing fresh atmospheric air to flow through the desiccants container.
Now, the building blocks are being integrated together to a combined wall-like structure:
(a) if more than two blocks are used, for optimal energy operating conditions, at any given moment, two third of the blocks are at the absorption stage and one third are at desorption stage, or any other ratio that provide highly energy and water production efficiency;
(b) all solar collectors are jointly connected and heat distribution between blocks is centrally controlled, while the solar heat flows from the solar collectors into the blocks that are in desorption stage, directly or through heat pump;
(c) the heat pump is also connected to central heat source that provides complementary heating that is utilized for the desorption process and provides energy to cool the condensers; and
(d) water from all blocks is collected into central container.
Reference is now made to
A solar heat collector 308 is provided adjacent outdoor dampers 304 while a condenser 310 that is adapted to allow condensation of water is provided on opposite to solar heat collector 308. A condenser blower 312 is adapted to move the air so it will pass through condenser 310.
Extracted water drains through a water outlet 314. An indoor damper 316 is provided in its vicinity while a heater or heat exchanger is adjacent to cassette 300.
Reference is now made to
The heat collected by solar heat collector 308 is utilized to cool condenser 310 using heat-pump technology. When the building block is in the absorption stage, the cold condenser, cooled by a heat-pump or electricity is used to cool the indoor atmosphere while indoor humidity that is condensed is released through water outlet (314) into a central water container (the container is not shown in the figure).
Reference is now made to
Reference is now made to
Reference is now made to
Reference is now made to
The building blocks are being connected to one another in a manner that is similar to regular building blocks construction. Interface concrete 404 is being placed between the units.
At any moment, for optimal energy consumption and water production, about two thirds of the building blocks are in the absorption stage while about one third are in the desorption stage. This ratio might be changed based on the desiccants characters and ambient relative humidity and temperature, without limiting the scope of the present invention. All solar collectors are jointly connected, and contribute heat to one third of the building blocks that are in the desorption stage. When all the absorbed water from the blocks that are in the desorption stage is extracted, outlet dampers 306 are opened and the next third of the blocks are returning to the desorption stage. The solar collectors are also connected to heat pumps that is being connected to alternative heat source, such as electric, gas, diesel or residual heat. The heat pump supply complementary heat, if necessary (such as at night time or in cloudy weather), for desorption, as well as energy to cool the condensers.
It should be clear that the description of the embodiments and attached Figures set forth in this specification serves only for a better understanding of the invention, without limiting its scope as covered by the following Claims.
It should also be clear that a person skilled in the art, after reading the present specification can make adjustments or amendments to the attached Figures and above described embodiments that would still be covered by the following Claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 195444 | Nov 2008 | IL | national |
This application is a continuation-in-part of co-pending, commonly assigned PCT Patent Application No. PCT/IL2007/000989, filed Aug. 8, 2007, which is based upon and claims the benefit of U.S. Provisional Patent Application Ser. No. 60/836,282, filed Aug. 8, 2006, and U.S. Provisional Patent Application Ser. No. 60/849,678, filed Oct. 4, 2006, and corresponds to and claims the benefit of Israeli Patent Application Serial No. 195444, filed Nov. 23, 2008.
| Number | Date | Country | |
|---|---|---|---|
| 60836282 | Aug 2006 | US | |
| 60849678 | Oct 2006 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/IL2007/000989 | Aug 2007 | US |
| Child | 12368026 | US |
