FIELD OF INVENTION 
       [0001]    The present field of invention generally relates to extraction of atmospheric water. More particularly, it relates to a system and a method for obtaining potable water from extracting atmospheric water. 
       BACKGROUND 
       [0002]    The earth consists mainly of water and water exists on the earth&#39;s surface, in aquifers in the soil as groundwater, and in the atmosphere as water vapour. Of all the water on earth, only less than 3 percent is fresh water. However, as majority of fresh water is trapped in ice caps, glaciers and aquifers, only less than 1 percent of the water supply on earth is portable and available for drinking purposes. 
         [0003]    In recent years, global concerns regarding insufficient fresh water sources have increased greatly. Currently, sources of fresh water include water provided by lakes, rivers, and artesian wells. Unfortunately, these fresh water sources are not sustainable because of decline both in capacity and purity at alarming rates due to expansion of deserts. Furthermore, factors such as climate changes, environmental pollution, as well as population growth further threaten existing fresh water sources. 
         [0004]    Besides having insufficient fresh water sources, there are also problems associated with provision of potable water. The provision of potable water is a serious problem in areas where rainfall is scarce, seasonal, or where there are relatively small water catchment areas and little natural local water storage. Additionally, as fresh water sources are not evenly distributed globally, some geographical locations do not have ready access to fresh water. Constructing reservoirs and water desalination plants usually alleviates this problem. However, many countries are unable to afford water desalination plants due to the relatively high capital investment and operational costs required. 
         [0005]    Another problem associated with the provision of potable water relates to the setting up and maintenance of potable water distribution networks, such as water piping networks, which require significant efforts and resources. Further, water piping networks have limited lifespan and are frequently associated with water leakage and contamination problems. Water piping networks typically use water pipes made from metal ducts, concrete ducts or polyvinyl chloride (PVC) pipes. Metal and concrete ducts are vulnerable to corrosion by inorganic acid and alkaline contaminants, whereas organic solvents present in soil and building materials can be absorbed by and permeated through PVC pipes. 
         [0006]    One way to overcome the aforementioned problems is by extracting water from the atmosphere. Approximately 577,000 km 3  of water evaporates into the atmosphere from water bodies, such as seas and rivers, and the earth&#39;s surface each year, with air remaining close to the earth&#39;s surface containing the greatest percentage of water. Commercial water production systems capable of extracting atmospheric water have made it possible to supply potable water without the need for tapping on a central water source via complex water distribution networks. Such water production systems are therefore an attractive alternative to conventional ways of deriving and distributing potable water. 
         [0007]    In principle, these commercial water production systems collect water droplets formed by condensation of water vapour present in the atmosphere on cold surfaces cooled by refrigeration means. The working principle is similar to the disclosure in patents filed to Ehrlich in 1978 (U.S. Pat. No. 4,255,937), Reidy (U.S. Pat. No. 5,106,512, U.S. Pat. No. 5,149,446, U.S. Pat. No. 5,203,989) and Morgen et al. in 2002 (U.S. Pat. No. 6,931,756B2). With the advent of more efficient refrigeration techniques, the cost of electricity needed for extracting an amount of water from the atmosphere can be lower than the price of a bottled water of equivalent volume, or that of the utility charge of obtaining an equivalent volume of water from the tap with the additional cost for boiling or purifying water using mechanical and chemical filtering means. 
         [0008]    However, the cost of hardware of a commercial water production system comprising compressor, condenser, evaporator and filtration means remains relatively high leading to unattractive return of investment. Additionally, for climates with low ambient temperature levels or where temperature fluctuates significantly, atmospheric water extraction becomes difficult. Typically, these commercial water production systems for water vapour extraction operate above 20° C. and above a relative humidity of 35%. 
         [0009]    U.S. Pat. No. 3,675,442 to Swanson discloses an atmospheric water collector, which employs a cooling coil immersed in a fresh water bath that cools the bath. The cooled water is pumped through a conduit and condensing frame. Water vapour present in winds that pass over the condensing frame is condensed and drained into a collector. However, the cooled water is periodically mixed with the condensed water subjecting the condensed water to contamination. 
         [0010]    U.S. Pat. No. 5,056,593 to Hull discloses, in several variations, the use of electrostatic and magnetic fields to substantially enhance water product extraction yields in a dehumidifying heat exchanger apparatus. Liquid water droplets are electrostatically collected on grounded or charged heat transfer tubes in the heat exchanger apparatus. In one variation, charged or grounded horizontally-declined heat transfer tubes with attached drainage wicks attract liquid droplets and accelerate condensing heat transfer by continuous absorption and transfer of condensate. The use of drainage wicks to absorb and confine condensate collected on the surfaces of the heat transfer tubes may result in the loss of water extracted and advance the growth of fungi and bacteria on the drainage wicks. Additionally, the heat exchanger apparatus may be electrically unsafe with charged electrode wires entrenched between the tubes of the heat exchange unit. 
         [0011]    U.S. Pat. No. 7,000,410 to Hutchinson discloses a device that utilizes a condenser type refrigerant system with multiple fans and two air chambers to produce water from the air. The apparatus further deploys a stainless steel ioniser to charge the ambient air to maximise extraction of moisture from the air. The two air chambers operate in tandem to mix desiccated ionised air that exited from the evaporator plates with fresh incoming air drawn through a compressor, a condenser and the ioniser. This causes partial drying of the newly formed condensation, which results in loss of condensation leading to reduced output and efficiency. 
         [0012]    JP Pat. No. 02,172,587 to Katsumi and U.S. Pat. No. 5,435,151 to Han disclose water making apparatus for use on vehicles. U.S. Pat. App. No. 20040040322 filed by Engel et al. discloses a similar water extraction device for vehicles, together with some applications including central air system and mobile unit. All the disclosed devices tap on existing or external air conditioning systems to simplify system design and lower device cost. However, conventional designs fail to function properly in many temperate areas where ambient temperature drops below 20° C. during the night or during cold spells and storms. This problem accentuates for water extraction devices installed on vessels and ships, on caravans and emergency vehicles. 
         [0013]    Therefore, there is a need for a system and a method for obtaining potable water from extracting atmospheric water, which at least addresses one of the aforementioned disadvantages. 
       SUMMARY 
       [0014]    The present embodiment of the invention disclosed herein provides an atmospheric water extraction system and a method for extracting atmospheric water for obtaining potable water. 
         [0015]    In accordance with a first aspect of the invention, there is disclosed an atmospheric water extraction system comprising a passage, a cooling unit and an ioniser. The passage comprises a condenser portion and a cooling portion inter-configured for cyclical passage of fluid therethrough. The cooling unit is in thermal communication with the cooling portion and is for extracting heat from liquid passaging through the cooling portion to thereby cool the liquid, in which the liquid is transportable to the condenser portion subsequent to passaging through the cooling portion. The ioniser is for ionising ambient air into ionised air, in which the ionised air is charged for enhancing adhesion of water vapour thereto. The ionised air is transportable for thermal interaction with the condenser portion of the passage for condensing the water vapour into water droplets, and the liquid passaging through the condenser portion receives heat from the ionised air during thermal interaction of the ionised air with the condenser portion. The liquid is then transportable to the cooling portion of the passage for re-cooling thereby subsequent to passaging through the condenser portion. 
         [0016]    In accordance with a second aspect of the invention, there is disclosed an atmospheric water extraction method. The method comprises providing a passage having a condenser portion and a cooling portion inter-configured for cyclical passage of fluid therethrough. The method also comprises extracting heat from liquid passaging through a cooling portion to thereby cool the liquid using a cooling unit, whereby the cooling unit is in thermal communication with the cooling portion. The liquid is then transportable to the condenser portion subsequent to passaging through the cooling portion. The method further comprises ionising ambient air into ionised air using an ioniser, in which the ionised air is charged for enhancing adhesion of water vapour thereto. The ionised air is transportable for thermal interaction with the condenser portion of the passage for condensing the water vapour into water droplets, and the liquid passaging through the condenser receives heat from the ionised air during thermal interaction of the ionised air with the condenser portion. The liquid is then transportable to the cooling portion of the passage for re-cooling thereby subsequent to passaging through the condenser portion. 
         [0017]    In accordance with a third aspect of the invention, there is disclosed an atmospheric water extraction system comprising an ioniser and a condenser portion. The ioniser ionises ambient air for obtaining ionised air therefrom, in which the ionised air is charged for enhancing adhesion of water vapour thereto. The condenser portion is disposed alongside the ioniser for condensing water vapour in the ionised air into water droplets. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0018]    An embodiment of the invention is described hereinafter with reference to the following drawings, in which: 
           [0019]      FIG. 1  shows a partial schematic diagram of an atmospheric water extraction system according to an embodiment of the invention; and 
           [0020]      FIG. 2  shows an operational flow of the atmospheric water extraction system of  FIG. 1 . 
       
    
    
     DETAILED DESCRIPTION 
       [0021]    An atmospheric water extraction system and a method for extracting atmospheric water are described hereinafter for addressing at least one of the aforementioned disadvantages. 
         [0022]    For purposes of brevity and clarity, the description of the invention is limited hereinafter to applications relating to atmospheric water extraction. This however does not preclude various embodiments of the invention from other applications. The fundamental inventive principles of the embodiments of the invention shall remain common throughout the various embodiments. 
         [0023]    An embodiment of the invention described in the detailed description provided hereinafter is in accordance with  FIG. 1  and  FIG. 2  of the drawings, in which like elements are numbered with like reference numerals. 
         [0024]    With reference to  FIG. 1 , an atmospheric water extraction system  100  (hereinafter known as system  100 ) for extracting atmospheric water is described according to an embodiment of the invention. The system  100  generally comprises an extraction unit  110 , a passage  111 , a water collection unit  112  and a cooling unit  113 . 
         [0025]    The extraction unit  110  is for extracting water vapour in ambient air and the extraction unit  110  has an intake  114  and an exhaust  116  formed therein for allowing flow of the ambient air therethrough. The extraction unit  110  comprises an ioniser  118  and a condenser portion  120 , in which the condenser portion  120  is disposed alongside the ioniser  118 . The extraction unit  110  further comprises an air filter  122 , a ventilator  124  and a water collection tray  126 . 
         [0026]    The ioniser  118  is for ionising the ambient air into ionised air. When the ioniser  118  ionises the ambient air, air particles present in the ambient air become positively or negatively charged, although negative charging is preferable in most uses. The charged air particles (ionised air) enhance adhesion of water vapour thereto for extracting atmospheric water over varying ambient temperatures and humidity. Due to the polar nature of water, each water molecule has an electric dipole moment. The oxygen atom in each water molecule has a partial negative charge while each hydrogen atom in each water molecule has a partial positive charge. As such, the difference in charge causes water molecules to be attracted to each other and to other polar molecules. Since the ionised air comprises charged particles, adhesion of water vapour thereto is enhanced due to the partial negative and positive charges present on water molecules. The ioniser  118  is also for sterilising the ambient air and for inhibiting growth of fungi and bacteria when the system  100  is in use. 
         [0027]    The condenser portion  120  is for condensing water vapour in the ionised air to obtain water droplets. The ionised air is transportable for thermal interaction with the condenser portion  120  for condensation of water vapour to take place. Condensation of water vapour occurs when a surface is colder than the dew point temperature (condensation threshold temperature) of the air surrounding the surface. At this temperature, the air has a relative humidity of equivalent to 100 percent and the air becomes saturated with water. The dew point temperature of the air is dependent on both air temperature and humidity. Therefore, surfaces of the condenser portion  120  over which the ionised air flows must have a temperature that is lower than the dew point of the ionised air. 
         [0028]    The passage  111  is inter-configured for cyclical passage of fluid therethrough. The passage  111  comprises a first fluid channel  128  and a second fluid channel  130  for interconnecting the extraction unit  110  and the cooling unit  113 . The first fluid channel  128  is for receiving liquid from the cooling unit  113  and a second fluid channel  130  for returning the liquid to the cooling unit  113 . The cooling unit  113  is in thermal communication with a cooling portion  132  for extracting heat from the liquid passaging through the cooling portion  132  to thereby cool the liquid. The liquid is then transportable to the condenser portion  120  subsequent to passaging through the cooling portion  132  for cooling the surfaces of the condenser portion  120  to a temperature that is lower than the dew point temperature of the air surrounding the surfaces for condensation of water vapour to occur. The surfaces of the condenser portion  120  can be made of any material of which water vapour condensation can occur in response to cooling of the material in a given environment. For instance, the material can comprise of metal, glass, plastic, or the like. 
         [0029]    Additionally, the surfaces of the condenser portion  120  are film-coated with food-grade materials, such as, gold, tin, Teflon or the like in compliance with public health requirements governing use of materials in contact with drinking water. The surfaces of the condenser portion  120  are preferably plated with gold or any material of which enhances the rate of heat transfer. The condenser portion  120  is preferably designed for optimising air circulation, velocity and distribution of air on the surfaces for achieving an optimal rate of water vapour extraction. 
         [0030]    The cooling unit  113  comprises a drive assembly  136  for displacing the liquid from the cooling unit  113  to the condenser portion  120  via the first fluid channel  128 . The drive assembly  136  comprises an actuator valve  138  and a fluid pump  140 . The fluid pump  140  is one of a centrifugal pump and a displacement pump. Further, the cooling unit  113  is couplable to an external cooling source (not shown) for extracting heat from the liquid to cool liquid. The external cooling source can comprise a refrigerant, such as Freon, for extracting heat from the liquid. As such, instead of relying on the cooling portion  132  for extracting heat from the liquid, the cooling unit  113  can tap on the external cooling source for cooling the liquid. The liquid is one of water and alcohol, or the like. The cooling unit  113  further comprises a temperature measurement device  142  for measuring the temperature of the liquid passing therethrough. The temperature of the liquid is preferably in the range of 5° C. to 15° C. 
         [0031]    Prior to ionisation of the ambient air by the ioniser  118 , the ambient air is passed through the air filter  122  of the extraction unit  110 . The air filter  122  is for filtering the ambient air and is disposed in the vicinity of the ioniser  118 . The air filter  122  can also be disposed in the intake  114  or in the vicinity of the intake  114 . Furthermore, the air filter  122  is replaceable and therefore can be replaced when necessary. 
         [0032]    The ventilator  124 , on the other hand, is disposed in the vicinity of the condenser portion  120  and is for displacing and directing the ambient air into the extraction unit  110 . The ventilator  124  is preferably a form or the like impeller-based air mover controllable to vary flow rate of the ambient air. By varying the flow rate of the ambient air, convecting air currents necessary for obtaining sufficient water vapour condensation on the surfaces of the condenser portion  120  is generatable. The ventilator  124  can also be disposed at or adjacent the exhaust  116 . The air filter  122  and the ventilator  124  are orientable or disposed as readily recognised by those skilled in the art to achieve effectively clean or dust-controlled airflow or circulation inside the extraction unit  110 . 
         [0033]    The water collection tray  126  of the extraction unit  110  is for receiving the water droplets from the condenser portion  120 . The water collection tray  126  is disposed in the extraction unit  110  such that the water droplets received are directed to the water collection unit  112 . The water collection unit  112  of the system  100  comprises a water collection tank  144 , a drive assembly  146  and a water purifier  148 . 
         [0034]    The water collection tank  144  is for receiving the water droplets from the water collection tray  126 . The water collection tank  144  preferably comprises a sediment filter (not shown) for filtering the water droplets received. The water collection tank  144  further comprises a water level measurement device  150  for measuring the water level present in the water collection tank  144  and a water purifier  152  for purifying the water droplets received. The water level measurement device  150  is an optical or a float switch type while the water purifier  152  preferably comprises an ultra-violet light or an ozone generator. Further, the water purifier  152  may incorporate other filtration means including any mechanical, chemical or biological filtering systems suitable for purifying water for drinking purposes. 
         [0035]    The drive assembly  146  is for transporting water collected in the water collection tank  144  to the water purifier  148  of the water collection unit  112 . The drive assembly  146  is one of a fluid pump, a centrifugal pump and a displacement pump. The drive assembly  146  provides additional gravitational pressure to extract the water collected out of the water collection tank  144  and displace the water through the water purifier  148 . The water purifier  148  comprises any suitable device capable of sterilising water, for instance, suitable chemical means, heating elements, ultra-violet radiation emitters, or the like. The water after passing through the water purifier  148  is suitable for drinking and can be transported through a fluid duct  153  to external appliances or any storage. 
         [0036]    The system  100  further comprises a temperature measurement device  154  for measuring ambient air temperature and a relative humidity measurement device  156  for measuring relative humidity of the ambient air. Additionally, the system  100  further comprises a controller  158  for controlling the system  100 . The controller  158  is couplable to a signalling interface module for relaying any control signals for operating any electrically driven parts and components of the system  100  that require instructions, signalling and/or electricity supply. 
         [0037]    The controller  158  preferably comprises a microprocessor (not shown) for storing and executing software applications or embedded codes capable of generating appropriate control signals in accordance with a set of pre-programmed instructions. Measured data is further processable in the controller  158  in which the processes include logging, reading and writing, storing and backing-up, analysing and displaying of measured and/or control data. Further, the controller  158  is coupled to external computing equipment via a wired or wireless data exchange interface (not shown). Finally, electrical power supplied to the controller  158  and the system  100  may be single-phase or multi-phase alternating current tapped from power grids or mobile electricity generators such as those used on vessels, cruises, caravans, oil rigs, construction sites and other similar facilities. Alternatively, electrical power can be supplied as direct current. 
         [0038]      FIG. 2  illustrates the operational flow  200  of the system  100 . Upon supplying electrical power to the system  100 , in a step  210 , the controller  158  activates the ioniser  118  and the ventilator  124 . Further, the controller  158  samples data measured by the temperature measurement device  142  of the cooling unit  113 , the water level measurement device  150 , the temperature measurement device  154  of the system  100  and the relative humidity measurement device  156  at a predetermined regular interval to obtain measured data therefrom. The controller  158  then analyses the measured data and determines the mode of operation, and may display the measured data for visual monitoring by an operator of the system  100  in a step  212 . 
         [0039]    Next in a step  214 , the controller  158  retrieves the required controls according to the mode of operation that is determined in the step  212 . Further, in a step  216 , the controller  158  looks up required controls for required parts of the system  100  based on the measured data. Finally, in a step  218 , corresponding control signals provided by the steps  214  and  216  are sent to the corresponding elements of the system  100 . 
         [0040]    An example of operating the system  100  is provided hereinafter. 
         [0041]    The controller  158  selects a first mode of operation denoted as a NORMAL mode when (a) the ambient temperature measured by the temperature measurement device  154  is greater than a first predetermined threshold TLA 01 , (b) the ambient relative humidity measured by the relative humidity measurement device  156  is greater than a first predetermined level RHL 01 , (c) the temperature of the liquid from the cooling portion  132  measured by the temperature measurement device  142  is lower than a predetermined threshold of TLC HI , (d) the water level in the water collection tank  144  detected by the water level measurement device  150  does not exceed a predetermined level WLC HI , and (e) if an external water storage tank is present (coupled to the system  100 ) and the external water storage tank does not indicate FULL state (not shown). 
         [0042]    If the above conditions are met, the controller  158  opens the actuator valve  138  to allow the liquid from the cooling portion  132  to flow into the first fluid channel  128 . Further, the controller  158  activates the fluid pump  140  to convey the liquid to the condenser portion  120  via the first fluid channel  128 . The liquid is then circulated from the condenser portion  120  back to the cooling portion  132  by means of the second fluid channel  130 . The liquid passaging through the condenser portion  120  receives heat from the ionised air during thermal interaction of the ionised air with the condenser portion  120 . The liquid is then transportable to the cooling portion  132  of the passage  111  for re-cooling thereby subsequent to passaging through the condenser portion  120 . The liquid passaging through the passage  111  is substantially isobaric. 
         [0043]    Excessive airflow generated by the ventilator  124  may hamper the extraction of water vapour from the ambient air. As such, the speed of the airflow generated by the ventilator  124  should preferably be controlled at a predetermined optimised rate. The controller  158  can control the ventilator  124  and the controller  158  attains a predetermined airflow by adjusting fan speed of the ventilator  124 . In the first mode of operation, the controller  158  sets the fan speed of the ventilator  124  to low or medium. The ambient air is then controllably induced into the system  100  by the ventilator  124 . The incoming air first passes through the air filter  122  followed by an ionising field created by the ioniser  118 . The ionised air then passes through the condenser portion  120  and surrounds the surfaces of the condenser portion  120  in which condensation of water vapour takes place. The water droplets obtained after condensation drips onto the water collection tray  126  and are directed into the water collection tank  144 . The water level measurement device  150  measures the water level present in the water collection tank  144  to detect predetermined high (WLC HI ) and low (WLC LO ) water levels. 
         [0044]    During the NORMAL mode and when the water level detected by the water level measurement device  150  exceeds a predetermined level low (WLC LO ) level, the water purifier  152  in the water collection tank  144  is activated by the controller  158  on either a continuous or regular basis with the water purifier  152  being periodically activated for a first duration of WPU ON1  and deactivated for a second duration of WPU OFF1 . When the water level measured by the water level measurement device  150  detects a predetermined high (WLC HI ) level, and if the external water storage tank is present and the external water storage tank does not indicate the FULL state, the controller  158  activates the drive assembly  146  to transfer the water from the water collection tank  144  through the water purifier  148  of the water collection unit  112 . The controller  158  can activate the water purifier  148  on either a continuous or regular basis. 
         [0045]    The controller  158  selects a second mode of operation denoted as a COLD mode when (a) the ambient temperature measured by the temperature measurement device  154  falls between the first predetermined threshold TLA 01  and a second predetermined threshold TLA 02 , (b) the ambient relative humidity measured by the relative humidity measurement device  156  is equal to or greater than the predetermined level RHL LO , (c) the temperature of the liquid from the cooling portion  132  measured by the temperature measurement device  142  equals to or lower than the predetermined threshold of TLC LO , (d) the water level in the water collection tank  144  detected by the water level measurement device  150  does not exceed the predetermined level WLC HI , and (e) if the external water storage tank is present (coupled to the system  100 ) and the external water storage tank does not indicate FULL status (not shown). 
         [0046]    If the above conditions are met, the controller  158  operates the system  100  through the same control and decision-making steps as performed for the NORMAL mode. The only exception is that the fan speed of the ventilator  124  is set to high for increasing the air circulation in the vicinity of the condenser portion  120 , leading to higher water vapour condensation efficiency when the ambient air temperature is low. 
         [0047]    The controller  158  selects a third mode of operation denoted as a SUSPEND mode when (a) the ambient temperature measured by the temperature measurement device  154  falls below the second predetermined threshold TLA 02 , or (b) the ambient relative humidity measured by the relative humidity measurement device  156  falls below a second predetermined level RHL 02 , or (c) the temperature of the liquid from the cooling portion  132  measured by the temperature measurement device  142  is higher than a predetermined threshold of TLC HI , or (d) the water level in the water collection tank  144  detected by the water level measurement device  150  equals or exceeds the predetermined level WLC HI , or (e) if the external water storage tank is present (coupled to the system  100 ) and the external water storage tank indicates FULL state (not shown). 
         [0048]    If any of the above conditions is met, the controller  158  stops all the steps required to extract water vapour. However, the ioniser  118  and the ventilator  124  can continue to operate controllably by the controller  158 . The controller  158  may also continue to monitor all measurement means if any. Further, should the water level in the water collection tank  144  is above WLC LO , the controller  158  may continue to activate the water purifier  152  of the water collection tank  144  on a continuous or periodic basis. 
         [0049]    Exemplary parameters that are preferably used in the system  100  for extracting atmospheric water are as follows: 
         [0000]    1) TLA 01 =25° C. and TLA 02 =15° C., as temperature threshold values used for classifying the modes of operation;
 
2) RHL 01 =50% and RHL 02 =25%, as relative humidity threshold values used for classifying the modes of operation;
 
3) TLC LO =5° C. and TLC HI =15° C., as temperature threshold values of the liquid being cooled by the cooling portion  132  used for activation and deactivation of the actuator valve  138  and drive assembly  146 ; and
 
4) WPU ON =30 seconds and WPU OFF1 =45 minutes, for periodic activation and cut off durations of the water purifier  152  of the water collection tank  144 .
 
         [0050]    The system  100  for extracting water vapour from the ambient air for obtaining potable water provides a solution to water harvesting without the need for extensive water distribution networks. Hence, the system  100  is well suited for indoor, outdoor, fixed and mobile applications. Further, as the system  100  is able to ride on external cooling sources such as existing refrigeration and central air system for extracting heat from the liquid for cooling the liquid, the system  100  offers a cost-effective water making system with relatively low equipment, operational and maintenance costs. 
         [0051]    Furthermore, the system  100  is able to operate at an ambient air temperature of as low as 15° C., thus making the system  100  well suited for many indoor and outdoor, fixed and mobile applications not only in tropical regions, but also in temperate areas with ambient air temperatures well below what conventional systems are designed to operate at. 
         [0052]    In the foregoing manner, an atmospheric water extraction system and a method for extracting atmospheric water are described according to one embodiment of the invention for addressing at least one of the foregoing disadvantages. Although only one embodiment of the invention is disclosed, the invention is not to be limited to specific forms or arrangements of parts so described and it will be apparent to one skilled in the art in view of this disclosure that numerous changes and/or modification can be made without departing from the scope and spirit of the invention.
The earth consists mainly of water and water exists on the earth's surface, in aquifers in the soil as groundwater, and in the atmosphere as water vapour. However, of all the water on earth, only less than 3 percent is fresh water. Due to factors such as climate changes, environmental pollution, as well as population growth, the available amount of fresh water sources is dwindling rapidly. In addition, there are many problems associated with provision of potable water using existing techniques. One way to overcome the aforementioned problems is to extract water from the atmosphere. However, hardware costs of current commercial systems are relatively high and they are not efficient in terms of performance. An embodiment of the invention provides a system and a method for obtaining potable water by extracting atmospheric water.