AMBIENT AIR WATER EXTRACTION AND SUPPLY APPARATUS AND METHOD
Cross-reference to Related Applications The present application claims the benefit of previously filed co-pending U.S. Provisional Patent Applications, Serial No.60/026, 342, filed September 19, 1996 and EE60978909505, filed May 1,1998.
Field of the Invention The present invention relates to water supply apparatuses, and is particularly directed to a relatively compact, lightweight, economical and portable apparatus, the internal components of which are sealed from the surrounding atmosphere, for extracting water from water vapor in filtered ambient air, and then treating, storing, filtering and dispensing purified water, by a water recovery scheme that also improves the quality of the air returned to the environment through a process of dehumidification, and filtration.
Background of the Invention
Although a variety of water extraction and treatment systems have been proposed to date for recovering potable water from the water vapor present in the ambient air, each has its own shortcomings, either from a standpoint of complexity and energy required (including heat dissipated into the atmosphere), or its failure to take into account a number of contaminant parameters that may be present in the air or in the water being made available for human consumption. While many of these Systems are touted as portable, their operation and the quality of the water produced by the extraction process is often dependent upon the environment in which they operate. For example, while a number of systems are condensation-based, the water recovery path to post extraction storage and treatment components may be
exposed to the environment and thereby allow entry of contaminants. In addition, many systems are not readily suited for indoor use for various reasons, one of which is their size or negative impact on the closed environment due to heating and recirculation of contaminants. The present invention can be free standing for installation at any selected location within the home, office, in the basement, garage, or any convenient location. An optional enclosure can be provided to match the decor of the location the apparatus is installed in.
Summary of the Invention In accordance with the present invention, the shortcomings of conventional water supply systems, including portable extraction systems intended for indoor use, are remedied by what is effectively an environmentally friendly water extraction apparatus, that not only provides highly purified water, but also improves the quality of the ambient air from which the water is being extracted prior to returning the air to the surrounding environment.
For this purpose, the present invention comprises an integrated arrangement of a water extraction stage, a water collection, chemical addition, storage/reservoir stage, and a water filtration sterilization and delivery stage. The entirety of the air and water processing paths through the integrated multistage system is sealed from the surrounding environment, so as to prevent entry of contaminants into any part of the system and thereby ensure purity of the water. This sealed configuration of the water extraction, purification, storage, filtration, sterilization, and delivery components of the present invention enables the invention to be utilized in substantially any environment, including those
containing substantial amounts of industrial, agricultural, biological, chemical, and other forms of pollutants.
The water extraction stage is operative to draw in and filter ambient air, and then extract water vapor from the ambient air. Once the drawn-in ambient air has been dehumidified by the water extraction process, the dehumidified filtered air is returned to the environment.
The water extraction stage resides in a sealed housing, so as to prevent leaks between the external ambient and the interior of the entire water extraction subsystem contained therein. This effectively eliminates any chance of unfiltered air or other contaminants from entering components of the water extraction stage , as well as downstream water collecting, chemical addition, storage, purification, and delivery subsystems.
By means of a forced air unit, ambient air is drawn through an air inlet port to an intake air filter section that includes an active, small particle (electrostatic) filter. This filter serves to filter the intake air of all dust, mold, animal dander, or any unwanted air-borne particles. The filtered intake air is then drawn through a water extraction (evaporation and condensation) section, which contains an evaporator and condenser coil arrangement, that condenses water from water vapor in the filtered intake air, prior to the air being returned to the surrounding environment. An optional deicing heater element or an automatic hot-gas defrost to prevent freezing of the evaporator coils when the unit is operating in temperatures below sixty-five degrees Fahrenheit, can be provided. The forced air unit is controlled in accordance with the output of a high level sensor, sensing the water level in the collection tank of the water collection stage. The forced air unit is activated (draws air into the system), as long as the high water level sensor element detects that the water within the storage tank is
below a prescribed "high" level (i.e. , the water storage tank is less than a predetermined level). As condensed water is collected, it is channeled through a water collection conduit to the water storage tank. When the water level sensor detects that the storage tank is full, the various powered components of the water extraction section are turned off.
The water storage stage includes a chemical treatment or disinfectant capability to treat stored water that has been condensed out of the filtered ambient air by the water extraction stage. The water filtration stage comprises a water filtration section installed in the water flow path between the water extraction stage and the storage tank. The water filter filters out, that is, absorbs or blocks, substantially all particulate, as well as dissolved chemicals and biological contaminants that may be in the condensed water.
Alternate filters may be provided to effectively adjust the pH of the water and remove particles of sediment, rust, dirt, and sand; absorb halogens and other contaminants, eliminating industrial and agricultural residual chemical compounds, as well as herbicides, pesticides, industrial and commercial cleaners and other Trihalomethanes (THMs).
As water is filtered by the filtration section, it flows by gravity into the storage tank. Electrical power for operating the water extraction system of the present invention may be derived from any conventional AC source. In addition, auxiliary power may be supplied by a number of sources, including a commercially available twelve volt direct current wind-driven generator, and a commercially available twelve volt direct current photoelectric solar array, connected via a switch to a twelve volt direct current storage battery. Also, an auxiliary emergency battery back-up trickle charge circuit may be coupled with
the switch to selectively provide a trickle charge to the battery. The trickle charger keeps the direct current storage battery fully charged, so that the battery can be used to power the extraction stage via the direct current-to-alternating current converter. The storage battery can be maintained fully charged, so as to enable the water extraction stage to be operated without conventional power for a limited period.
The above and other objects, features and advantages of the present invention should become even more readily apparent to those skilled in the art upon a reading of the following detailed description in conjunction with the drawings wherein there is shown and described illustrative embodiments of the invention.
Brief Description of the Drawings In the following detailed description, reference will be made to the attached drawings in which:
FIG. 1 is a diagrammatic view of the functional architecture of a sealed, purified water supply apparatus in accordance with an embodiment of the present invention;
FIG. 2 shows the details of the water extraction stage 100 of the apparatus of FIG. 1;
FIG. 3 shows the details of the optional multistage water filtration and delivery stage of the apparatus of FIG. 1; and
FIG. 4 is a diagrammatic view of sources of optional electrical power supply for operating the purified water supply apparatus of the present invention.
Detailed Description of the Preferred Embodiment For purposes of describing the preferred embodiment, the terminology used in reference to the numbered components in the drawings is as follows:
100. water extraction stage 310. multistage water filtration
101. sealed housing section
103. air inlet port 312. flow meter
104. condensing coil 320. valve
110. intake air filter section 321. pH adjustment filter
120. water evaporation and 323. carbon block filter condensation section 334. output valve
122. primary refrigeration 340. purified water delivery evaporator coil section
123. compressor unit 350. delivery section
124. fan assembly 372. water heater
124H . de-icing heater element 373. water cooler
130. exhaust section 375. chilled water supply
200. water storage stage 380. ultra violet light
204. water level sensor 390. carbonation tank
220. water storage tank 391. mixing valve
222. filter 392. beverage dispenser
224. biological treatment 401. direct current wind-driven
225. water flow pump generator
226. hand pump 403. direct current
227. gravity drain faucet photoelectric solar array
300. water filtration and 407. switch delivery 410. direct current storage stage battery
411. trickle charger
412. DC-AC converter
An embodiment of the purified water supply apparatus of the present invention will now be described with reference to FIGS. 1-4. The overall functional architecture of the invention is shown in FIG. 1, while FIGS. 2 through 4 illustrate the manner in which the components of the respective air and water processing stages of FIG. 1 are interconnected within a relatively space efficient structure, that is portable. When the optional multistage water filtration and delivery stage is added and the components are mounted within a cabinet, it shall be fitted with casters.
The present invention comprises essentially three stages, a sealed, integrated arrangement of a water extraction stage 100, a water storage stage 200, and a water filtration and delivery stage 300. The water extraction stage 100 (shown in detail in FIG. 2) is operative to draw in ambient air, and extract therefrom water vapor present in the air. The air flow path through the intake air filter section 110 is relatively "upstream" of a water evaporation and condensation section 120. Once the drawn-in ambient air is filtered and dehumidified in the water extraction stage it is then returned to the surrounding environment through an exhaust section 130. The water storage stage 200 includes a storage tank 220, coupled to the water extraction stage 100 through a filter 222 and covered, so as to prevent entry of any contaminants into the collected water flow path to the water storage tank 220, which stores water that has been extracted or condensed out of the filtered ambient air by the water evaporation and condensation section 120 of the water extraction stage 100.
As water is introduced into the storage tank 220, it receives biological treatment 224 by means of an optional ozone light or ultra violet light to kill any biological contaminant that may be in the water in the storage tank 220. The storage tank water level sensor 204 controls the operation of the evaporation and condensing section 120 by, among other controls, turns the system ON for low level and OFF for high levels.
Referring now to FIG. 2, the water extraction stage 100 is shown contained in a sealed housing 101 and having an air inlet port 103 through which ambient air enters stage 100. Because the housing 101 is sealed, there are no leaks between the external ambient and the interior of the entire air intake, water extraction, and air exhaust sections contained therein. This sealing effectively
eliminates any chance of unfiltered air or other contaminants, such as unwanted foreign airborne, insects, mold spores, dust, dust mites, or animal/insect dander from entering the water extraction, water storage, and multistage, filtration, and delivery stage components. The air inlet port is in fluid communication with the intake air filter 110 installed in the air intake stream, through which all air entering the stage must pass. The intake air filter section 110 includes at least one intake air filter, such as an active electrostatic small particle filter 110 (as a non-limiting example). Such filters serve to filter the intake air of all dust, mold, or other unwanted airborne particles.
Coupled in the intake airflow path immediately downstream of the intake air filter 110 is the evaporation and condensation section 120. As described briefly above, the water evaporation and condensation section 120 contains at least one water extraction element that is operative to extract water vapor present in the intake air that has passed through the intake air filter 110 upstream thereof.
For this purpose, the upstream end of the water evaporation and condensation section 120, contains a first or primary refrigeration evaporator coil
122, which is supplied with refrigerant from a compressor unit 123. An optional downstream second evaporator coil or additional coils, in combination with a pair of condenser coils, may be used to perform a two~stage process of water extraction and cooling of the air being returned to the surrounding environment.
This first evaporator coil 122 condenses water vapor present in the filtered intake air as the air passes over the coil. This evaporator coil 122, and associated compressor units employed in the invention may comprise commercially available components. In order to prevent corrosion and extend the life of the evaporator coils, it is mandatory that the coils be externally coated by a dipping, spraying,
brushing application and/or molecular deposition using a corrosion resistant material for use in potable water systems, approved by NSF and certified to ANSI/NSF 61. An option in association with the primary evaporator coil 122 is a de-icing heater element 124H, upstream of the evaporator coil and/or an automatic hot-gas defrost, which is controllably operative to prevent freezing of the evaporator coil when the unit is operating in temperatures below sixty-five degrees Fahrenheit, may be provided.
Also installed in the water evaporation and condensation section 120, downstream of condensing coil 104 is a forced air unit/fan assembly 124, which is controllably operative to draw ambient air into the system. The operation of the fan assembly 124 is controlled in accordance with the output of a high/low level sensor of the water storage tank 220 of the water storage stage 200. In particular, the fan assembly 124 is activated to draw air into the system, as long as the water level sensor element detects that the quantity or volume of water within the storage tank 220 is below a prescribed "fuH" or "high" level. However, when the high level sensor detects that the storage tank 220 is full, the various powered components of the water extraction stage 100, including the compressor(s) of the evaporator 122 and condenser unit(s) 104 and the forced fan 124 are turned off (as a non-limiting example). As an option in the airflow path immediately downstream of the fan assembly 124, an arrangement of one or more evaporator and condenser coils may be installed, comprising respective primary and secondary coils over which the drawn-in and filtered intake air passes. These coils condense/extract water from the water vapor in the air flowing through the water extraction stage 100. The condensed water drips through a filter element 222 into a storage tank 220
attached to the sealed housing of water extraction stage 100 and is channeled into the water storage tank 220.
FIGS. 1 and 2 show the water filter 222 and storage tank 220. The filtered water in the storage tank 222 is biologically treated with an optional ozone or ultraviolet light or other biological treatment.
As pointed out above and shown in FIG. 1, water usage is monitored by a water level sensor unit 204. The water level sensor 204 is operative to control the operation of the components of the water extraction stage 100, described above, including its fan and compressor units, in accordance with the water level within the water collection tank 220. As long as the water collection tank 220 is below the set point, the water extraction stage 100 is operative to draw ambient air into the system, and causing water vapor in the intake air to be extracted, collected, and supplied to the water storage stage 200. However, when the water level sensor 204 detects a "full" tank condition, it shuts off driven components [compressor(s), fan unit(s)] of the water extraction stage 100.
An optional water flow pump 225 may be provided and controlled by an internal pressure switch which activates the pump on low discharge head and stops the pump when set pressure is obtained.
The flow pump 225 delivers water under pressure to remote locations and to the refrigeration for chilled water or to the ice cube maker, additional filtration may be provided at the output of the water flow control pump 225. As described below, through a series of progressively finer porosity filters, the multistage water filtration and delivery stage 300, effectively filters out (absorbs/blocks) substantially all particulate, chemical, and biological contaminants from the treated water as its being pumped from the storage tank 220 for delivery to one or more water outlet valves of an optional purified water delivery section 340.
More particularly, an optional multistage water filtration section 310 may be provided to include an optional pH adjustment filter 321, such as a calcite filter or a 10 micron sediment filter.
The next filter may be a resin bead, a demand-release ionized disinfectant filter or a 0.5 micron carbon block filter 322 that absorbs chemical components, such as halogens (e.g., chlorine, bromine, iodine) and other chemicals, including industrial and agricultural residual chemical compounds, to improve taste, smell, and quality of water.
The final filter element of the multistage filtration section is a 0.5 or a 5.0 micron carbon block filter 323 installed downstream of the 0.5 micron carbon block filter 322. This filter also filters out herbicides, pesticides, industrial and commercial cleaners and other Trihalomethanes (THMs) . The carbon block filter 323 may also contain an ultra violet light to kill viruses and bacteria which may be in the water. This and other different combinations of filters at filter locations 321, 322, and 323 may be used to suit the user.
As water is pumped through the multistage filtration section 310, it is monitored via a flow meter 312, installed in the water flow path. Flow meter 312 prevents the flow of water through the water flow path to the purified water delivery section 340, when the system has reached a maximum gallon usage
(e.g. , 1200/1500 gallons), and the water filters require replacement.
As water is pumped through the multistage filtration section 310 it is supplied directly to the purified water delivery section 340, which provides the purified water on demand by way of output valves of a multi-tap water dispensing system. As described above, and as diagrammatically illustrated in FIG. 3, the purified water delivery section 340 is configured not only to directly deliver
purified room temperature water as filtered by the multistage filtration section 310, but contains a plurality of purified water conduits, that are respectively coupled to a water heater 372, a water cooler 373, a direct feed room temperature output valve 334, and a supply valve to the refrigerator ice maker and/or chilled water supply 375. In addition, it may be coupled to a flavoring additive supply tank which stores a flavoring additive, such as a flavored soft drink syrup and a carbonation tank 390. A mixing valve 391 thus allows the water to be mixed with additives (e.g., flavoring and/or carbonation), as desired to be delivered from a beverage dispenser 392 through a valve 320. The demand for water is sensed by operation of one of the water output valves of the multi-tap water dispensing system. This causes a reduction in the water pressure in the water flow path, which is sensed by a low pressure sensor in the pressure demand pump 225, activating the water pump 225, causing the water pump 225 to pump water through the multistage filtration section 310 to the purified water delivery section 340.
As described above, electrical power for operating the water extraction and purification system of the present invention may be derived from any conventional AC source, such as 110 VAC, 60 Hz, 230 VAC, 60 Hz, or 208 VAC, 50 Hz. In addition, as diagrammatically illustrated in FIG. 4, optional auxiliary emergency power for operating subsystem water supply components may be supplied by a number of sources. These sources include a commercially available 12 volt direct current wind-driven generator 401, and a commercially available 12 volt direct current photoelectric solar array 403, which are connected via external connection terminals and a switch 407 to a 12 volt direct current storage battery 410.
A DC-AC converter 412 is coupled to storage battery 410 for supplying emergency 110 VAC power or an optional voltage and frequency. An auxiliary emergency (power outage) battery back-up trickle charge circuit 411 may also be coupled in the circuit with the switch 407, to selectively provide a trickle charge to the battery 410. The trickle charger 411 keeps the 12 volt direct current storage battery 410 fully charged. Storage battery 410 maintains a full charge, so as to enable the water pump associated with the output taps of the water dispenser, to be operated, without conventional power. Thus, in the event of a power outage, the auxiliary power supply will at least power those components that will allow the user to be supplied with whatever water is in the water storage tank 220.
Units without the optional pressure demand flow pump 225 and multistage water filtration and delivery stage 300 are provided with a gravity drain faucet 227 on the storage tank 220 and/or an optional hand pump 226 to deliver pure water for consumption, as shown in FIGS. 1 and 2.
As will be appreciated from the foregoing description, the present invention provides a relatively compact, integrated and sealed purified water supply apparatus that is not only operative to extract, store, and purify water from water vapor in ambient air, but prevents entry of contaminants in the surrounding atmosphere from entering the system. The ambient air intake filtering section employs an active electrostatic filter which reduces airborne contaminants prior to extracting water from the air assuring water purity. Thus, when the filtered air is exhausted to the surrounding atmosphere it improves the air quality as well. The optional multistage water and delivery filtration section 310, provides superior water purification, eliminating ninety-nine percent of bacteria, viruses
and other microorganisms, ninety-seven percent of industrial and agricultural chemicals, and ninety-nine percent of herbicides, pesticides, solvents and other Trihalomethanes (THMs). In addition, the ultra violet light 380 is destructive to bacteria, mold, and viruses that may be in the water after filtration. This highly purified water is available to the user in a variety of optional modes by way of the purified water delivery section 340, and the optional delivery section 350.
Results of analysis of water extracted and purified by the present invention have shown a remarkable purity of the water, which is understood to far exceed requirements of the U.S. Environmental Protection Agency (EPA). Indeed, tests have shown that purified water provided by the extraction, treatment and filtration system of the present invention is free of ninety-nine percent (99%) of all bacteria, viruses and other microorganisms, herbicides, pesticides, industrial and commercial cleaners and other Trihalomethanes (THMs), and ninety-seven percent (97%) of chemical contaminants, including industrial and agricultural residual chemical compounds.
While we have shown and described an embodiment in accordance with the present invention, it is to be understood that the same is not limited thereto but is susceptible to numerous changes and modifications as are known to a person skilled in the art, and we therefore do not wish to be limited to the details shown and described herein, but intend to cover all such changes and modifications as are obvious to one of ordinary skill in the art.