Abstract:
The present invention relates to a portable water and climatic production system (“PH 2 OCP”). In the preferred embodiment, the system utilizes a desiccant rotor wheel to capture water vapor. The desiccant rotor wheel then rotates through a microwave heating chamber to release the water therefrom and heat the airflow as it rehydrates with the water released from the rotor wheel. The heated, moistened airflow then passes through a cooling and condensation system to create air conditioned airflow and water. The “PH 2 OCP” system is designed to operate and produce water in a wide range of global climatic conditions, including the most arid of environments. This is made possible due to the highly effective performance capabilities of the desiccant rotor technology in the extraction of water vapor molecules from any existing ambient air. The desiccant technology is designed to operate in combination with the microwave reactivation system in the regeneration or reactivation section and cooling coils assembly located in the condensation section.

Description:
CROSS-REFERENCE TO RELATED APPLICATION 
       [0001]    This non-provisional utility application is a continuation-in-part of U.S. patent application Ser. No. 12/923,154, titled PH2OCP—PORTABLE WATER AND CLIMATIC PRODUCTION SYSTEM, and is a continuation-in part of U.S. patent application Ser. No. 12/801,292, titled MICROWAVE REACTIVATION SYSTEM FOR STANDARD AND EXPLOSION-PROOF DEHUMIDIFICATION SYSTEM. This application incorporates by reference all of the disclosures therein. 
     
    
     BACKGROUND OF THE INVENTION 
       [0002]    The existence of moisture and humidity in all matter that surrounds us, in the air we breathe and in our environment play an integral part in promoting the essence of life. These same elements stem from the very source of all life which is water and of which in recent years has become extremely important and critical to properly manage, maintain and protect. This vital resource is becoming a priceless commodity due to the ever increasing global demands and population requirements for reusable, clean and potable water. 
         [0003]    In recent years, several water production technological processes and techniques have been designed and developed to address these ever increasing global requirements. Some of the water production conventional hybrid systems presently on the market operate primarily by using heating and expanding the air&#39;s capability to absorb and retain moisture and then subsequently by cooling the air temperature below its dew point which condenses the suspended moisture into water droplets. Alternately, technologies have emerged such as water desalination systems which have been developed to process ocean salt water into potable water. Though effective, this technological solution has also proven to be costly both on the transformation and production of potable water as well as the high cost of system purchase and maintenance. 
         [0004]    In addition, technologies such as water decontamination and filtration systems have also been developed as potable water production systems by removing harmful particles and bacteria in various non potable water sources. Whether these type systems deliver sanitized water or are limited in their processing and production capabilities, nevertheless, they still require a water source which may not always be existent and or available for use, in order to deliver decontaminated filtered water. 
         [0005]    The (PH2OCP) Portable Water and Climatic Production system is a new and innovative technology which operates on a completely different premise which is that of differential moisture vapor concentration, vapor pressures and water vapor extraction. 
         [0006]    All matter, substances including the ambient air and the environment hold moisture and water vapors that can be extracted. 
         [0007]    The greater the dampness and humidity in the air, the greater the water vapor concentration. The PH2OCP system is designed and incorporates a desiccant rotor/wheel with three simultaneously operational yet segregated processes; an extraction process, a reactivation process and a condensation process. 
         [0008]    The (PH2OCP) Portable Water and Climatic Production system combines high static and air velocity, a desiccant material for aggressive extraction of water vapors within the airstream, heat for air expansion and reactivation of the desiccant material and finally cooling for moisture vapor condensation and water production. In the preferred embodiment, the system is designed and can also be fitted and operated with a filtration and ultraviolet decontamination package to ensure that the resultant is free from particles and sanitized which then can be used as potable water. The operating principle of this system is that it incorporates a dry desiccant rotor/wheel constructed of a desiccant core material part of the extraction process. In the preferred embodiment, the core of the desiccant rotor/wheel is impregnated with silica gel which has a very low water vapor pressure. When damp humid high vapor pressure air molecules come in contact with the desiccant rotor/wheel surface low vapor pressure, the molecules move from high to low in an attempt to achieve equilibrium. As the wet damp airflow passes through the perforated desiccant material core in the desiccant rotor/wheel, the water vapor molecules are retained by the desiccant material part of the extraction process and the resulting discharge airflow is expelled extremely dry. 
         [0009]    The dry airflow temperature is then raised substantially approximately 200 to 250 degrees F. as it is pulled through the superheated microwave reactivation system coils assembly part of the reactivation process. The dry airflow is drawn coming in contact again with the moisture laden desiccant core material within the desiccant rotor/wheel. This desiccant rotor/wheel rotates slowly about its longitudinal axis completing a full rotation approximately every 8-10 minutes. The heated airflow continues its path as it is pulled again through the segregated section of the perforated desiccant core material within the desiccant rotor/wheel. Heat as the effect of demagnetizing and deactivating the desiccant core material, enabling the desiccant material to release the accumulated water vapors into the heated dry airflow as it passes through. 
         [0010]    The airflow continues to be drawn through the final section passing through the evaporator cooling coils in the condensation process where the water vapors are immediately cooled down to liquefy the vapors which condense into water. This water drips into a base receptacle located directly below the evaporator cooling coils and flowing through the filtration and decontamination section settling by gravity into the sealed water reservoir at the base of the unit. Though various filtration, purification and decontamination systems can be adapted and installed, in the preferred embodiment, the filtration is accomplished by an activated carbon filter and the decontamination and purification of the water by using an ultraviolet light UV lamp assembly which is enclosed in a transparent protective sleeve 
         [0011]    The airflow which is now cooled and dry is expelled through the process outlet by means of a high static pressure blower which maintains and ensures the constant airflow through the various sections and processes. The exhausted air can then be used as a byproduct to provide supplemental climatic conditioning and environmental temperature control within an enclosed space or area. 
         [0012]    Depending on the ambient temperature and operational conditions, the PH2OCP system control panel assisted by signals transmitted from the onboard sensors including temperature, humidity and airflow, which are located in the unit&#39;s process inlet and outlet. These sensors provide data to the (PLC) programmable logic controller panel which monitors and controls the proper operation and modulation of the components and processes in order to provide the maximum extraction and production of water within the specific climatic environment. These operational settings are activated automatically or manually programmed into the (PLC) programmable logic controller panel according to the onsite climatic conditions in order for the PH2OCP system to attract and extract the maximum air moisture vapors and optimize on water production. Given that the PH2OCP system employs various combinations of processes operating alternately or simultaneously through the input of the (PLC) controller panel and sensors, this allows the system the capability to effectively continue extracting and condensing vapors into water even when the dew point air temperature drops below freezing. 
         [0013]    Therefore, the (PH2OCP) Portable Water and Climatic Production system performance capabilities is maintained whether it operates in damp or dry environments within colder or warmer temperatures. The PH2OCP performance capabilities are not hampered or even affected by temperature conditions and variations like other conventional systems. These operational limitations and drawbacks are usually associated with conventional cooling-based and or hybrid heating/cooling systems where the water production output is directly affected and limited by existing climatic conditions and variations. The PH2OCP system new design uses alternately or simultaneously its various components to effectively operate and produce water in all climatic and environmental conditions. Its wide range operational capabilities extract moisture vapors from the ambient air within the surrounding environment including hot arid or extremely cold climatic conditions. Therefore, the PH2OCP system is capable of maximizing extraction and transformation of airborne moisture vapors found in the atmosphere into usable and or drinkable water in all climatic environments, anywhere in the world. The high efficiency and water extraction and production capabilities of the PH2OCP system are rendered possible due to the fact that it incorporates in its process a desiccant rotor/wheel assembly. The desiccant material impregnated within the core of the desiccant rotor/wheel is designed for extremely high water vapor collection, attracting and retaining up to 10,000 percent its dry weight in water vapors. As previously explained, in order to demagnetize and deactivate the rotor desiccant material to enable it to release the stored water vapors, a high (heat) temperature rise in the airflow is absolutely required in the reactivation process in order to dry out the rotor desiccant material and extract the moisture vapors, which usually translates into high energy requirements. 
         [0014]    The generating of heat can be accomplished with the use of but not limited to the following systems; electric heating banks or elements, flame gas burners or submersible heater immersed in a fluid running through coils located in the airflow pathway that act in a way to radiate and transfer heat onto the reactivation process airflow. These methods are generally the most commonly used means to heat the desiccant material, so that the airflow temperature rises to a degree set point before coming in contact with the surface of the desiccant material. In the case of a conventional water production system where heating and or cooling processes are utilized separately or in combination such as a hybrid system. The role of the heating section is to raise the temperature and expand the air volume allowing it to hold more moisture. This airflow then goes through the refrigerant coils which rapidly cool down the airflow temperature enabling the extraction by condensation suspended moisture vapors. 
         [0015]    The PH2OCP system design addresses this heat production issue by incorporating a new and highly energy efficient microwave reactivation system which is installed in the reactivation process. In the preferred embodiment, the microwave reactivation system is designed and intended to be a high heat generating source. This high heat source is crucial and required in order to substantially raise the temperature of the reactivation process airflow to the desired setting prior to coming in contact with the moisture laden desiccant core material. This microwave reactivation system incorporated within the PH2OCP system produces heat by generating electromagnetic waves which pass through materials and fluids, causing the molecules within to rapidly oscillate in excitation and in turn generating heat. 
         [0016]    In the preferred embodiment, the medium used in the microwave reactivation system to store and transmit this heat is a thermal fluid. This fluid is moved by means of supply and return pumps, flowing through a first parallel series of glass ceramic coils which is part of a closed-loop circuit, passing through the microwave heating chamber where the fluid molecules are treated and exposed to electromagnetic waves causing excitation and generating high heat. This super heated thermal fluid then flows through a second parallel series of metallic coils located in the reactivation process, in the direct path of the airflow. This heat transfer from the thermal fluid to the heat conductive metallic coils substantially raises the temperature of the airflow as it comes in contact and passes across the surface of the coils. This heated airflow is then used to deactivate the perforated desiccant material which is impregnated within the desiccant rotor/wheel as it passes through it. This heat laden airflow has a demagnetizing effect on the desiccant material enabling it to release the retained accumulated moisture vapors and thus greatly lowering the vapor pressure in the desiccant material within the desiccant rotor/wheel as it rotates back for reuse in the moisture vapor extraction process. It will be appreciated that while the microwave reaction system would be part of the preferred embodiment, nevertheless, other means of conventional heating outlined but not limited to, such as; electrical heating elements, submersible heating element immersed in a thermal fluid, gas fired or others can be utilized and incorporated in the reaction process section. Therefore, the (PH2OCP) Portable Water and Climatic Production system can extract transform and produce usable and or potable water in all climatic conditions whatever the operational environment. 
         [0017]    In addition, its new highly efficient systems and processes substantially diminish the electrical power demand and energy consumption without compromising on system capability and performance, surpassing all technologies presently used on the market. 
       BRIEF SUMMARY OF THE INVENTION 
       [0018]    According to the broad aspect of an embodiment of the present invention, there is provided a (PH2OCP) Portable Water and Climatic Production system which is designed to extract water vapors from the ambient environment and transformation of these water vapors into usable water. The (PH2OCP) Portable Water and Climatic Production system accomplishes this task by incorporating in its design a desiccant rotor/wheel with three segregated processes; an extraction process, a reactivation process and a condensation process. The PH2OCP also provides as a byproduct air conditioning and dehumidifying capabilities of its airflow discharge from the process outlet, for conditioning of an enclosed area or space. The (PH2OCP) Portable Water and Climatic Production system has a desiccant rotor/wheel assembly which is mounted and rotates within a cabinet made up of three separate isolated sections called processes; extraction process, reactivation process and condensation process. The desiccant rotor/wheels&#39; perforated core is impregnated with a desiccant type material which has the capability of capturing and retaining water vapors found in the ambient air and environment. The first section called the extraction process is intended as the collection and retention of the moisture/water vapors found in the ambient airflow. 
         [0019]    A high static blower located in the process outlet is provided to draw the airflow at high velocity into the process inlet and through the desiccant rotor/wheel, where the desiccant material collects and retains the moisture vapors. The resultant dry airflow is drawn into the second section called the reactivation process. In the reactivation process, this airflow comes in contact and is heated by a microwave reactivation system which is comprised of a microwave heating chamber and two segregated series of hollow serpentine coils which have an internal heated thermal fluid which flows through them. These coil assemblies though segregated are interconnected by means of two circulation pumps as part of a closed-loop circuit. One glass-ceramic coil assembly is constructed within the microwave heating chamber separately located above the reactivation process section and the other metallic coil assembly is constructed in the reactivation process directly in the pathway of the dry airflow. 
         [0020]    The thermal fluid is super heated as it is pumped through the glass-ceramic coil assembly in the microwave reactivation chamber and into the metallic coil assembly in the reactivation process section. The high heat radiated from the thermal fluid pumped in the reactivation process metallic coil assembly is transferred onto the dry airflow, substantially raising the dry airflow temperature before coming in contact with the desiccant rotor/wheel core surface. As the super heated dry airflow is drawn through the system passing through the desiccant rotor/wheel and perforated core material, this heated dry airflow effectively deactivates the moisture laden desiccant core material, enabling it to release the moisture vapors into the airflow. 
         [0021]    This moisture saturated airflow is then drawn, leaving the desiccant rotor/wheel core material and transporting the water vapors through the third section which is called the condensation process. In the condensation process section, the high temperature wet airflow transporting the water vapors passes through an evaporator cooling coil assembly part of the unit&#39;s air-conditioning components. The wet airflow temperature is rapidly cooled and as a resultant producing condensate or water. This water is gravity fed to a receptacle which directs it to a unit reservoir located at the base of the system. In the preferred embodiment, the water is directed through an active carbon filter and ultraviolet UV decontamination package which is located right below the evaporator cooling coils in the condensation process section. This would ensure that any existing contaminants, particles and bacteria have been removed and destroyed in order to provide the resultant which is sanitized, clean and potable water. The treated and conditioned dry airflow which is void of water vapors is then drawn through the high static blower located in the process outlet, discharging it to the ambient atmosphere. This treated airflow is a byproduct which can be then used for conditioning of an enclosure or space. Therefore, the (PH2OCP) Portable Water and Climatic Production system perpetual process allows for continuous water production in all temperatures whatever the climatic conditions in which the system operates. The following is a brief description of the two distinct sub-systems operating in conjunction with the desiccant rotor/wheel assembly and incorporated within the PH2OCP system. The first is the microwave reactivation system part of the reactivation process and the second is the air treatment and conditioning system part of the condensation process. 
         [0022]    These systems are both constructed and incorporated as part of the (PH2OCP) Portable Water and Climatic Production system design. The first sub-system is the microwave reactivation system part of the reactivation process. The microwave heating chamber is made up of an explosion-proof outer cabinet with an inner casing which includes a cavity with inner surfaces thereof forming a microwave heating chamber. A shielding plate forming a compartment located above the microwave heating chamber is to provide housing for the microwave power transformation components therein, such as; magnetron, high voltage transformer, diode, capacitor and other operational components. 
         [0023]    In the preferred embodiment, the microwave reactivation system is comprised of two separate coil assemblies combined as part of a single closed-loop circuit. They are mounted and firmly secured in place by using a series of shock resistant mounting brackets. There is a glass-ceramic coil assembly which is mounted in the microwave heating chamber and a metallic coil assembly which is mounted in the reactivation process section. These coil assemblies are firmly linked at two opposite points by means of fittings and seals which are securely connected to separate pumps, one for supply and the other for return. The pumps ensure a steady and continuous heated thermal fluid flow from the microwave section to the reactivation section and back again. These pumps are oppositely located in a shielding plate forming a compartment in between the microwave heating chamber and the reactivation process section. This closed-loop circuit passes through both the microwave heating chamber and the reactivation process section of the PH2OCP system. 
         [0024]    The hollow coil is constructed of one length and designed as a closed loop line, in which flows a thermal fluid, such as a; thermal oil or heater liquid, used to carry thermal energy. The thermal fluid is continuously heated within the microwave heating chamber as it is pumped and circulating through transferring the accumulated thermal energy/heat to the coils which radiate onto the airflow as it passes through the reactivation process section. The uninterrupted flow of the thermal fluid is ensured by the installation and operation of two pumps within the microwave reactivation system assembly. This ensures the circulation of the heated thermal fluid from the microwave heating chamber located in onto the reactivation process section and back again in a continuous perpetual process. This microwave reactivation system therefore generates the heat source and enables the proper airflow temperature rise which is required to successfully deactivate the desiccant core material found in the desiccant rotor/wheel assembly. This enables the release of the accumulated moisture/water vapors into the airflow being discharged to the ambient atmosphere. The enormous benefits of the microwave reactivation system is that it performs its primary function of providing a reactivation process heat source, while greatly reducing the energy requirement for heat generation and overall power consumption of the (PH2OCP) Portable Water and Climatic Production system. This important energy savings allow for the PH2OCP system to be more operationally viable specifically in areas which would have been previously unserviceable due to power supply limitations. The high energy requirements usually associated with the use of desiccant technology like the one incorporated in the PH2OCP system design is eliminated with the adaption of this microwave reactivation system. 
         [0025]    Present sources of heat generation usually installed and utilized in desiccant reactivation systems such as; electric elements and electric heating banks, account for the major share of operating energy of a desiccant or conventional HVAC heating/cooling system. Because of the greatly reduced electrical power requirements needed to operate the microwave reactivation system, it therefore allows the PH2OCP system to be operated at optimum performance in environments and applications even found onshore, offshore, marine and military, where power availability may be limited and or utilized for other critical operational requirements. In the preferred embodiment, the cabinet of the microwave heating chamber part of the microwave reactivation system is of explosion-proof construction. 
         [0026]    The second sub-system in the PH2OCP system is the air treatment and conditioning system part of the condensation process. In the preferred embodiment, the air treatment and conditioning system is constructed with the same components and configuration as a split air-conditioning unit. The system design includes a compressor, condenser coil assembly and fan, an expansion valve or refrigerant flow metering device, an evaporator cooling coil assembly and blower, a chemical refrigerant and an automatic temperature sensors which are installed in the condenser unit, the condensation process outlet and linked to the (PLC) programmable logic controller panel. The compressor acts as the pump, circulating the refrigerant through the system. Its job is to draw in a low-pressure, low-temperature, refrigerant in a gaseous state and by compressing this gas, raise the pressure and temperature of the refrigerant. This high-pressure, high-temperature gas then flows to the condenser coil assembly. 
         [0027]    The condenser coil assembly is a series of fined coils/piping with a fan that draws outside air across the coil assembly. As the refrigerant passes through the condenser coil assembly and the outside air passes across the coil fins, the heat from the refrigerant is rejected to the outside air which causes the refrigerant to condense from a gas to a liquid state. The high-pressure, high-temperature liquid then reaches the refrigerant flow metering device. The refrigerant flow metering device is the manager of the system and directed by input from the PLC controller panel. By sensing the temperature &amp;/or pressure of the evaporator cooling coils located in the condensation process section, it allows liquid refrigerant to pass through a very small orifice, which causes the refrigerant to expand to a low-pressure, low-temperature gas. This cold refrigerant flows to the evaporator. The evaporator cooling coils is a series of fined coils/tubes aided by a high static blower that draws the condensation process airflow across it, causing the evaporator cooling coils to absorb heat from the air. This heat transfer allows for rapid temperature drop, cooling the wet hot airflow which induces condensation of the moisture vapors into water. The byproduct is cooled and conditioned dry air which is siphoned into the high static blower and discharged to the enclosures and or areas to be air-conditioned. The refrigerant then flows back to the compressor where the cycle resumes once again. 
         [0028]    These new and advanced sub-systems in conjunction with the desiccant technology provide the (PH2OCP) Portable Water and Climatic Production system design with enormous operational versatility, increased efficiency, drastically reduced energy consumption and unmatched performance capabilities in water production. 
         [0029]    As an alternative, a modified reactivation process may be utilized in which the reactivation process includes a microwave reactivation system having a microwave heating chamber through which the desiccant rotor wheel rotates. As the desiccant rotor wheel rotates through the microwave heating chamber, the desiccant material in the rotor wheel is heated and deactivated, thereby releasing the moisture contained therein back into the airflow. Such a design eliminates the need for reactivation heating coils and internal heated thermal fluid which flows therethrough. 
         [0030]    Such an embodiment would allow for volumetric heating. The wave penetration into various materials has huge positive consequences in many applications. This volumetric heating gives rise to a very rapid energy transfer into the material being heated. In conventional heating, heat flow is initiated on the material&#39;s surface and the rate of heat flow into the centre is dependant on the material&#39;s thermal properties and the temperature differential. A conventional oven is required to be heated to temperatures much higher than is required by the material itself since there is asymptotical rise in workload temperature towards the required level. 
         [0031]    Thus, an energy savings of up to 70% may be achieved. The rapid heating of the workload (along with the fact that in a properly designed applicator the majority of the available energy is dissipated in the workload) causes lower temperatures associated with the cavity surroundings. Thus, radiation, conduction and convection heat losses are reduced. This can represent energy savings of up to 70%. It could also reduce equipment size (potentially down to 20%). 
         [0032]    This structure would also provide instantaneous control, as power can be controlled instantly giving better control of process parameters, rapid start-up and shut down. 
         [0033]    Further, a material&#39;s ability to be heated by electromagnetic energy is dependant on its dielectric properties. Therefore, in a mixture containing a number of differing constituents, the heating of each will vary. This can have profound positive consequences on energy usage, bulk reaction temperatures, moisture removal and process simplification, when selective heating occurs. 
         [0034]    Additionally, as the energy transfer mechanism from electromagnetic to thermal energy is a function of a material&#39;s electrical properties, a continuous dumping of energy into some materials is possible. Provided that heat losses can be controlled, very high material temperatures can be achieved with simple and relatively low power microwave generators. 
         [0035]    Further, the electromagnetic nature of microwaves means that energy transfer to a material is usually via some form of polarisation effect within the material itself. This direct transfer of energy eliminates many of the problems associated with organic fuel usage for the end user. 
         [0036]    Finally, many chemical reactions can be accelerated using microwaves. Solvent free reactions are gaining popularity in many labs, thus reducing problems associated with waste disposal of solvents and other hazardous chemicals. 
     
    
     
       BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING 
         [0037]    The embodiments of the present invention shall be more clearly understood by making reference to the following detailed description of the embodiments of the invention taken in conjunction with the following accompanying drawings which are described as follows: 
           [0038]      FIG. 1  is the schematic diagrams&#39; elevation and prospective views of the (PH2OCP) Portable Water and Climatic Production system according to the preferred embodiment of the invention. These corresponding views are enlarged and shown on the FIGS.  3 - 7 - 8  and  9 . 
           [0039]      FIG. 2  is a schematic diagram sectional view of the (PH2OCP) Portable Water and 
           [0040]    Climatic Production system processes such as the; extraction, reactivation and condensation shown in  FIGS. 4 ,  5 , and  6 . The view depicts the typical air flow movement drawn by the high static blower through the desiccant rotor/wheel during operation with the electric drive motor provided for the rotation of the desiccant rotor/wheel (not to scale). This will also be identified as the Front Page View. 
           [0041]      FIG. 3  is a schematic diagram elevation view of the (PH2OCP) Portable Water and Climatic Production system shown in  FIG. 1 . 
           [0042]      FIG. 4  is a schematic diagram full sectional view of the (PH2OCP) Portable Water and Climatic Production system cabinet shown in  FIGS. 1 and 3  with the various operational sections and processes exposed; extraction process, desiccant rotor/wheel assembly, reactivation process including the microwave reactivation system and finally the condensation process which includes the air treatment and conditioning system (not to scale). 
           [0043]      FIG. 5  is a schematic diagram sectional view of the PH2OCP system&#39;s sub-system identified as the microwave reactivation system and the closed-loop coil assemblies&#39; construction. The microwave heating chamber coil assembly is connected via two oppositely located thermal fluid circulation pumps to the reactivation process coil assembly shown also in  FIGS. 4 and 6 , along with some of the major operational components such as; capacitor, diode, high voltage transformer, magnetron, stirrer blades and wave guide (not to scale). 
           [0044]      FIG. 6  is a schematic diagram sectional view of the PH2OCP system&#39;s sub-system identified as the air treatment and conditioning system. The construction is of a split type assembly where the compressor, condenser coils including metering device and valves are mounted above the extraction process section and the evaporator cooling coils are mounted below in the condensation process section, both linked by refrigerant gas piping, shown in  FIG. 4 . 
           [0045]      FIG. 7  is a schematic diagram elevation view of the airflow process inlet and outlet side including the high static direct drive axial type blower, shown in  FIG. 1 . 
           [0046]      FIG. 8  is a schematic diagram perspective view shown in  FIG. 1 . 
           [0047]      FIG. 9  is a schematic diagram perspective view shown in  FIG. 1   
           [0048]      FIG. 10A  is a perspective view of an alternative embodiment of the reactivation portion of the PH2OCP system in which the rotor wheel rotates through a microwave heating chamber. 
           [0049]      FIG. 10B  is a front elevation view of the alternative reactivation portion of the PH2OCP system of  FIG. 10A . 
           [0050]      FIG. 11  is a schematic diagram sectional view of the PH2OCP system processes in which the alternative reactivation portion shown in  FIGS. 10A and 10B  is installed. 
       
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
       [0051]    The description which follows and the embodiments described therein are provided by way if illustration of an example, or examples of particular embodiments of principles and aspects of the present invention. These examples are provided for the purpose of explanation and not of limitation, of those principles of the invention. 
         [0052]    In the description that follows, like parts are marked throughout the specification and the drawings with the same respective reference numerals. 
         [0053]    With regards to the nomenclature, the term “PH2OCP” as it is used throughout the specification identifies the Portable Water and Climatic Production system  FIGS. 3 ,  4 ,  7 ,  8 ,  9 , which will be designated generally with reference numeral  72   FIG. 1 . The PH2OCP system herein includes various components and main sub-systems such as; desiccant rotor or wheel technology, microwave reactivation system, the air treatment and conditioning system as well as all parts, modules and electrical components. Referring to  FIGS. 3 ,  4 ,  7 ,  8 ,  9 , there are shown the PH2OCP system views illustrated on unit views  1 ,  2 ,  3  and  4   FIG. 1  as; elevation, sectional and perspective or isometric. 
         [0054]    As will be explained in greater detail below, that the PH2OCP system through its processes such as; extraction, reactivation and condensation is operable and capable to extract moisture vapors from the ambient air and transform these same vapors into a usable water source. 
         [0055]    The PH2OCP system as illustrated on  FIG. 1  unit views  1 ,  2 ,  3  and  4 , due to its new and advanced engineering design, this system can be installed and operated in any and all climatic environments to successfully produce usable water. In the preferred embodiment, the PH2OCP operational design incorporates the desiccant rotor technology coupled with two distinct subsystems; microwave reactivation system part of the reactivation process and air treatment and conditioning system part of the condensation process. In the preferred embodiment, the PH2OCP system  72  can also be fitted with components which enable water sanitization, ensuring that the resultant is clean decontaminated potable water. This water sanitization process is accomplished by incorporating the following components; an active carbon filter or layered filters and an ultraviolet (UV) lamps assembly which are both installed and located right below the evaporator cooling coils in the condensation process section. This water sanitization process enables water purification and decontamination which ensures that any existing particles, contaminants and bacteria have been removed and or destroyed in order to provide the resultant which is filtered, sanitized and drinkable potable water. The (PH2OCP) Potable Water and Climatic Production system operational design delivers enormous versatility and adaptability enabling the system to function efficiently at peak performance for continuous water production capability within all climatic conditions and environments. 
         [0056]    As it will be explained below in greater detail, the PH2OCP system  FIG. 1  unit views  1 ,  2 ,  3 , and  4 , is supported and mounted inside a rectangular box-like, rigid steel frame  18   FIGS. 3 ,  4 ,  7 ,  8 ,  9 . 
         [0057]    This frame is constructed from several structural members assembled from top to bottom as; longitudinal beams  19   a    FIGS. 3 ,  8 ,  9 ,  19   b    FIGS. 8 ,  9 , longitudinal base beam  69   FIGS. 3 ,  7 ,  8 ,  9 , transversal beams  20 ,  21  and  22   FIGS. 3 ,  7 ,  8 ,  9 , vertical posts  23   FIGS. 3 ,  7 ,  8 ,  9 , and diagonal brace members  24   FIGS. 3 ,  8 ,  9 . 
         [0058]    The control and electrical section is also supported by; electrical panel and (PLC) programmable logistic controller, transversal beams  66   a,    FIGS. 7 ,  8  and  9 .  66   b    FIGS. 8 ,  9 , vertical posts  67   a    FIGS. 7 ,  8 ,  9 ,  67   b    FIG. 9 , longitudinal beams  68   a    FIGS. 3 ,  8 ,  9 ,  68   b    FIG. 3 , longitudinal base beams  69   a    FIGS. 3 ,  7 ,  9 ,  69   b    FIGS. 7 ,  8 , and transversal beams for PLC panel  71   a    FIGS. 7 ,  8 ,  9 , and  71   b    FIG. 9 . The frame  18   FIG. 3 ,  4 ,  7 ,  8 ,  9  also includes two base feet  25   FIGS. 3 ,  7 ,  8 ,  9 , located at both ends for positioning on a structural support surface as well as two sleeve channels  26   FIGS. 3 ,  8 ,  9 , located in the base center for fork lifting and four corner lifting points  27   FIGS. 3 ,  7 ,  8 ,  9 , located at the top corners of the frame for inserting the hooks of a sling assembly to enable manipulation and displacement on a roof, floor or platform. The PH2OCP system various operational mechanical components and sub-systems are enclosed and shielded within a rectangular shaped cabinet  31   FIGS. 3 ,  7 ,  8 ,  9 , with several access panels unit views  1 ,  2 ,  3 ,  4 ,  FIG. 1 and 33   a, b, c, d, e, f, g, h,    FIG. 3 , to enable penetration into the various system compartments for periodic verification and maintenance of PH2OCP system  72  components. The PH2OCP system  72  side walls as illustrated on unit views  3  and  4   FIG. 1 and 33   a  to  h,    FIG. 3 , have duplicate access panels which are symmetrical on both side walls. This allows for easier access and maintenance by enabling accessibility to the various operational compartments on either side of the cabinet  31 . 
         [0059]    In the preferred embodiment, the PH2OCP system  72  frame  18  and overall cabinet  31  are preferably constructed of stainless steel or aluminum in order for the metal surfaces to prevent rust accumulation, corrosion and deterioration even when used in abrasive environments, such as offshore marine applications or at sites located in proximity to salt laden ocean water. In an alternate but limited to the embodiment, an epoxy coated resistant steel frame  18  and cabinet  31  type construction may also be used. Therefore, the PH2OCP system  FIG. 1  unit views  1 ,  2 ,  3  and  4 , is well supported by this frame structure  18   FIGS. 3 ,  4 ,  7 ,  8 ,  9  benefits from enhanced and secured portability in all environments and locations. It can be transported and deployed with ease to various temporary or permanent work sites, remote locations and distant facilities which have limited or no accessibility to sources of water. 
         [0060]    As shown in  FIGS. 1 ,  3 ,  4 ,  7 ,  8  and  9  the frame  18  is open to thereby facilitate and enable access to the overall cabinet  31   FIG. 3 ,  7 ,  8 ,  9 , the control and electrical panels  28 ,  29 ,  63   FIG. 3 ,  4 ,  7 ,  8 ,  9 , of the PH2OCP system in order to verify the components and perform routine maintenance checks and repairs. However it must be understood that in an alternative embodiment, the entire frame  18  and cabinet  31 , could be covered with an outer shell or walls which would encapsulate and form an enclosure which would be designed and adapted to house the PH2OCP system as well as its operating components and sub-systems such as; desiccant rotor/wheel assembly, microwave reactivation system, air treatment and conditioning system as well as control and electrical panels as described and illustrated in  FIG. 1 to 9 . 
         [0061]    The construction of such an enclosure would definitely provide the PH2OCP system components with additional protection and limiting access for reasons of security dependent upon where the PH2OCP system may be required to operate. This enclosure (not shown) constructed and surrounding the PH2OCP system frame  18  and cabinet  31  would be designed for adaptation to the PH2OCP system functionality. To further elaborate on the use of this new technology; deployment and operation of the PH2OCP system  FIG. 1  unit views  1 ,  2 ,  3  and  4 , in any climatic or environmental conditions, will guarantee to provide maximum moisture vapor extraction for ultimate water production. 
         [0062]    In addition, by incorporating effective and efficient components and sub-systems in the PH2OCP system, such as; the desiccant rotor/wheel technology  7 , the microwave reactivation system  36  within the reactivation process  9   FIGS. 2 ,  4 ,  5 ,  6 , and the air treatment and conditioning system  61  within the condensation process  15   FIGS. 2 ,  4 ,  6 , allow for enormous reduction of electrical power requirement and consumption while using the desiccant rotor/wheel technology without compromising on the system&#39;s performance and capabilities of water production. This important addition of the microwave reactivation system  36  as part of the reactivation process  9 , enables the capabilities of substantial energy reduction and savings without compromising on the benefits and advantages of the PH2OCP system  72  to effectively transform moisture vapors into usable water, even in areas, applications and sites with power supply availability limitations. 
         [0063]    In reference to the PH2OCP system  72  internal construction  FIG. 2 ,  4 ,  5 ,  6 , demonstrate the processes, sub-systems and components of the PH2OCP system  72   FIG. 1 . There is included an extraction process section  6  with a desiccant rotor/wheel assembly  7 , a reactivation process section  9  with a microwave reactivation system  36  which incorporates a microwave heating chamber  35  and reactivation heating coils  34 . Finally there is a condensation process section  15  with an air treatment and conditioning system  61  split design incorporating the evaporator cooling coils assembly  14  which is linked to a compressor  59   FIGS. 4 ,  6 , condenser coil assembly,  58   FIGS. 4 ,  6 , exhaust fan and motor assembly  61   FIGS. 4 ,  6 ,  8 ,  9 , metering valve  64   FIGS. 4 ,  6 , and components (not shown). The PH2OCP system  72  process airflow  11   a, b, c  and  d    FIG. 2 , is maintained by means of a high static direct drive axial type blower and motor assembly  16   FIGS. 2 ,  4 ,  6 ,  7 , located at the process outlet  17   FIGS. 2 ,  3 ,  4 ,  6 ,  7  and  9 . 
         [0064]    The (PH2OCP) Portable Water and Climatic Production system  72  processes and operation will now be explained in greater detail. The ambient airflow  11   a    FIG. 2 ,  4 ,  6 , is drawn into the process inlet  5   FIG. 2 ,  3 ,  4 ,  6 ,  7 ,  9 , by means of a high static direct drive axial type blower and motor assembly  16   FIGS. 2 ,  4 ,  6  and  7 . This high static blower and motor assembly  16  is located in the process outlet  17   FIGS. 2 ,  3 ,  4 ,  6 ,  7 ,  9  and maintain both airflow pressure and velocity through the PH2OCP system  72 . The process airflow  11   a, b, c, d,    FIG. 2  is then drawn through the first section called the extraction process  6   FIG. 2 ,  4 ,  5 ,  6 , which is intended to perform the collection and retention of the moisture/water vapors found in the ambient air. 
         [0065]    The desiccant rotor/wheel assembly  7   FIG. 2 ,  4 ,  5 ,  6 , construction includes a desiccant core material  8   FIG. 2  impregnated with silica gel which collects and retains the moisture vapors. The resultant dry airflow  11   b    FIG. 2 ,  4 ,  5 ,  6 , is drawn into the second section called the reactivation process  9   FIGS. 2 ,  4 ,  5  and  6 . In the reactivation process  9 , this dry airflow comes in contact and is heated by the reactivation heating coils  10  part of the microwave reactivation system  36   FIGS. 2 ,  4 ,  5  and  6 . The microwave reactivation system  36  is comprised of a microwave heating chamber  35  and reactivation heating coils  10   FIGS. 2 ,  4 ,  5 ,  6  having each their segregated series of hollow serpentine coils assemblies  FIGS. 4 ,  5 ,  6 ; glass ceramic  34  and metallic  10 , having an internal heated thermal fluid (not shown) which flows through them. 
         [0066]    These coil assemblies  34  and  10   FIGS. 4 ,  5 ,  6 , though segregated are interconnected by means of two circulation pumps  43   FIG. 4 ,  5 ,  6 , as part of a closed-loop circuit. One glass-ceramic coils assembly  34   FIGS. 4 ,  5 ,  6 , is constructed and located separately within the microwave heating chamber  35   FIGS. 4 ,  5 ,  6 , above the reactivation process section  9   FIG. 2 ,  4 ,  5 ,  6 . The other metallic coils assembly  10   FIG. 2 ,  4 ,  5 ,  6 , is constructed and located in the reactivation process  9   FIG. 2 ,  4 ,  5 ,  6 , directly in the pathway of the dry airflow  11   b    FIGS. 2 ,  4 ,  5  and  6 . The thermal fluid (not shown) is super heated as it is pumped through the glass-ceramic coil assembly  34  in the microwave heating chamber  35  and into the metallic coil assembly  10  in the reactivation process section  9 . 
         [0067]    The high heat radiated from the thermal fluid (not shown) pumped in the reactivation process  9  metallic coils assembly  10  is transferred onto the dry airflow  11   b,  substantially raising the airflow temperature before coming in contact with the desiccant core material  8  within the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4  and  6 . 
         [0068]    As the super heated dry airflow  11   b  is drawn through the system passing through the desiccant rotor/wheel assembly  7  and perforated desiccant core material  8 , this airflow effectively deactivates the moisture laden desiccant core material  8 , enabling it to release all the moisture vapors back into the hot airflow  11   c    FIGS. 2 ,  4  and  6 . This moisture saturated hot airflow  11   c    FIGS. 2 ,  4 ,  6 , is then drawn, leaving the desiccant rotor/wheel  7  and core material  8   FIG. 2 ,  4 ,  6 , transporting the water vapors through the third section which is called the condensation process  15   FIGS. 2 ,  4  and  6 . In the condensation process section  15 , the moisture saturated hot airflow  11   c  transports the water vapors passing through an evaporator cooling coils assembly  14   FIGS. 2 ,  4 ,  6 , part of the air treatment and conditioning system  61   FIGS. 4 and 6 . The wet airflow temperature is rapidly cooled and as a resultant producing condensate which transforms into water  70   FIGS. 4 and 6 . This water  70  is gravity fed to a base funnel (not shown) located directly beneath the evaporative cooling coils assembly  14 , which directs the water stream downward towards the system reservoir  48   FIGS. 4 ,  6 , located at the base of the PH2OCP system  72 . In the preferred embodiment, the condensate which is transformed into water  70 , is directed through a water sanitization process which occurs directly beneath the condensation process section  15 . 
         [0069]    This water sanitization process incorporates an active carbon filter  39  and ultraviolet (UV) lamps assembly  40   FIGS. 4 ,  6 , for decontamination, located right below the evaporator cooling coils assembly  14  in the condensation process section  15   FIGS. 2 ,  4  and  6 . This would ensure that any existing contaminants, particles and bacteria have been removed and destroyed in order to provide the resultant which is sanitized, clean and potable water. In the preferred embodiment, the components such as the carbon filter  39  and ultraviolet UV lamps assembly  40   FIGS. 4 ,  6 , that make up the water sanitization process are accessible through one of the cabinet  31  access panel  33   f    FIG. 3 . These components are also replaceable, in order to upkeep and optimize on the PH2OCP systems&#39; water cleansing and purification capabilities when the resultant must be for use as potable water. In an alternative embodiment, other water cleansing filters may be used depending on the environmental requirements. 
         [0070]    In the preferred embodiment, a single or superimposed twin carbon filter  39  pack is installed coupled with a “High Output Germicidal UV” type lamps assembly  40  (not shown) incorporate industrial grade lamps and tubing construction. This high output germicidal (UV) ultraviolet lamps assembly  40  provides high (UV) ultraviolet output over a great temperature spectrum, it has a long operational life and excellent sterilization capabilities which are required for operation within the PH2OCP system  72 . This UV lamps assembly  40  is available in different sizes and may be operated either from a single transformer or in series through the medium of high voltage transformers. 
         [0071]    The treated and conditioned dry airflow  11   d  FIG.  2 #,  FIG. 2 ,  4 ,  6 , which is void of water vapors is then drawn through the high static direct drive axial blower  16   FIG. 2 ,  4 ,  6 ,  7 , located in the process outlet  17   FIG. 2 ,  3 ,  4 ,  6 ,  7 ,  9 , discharging it to the ambient atmosphere. This treated airflow  11   d  is a useful byproduct, which can then be used for conditioning of an enclosure or space. An electronic control panel (PLC) or more specifically a programmable logistical controller  29   FIG. 3 ,  4 ,  7 ,  8 ,  9 , is responsible for governing and synchronizing the operations of the various PH2OCP sub-systems including all components. 
         [0072]    The PLC control panel  29  also governs the operation of the desiccant rotor/wheel assembly  7  and rotation motor assembly  12   FIGS. 2 ,  4 ,  6 , which are two of the main operational components of the PH2OCP system  72 . The electrical panel  63   FIG. 7 ,  8 ,  9 , the (PLC) programmable logistical controller  29   FIG. 3 ,  4 ,  7 ,  8 ,  9 , and plug-in power cable connector panel  28   FIG. 3 ,  4 ,  7 ,  9 , are housed in generally square or rectangular design water resistant protective enclosures. The PLC panel  29  has a hinged lid and screw type fasteners and angles at various points for attachment and tight sealing of the lid. The electrical panel  63 , PLC panel  29  and the plug-in power cable connector panel  28  protective type enclosures can be designed to adapt to the various operational environments of the PH2OCP system  72 . In the preferred design, the PLC panel  29 , electrical panel  63 , and plug-in power cable connector panel  28  are constructed of either stainless steel or of aluminum. 
         [0073]    Referring to  FIG. 2 ,  3 ,  4 ,  5 ,  6 , the PH2OCP system  72  desiccant rotor/wheel assembly  7  is housed in a rectangular box shaped cabinet  31   FIG. 1 ,  3 ,  7 ,  8 ,  9 , and accessible through a panel  33   c    FIG. 3 , supported on cross members (not shown). 
         [0074]    In the preferred embodiment, the cabinet  31  is constructed from stainless steel to resist corrosion or from welded aluminum, coated with a durable resistant enamel or air-dry polyurethane corrosion resistant paint. The cabinet  31   FIG. 1 ,  3 ,  7 ,  8 ,  9 , includes top and bottom walls, front and rear spaced walls and opposed side walls as shown. As shown in  FIG. 1  unit views  1 ,  2 ,  4 ,  FIGS. 3 ,  7 ,  9 , adjacent the bottom wall, the front wall has the air process inlet  5  (above)  FIGS. 2 ,  3 ,  4 ,  6 ,  7 ,  9 , and air process outlet  17  (below)  FIGS. 2 ,  3 ,  4 ,  6 ,  7  and  9 . The process inlet  5  is to allow ambient air  11   a    FIG. 2 ,  3 ,  4 ,  6 ,  7 ,  9 , to flow into the PH2OCP system  72  through the extraction process section  6   FIG. 2 ,  4 ,  5 ,  6 , and the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5  and  6 . In the preferred embodiment, mounted at the intake of the process inlet, there could be installed an inlet filter  5   a    FIG. 2  for removing airborne contaminants or dust particles found in the ambient air, prior to it entering the extraction process section  6   FIG. 2 ,  4 ,  5 ,  6 , and flowing through the desiccant rotor/wheel  7  perforated desiccant core material  8   FIG. 2 . 
         [0075]    The filter installation tends to prevent the dust particles from accumulating within the PH2OCP system  72  and clogging the desiccant rotor/wheel core material  8   FIG. 2  which could if exposed long term, affect the performance and overall operating PH2OCP system  72 . 
         [0076]    In the preferred embodiment, the process inlet  5  filter  5   a  is a metallic mesh filter which is washable and can be removed for cleaning and rinsing of dust particles and reinstalled. As also shown in view  2   FIG. 1 , the front wall also has a process outlet  17  dry air discharge  11   d.  This discharged airflow  11   d  permits the PH2OCP system  72  to provide as a byproduct not only dry but conditioned air as well that can be utilized to climatize an enclosure or space. Mounted in the process outlet  17  there can be installed a manually operated damper assembly (not shown) including at least (1) one or more rotating louvers for selectively restricting the air flow out of the process outlet  17 . The use of this feature can increase both air pressure and temperature to enable greater heat retention within the reactivation process section  9  which will in turn increase the efficiency of the desiccant rotor/wheel  7  and core material  8 . The temperature rise speeds up the release of moisture vapors in the condensation process section and drying out the desiccant core material  8  so that it can resume its operating cycle as it rotates back into the extraction process section  6 . Therefore, depending on the climatic conditions, this mechanical feature found in the PH2OCP system  72  could be beneficial in allowing the desiccant core material  8  within the desiccant rotor/wheel  7  to release greater quantities of accumulated moisture and thus increasing its water production capability as required. In the preferred embodiment, constant airflow  11   a, b, c, d,  and pressure is provided and maintained by means of (1) one high static direct drive axial type blower  16  driven by an electric motor (not shown)  FIG. 2 ,  4 ,  6 ,  7 , which is located at the process outlet  17  installed and secured within the casing. 
         [0077]    The process outlet  17  high static direct drive axial blower  16  allows for the discharge of the dry conditioned airflow  11   d  which is drawn through the PH2OCP system  72  processes and directly into the enclosure or space to be treated and conditioned. Mounted in the process outlet  17  there can be installed a manually operated damper assembly (not shown) including at least (1) one or more rotating louvers for selectively restricting the air flow out of the process outlet  17  (dry conditioned air supply  11   d ) to the enclosure or space when required. 
         [0078]    In alternative embodiments, if a larger PH2OCP system  72  design with greater airflow and pressure is required for increased water production capability, there may be installed (2) two high static direct drive axial type blowers, one located at the process inlet  5  and the other at the process outlet  17 . This design could ensure that in a larger system design increased airflow and pressure requirements would be maintained as well as system continuity and redundancy in case one of the two blowers would cease operation. 
         [0079]    However it will be appreciated and understood that the electric motor (not shown) which drives the PH2OCP system  72  high static direct drive axial type blower  16  need not necessarily be an electric type motor. In alternative embodiments, there may be installed either a hydraulic, pneumatic or steam driven motor, designed and approved, which could be utilized to accomplish the same task of driving the PH2OCP system  72  process high static axial blower  16 . The process outlet  17  supply port has an extension which is adapted to receive flexible or rigid ducting to allow distribution of conditioned dry air to specific target areas to be treated. As shown in  FIG. 1  unit views  1 ,  3 ,  4 ,  FIG. 3 ,  8 ,  9 , that each of the side walls have outer access panels  33   a  to  h,  which are constructed and symmetrical on both sides of the cabinet  31  and can be attached to the cabinet with bolt and clip nut assemblies (not shown) or equipped with latch assemblies (not shown) which unlock and permit panel opening for easy access during servicing and maintenance without having to disassemble or disconnect any air distribution ducting or electrical power supply cables. These various panels  33   a  to  h,  enable quick access to all the unit compartments which house the PH2OCP system  72  operational sub-systems and related components, such as; extraction process section  6 , desiccant rotor/wheel assembly  7 , the reactivation process section components  9 , the condensation process section  15  components including the filtration and decontamination package  39  and  40 . 
         [0080]    All of these access panels may be designed and provided with a small window (not shown) in order to allow for visual inspection, including but not limited to the various operational sub-systems and components. With reference to the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , it is mounted within the cabinet  31   FIG. 3  in access panel  33   c    FIG. 3 , between two interior walls thereof as shown on  FIGS. 4 ,  6 , (not shown) which are located fwd and aft of the desiccant rotor/wheel assembly  7   FIGS. 4 and 6 . 
         [0081]    The desiccant rotor/wheel assembly  7  includes the desiccant rotor/wheel  7  supported on a set of roller bearings (2) assemblies  41   FIG. 6 , one on either side at the base of the desiccant rotor/wheel assembly  7   FIG. 6  on which the desiccant rotor/wheel  7  rests during rotation and operation. 
         [0082]    In the preferred embodiment, there is an electric drive rotation motor  12   FIG. 2 ,  4 ,  6 , which provides for driving rotation of the desiccant rotor/wheel assembly  7  along its longitudinal axis. The electric drive rotation motor is encapsulated within a housing (not shown). In an alternative design adapted for some applications, the electric drive rotation motor may include an internal ventilation fan for cooling the drive motor. Though the preferred embodiment demonstrates the use of an electric drive rotation motor  12 , it must be appreciated that in other alternative embodiments, the drive rotation motor  12  could be powered and driven pneumatically or hydraulically in order to perform the same function. The electric drive rotation motor  12  is connected to the desiccant rotor/wheel assembly  7  by way of a gearbox (not shown) which in turn drives a self-tension drive belt  13  arrangement  FIGS. 2 ,  4  and  6 . The gearbox (not shown) provides for drive motor speed to be reduced allowing for the specified desiccant rotor/wheel assembly  7  rotations to be achieved. In the preferred embodiment, the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , is driven to operate between 8 to 10 complete rotations per hour. The rotations could vary according to the type of desiccant core material  8 , diameter and thickness of the desiccant rotor/wheel  7  as well as the specific applications where it may be utilized. The electric drive rotation motor  12  is connected by means of an electrical cable to a junction box (not shown). The junction box electrical cable runs through an electrical conduit (not shown) within and down the cabinet  31  through the frame  18  base longitudinal beam  69   a  and up the vertical post  23  where it is connected to the PLC programmable logic control panel  29  for protection from the external elements. 
         [0083]    This electrical conduit (not shown) houses the PH2OCP systems&#39; insulated electric cables and wires (not shown). In an alternative embodiment, it must be appreciated that the electrical conduit system which houses the electrical cables and wiring may be designed and housed externally on the unit frame  18 . As best demonstrated in  FIG. 2 , the desiccant rotor/wheel assembly  7  includes an outer metal shell or casing and a monolithic core which is the desiccant material  8 . In the preferred embodiment the outer casing or shell of the desiccant rotor/wheel  7  is made of aluminum, however, it will be appreciated that in alternative embodiments other alloys or metals could also be used in the fabrication of the desiccant rotor/wheel  7  outer shell or casing. The core of the desiccant material as shown in  8   FIG. 2 , is perforated and has a matrix made up of small uniformed tunnels or channels with the walls shaped resembling a honeycomb. These small uniformed tunnels run parallel to the axis of the process airflow  11   a, b, c, d,  which moves through the three processes; extraction  6 , reactivation  9  and condensation  15 . The desiccant core material  8   FIG. 2 , tunnel walls are constructed of a non-metallic, non-corrosive inert composite. The walls are made of extruded fiberglass paper fibers with an opening measuring at least 5 microns in diameter and are coated/impregnated with a solid desiccant type material which in the preferred embodiment will be, but not limited to; silica gel. Other desiccant materials which will not contaminate the water may be used such as molecular sieve, including other types of desiccant materials which can withstand repeated temperature fluctuations and moisture retention and release cycling. The desiccant type material is evenly spread throughout the core  8   FIG. 2  of the desiccant rotor/wheel assembly  7 . 
         [0084]    In the extraction process  6 , the desiccant core material  8   FIG. 2  vapor moisture content is very low and dry therefore attracting airborne moisture vapors extracting them from the process inlet  5  airflow  11   a  called sorption. In this process section the desiccant core material  8  has a very low vapor pressure/very low moisture concentration in comparison to the damp and humid ambient incoming process inlet  5  airflow  11   a.  Conversely, in the reactivation process section  9 , the desiccant core material  8  will release its accumulated moisture vapors back into the hot dry process airflow  11   b  as it passes through called desorption. 
         [0085]    This is made possible because under the conditions produced, the desiccant core material will have a high vapor pressure/higher moisture concentration in comparison to the process airflow  11   b.  The desiccant rotor/wheel assembly  7   FIG. 2 ,  4 ,  5 ,  6 , is considered to be an active component because it performs its tasks of sorption and desorption by continuously rotating about its longitudinal axis, passing through the extraction  6 , reactivation  9  and condensation  15  processes and back again as part of a perpetual cycle. The alternating cycle from high to low vapor pressures such as the extraction  6  and reactivation  9  processes, enable the PH2OCP system  72  the capability to absorb and release enormous quantities of moisture vapors from ambient airflow  11   a, b, c, d,    FIG. 2 . In the preferred embodiment, the PH2OCP system  72  uses reactivation process  9  airflow  11   b  which is heated by the reactivation heating coils  10  part of the sub-system identified as the microwave reactivation system  36   FIG. 2  located within the reactivation process section  9 . 
         [0086]    This heated reactivation process  9  airflow  11   b  demagnetizes the desiccant core material  8  within the desiccant rotor/wheel assembly  7   FIG. 2 . The desiccant core material  8  when heated at a high temperature looses its capacity to retain moisture vapors therefore releasing and discharging them back into the process airflow  11   c.  Because the moisture removal in the desiccant rotor/wheel  7  occurs in the vapor phase, there is no liquid condensate. Therefore, the PH2OCP system  72  can continue to extract moisture vapors from the extraction process  6  airflow  11   a,  even when the dewpoint of the process airflow  11   a  is below freezing. Consequently, in comparison to the conventional moisture extraction systems, the PH2OCP system  72  is much more operationally versatile, able to fully function and completely adaptable in various environmental and climatic conditions found around the globe. In the preferred embodiment, the desiccant rotor/wheel assembly  7  installed and utilized within the PH2OCP system  72  can be constructed and supplied by any approved desiccant rotor/wheel manufacturer which meets the approved equipment performance specifications and industry standards. 
         [0087]    In the preferred embodiment, the portion of the desiccant core material  8  of the desiccant rotor/wheel assembly  7  which is reactivated or regenerated  FIG. 2 , is sectioned off by a V-shaped partition member  FIG. 2 , which is mounted in the cabinet  31 . This V-shaped partition member isolates and segregates a pie-shaped section approximately one-quarter (¼) of the desiccant rotor/wheel  7  core material  8  from the remaining portion of the desiccant core material thereof, which defines the reactivation process section  9   FIG. 2  of the desiccant rotor/wheel assembly  7 . 
         [0088]    The remaining portion approximately three-quarters (¾) of the desiccant rotor/wheel  7  core material  8   FIG. 2 , defines the extraction process section  6   FIG. 2  of the desiccant rotor/wheel assembly  7 . In the preferred embodiment, the reactivation process  9  portion of the desiccant rotor/wheel assembly  7  may cover between one-quarter to one third of the surface desiccant core material  8  area of the desiccant rotor/wheel assembly  7 . In alternate embodiments, both the extraction  6  and reactivation  9  processes could each cover one-half (50%) of the surface desiccant core material area. During the operation of the PH2OCP system  72 , the portions of the desiccant rotor/wheel assembly  7  core material  8  which define the extraction process section  6   FIG. 2  and the reactivation process section  9   FIG. 2 , are constantly changing. This occurs as a result of the rotation of the desiccant rotor/wheel assembly  7   FIG. 2 , by means of a electric drive rotation motor  12   FIG. 2  which are linked by a rotation belt  13   FIG. 2 . 
         [0089]    Accordingly, as the portion of the desiccant rotor/wheel assembly  7  core material  8  that is exposed to the extraction process  6  airflow  11   a    FIG. 2  defines the extraction process section  6   FIG. 2 , likewise, the portion of the desiccant rotor/wheel assembly  7  core material  8  that is exposed to the reactivation process  9  airflow  11   b    FIG. 2 , defines the reactivation process section  9   FIG. 2 . Only the airflow  11   a  and  11   b  from these two processes is introduced into the desiccant rotor/wheel assembly  7  core material  8 , inducing a reaction of vapor sorption and desorption. The condensation process section  15   FIG. 2  in turn is solely responsible for the transformation of the process airflow  11   c  hot moisture vapors into condensate and water  70   FIGS. 4 ,  6 , with the treatment and conditioning of the resulting discharge process airflow  11   d    FIG. 2 . 
         [0090]    Passing through three-quarters (75%) portion of the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , core material  8   FIG. 2  surface area, the extraction process  6   FIGS. 2 ,  4 ,  5 ,  6 , airflow  11   a    FIG. 2 ,  4 ,  5 ,  6 , is drawn through the process inlet  5   FIGS. 2 ,  3 ,  4 ,  6 ,  7  and  9 . Having transferred its moisture onto the desiccant core material  8   FIG. 2 , the process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , continues its path as it is drawn into the reactivation process section  9   FIG. 2 ,  4 ,  5 ,  6 , through a metallic coils assembly identified as the reactivation heating coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , part of the microwave reactivation system  36   FIGS. 4 ,  5 ,  6 , which incorporates a circulating super heated thermal fluid (not shown). This dry and heated process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , is then drawn increasing its velocity as it passes through a narrower curved pathway which is redirected back again passing through the V-shaped one-quarter (25%) portion of the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , core material surface  8   FIG. 2 . This portion of the desiccant core material  8   FIG. 2 , being saturated with moisture vapors, releases these vapors back into the dry heated process airflow  11   b  FIGS.  FIGS. 2 ,  4 ,  6 , which demagnetizes the desiccant core material  8   FIG. 2  as it passes through it. The process airflow  11   c    FIGS. 2 ,  4 ,  6 , leaving the desiccant core material  8   FIG. 2 , now saturated with moisture vapors, passes through the condensation process section  15   FIGS. 2 ,  4 ,  6 , where moisture vapors are rapidly cooled, condensed and transformed into water droplets  70   FIGS. 4 ,  6 , which are funneled downward into a unit base reservoir  48   FIGS. 4 and 6 . The resulting process airflow  11   d    FIGS. 2 ,  4 ,  6 , which is once again dry and conditioned, is then expelled by means of a high static direct drive axial blower  16   FIGS. 2 ,  4 ,  6 ,  7 ,  9 , located at the airflow discharge process outlet  17   FIGS. 2 ,  3 ,  4 ,  5 ,  7 ,  9 . 
         [0091]    It will thus be understood that though there is only one process airflow  11   a  to  11   d  passing through the PH2OCP system  72 , as it rotates about its longitudinal axis the desiccant rotor/wheel assembly  7  and core material  8   FIGS. 2 ,  4 ,  5 ,  6 , is exposed to completely separate and isolated processes; the extraction process  6 , the reactivation process  9  and the condensation process  15 . Pressure seals (2)  42   FIG. 5 ,  6 , mounted fore and aft of the desiccant rotor/wheel assembly  7   FIGS. 5 ,  6 , at the extremities of the outer shell rim and at the edges of V-shaped partition member (not shown), are provided in order to separate and completely isolate the three (3) processes extraction  6 , reactivation  9 , condensation  15  and eliminate any possible air or moisture crossover leakage within the three (3) operating process sections located in the PH2OCP system  72  cabinet  31   FIGS. 1 ,  3 ,  7 ,  8  and  9 . In the preferred embodiment, the frame  18   FIG. 3 ,  4 ,  7 ,  8 ,  9 , will serve as ground, but it will be appreciated that in other embodiments, an alternative ground system including an electrical ground could be utilized. With reference to  FIGS. 2 ,  4 ,  5 ,  6 , the PH2OCP system&#39;s operational sub-systems; microwave reactivation system  36   FIGS. 4 ,  5 ,  6  and air treatment and conditioning system  61   FIGS. 4 ,  6 , will now be described in greater detail. The microwave reactivation system  36   FIGS. 4 ,  5 ,  6 , provides the means for regeneration and reactivation of the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  6 , core material  8   FIG. 2  in the PH2OCP system  72 . In the preferred embodiment, the microwave heating chamber  35   FIGS. 4 ,  5 ,  6 , including the microwave components and high voltage part  49   FIG. 5 , as part of the microwave reactivation system  36   FIGS. 4 ,  5 ,  6 , are encapsulated in an explosion-proof type casing for enhanced operational safety and to avoid harmful exposure. 
         [0092]    In an alternative embodiment, these same components can be installed inside an industry standard casing which would be deemed safe for operation. This microwave reactivation system  36   FIGS. 4 ,  5 ,  6 , produces heat by generating electromagnetic RF waves which passes through materials and fluids, causing the molecules within to move rapidly in excitation, causing atomic motion which generates heat. In the preferred embodiment, the medium used to store and transmit this heat is a synthetic thermal fluid (not shown) located in the hollow coils assembly  34  and  10   FIG. 5  of the microwave reactivation system  36   FIGS. 4 ,  5 ,  6  closed-loop circuit. This fluid is moved by means of a supply pumps  43   a    FIGS. 4 ,  5 ,  6 , located in the isolated compartment beneath the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . The thermal fluid flows through a first series of parallel glass ceramic coils assembly  34   FIGS. 4 ,  5 ,  6 , located in the microwave heating chamber  35   FIGS. 4 ,  5 ,  6 , where the fluid molecules are treated and exposed to electromagnetic waves causing excitation, high temperature rise and heat generation within the thermal fluid (not shown). 
         [0093]    This super heated thermal fluid is then pumped and flows through a second series of parallel metallic coils  10   FIGS. 2 ,  4 ,  5 ,  6 , located in the isolated compartment below directly in the pathway of the process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , called the reactivation process section  9   FIGS. 2 ,  4 ,  5  and  6 . The heat transferred onto the process airflow l lb from the hot thermal fluid (not shown) within the series of parallel metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , in the reactivation process section  9   FIG. 2 ,  4 ,  5 ,  6  and substantially raises the temperature of the process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , as it comes in contact and passes across the surface of the metallic coils assembly  10   FIGS. 2 ,  4 ,  5  and  6 . This heated reactivation process  9   FIG. 2 ,  4 ,  5 ,  6 , process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , is then used to deactivate the perforated desiccant core material  8   FIG. 2  within the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  6 , as it passes through it. This dry and heated process airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , is redirected through the cabinet  31   FIGS. 4 ,  6  process airflow air tunnel within the PH2OCP system  72  and back to the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  6 , where it has a demagnetizing effect on the desiccant core material  8   FIG. 2 . This treated reactivation process  9   FIG. 2 ,  4 ,  5 ,  6  and airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , enables the desiccant core material  8  to release onto it the retained accumulated moisture. 
         [0094]    This effect greatly lowers the vapor pressure within the desiccant core material  8   FIG. 2 , enabling the core material to resume its moisture retention or sorption capabilities as it rotates back into the extraction process section  6   FIGS. 2 ,  4 ,  5  and  6 . The hot and moisture saturated process airflow  11   c    FIGS. 2 ,  4 ,  6 , is drawn into the condensation process section  15   FIG. 2 ,  4 ,  6 , for air treatment and conditioning. In the preferred embodiment, the microwave reactivation system  36   FIGS. 4 ,  5 ,  6 , power generation is divided into two parts, the control part and the high-voltage part. The control part is the programmable logic controller (PLC)  29   FIGS. 3 ,  4 ,  7 ,  8  and  9 . The PLC  29  controls and governs the power output and desired operational settings, monitors the various system functions, interlock protections and safety devices. Also in the preferred embodiment, to ensure operational safety, the components in the high-voltage part  49   FIG. 5 , are encapsulated in an explosion-proof rated housing. These components serve to step up the voltage to a much higher voltage. 
         [0095]    The high voltage is then converted into microwave energy in the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . Generally, the control part (not shown) includes either an electromechanical relay or an electronic switch called a triac (not illustrated). Once the system is turned on, sensing that all systems are “go,” the control circuit in the programmable logic controller panel  29  generates a signal that causes the relay or triac to activate, thereby producing a voltage path to the high-voltage transformer  50   FIG. 5 . By adjusting the on-off ratio of this activation signal, the control part governs the flow of voltage to the high-voltage transformer  50  thereby controlling the on-off ratio of the tube within the magnetron  51   FIG. 5  and therefore the output power to the microwave heating chamber  35   FIG. 5 . In the high-voltage part  49   FIG. 5 , the high-voltage transformer  50   FIG. 5  along with a special diode  53   FIG. 5  and capacitor  52   FIG. 5  arrangement serve to increase the voltage to an extreme high voltage for the magnetron  51   FIG. 5 . The magnetron  51  dynamically converts the high voltage it receives into undulating waves of electromagnetic energy. This microwave energy is then transmitted into a metal rectangular channel identified as a waveguide  55   FIG. 5 , which directs the microwave energy or waves into the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . 
         [0096]    The effective and even distribution of the electromagnetic energy or waves within the entire microwave heating chamber  35   FIG. 4 ,  5 ,  6 , is achieved by the revolving metal stirrer blades  54   FIG. 5 , powered by the motor assembly  56   FIG. 5 . A metal conduit  57   FIG. 5  houses the electrical wiring between the high voltage part components  49   FIG. 5  to the stirrer blades  54  motor assembly  56   FIG. 5   
         [0097]    In the preferred embodiment, high tensile resistant glass ceramic hollow tubing is used in the construction of the glass ceramic coils assembly  34   FIG. 4 ,  5 ,  6 , located in the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . The electromagnetic energy or waves produced by the magnetron  51   FIG. 5  are dispersed by the metal stirrer blades  54   FIG. 5  and come in contact with the entire glass ceramic coils assembly  34   FIG. 4 ,  5 ,  6 , located within the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . The heater fluid (not shown) flowing in these hollow coils is then simultaneously treated and exposed to this electromagnetic energy causing molecular excitation, atomic motion, high temperature rise between 250-300 degrees Fahrenheit and heat generation. This super heated fluid (not shown) is siphoned and propelled by means of supply and return pumps  43   FIG. 4 ,  5 ,  6 , flowing into and through the metallic coils assembly  10   FIG. 2 ,  4 ,  5 ,  6 , located in the compartment below called the reactivation process section  9   FIGS. 2 ,  4 ,  5  and  6 . 
         [0098]    In the preferred embodiment, the hollow tubing of the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , located in the reactivation process section  9   FIGS. 2 ,  4 ,  5 ,  6 , is constructed of steel, aluminum or other high heat resistant metal which is adaptable to extreme temperature variances and which can effectively retain and transmit heat. It is important to note that the diameter of the tubing of the metallic coils assembly  10  in the reactivation process section  9  is smaller in comparison to the diameter of the glass-ceramic coils assembly  34  in the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . 
         [0099]    Also in the preferred embodiment, the distance between the coils of the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , in the reactivation process section  9   FIGS. 2 ,  4 ,  5 ,  6 , is narrower and the number of actual coils is 1.5 but in an alternate design may be up to 2 times greater in number of coils comparatively to the glass-ceramic coils assembly  34   FIG. 4 ,  5 ,  6 , located in the microwave heating chamber  35   FIGS. 4 ,  5  and  6 . This construction allows for a greater temperature rise and a more efficient heat transfer and distribution to the reactivation process  9  airflow  11   b    FIGS. 2 ,  4 ,  5 ,  6 , as it comes in contact passing across the surface and through the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , in the reactivation process section  9   FIGS. 2 ,  4 ,  5  and  6 . Therefore, the tightly spaced coil design of the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , allows for a more effective and substantial heat transfer radiated from the thermal fluid (not shown) onto the metal coils and finally to the reactivation process  9  airflow  11   b    FIGS. 2 ,  4 ,  5  and  6 . A substantial temperature rise of the reactivation process  9  airflow  11   b  of 170-200 degrees Fahrenheit is achieved as it passes through the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , in the reactivation process section  9   FIGS. 2 ,  4 ,  5  and  6 . 
         [0100]    This temperature rise of the reactivation process  9  airflow  11   b  deactivates the desiccant impregnated core material  8   FIG. 2  within the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , lowering its vapor pressure as the dry hot airflow  11   b  passes through the desiccant impregnated core material  8 . This dry heated airflow  11   b  with a very low vapor pressure and concentration, enables the desiccant core material  8  to rapidly release the retained accumulated moisture into this airflow  11   b  as it passes through the desiccant rotor/wheel assembly  7  core  8 . 
         [0101]    This emerging wet and hot process airflow  11   c  is then pulled through the evaporator cooling coils assembly  14   FIGS. 2 ,  4 ,  5 ,  6 , part of the air treatment and conditioning system  61   FIG. 6  in the condensation process section  15   FIGS. 2   4 ,  5  and  6 . The desiccant core material  8   FIG. 2  is then ready for reuse, as the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5 ,  6 , rotates about it longitudinal axis and back into the extraction process section  6   FIGS. 2 ,  4 ,  5  and  6 . The heater fluid (not shown) continues to transfer its heat, flowing through the metallic coils assembly  10   FIGS. 2 ,  4 ,  5 ,  6 , in the reactivation process section  9   FIGS. 2 ,  4 ,  5  and  6 . The thermal fluid is then siphoned by means of a return pump  43   b    FIG. 4 ,  5 ,  6  and propelled back into the glass-ceramic coils assembly  34   FIGS. 4 ,  5 ,  6 , in the microwave heating chamber  35   FIGS. 4 ,  5 ,  6 , as part of a closed-loop fluid circuit. 
         [0102]    Therefore, in a perpetual cycle, the thermal fluid undergoes repeated exposure to the microwave electromagnetic energy causing molecular excitation, atomic motion, high temperature rise between 250-300 degrees Fahrenheit and heat generation. Consequently, the thermal fluid (not shown) is the medium which moves back and forth passing through the microwave heating chamber  35  where it absorbs and is super heated, then to the reactivation process section  9  where it then dissipates and radiates its heat as part of the microwave reactivation system  36   FIGS. 4 ,  5  and  6 . It will be understood that in alternative embodiments, the microwave reactivation system  36  will incorporate design modifications which will allow for variations in performance capabilities. The modifications will determine size, output capacity and operational ranges in order to adapt to any PH2OCP system  72  performance requirements. 
         [0103]    In the preferred embodiment, the thermal heater fluid (not shown) circulation pumps  43   a  and  43   b    FIG. 4 ,  5 ,  6 , are of industrial construction grade and are rated to operate within high temperatures due to the thermal fluid. The modulation and cycling of the power to the high voltage part  49   FIG. 5 , is governed by temperature thermocouple and airflow pressure type sensors  44   a  and  44   b    FIGS. 5 and 6 . One temperature sensor  44   a  is located in the microwave heating chamber  35   FIGS. 5 ,  6 , another temperature and airflow pressure sensor  44   b  is located in the reactivation process section  9   FIGS. 4 ,  5 ,  6 , just forward of the desiccant rotor/wheel assembly  7   FIGS. 2 ,  4 ,  5  and  6 . Two more temperature and airflow pressure sensors  44   c  and  44   d  are located; one airflow and temperature sensor  44   c    FIG. 6  is in the extraction process section  6   FIG. 6  and the other  44   d    FIG. 6  is located at the process airflow outlet  17   FIG. 6 . All sensors are mounted in place by a support bracket (not shown) and wiring installed in a system of metallic conduits (not shown) to the control part and to the circuit in the (PLC) programmable logic controller panel  29   FIGS. 3 ,  4 ,  7 ,  8  and  9 . These sensors enable the detection of temperature and air pressure variations in the extraction  6 , reactivation  9  and condensation  15  processes and relay this information to the PLC panel  29  which in turn governs the various components and sub-systems and specifically the high voltage part  49   FIG. 5  to direct output power to the microwave heating chamber  35   FIGS. 4 ,  5 ,  6 , which produces the heat generation for the reactivation of the main components of the PH2OCP system  72  which is the desiccant rotor/wheel assembly  7  and core material  8 . 
         [0104]    Consequently, the temperature thermocouple type sensor  44   a    FIG. 5 ,  6 , located in the microwave heating chamber  35 , ensures that the system operates and modulates as required in order to automatically generate the microwave energy needed to maintain the desired high temperature of the thermal fluid as it flows through the coils assembly  34  in the microwave heating chamber  35  and into the reactivation heating coils assembly  10  in the reactivation process section  9 . This thermocouple type sensor detects the temperature generated within the microwave heating chamber  35  as it is emitted off of the glass-ceramic coils assembly  34  which contains the heat radianting thermal fluid. This interaction between the temperature and airflow pressure sensors  44   a, b, c, d,  the high voltage part  49 , the control part or PLC  29  as part of the overall operation of the microwave reactivation system  36  within the PH2OCP system  72 , ensures that the specified reactivation process airflow  11   b  temperature rise is achieved and maintained for an effective regeneration of the desiccant rotor/wheel assembly  7  core material  8 . This guarantees the maximum discharge of moisture vapors from the desiccant rotor/wheel  7  core material  8  for transformation into condensate and water by the condensation process  15  as part of the PH2OCP system  72 . Therefore, the temperature and airflow pressure sensors in the extraction  6 , reactivation  9  and condensation  15  process sections ensure that proper process airflow  11   a, b, c, d,  temperature and static pressure is consistently maintained throughout the PH2OCP system  72  operation. These sensors are also safety devices during operation which will identify and signal an alarm on the PLC  29  touch screen  37   FIGS. 3 ,  4 ,  9 , if there is a malfunction such as low reactivation process  9  temperature or drop in process airflow  11   a, b, c, d,  pressure. 
         [0105]    These sensors will also shut down the Ph2OCP system  72  by signaling the control circuit in the PLC panel  29  in the case where the temperature exceeds the prescribed high temperature operating limit set by the manufacturer or when there is a substantial drop or loss of process airflow  11   a, b, c, d,  pressure through the PH2OCP system  72 . In the preferred embodiment, the electrical connections of these components to each other and the control part or PLC panel  29  is achieved by way of several electrical conduits which are constructed and connected in part to the PH2OCP system  72  frame  18  (not shown), yet accessible for maintenance and verification purposes. In the preferred embodiment, all of the electrical conduits and wiring in the PH2OCP system are designed and rated as industrial grade. 
         [0106]    The following is a resume of the operation of the microwave reactivation system  36   FIGS. 4 ,  5 ,  6  and air treatment and conditioning system  61   FIG. 6  as operational sub-systems within the PH2OCP system  72   FIGS. 1 ,  3 ,  4 ,  7 ,  8  and  9 . 
         [0107]    Upon deployment of the (PH2OCP) Portable Water and Climatic Production system  72 , the desiccant rotor/wheel assembly  7  is driven to rotate by an electric drive motor  12  and rotation belt assembly  13  along its longitudinal axis. The process airflow  11   a  is simultaneously drawn, moving through the PH2OCP system  72  process inlet  5 , by means of a high static direct drive axial blower  16  at the process outlet  17  which siphons the ambient air. The process air  11   a  flows through the process inlet  5  and filter  5   a  from ambient into the extraction process section  6  and through the desiccant rotor/wheel assembly  7  core material  8 . 
         [0108]    As the process airflow  11   a  passes through the desiccant rotor/wheel assembly  7  core material  8 , it is stripped of its moisture by the desiccant core material  8  which is impregnated within its inner walls by a desiccant substance (silica gel) as part of the desiccant rotor/wheel assembly  7 . The resultant is dry process airflow  11   b  exhausted from the desiccant rotor/wheel assembly  7  core material  8 . The high static direct drive axial blower  16  will maintain a recommended airflow and static pressure for various flow rates (cubic feet per minute—CFM) of at least 2.0 to 3.0+ inches of water column (WC) to provide effective airflow distribution throughout the PH2OCP system  72  processes to ensure at all times the maximum water production output as well as proper conditioned air discharge temperature for air treatment and conditioning within an area or enclosed space. 
         [0109]    In the preferred embodiment, the reactivation process  9  airflow  11   b  rates will be maintained at least at 15 cubic meters per minute/530 cubic feet per minute. As the airflow  11   b  passes through the reactivation process section  9 , its temperature dramatically increases as a result of an intense heat transfer radiated from the thermal fluid (not shown) within the metallic coils assembly  10  part of the microwave reactivation system  36 . Though there could be acceptable variations in the reactivation process  9  airflow  11   b  temperature, the recommended operating temperature of the reactivation process  9  airflow  11   b  should reach between degrees; 120 C to 150 C 170 F to 300 F. Subsequently, the super heated reactivation process  9  airflow  11   b  with a very low vapor pressure/moisture concentration, passes through the desiccant core material  8 , which is saturated with moisture and having a high vapor pressure. 
         [0110]    This super heated reactivation process  9  dry airflow  11   b  serves to regenerate the “V” shaped section of the desiccant rotor/wheel assembly  7  by heating the inner walls of the perforated desiccant core material  8 . Consequently, this dry heated airflow  11   b  causes the desiccant core material  8  to de-energize/demagnetize releasing its accumulated moisture back into the airflow  11   c.  This process airflow  11   c  which is once again moisture saturated is drawn passing through the condensation process section  15  where it is cooled by means of an evaporator cooling coils assembly  14  as part of the air treatment and conditioning system  61 . The moisture vapors within the process airflow  11   c  condense as they are rapidly cooled down through the evaporator cooling coils  14  transforming the condensate into water  70 . This water  70  is gravity fed into a funnel (not shown) located beneath the evaporator cooling coils  14 , passing through the filtration  39  and sterilization  40  unit and settling into the unit base reservoir  48 . The byproduct which is treated and conditioned process airflow  11   d  is discharged through the process outlet  17  into the space or enclosure to be treated. During the rotation of the desiccant rotor/wheel assembly  7 , prior to re-entering the extraction process section  6 , the desiccant rotor/wheel assembly  7  core material  8  having released its moisture vapors due to the effect of the reactivation process  9  airflow  11   b,  back into the condensation process  15  airflow  11   c,  has once again a very low vapor pressure. This highly effective process of sorption and desorption made possible by the operational capabilities of the desiccant rotor/wheel assembly  7  core material  8 , allows it to again resume its operation of moisture vapors retention in the extraction process  6 . 
         [0111]    The slow rotational speed of the desiccant rotor/wheel assembly  7  which is one full rotation every 8 to 10 minutes, is required to enable the cooling of the desiccant rotor/wheel assembly  7  core material  8 , allowing it to achieve maximum performance as it rotates passing through the various operational PH2OCP system  72  processes. 
         [0112]    The air treatment and conditioning system  61   FIG. 6  within the condensation process  15  provides the means for cooling the process airflow  11   c  and condensing the moisture vapors transforming them into water  70 . This water  70  flows downward through a funnel (not shown) where it is cleansed through a carbon filter  39 , sanitized and purified with a (UV) ultraviolet lamps assembly  40  depositing into the unit base reservoir  48 . A level floater  47  and shaft assembly is fixed and mounted vertically inside the PH2OCP system  72  base reservoir  48 . This level floater  47  is allowed to move vertically up or down the shaft assembly depending on the volume of water within the base reservoir in order to avoid overflow. There is a pressure sensor (not shown) located at the top extremity of the shaft which the level floater will energize once it rises to the top of the shaft, making contact with the pressure sensor which transmits a signal to the PLC controller panel  29  which terminates the operation of both the microwave reactivation system  36  and the air treatment and conditioning system  61 . If the unit base reservoir  48  is filled, by ceasing the operation of these two sub-systems, the PLC controller  29  ceases the PH2OCP system  72  water production process. Nevertheless, the PLC controller  29  will still enable the PH2OCP system  72  components to continue operating, such as; rotation of the desiccant rotor/wheel assembly  7  and operation of the high static direct drive axial blower  16  to allow for the desiccant rotor/wheel cool down and proper shut-down of the PH2OCP system  72  which can be restarted on demand. In the preferred embodiment, the PH2OCP system  72  unit base reservoir  48  is equipped with two sump pumps  45   a, b,    FIGS. 4 ,  6 , located at opposite ends of the unit base reservoir  48  and interconnected with a pressure line  46   FIGS. 4 ,  6 , which feeds the water manifold and supply drain assembly  32   FIGS. 4 ,  6 , located on the cabinet  31  rear wall. This water manifold and supply drain assembly  32  delivers a pressurized flow of fresh production water upon depressing the supply drain lever (not shown). The air treatment and conditioning system  61  incorporates an evaporative cooling coils assembly  14  located in the condensation process section  15 , directly in the pathway of the process airflow  11   c.  These evaporative cooling coils  14  hollow design allows for a refrigerant gas (not shown) to flow within , enabling it to rapidly cool down the process airflow  11   c  temperature by extracting its heat. The evaporator cooling coils assembly  14  is connected to the other components; including the compressor  59  and condenser coils  58  by means of two (2) metal pipes  65 ; supply and return piping or lines. 
         [0113]    These supply and return hollow piping/lines  65  serve to circulate the refrigerant gas from the evaporator cooling coils assembly  14  to the compressor  59  and onto the condensing coils assembly  58 . The refrigerant gas then leaves the condenser coils assembly  58  passing through a receiver dryer (not shown) and expansion/metering valve  64  and fed back to the evaporator cooling coils assembly  14  as part of a closed-loop split type air treatment and conditioning system  61 . The condenser coils assembly  58  hollow design and fins (not shown) serve to cool down the heat laden refrigerant gas flowing within. 
         [0114]    This cooling effect is provided by means of a high velocity exhaust fan and motor assembly  60  which is located on top of the PH2OCP system  72  cabinet  31  above the compressor  59  and condenser coils assembly. 
         [0115]    This exhaust fan motor assembly  60  draws ambient air through the cabinet  31  side wall intake  30  and across the condenser coils assembly  58 , to collect and evacuate the heat emitted from the condenser coils  58  by the circulating hot gas within. The exhaust fan motor assembly  60  siphons and expels the hot airstream upward and away from the condenser coils assembly  58  and into ambient. This effect cools the condenser coils assembly  58  which in turn cools down the refrigerant gas as it is circulated back into the evaporator coils assembly  14  part of this split type air treatment and conditioning system  61 . Though any legal refrigerant gas can be utilized in the PH2OCP system  72 , in the preferred embodiment, the refrigerant gases used for reasons of safety and to meet environmental standards are either; R417A as a replacement for R22 or alternate gases such as; R134A, R407C, R410A. These refrigerant gases have a low chlorine content and ozone depletion potential (ODP) as compared to gases such as; R22 which though still in use, is considered more harmful to the environment. While the evaporator cooling coils assembly  14  is located in the condensation process section  15 , the other components such as; condenser coils assembly  58 , compressor  59 , high velocity exhaust fan and motor assembly  60 , receiver dryer (not shown) and expansion/metering valve  64  are located in a separate compartment within the cabinet  31 , above the extraction process section  6 . 
         [0116]    The supply and return piping  65  linking the evaporating  14  and condensing  58  parts of the air treatment and conditioning system  61  are installed within a sealed and insolated metal conduit or channel (not shown) which is constructed as part of the inner cabinet  31 . 
         [0117]    This metal conduit or channel (not shown) runs from the condensing unit compartment (access panel  33   e ), down the inner cabinet  31 , through the extraction process section  6  and the condensation process section  15  (access panel  33   d ). 
         [0118]    In an alternative embodiment, a modified reactivation process  9 A may be utilized, as illustrated in  FIGS. 10A ,  10 B and  11 . In this alternative embodiment, the reactivation process  9 A includes a microwave reactivation system  36 A having a microwave heating chamber  35 A through which the desiccant rotor wheel  7  rotates. As the desiccant rotor wheel  7  rotates through the microwave heating chamber  35 A, the desiccant material  8  in the rotor wheel  7  is heated and deactivated, thereby releasing the moisture contained therein back into the airflow. Such a design eliminates the need for reactivation heating coils  10  and internal heated thermal fluid which flows therethrough. 
         [0119]    As can be seen in  FIGS. 10A and 10B , the microwave heating chamber  35 A is constructed such that a portion of the rotating desiccant rotor wheel  7  passes directly through the microwave heating chamber  35 A. In order to accommodate the desiccant rotor wheel  7 , at least one wall of the microwave heating chamber  35 A includes a through-hole or cutout sized and shaped to receive the desiccant rotor wheel  7  therethrough. As shown in  FIGS. 10A and 10B , walls  84  and  86  of microwave heating chamber  35 A include cutouts which allow the rotor wheel  7  to pass therethrough. It is noted that a sealing material may be utilized between the walls of the microwave heating chamber  35 A and the desiccant rotor wheel  7  which would help to maintain a seal between the two, while still allowing the desiccant rotor wheel  7  to rotate. Such sealing material would preferably be resistant to damage and extreme heating due to the microwaves in the microwave reactivation system  36 A. 
         [0120]    Airflow outlet  80  can also be seen in  FIGS. 10A and 10B . It is noted that a substantially similar airflow inlet  82  is also provided on the microwave heating chamber  35 A opposite the airflow outlet  80 . Though airflow inlet  82  is not pictured due to the orientation of the microwave reactivation system  36 A, its position is shown in  FIG. 10A . Either or both of airflow inlet  82  and airflow outlet  80  in the microwave reactivation system  36 A may include fans or blowers as described above to assist in moving the airflow. 
         [0121]    As shown in  FIG. 11 , after the ambient airflow  11   a  is pulled into the PH2OCP system, it enters the extraction process section  6  and passes through the desiccant rotor wheel  7  as described above. The airflow  11   a  thereby impregnates the desiccant rotor wheel  7  with the water vapor therein, resulting in dry airflow  11   b.  In the embodiment described above in connection with  FIGS. 1-9 , the dry airflow  11   b  then passes through the reactivation heating coils  10  of thermal fluid (which was previously heated in a microwave heating chamber  35 A) so as to heat the dry airflow  11   b.  The heated, dried airflow  11   b  would then pass back through the desiccant rotor wheel  7  to deactivate the desiccant material  8 . The heated, dried airflow  11   b  thereby becomes rehydrated, forming the heated, moisture saturated airflow  11   c.    
         [0122]    However, in the alternative embodiment of  FIG. 11 , the dry airflow  11   b  coming from the desiccant rotor wheel  7  does not pass through reactivation heating coils  11 . Instead, it next passes directly into microwave heating chamber  35 A. As the desiccant rotor wheel  7  rotates through the microwave heating chamber  35 A, the microwave heating chamber  35 A generates microwaves which heat the desiccant material  8  and/or the water held in the desiccant material, thereby deactivating the desiccant material  8 . When the dry airflow  11   b  enters the microwave heating chamber  35 A and passes back through the heated and deactivated section of the desiccant rotor wheel  7 , it picks up the now-released water molecules from the desiccant rotor wheel  7 , thereby rehydrating. Further, due to the microwaves within the microwave heating chamber  35 A, and/or the heat of the water and desiccant rotor wheel  7 , the airflow is, itself, heated. The airflow therefore becomes the same heated, moisture saturated airflow  11   c  when exiting the microwave heating chamber  35 A as is shown exiting the desiccant rotor wheel  7  in  FIG. 2 . The saturated hot airflow  11   c  then moves into the condensation process section  15  as discussed above, and exists as dehumidified, air conditioned airflow  11   d.  As above, the condensation process section  15  may include an air treatment and conditioning system  61  split design incorporating the evaporator cooling coils assembly  14  which is linked to a compressor  59 , condenser coil assembly  58 , exhaust fan and motor assembly  60 , metering valve  64 , and components (not shown). 
         [0123]    Throughout the embodiment shown in  FIGS. 10A ,  10 B and  11 , airflow  11   a - 11   d  may be maintained by means of the same high static direct drive axial type blowers and motor assemblies as were described above in connection with the embodiment shown in  FIGS. 1-9 . 
         [0124]    Although the foregoing description and accompanying drawings relate to specific preferred embodiments of the present invention and specific sub-systems, methods and processes for the PH2OCP system  72  as presently contemplated by the inventor, it will be understood that various modifications, changes and adaptations, may be made without departing in any way from the spirit of the invention.