Abstract:
A method and apparatus for removing the sulfation from the plates of the battery and driving the sulfate crystals back into the electrolyte solution without overheating the battery is presented. The present invention includes a rotary magnetic hub and coil assembly to produces a unique output not found in other charging systems on the market. The battery desulfation method and apparatus of the present invention is self-adjusting to the battery, regardless of voltage and works by removing the sulfate crystals from the plates of lead acid batteries. As a result, the normal life of the average battery may be greatly extended. Heavily sulfated batteries may be brought back to working condition. When used for short durations for healthy batteries, the present invention keeps the sulfate crystals off the plates and in solution to extend the working life of the battery.

Description:
CROSS-REFERENCE TO RELATED APPLICATIONS 
     This application claims the benefit of application Ser. No. 61/600,761, filed on Feb. 20, 2012, entitled METHOD AND APPARATUS FOR BATTERY DESULFATION; and application Ser. No. 13/771,978, filed on Feb. 20, 2013, entitled METHOD AND APPARATUS FOR BATTERY DESULFATION. 
    
    
     FIELD 
     The present invention relates to a method and apparatus for battery conditioning, and more particularly, to a method and apparatus to desulfation lead acid batteries. 
     BACKGROUND 
     Lead acid batteries are a fundamental staple of our modern electrical society, these batteries are found in almost every aspect of our daily lives whether we realize it or not. Lead acid batteries are used in transportation, heavy equipment, telecommunications, computer networking, backup power supplies, alternative energy solutions (a.k.a. solar, wind, and small hydro turbine solutions). 
     As the need to store and have electrical energy ready as demand increases, so does the importance of the battery. Lead acid batteries have been the workhorse of this need for more than a century. One of the problems that arises from the use of these batteries is the sulfation of the lead plates within the battery that limit and ultimately render useless the energy obtainable from them. 
     During use of the battery the sulfuric acid chemical solution electrolyte deposits sulfide crystals on the plates of the battery. As the crystals grow the battery&#39;s output declines sharply, as less and less surface area of the lead plate has the ability to interact with the electrolyte solution. 
     The conventional solution to this build up is to do what is called an equalization charge. This charge is really a controlled over charge of the battery. High amperage and a voltage capable of putting the battery into reverse or charge mode is applied to the battery. This high amperage charging leads to internal heating, which leads to less conduction, which in turn leads to more heating. If not carefully controlled, the battery can enter a thermal runaway effect that overheats the battery and causes excessive off gassing of the electrolyte solution. This situation usually irreversibly damages the battery. 
     Current charging systems basically fall into one of two categories: 1. Standard high amperage regulated voltage charger with trickle charge capacity; 2. Low amperage pulse charge systems with timed charging. 
     Standard high amperage and trickle chargers apply a regulated voltage of sufficient value to put the battery into charge mode and a moderate to high current level to charge the battery. This charge may remove a small amount of the sulfate crystal growth, but it still has the disadvantage of heating the battery, and cannot remove the crystal growth effectively enough to keep the battery from sulfating. 
     Pulse charging attempts to apply a low current voltage with a resonate frequency square wave to the battery in order to induce desulfation without overheating the battery. These charging systems tout the ability to keep a battery from heavy sulfation through the use of a low amperage continuous pulse charge. This system has the distinct disadvantage of having to constantly keep the battery on the charger in order to keep the sulfation process at bay. 
     SUMMARY 
     The method and apparatus of the present invention seeks out and removes the sulfation from the plates of the battery and drives it back into the electrolyte solution without overheating the battery. The present invention includes a rotary magnetic hub and coil assembly to produces a unique output not found in other charging systems on the market. 
     The battery desulfation method and apparatus of the present invention is self-adjusting to the battery, regardless of voltage (6V, 12V, 24V, 36V, 48V, etc.) and works by removing the sulfate crystals from the plates of lead acid batteries. As a result, the normal life of the average battery may be greatly extended. Heavily sulfated batteries may be brought back to working condition. When used for short durations for healthy batteries, the present invention keeps the sulfate crystals off the plates and in solution to extend the working life of the battery. 
    
    
     
       DESCRIPTION OF THE DRAWINGS 
         FIG. 1  is a functional block diagram of the apparatus of the present invention. 
         FIG. 2  is an illustration of the desulfation process of the present invention. 
         FIG. 3  is an illustration of the nonlinear magnetic arrangement of coils with the magnetic poles of the rotating magnetic hub. 
         FIG. 4  is a double magnetic impulse output waveform from rectifier circuits. 
     
    
    
     DETAILED DESCRIPTION 
     As required, detailed embodiments of the present invention are disclosed herein. However, it is to be understood that the disclosed embodiments are merely exemplary of the invention that may be embodied in various and alternative forms. The figures are not necessarily to scale; some features may be exaggerated or minimized to show details of particular components. Therefore, specific structural and functional details disclosed herein are not to be interpreted as limiting, but merely as a representative basis for the claims and/or as a representative basis for teaching one skilled in the art to variously employ the present invention. 
     Moreover, except where otherwise expressly indicated, all numerical quantities in this description and in the claims are to be understood as modified by the word “about” in describing the broader scope of this invention. Practice within the numerical limits stated is generally preferred. Also, unless expressly stated to the contrary, the description of a group or class of materials as suitable or preferred for a given purpose in connection with the invention implies that mixtures or combinations of any two or more members of the group or class may be equally suitable or preferred. 
     Referring to the  FIG. 1 , the desulfation apparatus of the present invention is generally indicated by reference numeral  100 . The desulfation apparatus  100  includes an electric motor  3 , a weighted flywheel  4 , two drive belts  5  and  14 , and two pulleys  6  and  7 , two rotating magnetic hubs  10  and  11  with 48 magnetic poles each, one 30-pole stator  12  wound with copper wire around independent, insulated ferrous cores, a one 36 pole coil assembly  13  wound with copper wire around independent, insulated ferrous cores, a variable transformer  1 , and three DC rectifier electrical circuits  2 ,  16  and  17 . 
     The AC variable transformer  1  receives input power from a standard wall outlet of 115-120V AC at 20 Amperes power through a switch and varies the power input from zero to 160V AC with up to 20 amps output. 
     The variable transformer  1  output is rectified through a rectifier circuit  2  into a DC voltage output and coupled to a 3HP 170V DC motor  3 , for example. The rotor of the DC motor  3  is coupled to the weighted flywheel pulley  4  that is coupled to the shaft  8  of a first rotor  10  by means of a belt drive  5  and pulley  6 . 
     Pulley  6  is a double pulley with one pulley receiving belt  5  from the motor&#39;s weighted flywheel  4  and the other pulley receiving belt  14  to transfer mechanical rotation to a shaft  9  of a second rotor  11 . Shaft  9  is coupled to a 4:1 pulley  7  for receiving mechanical rotation from shaft  8  via belt  14 . Thus, the second rotor  11  has a 4-times greater torque ratio than the first rotor  10 . 
     The variable transformer  1  may be used to control the speed of rotation of the first rotor  10  and second rotor  11  for the purpose of generating electricity from a first stator  12  and second stator  13 . The electricity produced by the rotating of the first rotor  10  magnetic hub and the second rotor  11  magnetic hub and the first stator coil assembly  12  and the second stator coil assembly  13  is sent through wiring harness  25  and wiring harness  15  to rectifier circuit  17  and rectifier circuit  16  and then to battery  21  and battery  20 . The first stator coil assembly  12  includes a group of 30 coils. These coils generate electricity by the rotation of first rotor magnetic hub  10 . The magnetic rotor hub  10  includes 48 magnets. 
     The first stator coil assembly  12  is wired into five phases, each with six coils in a star configuration. These coils are electrically connected but are not magnetically phased with a ferrous metal like most generators. The magnetic flux does not completely saturate the core for flux containment. 
     The output of rotor  10  and stator coil  12  through rectifier circuit  17  is coupled to battery  21  to put the battery in charge mode. The output power of the stator coil  12  is fixed, however the voltage output is configured to allow it to float up and down from 0 to 600 volts, for example, to match the battery voltage in order to go into reverse mode and charge the battery. As a result, a heavily sulfated battery usually requires a higher voltage than normal to begin the desulfation process and a lower current, which may range from 0 to 4 amps, for example. 
     After a period of time, typically 10 to 20 minutes, for example, the battery  21  is disconnected from stator coil  12  and connected to stator coil  13 . Stator coil  13  is a 36 coil assembly and rotor  11  has a 48 pole magnetic hub. As with stator coil  12 , more magnetic poles exist than stator coil poles. However, unlike stator coil  12 , stator coil  13  is arranged into 6 parallel groups of 3 phase 2 pole assemblies. This arrangement provides a second stage in the desulfation process. 
     After the sulfate has been forcibly removed from the lead plates, the battery will be able to accept and retain much more current when under charge. The stator coil  13  provides a much larger amount of current to the battery  20  to charge the battery, up to 18 amps, for example. 
     This setup creates a nonlinear arrangement where three of the six coils in each phase are slightly misaligned with the magnetic poles of the rotating first magnetic hub  10  ( FIG. 3 ). The result is a double magnetic impulse wave that travels longitudinally with the AC voltage wave ( FIG. 4 ). This AC voltage is rectified  17  and sent to battery  21 . The double impulse longitudinal magnetic wave continues to battery  21  along with the DC voltage from the stator coil assembly  13 . 
     While the AC voltage produced is rectified to DC voltage through the rectifier circuit  17  the magnetic wave continues at a rate of approximately 1.43 kHz, with a setting of 110V AC output from the variable transformer  1 . The higher the output voltage from the variable transformer  1 , the higher the rotation speed of the DC motor  3 , and thus the higher the magnetic wave output frequency generated. 
     This frequency was measured at the battery terminals themselves. Although an oscilloscope will show only a DC voltage signal with some associated noise, frequency counters and spectrum analysis reveal the super imposed magnetic wave component frequency. It is the combination of this DC voltage potential and the underlying super imposed magnetic wave that accomplishes the desulfation work inside the battery as described. 
     As the speed of the rotation determines the power output, and the power output is fixed due to the magnetic flux of the rotor and stator coil assemblies, it is common for open load voltage to be 200 to 600 volts or more in stage  1  when no current flow is present. When presented with a load (battery), the voltage drops to accommodate the internal resistance of the load (battery) and the current increases from 0 to 18 amps for example, based on the load resistance. The internal resistance (impedance) of the load determines the current output. In this manner, the output changes as the battery resistance changes (lowers). Because the current is minimal during the reconditioning process, the battery chemistry does not heat excessively. As the reconditioning process continues, the resistance (impedance) continues to lower, reducing the electromotive action of the voltage potential and increasing the current absorption rate of the battery. A higher than normal resistance in the battery reduces the current flow and increases the voltage applied to the battery. 
     A sulfated battery plate represents a higher than normal resistance value inside a lead acid battery. As the sulfate crystals accumulate on the lead plates less and less surface area is exposed to the electrolyte. This action limits the ability of the battery&#39;s chemistry to produce electrical power and current flow. 
     Referring to  FIG. 2 , a cross-section of a lead acid battery  21  is illustrated. Sulfate crystals  31  form on the lead plates  22  and  23  inside the battery  21 . This action tends to create additional electrical resistance in a typical lead acid battery. The output of the first rotor  10  and first stator coil assembly  12  through rectifier circuit  17  comes into battery  21  through its post terminals to put the battery into charge mode. 
     The output from the first stator assembly  12  has a fixed amount of power it can provide, however, the voltage output is configured in such a way as to allow it to float up and down to match what the battery needs to go into reverse mode and charge. 
     As a result, heavily sulfated batteries will begin the process with a higher voltage than normal, but less current. The voltage, when applied to the lead plates  22  and  23 , will cause negative ions  26  to accumulate behind the sulfate crystals  31  creating an outward electromotive force  28  as the electrons seek out weak areas in the sulfate crystals  31  in order to follow the magnetic wave  27  through the electrolyte  24 . As the sulfate crystals  31  breakaway from the lead plate  22 , the overall battery resistance drops, resulting in a drop of the applied voltage and a rise in the applied current flow. This process continues until normal operating levels are achieved. 
     After a period of time, typically 10 to 20 minutes, the battery is moved or automatically switched from the first stator coil assembly  12  to receive power from the second stator coil assembly  13 . The switching may be accomplished with a timer or with a switching relay based on the voltage or current applied to the battery. The second stator coil assembly  13  is a 36-coil assembly with the second rotor  11  being a 48 pole magnet hub. As with the first stator assembly  12  more magnetic poles exist than stator coil poles. However, unlike the first stator assembly  12  with 5 phases consisting of three offset magnetic poles and three phase oriented poles for a total of 30 stator poles, the second stator assembly  13  is wired into six parallel groups of three-phase 2 pole assemblies. This arrangement is designed to act as a second stage in the process. 
     After the sulfate has been forcefully removed from the lead plates  22 , the battery will be able to accept and retain much more current when under charge. The second stator coil assembly  13  provides a much larger amount of amperage to the battery for that purpose. 
     It is to be understood that while certain now preferred forms of this invention have been illustrated and described, it is not limited thereto except insofar as such limitations are included in the following claims.