IONIZATION CHAMBER DESIGNED TO ENHANCE COVALENT BONDING OF ATOMIC ELEMENTS FOR THE RELEASE OF RAW HYDROGEN AND TO ELIMINATE WASTE WATER IN THE PROCESS
An ionization chamber is disclosed that can free ions in water creating polarized atoms of hydrogen and oxygen derived from water in the process. The water can be comprised of non potable waste water. Once the hydrogen and oxygen ions are released, and polarized in the process, the electrons can be aligned such that the end product is the release of hydrogen and the bonding of the oxygen with the free electrons of the other element(s) such as Titanium or Tungsten for example, without high heat or pressure as is normally required. The chamber is comprised of a series of metallic rods, a series of solid nickel mesh plates, a vacuum pump, a dual pulsed D.C. Power supply (from 200-800 VDC pulsed and a low power, −24 VDC pulsed at 400-600 Hz.), a water bath chamber, a ceramic or teflon encapsulated feeder assembly, and an R.F. Pulse generator.
A description of Debye-Hückel theory includes a very detailed discussion of the assumptions and their limitations as well as the mathematical development and applications. A snapshot of a 2-dimensional section of an idealized electrolyte solution as depicted in
In an ideal electrolyte solution the activity coefficients of all the ions are equal to one. Ideality of electrolyte solution can be achieved only in very dilute solutions. Non-ideality of more concentrated solutions arises principally (but not exclusively) because ions of opposite charge attract each other due to electrostatic forces, while ions of the same charge repel each other. In consequence ions are not randomly distributed throughout the solution, as they would be in an ideal solution. By generating a plasma, the charged particles can be controlled and steered in a variety of ways including magnetically.
Activity coefficients of single ions cannot be measured experimentally because an electrolyte solution must contain both positively charged ions and negatively charged ions. Instead, a mean activity coefficient, is defined as (ν). For example, with the electrolyte NaCl ν=(Na+Cl−)1/2 as depicted in
In the present invention a series of shrouded metal rods comprised of the same type of metal are set in a feeder assembly to act as one side (anode side) of an ionic generator wherein the cathode side of the generator is comprised of a like numbered series of perforated solid nickel plates separated by a similar number of solid metal nickel plates that are polarized as neutral. The cathode and anode are charged with a variable 400 to 800 volts D.C. and a pulse generator pulses the signal at or between 400 to 600 Hz utilizing an R.F. modulated signal, where the entire assembly is designed to be submerged in water within a ceramic coated chamber wherein a circulatory pump stirs the liquid in the bottom of the tank, and the solution is passed through a filter which removes unwanted particles and debris, while a vacuum of approximately 15 inches of mercury or in other words about 0.5 atmospheres draws off the subject H2 (hydrogen gasses), or gasses, as depicted in
The process of ionic bonding otherwise known as electrovalent bonding is heretofore a well known process. What has not been practiced in prior teachings is the release of hydrogen gas without a separation bladder to prevent the oxygen (O) gas that has been freed in the plasma process from contaminating the released hydrogen and causing an explosive potential. In fact other teachings show the sequestering of the oxygen product of the electrolysis being sequestrated by various forms of carbon under high heat and under extreme pressure which releases toxic carbon dioxide into the atmosphere in the process, whereas the present teaching does not. In the present invention the highly charged oxygen atoms readily combine with the metal particles of the metal rods to form (in the case of Titanium rods) TiO2.
Titanium Dioxide. TiO2 is commonly used in cosmetics, paints and even some foods for coloration enhancement (more commonly known as Pigment White 6—PW6). The production method of Titanium Dioxide typically is through the use of Ilmenite mixed with sulfuric acid. In this process the Rutile (as it is called) is further refined with pure oxygen or plasma at 1500-2000 degrees K.
In the present teachings the pure Oxygen released in the ionic chamber readily combines with the Titanium atoms and can be easily extracted using a recirculation pump at close to room temperatures. The metal rods can also be comprised of other metals such as Tungsten wherein the Tungsten for example combines with the pure Oxygen to give a resulting Tungsten Trioxide or WO3. This compound is also typically found as a pigment in paints due to its' rich yellow color. WO3 is also used in x-ray screen phosphors as well as fireproofing of fabrics. In recent years WO3 has been used for electrochromic windows or smart windows in an electrically switchable glass when a voltage is applied to tint or occlude the window. WO3 is also used in semiconductor manufacturing for conduction of electrons in a process known as doping. WO3 is typically produced by the use of Hydrochloric acid at temperatures of 1800 degrees K. In the present invention again the WO3 can be drawn off at room temperature with a recirculation pump.
In the present invention the byproduct of the above two examples utilizing tungsten rods and titanium rods is the release of raw pure hydrogen from the process which can be used as fuel for energy or heat in a number of various applications including combustion in a piston type reciprocating or turbine engine.
Claims
1. A means or method for creating an ionic plasma in an aqueous solution comprising an anode comprised of a perforated solid nickel plate and an anode comprised of a perforated nickel plate with an open cathode submerged in a solution. The anode and cathode are driven by a power supply comprising a high voltage positive and negative D.C. supply and further comprising a low voltage pulse modulated RF supply.
2. Wherein the Anode is comprised of insulated rods comprising a bundle of carbon, titanium, or tungsten rods, and the Cathode is comprised of a series of stacked perforated metal plates comprised of solid nickel material.
3. Wherein the said carbon, titanium, or tungsten rods comprising the anode may be replaced as needed by replacement tips fed through a copper encasement sleeve for purposes of ease of replacement of the rods in field applications as is needed from time to time.
4. Wherein the derived ionic mass from the plasma reaction is guided and steered by a set of rotating magnets comprised of both permanent magnetics and electromagnets in a cluster or array.
5. Wherein the said magnets in claim 4 are neodymium magnets and can be rotated or manipulated by a stepper motor.
6. Wherein the said magnets in claims 4, and 5 can be housed in an air-tight housing that is made impervious to the elements found in the ionic mass or aqueous solution.
7. Wherein the aqueous solution is comprised of toxic or non-potable waste water that is purified by the process of ionic separations of the good elements from the bad elements by use of the ionic steering referred to in claims 4, 5, and 6 described herein above.
8. Wherein the aqueous tank is vacuumed and the unwanted waste water and contaminant, debris is removed by a circulation pump attached to the aqueous solution's container at the bottom, and further comprising a waste water filter and or purifier.
9. wherein the system further comprises a vacuum pump at the top of the container to exhaust the gasses and molecular elements that are required to be harvested from the ionic process as a result.
10. wherein the system comprises and operates on a low current battery powered energy supply made possible by the ionic steering of the ionic mass of unwanted waste in the solution by the positioning of the various magnetics of claims 4, 5, and 6 described herein above.
Type: Application
Filed: Apr 26, 2018
Publication Date: Oct 31, 2019
Inventor: Kenneth Stephen Bailey (Pinole, CA)
Application Number: 15/963,603