WO2015005921A1

WO2015005921A1 - Multifactorial hydrogen reactor

Info

Publication number: WO2015005921A1
Application number: PCT/US2013/050031
Authority: WO
Inventors: Konstantin BALAKIRYAN; Hakop AGANYAN
Original assignee: Balakiryan Konstantin; Aganyan Hakop
Priority date: 2013-07-11
Filing date: 2013-07-11
Publication date: 2015-01-15

Abstract

The present invention provides multifactorial hydrogen reactor with elevated hydrogen production due to complex set of sixteen (16) physical and chemical processes, acting simultaneously on the hydrogen bonds in aqueous solutions of electrolytes. This is achieved due to the process, which takes place in forty two (42) distributed volumes of hydrogen reactor under the effect of the electro-hydraulic shock, which forms local micro-cavities with pressures in the hundreds of thousands of atmospheres and a temperature of several thousand degrees (plasma). Frontline water wave pressure passing through electrolyzer's electrodes creates in micro-environment infrasonic, sonic, and ultrasonic vibrations that, along with the heat, ultrasound and hydrodynamic cavitation, turbulence, high-pressure, chemical catalysts, light energy, electrostatic and electromagnetic fields, dramatically increases decomposition process of water molecules. Simultaneously, electro-hydraulic shock destroys the oxide film, allowing the oxidation reaction of reactive metals to continue continually; reactive metals, from which plates of electrolyzer are made, are part of the hydrogen reactor.

Description

MULTIFACTORIAL HYDROGEN REACTOR

BACKGROUND OF THE INTENTION Field of the Invention.

The present invention relates to a hydrogen reactor, and, more particularly to a multifactorial hydrogen reactor for use in the mtemal combustion engines for improving the fuel efficiency and performance thereof and production of the electricity. Description of the Related Art.

Hydrogen is the most promising energy source first of all, because it is the most abundant element in the universe. Furthermore, as is known, the combustion of hydrogen produces water again.

Expectmg that the gas mixture obtained in dissociation of water may have a different purpose we provide modern methods of separation and purification of gases, including mixtures of gas separation technology, based on the action of a special kind of barriers (membranes) possessing selective permeability properties of the gas mixture components.

As the material presented herein, the hydrogen reactor combines two processes - electrolysis produces hydrogen-oxygen mixture (Brown's Gas) and oxidation reaction product of which is hydrogen. Therefore, there are two types of consumers - diesel or petrol engine, for which gas mixture and storage are preferable, which for technological and safety reasons requires pure hydrogen.

The problem of decomposition water molecules to produce hydrogen for using as a substitute for fossil fuels and the following transformation to all existing forms of energy: mechanical, electrical, light, electromagnetic, which is the main source of existence of our civilization for more than a few decades and is a focus of the world of science.

In order to break the hydrogen bonds in water and aqueous solutions, researchers are using all kinds of physical and chemical processes. In our opinion, the most accessible and popular way to produce hydrogen is electrolysis and oxidation of reactive metals. For all its merits electrolysis has one major drawback - a relatively high energy-consuming. As is known mass of one gram equivalent of hydrogen - 1 g (1/2 mole), which corresponds to the volume of 11.2 liters fSTP). The weight of one gram equivalent of oxygen - 8 grams (1/4 mole), which corresponds to volume 5.6 liters (STP). Consequently, the passage of 96485 C charge is allocated 11.2 liters + 5.6 L = 16.8 liters of Brown's gas, and thus to obtain it the unit cost of electricity (charge) will be 96485 C: 16.8 liters = 5743 C/i.

Many researchers have tried to solve the task of reducing energy costs:

EP0103656A3, Resonant Cavity for Hydrogen Generator, Inventors: Stenley Meyer; Publication date: Aug 22, 1984.

US 5,089, 107 Bi-polar autoelectric hydrogen generator; Inventors: Francisco Pacheco;

Publication date: 02/18/1992.

WO2012054842 A2, Enhanced water electrolysis apparatus and methods for hydrogen generation and other applications; Inventors: Michael Lockhart; Publication date: Apr 26, 2012. In an effort to increase efficiency in the production of hydrogen in the electrolysis cells have been used a variety of approaches, w^rhere the relative success achieved either through design changes, or due to a combination of electrolysis with other methods of exposure to hydrogen bonds.

However, until now, results obtained in the aforementioned patents not widespread, because they are energy- intensive and failed to become model for the industrial mass production of hydrogen. Only shown in this application hydrogen reactor, in which energy costs for electrolysis compensated by a parallel reaction can solve the problem of an unlimited hydrogen production at a price of 90 cents per 1 kg, which is 3-4 times lower than existing today in the world prices for hydrogen.

US 8,075,748 B2, Electrolytic cell and method of use thereof; Inventors: Roy E. McAlister; Publication date: Dec 13, 201 1.

This patent proposed an electrolytic cell, comprising a tight vessel, electrodes, electric current source in electrical contact with the electrodes, electrolyte, and gas. Wherein this gas formed during the electrolysis at the first electrode or near; while cell is provided with a separator, which has an inclined surface, and includes an electrode to be able to direct the flow of the electrolyte and the gas by the difference between the density of the electrolyte and the total density of the electrolyte and the gas, so that the gas is moved toward the second electrode. The advantage of the hydrogen reactor over the proposed electro-lytic cell lies in the fact that instead of one-electrolysis process, sixteen (16) factors used accelatrating hydrogen production process.

US 7922878 B2, Electrohydrogenic reactor for hydrogen gas production; Inventors: Bruce Logan; Publication date: Apr 12, 2011.

US 200600114 1 Al , Bio-electrochemically assisted microbial reactor that generates hydrogen gas and methods of generating hydrogen gas. Inventors: Stephen Grot, Bruce Logan; Publication date: Jan 19, 2006.

The process of oxidation of reactive metals, particularly relatively cheap aluminum devoted subject of hundreds of studies. Among them, the most interesting patents and scientific papers: EP 1301433 A 1, Hydrogen production from aluminum water and sodium hydroxide.

Inventor: Andersen Erling Reidar; Apr. 16, 2003;

Hydrogen Generation by Accelerating Aluminum Corrosion in Water with Alumina, World Academy of Science, Engineering and Technology 55, 2011, Inventors: J. Skrovan, A. Alfantazi, and T. Troczynski.

Activation of aluminum metal to evolve hydrogen from water, Int. J. Hydrogen Energy, 33 (2008) 3073-3076, inventors: A. V. Parmuzina O. V. ravchenko.

None of the methods proposed in the aforementioned patents and scientific papers, including all known chemical dissolution reaction of the oxide film does not make a continuous oxidation reaction of hydrogen. While production of hydrogen by aluminum would help revolutionize the energy sector, if the oxidation process was not so brief and not stopped at the appearance of the oxide film on the surface of reagent; where the oxide film must be removed continuously until the total oxidation of aluminum participating in the reaction. In practice, the oxide film is removed amalgamation or hot solutions of alkali, however, the chemical process to be interrupted or use other reagents in the oxidation of aluminum, often highly toxic such as mercury chloride. In the represented here hydrogen reactor the oxide the film is continuously is removed under the action of a series of electro of hydraulic shock.

We conducted a patent search to a depth of 50 years and unfortunately found no methods or devices that would make the process of hydrogen production cost and scale that can be the foundation of future hydrogen energy. However, this search has allowed us to define the priorities in choosing the physical and chemical processes that, while the impact on the water

3

SUBSTITUTE SEIEET (RULE 26) molecules will be able to break tire hydrogen bonds splitting Ή2Ο" on the Ή2" and "O", necessary to humanity.

Here is a list of physical processes that we are interested in, and links to scientific papers and patents that study these processes: Electrolysis.

Electrolysis of water is the most well-known and well-researched method of hydrogen production. It provides the pure product (99,6-99,9% H2) in one process step. However, the cost of electricity for production of hydrogen is approximately 85.5%; thus making existing methods for producing hydrogen via electrolysis uneconomical.

US Patent US830891 S B2, Hydrogen generator; Inventors: Jae Hyoung Gil Jae Hyuk Jang Chang Ryul JUNG.

US 20080245673 Al; Hydrogen generation system; Inventors: Asoke Chandra Das Chaklader, Debabrata Ghosh, Zhaolfn Tang, Zhong Xia.

US 8282812 B2; Apparatus for producing hydrogen from salt water by electrolysis; Inventors: John Christopher Buitcli.

US 7922781 B2, Hydrogen generation apparatus and method for using same; Inventor: Anand S. Chellappa, Michael Roy Powell, Charles J. Call.

US 8075958 B2; Methods for providing thin hydrogen separation membranes and associated uses; Inventor: Anand Chellappa, Thomas R. Vencill, W. Doyle Miller.

US 20130105307A1 ;Hydrogen and oxygen generator Inventor: Dejan Pavlovich, Nenad Pavlovic, Oct 31, 2012.

None of the above works were able to make production of hydrogen be cost-effective i.e.

recommend it for industrial production; only our hydrogen reactor was able to solve this problem due to combination of new methods and technology solutions.

Production of hydrogen with aluminum.

To produce hydrogen from water can be considered a method of "crowding out" of hydrogen from w^rater by active metals and alloys. Among the most promising of these metals is aluminum which is capable of radically solving this problem. Therefore, aluminum has become the primary active metal in our hydrogen reactor.

U.S. Patent 6,440,385; Hydrogen generation from water split reaction; August 27, 2002;

Inventors: Asok CD. Chaklader; Assignee: The University of British Columbia.

Attempts to generate hydrogen from water on demand by water decomposition reaction have been partly successful in some newer developments, which have been disclosed in these patents. Aluminum was used to generate hydrogen from water, but is not very efficient, as this method requires large concentration of other materials in Al to accomplish the water split reaction. The advantage of our hydrogen reactor compared with tw o above-mentioned patents is that in our reactor there are no other reactants and reaction products but only hydrogen and oxygen. U.S. Patent 4,308,248; Material and method to dissociate water; December 29, 1981 ; Inventor: Eugene . Anderson; Assignee: Horizon Manufacturing Corporation.

U.S. Patent 7,144,567; Renewable energy carrier system and method; December 5, 2006;

Inventor: Erling Jim Andersen.

Aluminum is a veiy promising raw material for the production of hydrogen: it is cheap, very common on the planet and is very active oxidized in water; however, as has been shown above, oxidation process is stopped once the appearance of the oxide film on its surface, which makes it possible to use aluminum for food dishes and is unsuitable for continuous hydrogen. None of the foregoing patents have a data that anyone in the world succeeded with minimal cost (less than 1 kW/h) in making the oxidation of aluminum continuous. For the first time in the world such a result was achieved in our hydrogen reactor.

Cavitation.

Cavitation is the formation of cavities in the liquid (cavitation bubbles) filled with gas, vapor or a mixture thereof. Cavitation is the result of local reduction of pressure in the fluid, which can occur either by increasing its velocity (hydrodynamic cavitation), or in the passage of acoustic waves of high intensity during the half-life (acoustic cavitation).

Cavitation process in our hydrogen reactor occurs when the frontal water wave of the electro- hydraulic shock passes through the holes in the electrolyzer's electrodes. US 6719817 Bl; Cavitation hydrogen generator; Apr 13, 2004, Inventor: Daniel J Marin.

US 20120058405A1; Cavitation assisted sonochemical hydrogen production system; Mar 8, 2012, hiventors: Jenifer Jeong, et.el.

Laborde JL (1998), Acoustic cavitation field prediction at low and high frequency ultrasounds. The patents cited above strongly support effectiveness of the impact of acoustic cavitation process for hydrogen production. However, it requires energy to power the generator producing electrical impulses applied to the acoustic tr ansducers (piezoelectric or magnetostrictfve).

The advantage of our hydrogen reactor is that cavitation therein is a byproduct of the electro- hydraulic shock aimed at removing the oxide film and the effect of the shock wave, which passes through the holes of the electrodes creates a powerful cavitation effect.

Sound vibrations: sound, infrasound, uitrasound, hypersound.

A person's hearing can perceive frequencies 16 - 18,000 Hz, which are called sound. But the world around us is filled with the sounds that lie above and below this range - infrastructure and ultrasounds. The lower boundary of the ultrasonic range is called the elastic vibrations of a frequency of 18 kHz. The upper limit is determined by the nature of elastic ultrasonic waves which can propagate only on the condition that the wavelength is much greater than the mean free path of the molecules (in gases) and interatomic distances (in liquids and gases), hi gases, the upper limit is "106 kHz, in liquids and solids," 1010 kHz, Typically, the ultrasound is called frequency 106 kHz. The higher frequencies are called hypersound. In many universities in the world in all its sound range is one of the main tools in the study of liquid systems, including the process of rupture of hydrogen bonds.

In our hydrogen reactor, sound in a wide frequency range occurs when shock wave passes through the holes in electrodes forming gas bubbles.

US 5404754; An Ultrasonic detection of high temperature hydrogen attack; hiventors: Weicheng D. Wang.

Ionization.

The ionization of water located in the cells that produce hydrogen is due to the pulsed discharge of electric current, supplied to the electrodes.

US 5 I49407A; Process and apparatus for the production of fuel gas and the enhanced release of thermal energy from such gas; Inventors: Stanley A. Meyer; Publication date Sep 22, 1992. US 5616221A; Electrolytic ionized water producing apparatus; Inventors: Hidemitsu Aoki, et el. The thermal energy.

The decomposition of water molecules in the hydrogen generator is most often due to an increase in rotational kinetic energy of the molecules and the energy of their oscillations. Thermal energy is just the kinetic energy of a molecular scale. Charging energy to increase the kinetic energy of the molecules is a micro hydraulic shocks sent into the liquid medium of the hydrogen reactor.

EP 2433902 Al ; Method and device for producing combustible gas, heat energy, hydrogen and oxygen; Inventors: PartnouYauheni Viktorovich; Publication date Mar 28, 2012. Plasma.

The concept has emerged in the process of our research involves extensive ionization of hydrogen gas in the reactor, and in combination with high pressure and temperature identification with the plasma. Therefore, the works associated with the use of plasma for the decomposition of water molecules were at the center of our attention. In our hydrogen reactor under the impact of electro-hydraulic shock in distributed microscopic fluid generates powerful light emission, the pressure in the tens of thousands of atmospheres and temperatures of several thousand degrees; all of this is certainly a cause and a consequence of plasma formation under the influence of electro-hydraulic shock.

US 20090035619A1 ; Methods and systems of producing molecular hydrogen using a plasma system in combination with an electrical swing adsorption separation system; Inventors: Charles Terrel Adams; Publication date Feb 5, 2009.

Cited above invention is certainly of scientific interest, though created in the "low-temperature plasma" raises questions. Furthermore, unlike the hydrogen reactor, great advantage of which is the fact that its production is a completely environmentally friendly product, in this patent plasma system producing molecular hydrogen in the gas stream along with hydrogen and carbon monoxide. Therefore, only when used for industrial production of hydrogen from our reactor can guarantee global transition to "green" energy technologies.

US 6806651 Bl; High - density plasma source; Inventor: Roman Chistyakov; Pub: Oct.19, 2004 Membrane Technology.

Assuming though that the gas mixture obtained at the decomposition of water may have a different purpose, we have provided methods and advanced separation and purification of gases including mixtures of gas separation technology based on the action of a special kind of barriers (membranes) with the selective property permeability gas mixture components. In the broadest sense, the membrane should be understood as a non-equilibrium system open at the boundaries of different compositions which are supported shared mixture under the influence of various factors (temperature, pressure, gravity or the magnetic field, centrifugal force). Separating capacity of the system depends on the properties of the membrane and separated mixture component properties as well as their interaction. US 20060147763 Al ; Upflow microbial fuel cell (UMFC); Inventors: Largus Angenent, Zhen He; Publication date is Jul 6, 2006.

US 7922781 B2; Hydrogen generation apparatus and method for using same; Inventors: Anand S. Chellappa, Michael Roy Powell, Charles J. Call; Publication date: Apr 12, 2011.

Catalyst.

Most processes in the chemical industry today run using heterogeneous catalysts. Catalyst is a substance that accelerates the rate of a chemical reaction without entering it. In fact among these substances may occur many chemical reactions. As a rule, a catalyst system "tuned" only for one of them. That is each particular catalyst can accelerate only a single process.

During the development of our hydrogen reactor has been used variety of catalysts, including coverage of the platinum group metals, and various composite materials, but aluminum was preferred.

EP 2571805 Al; A process for the production of hydrogen, the sequestration of carbon dioxide and the production of building materials starting from slags and/or industrial ashes; Inventors: Paolo Plescia, Enrico Barbarese, Maurizio Pinna; Publication date: Mar 27, 2013. Turbulence.

Cause of Turbulence in the hydrogen generator may be virtually any external influence directed to the liquid in the cell box.

Each of the frontal water waves propagating inside the hydrogen reactor during the motion loses energy, including passing through holes in electrodes turning in a relatively slow flow of water with a twist, which can be considered the turbulence, which helps to remove the gas bubbles from the surface of the electrodes.

RU2357109C1 ; Apparatus and method for influencing the vortex structures in turbulent air stream; Inventor: Ostrikov Nicholas; 07.1 1 2007.

The electrostatic field.

The electrostatic field inside our hydrogen reactor is created by potential difference voltage (10- 12 volts) supplied to the vessel, where the minus applied to body container and the plus to the lid of the body, which is insulated from the container. The negatively charged hydrogen ions will move toward the positively charged cover, where there is an exit for hydrogen.

Electromagnetic field.

In our hydrogen reactor, under the influence of electro-hydraulic shock occurs the excitation of the weak quasi-static and low-frequency electromagnetic fields. Their nature so far poorly understood, but neglect their influence on the decomposition of w^rater molecules would be unwise.

The light energy.

Well-known fact in science is that the light energy is an effective tool for the decomposition of water molecules. Accordingly, in our hydrogen reactor, the light energy of the plasma arising due to electro hydraulic shock makes a significant contribution to the production of hydrogen.

The use of hydrogen reactor.

The hydrogen reactor of this invention can be used in two main areas:

1. For hydrogen production, followed by compression, storage and transport to the place of consumption in vehicles or pipelines.

2. For the production of electricity with a further transformation of her in all possible forms of energy (mechanical, electromagnetic, sound, light and chemical). In this case, the source of energy is as close to the consumer, allowing the user to save enormous material resources by eliminating the need for costly transmission lines, as well as raising and lowering transformer substations.

Hydrogen is produced by the hydrogen reactor can be as basic fuel for the newly constructed facilities, and optional for the existing ones using fossil fuels (oil, natural gas, coal) for process requiring heat.

In this case, the hydrogen can provide (80-90) % saving primary fuel and dramatically alter the ecological situation in the region by reducing harmful emissions into the atmosphere.

One of the important advantages of hydrogen energetics is that it allows to save the existing energy infrastructure facilities. Thus hydrogen either in pure form or mixed with other fuels can be effectively used in nuclear power plants, solar plants, nuclear aircraft carriers, nuclear-powered ships (civilian or military), nuclear submarines, coal-fired power plants, power plants using natural gas, on diesel power generation plants, biofuels, waste incineration plants, in all the modes of transport: water, rail, road, including freight etc. The market volume of world hydrogen production is estimated at 53-55 million tons in 2013. Asia and the Pacific region is the largest market for about 40% of world production of hydrogen. The region produces about 20 -21 ,000,000 tons of hydrogen per year. In addition, Asia and Pacific region is its largest customer. Europe and Eurasia is the second largest producer followed by North America, which comes third.

Major Benefits of the Hydrogen Reactor of this invention:

1. The main obvious advantage of Hydrogen Reactor is hybrid conversion in internal combustion engines to save on gas.

2. Unlike fossil fuels, hydrogen is produced in Hydrogen Reactor from water. 3. It lowers the consumption and saves on combustion of fuel

4. Hydrogen produced by Hydrogen Reactor doesn't require any storage.

5. It does not require any contained pressure in heavy cylinders like CNG. 6. If hydrogen reactor is used on tmcks and small vehicles there will be a huge increase in fuel savings and fewer trips to gas station.

7. Burning garbage or unbiirned leftovers of garbage has always been a problem for industrial or municipal incinerators. Specific heat of Hydrogen can lower the moisture content from 50% to 30% of unbiirned garbage because hydrogen burns faster and hotter which helps to boost combustion of garbage completely.

8. If Hydrogen Reactor is coupled with solar, it will increase the efficiency of production of hydrogen.

9. Hydrogen Reactor is 100% carbon free technology.

10. Hydrogen Reactor solves and lowers hazardous air pollutants and gas emissions of particulates related to coal and diesel.

11. Hydrogen reactor can work with all types of fuel including Gasoline, Propane, Natural Gas, Coal, Clean Coal, Diesel, Biofuel, Bio diesel, Biomass, Ethanol, Solar, etc.

12. Following fields and sectors that could extremely benefit: Energy sector, automotive industry, home appliances, waste treatment, environment, health, safety, community development etc.

13. Produced hydrogen from Hydrogen Reactor will boost internal combustion engine's performance while preventing smog and damage on engine.

14. People can benefit from the Tax refunds owed to them by law for using green technology.

15. Multi -process Hydrogen Reactor development will bring new discoveries, new products and services to the market.

SUMMARY OF THE INVENTION

It is object of the present invention to provide an improved apparatus for decomposition of into hydrogen and oxygen for use in internal combustion engines and production of the electricity.

It is another object of this invention to create a device that would provide humanity with a sufficient amount of low-cost and environmentally friendly fuel. The present invention provides multifactorial hydrogen reactor with elevated hydrogen production due to complex set of the following sixteen (16) physical and chemical processes, acting simultaneously on the hydrogen bonds in aqueous solutions of electrolytes:

- Electrolysis.

- Production of hydrogen with aluminum.

- Cavitation process in this hydrogen reactor occurs when the frontline water wave of the electro-hydraulic shock waves passes through the holes in the electrolyzer's electrodes.

- Sound vibrations as sound perceived by humans (In the hydrogen reactor, sound in a wide frequency range occurs when shock wave passes through the holes and formation of gas bubbles);

- In this hydrogen reactor, acoustic vibrations of different frequencies: infrasound, sound, ultrasound, hypersound, caused by the passage of the frontline water wave through the holes in the electrolyzer's electrodes 3 & 4.

- Ionization. The ionization of water located in the cells that produce hydrogen is due to the pulsed discharge of electric current, supplied to the electrodes.

- The thermal energy. The decomposition of water molecules in the hydrogen generator is most often due to an increase in rotational kinetic energy of the molecules and the energy of their oscillations. Thermal energy - it's just the kinetic energy of a molecular scale. Charging energy to increase the kinetic energy of the molecules is a electro-hydraulic shocks sent into the liquid medium of the hydrogen reactor.

- Plasma. In our hydrogen reactor under the influence of electro-hydraulic shock in

distributed microscopic fluid generates powerful light emission, the pressure in the tens of thousands of atmospheres and temperatures of several thousand degrees, all of this is certainly a cause and a consequence of plasma formation under the influence of electro hydraulic shock.

- Membrane Technology. Assuming though that the gas mixture obtained at the

decomposition of water may have a different purpose, we have provided methods and advanced separation and purification of gases including mixtures of gas separation technology based on the action of a special kind of barriers (membranes) with the selective property permeability gas mixture components. In the broadest sense, the membrane should be understood a non-equilibrium system open at the boundaries of different compositions which are supported shared mixture under the influence of various factors (temperature, pressure, gravity or the magnetic field, centrifugal force).

Separating capacity of the system depends on the properties of the membrane and separated mixture component properties as well as their interaction.

- Catalysis. Most processes in the chemical industry today run using heterogeneous

catalysts. Catalyst - a substance that accelerates the rate of a chemical reaction without entering it. In fact, among these substances may occur many chemical reactions. As a rule, a catalyst system "tuned" only for one of them. That is, each particular catalyst can accelerate only a single process. During the development of our hydrogen reactor has been used variety of catalysts, including coverage of the platinum group metals, and various composite materials, but titanium was preferred.

- Turbulence. Each of the microwave fronts propagating inside the hydrogen reactor during the motion loses energy, including passing through cavitators turning in a relatively slow flow of water with a twist, which can be considered the turbulence, which helps to remove the gas bubbles from the surface of the electrodes.

- The electrostatic field. The electrostatic field inside our hydrogen reactor is created by potential difference voltage (10-12 volts) supplied to the vessel, where the minus applied to body container and the plus to the lid of the body, which is insulated from the container. The negatively charged hydrogen ions will move toward the positively charged cover, where there is an outlet for hydrogen.

- Electromagnetic field. In the hydrogen reactor, under the influence of electro-hydraulic shock occurring the excitation of the weak quasi-static and low-frequency

electromagnetic fields.

- The light energy. Well-known fact in science is that the light energy is an effective tool for the decomposition of water molecules. Accordingly, in our hydrogen reactor, the light energy of the plasma aroused due to electro-hydraulic shock makes a significant contribution to the production of hydrogen.

This hydrogen reactor, in which energy costs for electrolysis compensated by a parallel reaction can solve the problem of an unlimited hydrogen production at a price of 90 cents per 1 kg, which is 3-4 tunes lower than existing today in the world prices for hydrogen. A) In order to reduce energy costs in our reactor we merged two chemical reactions - exothermic and endothermic - product of which is hydrogen.

These reactions are:

Ai + 2H₂0 -» Ai-OOH + 3/2H₂ + Qi.

In these reactions, Qi and Q2 have the same sequence of magnitude and substantially cancel each other. The heat required for the electrolysis reaction: Ai + 2H2O -» Ai-OOH + 3/2H2 + Qi is obtained by the reaction of the oxidation of aluminum: 2H2O -» 2H2 + 20 - Q2.

The heat required for the electrolysis reaction, which is coming from the oxidation of aluminum is continuously supplied as aluminum oxide film continues to be destroyed by the electro- hydraulic shock. The oxidation of aluminum, produced in the hydrogen reactor, i.e., production of hydrogen, may^¬ be 10-20% greater when bauxite or alum earth are used as a reagents.

B) The oxidation of aluminum in the water would already ensure the production of hydrogen in virtually unlimited quantities, but the oxide film formed on the surface making this route unprofitable.

We have fully solved this problem. The method we used is electro-hydraulic shock effect occurs in liquids such as water, with electric discharge therein, and is an electric explosion in the liquid with substantially instantaneous release of energy at a given point. Number and rate of allocated kinetic and thermal energy in the electric discharge area depends on many factors, including the parameters of the electrical discharge and fluid properties. Electro-hydraulic effect is to generate shock waves in the liquid at her breakdown. Electro-hydraulic shock is a complex set of phenomena. In its first step, lasting microseconds plasma channel is formed at a temperature of 40 000 ⁰ C. The plasma expands at a speed commensurate with the speed of sound in water (1410 m / sec).

This forms the first shock w ave and the cavity filled with hot steam and gas, which gradually completes its expansion, then begins to throb and eventually collapses. As a result occurring decomposition and ionization of molecules in the resulting plasma and concomitant light radiation, shock waves, intense sound waves in a wide frequency range, as well as cavitation and pulsed electromagnetic fields.

In our reactor electro-hydraulic shock is used to remove oxidation film from the aluminum making oxidation of aluminum and production of the hydrogen uninterrupted until all aluminum is oxidized by transforming this momentum into a sequence of low- power pulses distributed to 42 electrodes.

Due to this effect in the hydrogen reactor electro-hydraulic shock on the water molecules is carried out not by the entire volume of the device but in each individual "point." This means that the device creates the so-called local centers of the

decomposition of water molecules.

It is known that phase transitions in water is typical behavior in which first formed in the initial phase the local centers of the next phase. Thus the transition from the liquid water phase is preceded by the formation of local ice nucleation.

In our hydrogen generator is explained by the fact that the local energy centers affects micro-volumes that allows to raise the temperature more precisely, the kinetic energy of the molecules exclusively in the particular microscopic volumes, in which due to the ultra-high pressure and temperature occurs an avalanche process of decomposition.

In general, the phase transition of water is characterized by the formation of local centers of a new phase, so the transition of liquid water to ice proceeded by the formation of local centers of crystallization. C) For the first time in one device - our hydrogen reactor, we were able to combine sixteen different physical-chemical means to affects hydrogen bonding of water molecules. The following table presents the physical and chemical processes that became the means to affect hydrogen bonding of water molecules in a hydrogen reactor created by us.

Thus in the hydrogen reactor we were able to replace energy "swapping" of all the above mention processes with the single pulses, with help of the set of "converters" placed in the reactor would convert to a mechanical, sound, light, electricity and electromagnetic energy.

A special role is played here by the electrostatic field that will cause the dipoles of water molecules rotate in the direction of the electrodes by its poles. A working prototype hydrogen generator is a closed vessel shaped like a parallelepiped made of titanium because the inner sides of the vessel are catalyst for chemical reactions occurring in the reactor.

Body and the electrodes of electrolyzer can also be made of nickel, titanium and PGMs.

Dielectric isolation gasket made of teflon, covers the entire bottom of the device; it can sustain high temperature and is not involved in the process of reaction of the device.

The major parts of the hydrogen reactor are electrolyzer's electrodes, having form of rectangular serpentine spring, perforated aluminum plates, cartridges holding perforated aluminum plates and electro-hydraulic electrodes holder, wherein the electro-hydraulic electrodes holder, having vertical openings/ports and parallelepiped shaped technological rectangular cav ity hollowed out along the diagonal of the body or at an angle of 45 degrees to the bottom surface of the housing, high voltage multipin connectors, dielectric isolation gasket, covering entire floor of the reactor, the thennometer and pressure sensor - indicator Boiler Gauges located on the surface of the cover, high pressure release valve for adjusting die pressure inside of hydrogen reactor, exhaust pipe, is a tube trough which hydrogen is supplied to the consumer, electro-impulse dispenser, which transmits impulses to the electrolyzer's electrodes synchronously through high voltage multipin connectors.

Electrolyzer's electrodes and perforated aluminum plates accelerate the oxidation of aluminum, where electrodes converting the shock waves into the sound vibrations over a wide frequency range. Configuration of electrolyzer's electrodes was determined based on the functional requirements laid down in the hydrogen reactor; electrolyzer's electrodes are made of titanium and perform the functions of actual electrodes, catalysts and cavitators.

Power wire connects to electrolyzer's electrodes, where one of them is anode and the other is cathode.

The intensity of the process according to the laws of Faraday is directly proportional to the amount of electricity flowing through the electrolyte that is current in the circuit. It is obvious that the series connection of the electrodes in accordance with Ohm's law allowed having a maximum current of all the electrodes from the power source. This determined the configuration of the cathode and anode in the form of rectangular serpentine spring.

Electrolyzer's electrodes at the same time are titanium catalysts and cavitators in the cavitation reaction. Since the intensity of the process is directly proportional to the amount of charge passing through the electrolyte than the chosen configuration of electrodes, which consists of seven sections and the series of connections of these sections allows having all electrodes the maximum current from the power source.

Electrolysis in our reactor taking place at the electrodes when the flow of direct electrical current through the electrolyte solution or the molten electrolyte.

The cavitation effect was achieved through holes in the electrolyzer's electrodes, being made of three different diameters: the holes covered the entire surface of the electrodes.

Hydrodynamic cavitation occurs during the passage of the shock wave through the holes of electrolyzer's electrodes providing additional energy, said energy contributes to the breaking of hydrogen bonds, wherein said electrodes are also cavitators in the cavitation reaction;

Acoustic vibrations of different frequencies: infrasound, sound, ultrasound, hypersound, caused by the passage of the frontline water wave through the holes in the electrolyzer's electrodes, said holes covering the entire surface of the electrodes and made in three different diameters: 4, 6 and 8 mm respectively.

The advantage of our hydrogen reactor is that cavitation therein is a byproduct of the electro- shock aimed at removing the oxide film and the effect of the shock wave, which passes through the holes of the electrodes creating a powerful cavitation effect.

In this hydrogen reactor, sound in a wide frequency range occurs when shock waves pass through the holes of the electrodes forming gas bubbles.

This is achieved due to the process, which takes place in forty two distributed volumes of hydrogen reactor under the effect of the electro -hydraulic shocks; which forms local micro- cavities with pressures in the hundreds of thousands of atmospheres and a temperature of several thousand degrees (plasma).

The formation of all processes in the hydrogen reactor contributes by the fact that frontline water wave pressure occurs in forty two (42) distributed micro-volumes due to electro-hydraulic shocks.

Forty two distributed micro-volume achieved by multiplying seven electro-hydraulic electrodes holders by six electrodes inserted into the vertical openings/ports in each of said frames.

Frontline water wave pressure passing through holes in the said electrodes creates in micro- environment the heat, ultrasound, hydrodynamic cavitation, turbulence, high-pressure, chemical catalysts, light energy, electrostatic and electromagnetic fields, i.e. instantaneous release of energy in the empty cavity of the electro-hydraulic device. This process creates due to electronic impulse distributor, where the electrodes create an electro-hydraulic shock.

One of the major works performed by electro-hydraulic shocks in our reactor is that oxide film covering the aluminum plates, brakes by electro-hydraulic shock. Formation of an oxide film on the aluminum surface is a natural process. In our reactor electro-hydraulic shocks disrupt the oxide film allowing continuing uninterrupted oxidation reaction of reactive metals, in this case aluminum. The oxidation of aluminum does not stop or interrupts due to the disruption of the oxide film by electro-hydraulic shocks and therefore, the process continues until the complete oxidation of full volume of the aluminum and thus until the complete release of hydrogen.

Calculations show that for the production of 1 kg of hydrogen requires oxidizing of 9 kg aluminum. Therefore to simplify the calculations of performance reactors, cartridges of hydrogen reactor designed to produce different amounts of hydrogen must have a weight of 9 times, those: (9-18-27-36-45 etc) kg. Or (045-0275-0137 5-00685 etc.) kg.

In our hydrogen reactor, electro-hydraulic shock implemented through electrodes.

In order to avoid "run-off' charge ends of the electrodes having the shape of a hemisphere.

This reactor has six-discharge electrode assembly for alternately inducing electro-hydraulic shock. Petrol engine with 180 hp (134) kW fueled part of the oxygen-hydrogen mixture produced in the hydrogen reactor has a volume of 8 liters per minute in the overall performance of the prototype 30-32 liters per minute.

Pure hydrogen (22-25) liters per minute passed through membrane filters went in the store with a further compression for the intended use. The rotary movement of the cardan shaft of the engine transmitted to the rotor electric power capacity of 120 kW.

Electricity produced redistributed between the consumer and the power system of the hydrogen reactor at a ratio of 1 1: 1 i.e. 110 kW received the consumer, and spent 10 kW to power the pulse generator designed for the implementation of the electro -hydraulic shock and charging battery supply of electrolyzer chain.

Testing of the hydrogen reactor was carried out several series of 10 hours. The products of each series were 1,200 kW / h of electricity 18,000 liters of pure (99.9) of hydrogen under normal conditions. The average value of the costs of the entire series of tests was 2 gallons of gasoline, or about $8, the cost of 20 pounds of aluminum is $ 0.78 x 20 = S 15.6. Thus the production of 1 ,200 kW h of electricity and 18,000 liters of pure (99.9%) of hydrogen under normal conditions, it took $ 23.6. Since liter of hydrogen weighs 0.0899 grams, the total weight of hydrogen produced was 1618.2 grams. Consequently, even a prototype hydrogen reactor can produce hydrogen at $ 0.9 per kilogram and electricity at S0.0183 i.e. by 1.9 percent. Serial produced hydrogen reactors still will be able to reduce the above-mentioned prices are multiplied by 10.

The oxidation of aluminum, produced in the hydrogen reactor, i.e., production of hydrogen, may^¬ be 10-20% greater when bauxite or alum earth are used as a reagents.

The big advantage of the hydrogen generator is the fact that with the help of produced hydrogen can store energy generated by power plants at night and on weekends, as well as renewable energy sources (solar, wind). BRIEF DESCRIPTION OF THE DRAWINGS

The forgoing aspects and many of the attendant advantages of this invention will become more appreciated as the same becomes better understood by reference to the following detailed description, when taken in conjunction with the accompanying drawings, wherein:

FIG. 1 is a schematic top view of the housing body/corpus of the multifunctional hydrogen reactor in accordance with the present invention;

FIG. 2 shows a schematic view of the first electrolyzer's electrode;

FIG. 3 shows a schematic view^r of the second electrolyzer's electrode;

FIG. 4 shows a schematic view of the one of the proposed shapes of gaskets, which are spacing apart two electrodes of the FIG. 2 and FIG. 3; FIG. 5 is a schematic view of the cartridge 5;

FIG. 6 is a schematic side view of electro-hydraulic electrodes holder 6;

FIG. 7 is a schematic side view of the lid/cover of electro-hydraulic electrodes holder 6;

FIG. 8 is a schematic side view of the lid of the multifactorial hydrogen reactor in accordance with the present invention; FIG. 9 is a schematic view of the system of the multifactorial hydrogen reactor in accordance with the present invention.

FIG. 10 is a schematic view of the negative and positive charges of power connected to the electrolyzer's electrodes through housing/corpus of the reactor.

DESCRIPTION OF THE PREFERRED EMBODIMENT

It should be understood that these embodiments are only examples of the many advantageous uses of the innovative teachings herein. In general, statements made in the specification of the present application do not necessarily limit any of the various claimed inventions. Moreover, some statements may apply to some inventive features but not to others. In general, unless otherwise indicated, singular elements may be in the plural and vice versa with no loss of generality.

FIG. 1 - shows a general view of working prototype of Multifactorial hydrogen reactor. The reactor housing/corpus 1 is a closed vessel. It is shaped like a parallelepiped with sides of 24"xl2"x9". If necessary, frame size can be increased proportionally. The reactor housing is made of titanium sheet 3-5mm thick. Its inner walls serve as catalysts in the chemical reactions occurring in the reactor. Dielectric isolation gasket 2 made of teflon thickness min. ¼ ": it covers the entire bottom of the device; it can sustain high temperature and is not involved in the process of reaction of the device.

With reference to Fig. 1 and Fig. 8 the major parts of the hydrogen reactor are power supply, electrolyzer's system including electrodes 3 & 4, perforated aluminum plates 7 and water, cartridges 5, electro -hydraulic electrodes holder 6, dielectric isolation gasket 2, means for electrically connecting the positive and negative electrodes to the to the power source, corpus lid 27, closure 28, tridicator boiler gauges 22, high pressure release valve 23, exhaust pipe 24, high voltage multipin connector 13. electro-impulse dispenser 26. Electrolyzer's electrodes 3 & 4 and perforated aluminum plates 7 accelerate the oxidation of aluminum, where electrodes 3 & 4 converting the shock waves into the sound vibrations over a wide frequency range.

Electrolyzer's electrodes 3 and 4, Fig. 2 and Fig. 3 accordingly, at the same time are aluminum catalysts and cavitators in the cavitation reaction, Electrolyzer is composed of electrodes 3 and 4 put together with gaskets 30, Fig. 4 submerged in the water. Electrodes 3 and 4 made of perforated titanium sheet. Power supplied to the electrodes 3 and 4, where one of them is anode and die other is cadiode. Electrodes 3 and 4 also are catalysts of the aluminum plates 7. Since the intensity of the process is directly proportional to the amount of charge passing through the electrolyte than the chosen configuration of electrodes 3 & 4, which consists of seven sections and the series of connections of these sections allows having all electrodes the maximum current from the power source. The configuration or the geometric shape of the anodes and cathodes are in the shape of a rectangular serpentine spring. Hydrodynamic cavitation occurs during the passage of the shock wave through the holes of electrolyzer's electrodes 3 & 4, where 3 & 4 are cavitators in cavitation process.

These holes covering the entire surface of the electrodes 3 & 4. The holes are made in three different diameters: 4, 6 and 8 mm alternately, covering the entire surface of the electrodes 3 & 4 (see 29, Fig. 2). Prerequisite for intensive decomposition of water molecules is also the clearances between the electrodes 3 & 4. But the process of cavitation occurs due to the main cartridge 5, Fig. 5. Seven cartridges 5 inserted into the cells/openings formed by the shape of electrodes 3 & 4.

Positive voltage is applied on the rod 133, therefore, it must be insulated from the

housing corpus of the reactor; it only contact the electrode 4 - anode, plus; rod 133 passes through the corpus/housing of the reactor w ithout touching it using the dielectric sleeve 134, which is located within the housing. Two nuts 135 fix sleeve 134 from different angles. The diameter of nut 135 is greater than the diameter of sleeve 134. Nuts 135 made from dielectric material. Metal nuts 136 attach wire to the anode (positive). 131 and 132 are the bolts with the nuts. A bolt 132 passes through an opening in the housing; where the bolt head is located inside the reactor; where the bolt head size is 2.5 cm and the entire length of the bolt with its head is 3.6 cm. Bolt 132 does not touch electrode 4 - anode. An electric current provided to a bolt 132 on the outside of the reactor housing via negative wire. Bolt 1 2 supplies a negative charge of electricity to the body of the reactor; from the body a negative charge of electricity supplied to the bolt 131, which is passes through the opening in the housing of the reactor; bolt 131 in contact with the housing of the reactor; bolt 131 is in direct contact with the electrolyzer's electrode 3 - cathode. Thus, electrode 3 having negative charge of electricity is cathode.

The advantage of our hydrogen reactor is that cavitation therein is a byproduct of the electro- hydraulic shock aimed at removing of aluminum oxide film and the effect of the shock wave, which passes through the holes of the electrodes 3 & 4 creating a powerful cavitation effect. In this hydrogen reactor, acoustic vibrations of different frequencies: infrasound, sound, ultrasound, hypersoimd, caused by the passage of the frontline water wave through the holes in the electrolyzer's electrodes 3 & 4. This is achieved due to the process, which takes place in forty two (42-x) distributed volumes of hydrogen reactor under the effect of the electro-hydraulic shocks; which forms local micro-cavities with pressures in the hundreds of thousands of atmospheres and a temperature of several thousand degrees (plasma).

The formation of all processes in the hydrogen reactor contributes by the fact that frontline water wave pressure occurs in forty two (42) distributed micro-volumes of the electro-hydraulic electrodes holder 6 due to electro-hydraulic shocks.

Forty two distributed micro-volume achieved by multiplying seven electro-hydraulic electrodes holder 6 by six electrodes 42-47 inserted in the ports 10A, Fig. 6.

Frontline water wave pressure passing through electrodes - cavitators 3 and 4 it creates microenvironment of subsonic, sonic and ultrasonic vibrations, i.e. instantaneous release of energy in the empty cavity of electro-hydraulic electrodes holder 6. This process creates due to electronic impulse distributor 26, Fig.8, where the electrodes create an electro-hydraulic shock. It causes a complex set of phenomena, which lasts for a microsecond, to form plasma, light emission, shock waves, sound waves, as well as cavitation and pulsed electromagnetic fields.

Infrasonic, sonic, and ultrasonic vibrations that, along with the heat, ultrasound and hydrodynamic cavitation, turbulence, high-pressure, chemical catalysts, light energy, electrostatic and electromagnetic fields, dramatically increases the process decomposition of water molecules.

One of the major works performed by electro-hydraulic shocks is that oxide film covering the aluminum plates 7, Fig. 5, brakes by electro-hydraulic shock. Formation of an oxide film on the aluminum surface is a natural process. Thus, electro-hydraulic shocks disrupt the oxide film to continue the uninterrupted oxidation reaction of reactive metals, in this case aluminum. The oxidation of aluminum does not stop or interrupts due to the disruption of the oxide film by electro-hydraulic shocks and therefore, the process continues until the complete oxidation of full volume of the cartridge and thus until the complete release of hydrogen.

Our hydrogen reactor combines two chemical reactions: exothermic and endothermic, product of which is hydrogen.

Due to all the processes occurring in this reactor: the allocation of light energy, heat, high pressure, ionization of the liquid, the acoustic effect, and cavitation, etc. occurs simultaneously intensive breaking of hydrogen bonds. Parallel exothermic and endothermic reactions occurred in the process of electrolysis. The heat required for the electrolysis reaction: Ai + 2H2O -» Ai-OOH + 3/2H2 + Qi is obtained by the reaction of the oxidation of aluminum: 2H2O -» 2H2 + 20 - Q2. The heat required for the electrolysis reaction, which is coming from the oxidation of aluminum is continuously supplied as aluminum oxide film continues to be destroyed by the electro-hydraulic shock. Fig. 2 shows electrode 3, made of perforated titanium, with thickness 1.5 - 2 mm. Fig. 3 shows electrode 4, made of perforated titanium, with thickness 1.5 - 2 mm. Electrode 3 is the anode, the other electrode 4 is the cathode. The configuration or the geometric shape of the anode and cathode is made in the shape of a rectangular serpentine spring. Titanium catalyst electrode 3 at the same time is the catalyst; it is made of titanium sheet. The cavitation effect is achieved by holes 29, made in three different diameters: 4, 6 and 8 mm alternately, covering the entire surface of the electrodes 3 & 4. Chosen configuration of electrodes 3 & 4 consist of seven sections and the series of connection of these sections. Size and shape of electrodes 4 is made accordingly to be inserted into electrode 3. Distance between electrodes 3 & 4 is 1.5 mm, which is achieved by gasket 30, Fig. 4. Gasket 30 prevents contact between electrodes 3 & 4. Gasket 30 made of dielectric material. Fig. 4 showing suggested shape of gasket 30, but gasket may have any shape. Its thickness is 1.5mm, and it could be made of teflon, ceramic, porcelain, etc. Each section of the cartridge may contain minimum four gaskets. Voltage is supplied to electrodes 3 and 4. Electrolyzer is composed of electrodes 3 and 4 together with gaskets 30, Fig. 4 submerged in the water, where electrode 3, is the anode, and electrode 4 is the cathode. Electrodes 3 and 4 are also cataly st of the aluminum plates 7. Hvdrodynamic cavitation occurs during the passage of the shock wave through the holes of electrolyzer' s electrodes providing additional energy; said energy contributes to the breaking of hydrogen bonds, wherein said electrodes are also caviiators in the cavitation reaction. Thus, through electrodes 3 & 4 the hydrogen reactor implemented electro-hydraulic shock. Configuration of electro lyzer's electrodes 3 & 4 was determined based on the functional requirements laid down in the hydrogen reactor; electrodes 3 &4 are made of Titanium and perform the functions of actual electrodes, catalysts and cavitators.

Acoustic vibrations of different frequencies: infrasound, sound, ultrasound, hypersound, caused by the passage of the frontline w^rater wave through the holes in the electrolyzer' s electrodes 3 and 4, said holes covering the entire surface of the electrodes and made in three different diameters: 4. 6 and 8 mm respectively.

As is known electrolysis - a redox process taking place at the electrodes when the flow of direct electrical current through the electrolyte solution or the molten electrolyte.

FIG. 5 shows the frame 12 of the cartridge 5 made of a dielectric material. The process of cavitation occurs due to the main cartridge 5. This reactor has seven cartridges 5. Frame of the cartridge 5 has 3 sections/chambers: 39, 40 and 41. Each section/chamber carries out its function. Ledges 16 and 48 together create cavities which include perforated aluminum plates 7, which are parallel to each other. Sections/chambers 39 and 41 have four plates 7 each, therefore, each cartridge 5 having eight aluminum plates 7. Four plates 7 to the left and four plates 7 to the right of the electro-hydraulic electrodes holder 6. Six ports/opening 10A with inserted electrodes 42- 47 multiplied by seven sections of electrode 4 inserted into electrode 3, Fig. 2 & 3 create forty two (42) micro-volumes. Electro-hydraulic electrodes holder 6 is inserted in the section'chamber 40 of the cartridge 5 and is located in the middle of the frame 12. Fig. 6 shows six-discharge electrode assembly in the electro-hydraulic electrodes holder 6 for alternately inducing electrohydraulic percussion. This reactor has seven electro-hydraulic electrodes holders 6. Electro-hydraulic electrodes holder 6 is made of a dielectric material. It is in the form of a parallelepiped. It has technological rectangular cavity 11 , which extends across three quarters of the electro-hydraulic electrodes holder 6. Technological rectangular cavity 1 1 hollowed out along the diagonal of the body 8 or at an angle of 45 degrees to the bottom surface of the housing 8. In the body 8 of electro-hydraulic electrodes holder 6 six vertical ports 10A are arranged uniformly from top of the frame, where vertical ports 10B are arranged uniformly from the bottom. They serve as nests for electrodes. Six electrodes inserted at the top and six electrodes at the bottom in each of seven electro-hydraulic electrodes holders 6. Then, all the electrodes are inserted through the lid 31, (see Fig. 7), which is top part of the electro-hydraulic electrodes holder 6.

Synchronicity of the impulse is according to the number of electrodes 42-47, Fig. 6. The whole process continues without interruption because aluminum plates 7 are not covered by the oxidation film. That is, oxidation process occurs but the film gets broken by electro-hydraulic shocks and the plates continue to displace hydrogen from water. The ends of the electrodes 42- 47 working in the hollow cavity 11 should have shape of hemisphere that the charges would not discharge. In this hydrogen reactor electrohydraulic percussions implemented through electrodes 42-47.

Process continues without interruption due to the fact that the aluminum plates 7 are not covered by the oxidation film. Ports 10A and 10B are for electrodes. Length of them changed proportionally along the line of the rectangular cavity 11. Depending on the angle of the rectangular cavity 11, length of the ports 10A, ports 10B and electrodes 42-47 changes. The interelectrode distance (the distance between the heads-up of electrodes) in the center of the rectangular cavity 11 is 1.5 - 2mm. Electrode heads must be semi spherical. Negative wire 21 is connected to all six electrodes installed at the bottom of electro-hydraulic electrodes holder 6 in sequence.

Oxidation process of aluminum occurs, but the oxidation film formed on the aluminum plates 7 gets broken by electro-hydraulic shocks, and therefore, the plates continue to displace hydrogen from water. The whole process continues without interruption because aluminum plates 7 are not covered by the oxidation film due to oxidation film being continuously broken by electro- hydraulic shock.

Due to the electro hydraulic shock formed when submitting an electrical pulse to the electrodes 42-47 and 52-57 of electro-hydraulic frame 6, there is electro-hydraulic effect that accompanied by the formation of plasma and release of light energy, heat, high pressure and ionization of the liquid.

This powerful electro-hydraulic shock disuibuted by forty two (42) electrodes powered by a pulse generator.

FIG. 7 shows the cover/lid 1. It is connected to the body 8 (see Fig. 6). It also has six vertical ports/openings IOC; they are parallel to the openings/ports 10A of the body 8. Electrodes are inserted into these ports. Positive wires 14-19 connected to the electrodes 42-47 (see Fig. 6) and to the bottom pats of the High Voltage Multipin Connector 13. High Voltage Multipin Connector 13 is located in the middle of the cover/lid 31 and serves as high voltage impulse to the electrodes in several microseconds. The electrodes must be made of conductive material. FIG. 8 shows the cover 27 of the reactor's housing/corpus 1 (see Fig. 1). Since a positive charge is applied to the of lid cover of reactor and negative charge is applied on the housing/corpus of the reactor, thus electro-static field occurs, which orders the process of movement of positively and negatively charged ions in different directions. The electromagnetic field is the result of an orderly movement of positively and negatively charged ions. Between the housing/corpus 1 and the lid 27 fitted gas-tight gaskets 100. The thermometer and pressure sensor - indicator Boiler Gauges 22 located on the surface of the cover 27. High Pressure Release V alve 23 for adjusting the pressure inside of hydrogen reactor. Exhaust Pipe 24, is a tube trough w hich hydrogen is supplied to the consumer. On the surface of the cover 27 placed seven top parts of high voltage multipin connectors 13. Said top parts of the high voltage multipin connectors of the lid/cover of the reactor connected to the bottom parts of high voltage multipin connectors located on the lid of the electro-hydraulic electrodes holder. On the cover 27 situated an electro-impulse dispenser 26, which transmits impulses to the electrolyzer's electrodes synchronously through high voltage multipin connectors 13. Impulses supplied simultaneously to all the first electrodes of all seven electro-hydraulic electrodes holders 6; then, to all second and so on until the last electrode. 28 is reactor's closure/latch to seal reactor tightly. Through the electro-impulse dispenser 26 create a powerful shocks by affecting electrodes. Female part of the connector 13 is attached to the lid 27 of reactor; male part of tire connector 13 is attached to the electro-hydraulic electrodes holder 6. Contact wires 32-38 connected to the electro-impulse dispenser 26. FIG. 9 shows is a schematic view of the system of the multifunctional hydrogen reactor in accordance with the present invention.

FIG. 10 shows a schematic view of the negative and positive charges of power connected to the electrolyzer's electrodes through housing/corpus of the reactor. Positive voltage is applied on the rod 133, therefore, it must be insulated from the housing/corpus of the reactor; it only touch the electrode 4 - anode, plus; rod 133 passes through the corpus/housing of the reactor without touching it using the dielectric sleeve 134, which is located within the housing. Two nuts 135 fix sleeve 1 4 from different directions. The diameter of nut 135 is greater than the diameter of sleeve 134. Nuts 135 made from dielectric material. Metal nuts 136 attach wire to the anode (positive). 131 and 132 are the bolts with the nuts. A bolt 132 passes through an opening in the housing; where the bolt head is located inside the reactor; where the bolt head size is 2.5 cm and the entire length of the bolt with its head is 7.6 cm. Bolt 132 does not touch electrode 4 - anode. An electric current provided to a bolt 132 on the outside of the reactor housing via negative wire. Bolt 132 supplies a negative charge of electricity to the body of the reactor; from the body a negative charge of electricity supplied to the bolt 131, which is passes through the opening in the housing of the reactor; bolt 131 in contact with the housing of the reactor; bolt 131 is in direct contact with the electrolyzer's electrode 3 - cathode. Thus, electrode 3 having negative charge of electricity is cathode.

Claims

We claim:

1. A multifactorial hydrogen reactor for generating hydrogen from water decomposition reaction comprising:

a. a housing having the corpus and the lid of the hydrogen reactor assembled together as a closed vessel, wherein the housing of the reactor made of titanium sheet approximately 3 -5mm thick, said housing having shape of a parallelepiped, said housing/corpus having a function as catalyst in generating hydrogen in the reactor; b. electrolysis chamber and electrolyzer located in said electrolysis chamber;

c. spaced apart negative and positive electrodes of electrolyzer;

d. a power source, wherein power is supplied to said electrodes, providing electrical power to the electrolysis cells;

e. electrolyzer's cells formed by the shape of electrolyzer's electrodes;

f said electrolyzer's cells comprising a housing for seven cartridges;

g. seven cartridges inserted into electrolyzer's cells;

h. seven electro-hydraulic electrodes holders inserted into seven cartridges, each

cartridge include only one electro-hydraulic electrodes holder;

i. dielectric isolation gasket, said dielectric isolation gasket covers the entire bottom of the housing of the hydrogen reactor, wherein said dielectric isolation gasket can sustain high temperature and is not involved in the processes of reactions in the reactor;

j. the lid of the hydrogen reactor, wherein a positive charge is applied to the of lid/cover of reactor and negative charge is applied on the housing corpus of the reactor, thus electro-static field occurs, which orders the process of movement of positively and negatively charged ions in different directions, said electromagnetic field in the reactor is the result of an orderly movement of positively and negatively charged ions, wherein negatively charged hydrogen ions will move toward the positively charged cover having an outlet for hydrogen.

2. A multifactorial hydrogen reactor in accordance with claim 1 wherein the lid of the hydrogen reactor comprising: - gas-tight gaskets fitted between the corpus and the its lid of the reactor;

- the thennometer and pressure sensor located on the surface of the lid/cover;

- high pressure release valve for adjusting the pressure inside of hydrogen reactor;

- exhaust pipe for conveying hydrogen to the consumer;

- seven top parts of high voltage multipin connectors, said top parts of the high voltage multipin connectors of the lid/cover of the reactor connected to the bottom parts of high voltage multipin connectors located on the lid of the electro-hydraulic electrodes holder.

- electro-impulse dispenser for transmiting impulses to the electrolyzer's electrodes synchronously through high voltage multipin connectors, said impulses supplied simultaneously to all the first electrodes of all seven electro -hydraulic electrodes holders, then, to all second and so on until the last electrode;

- reactor closures/latches for connecting reactor housing/corpus with the reactors lid/cover to seal reactor tightly;

- the electro-impulse dispenser creates a powerful shocks by affecting electrodes;

- contact wires connected to the electro-impulse dispenser.

A multifactorial hydrogen reactor in accordance with claim 1 wherein the system of electrolyzer comprising:

- two spaced-apart negative and positive electrodes, eight perforated aluminum plates of each of seven cartridges, wherein said electrodes put together with gaskets separating them and eight perforated aluminum plates submerged into the water, said electrodes having a shape of rectangular serpentine spring, said electrodes made of perforated titanium sheet, wherein first electrode having the size and shape allowing the second electrode to be inserted into the first one, wherein two electrodes are spaced-apart due to the size of the separating gaskets between them, wherein the entire surface of said electrodes covered with the holes, said holes made in three different diameters: 4, 6 and 8 mm respectively, wherein there is minimum of four separating gaskets on each surface of the electrodes, said separating gaskets are made of dielectric material and having minimum width of 1.5 mm, said width is a prerequisite for intensive decomposition of water molecules; - said seven cartridges with the eight perforated aluminum plates each inserted into seven cells formed by the electrodes' shape;

- a power supply for supplying power to said electrodes, wherein one of them is anode and the other is cathode;

- said two electrodes also are catalysts in oxidation reaction of the aluminum plates;

- said two electrodes and eight perforated aluminum plates of each cartridge accelerate the oxidation of aluminum and its reaction with water to produce hydrogen;

- parallel exothermic and endothermic reactions occurred in the process of electrolysis, wherein the heat required for the electrolysis reaction: Ai + 2HiO -» Ai-OOH + 3/2H2 + Qi is obtained by the reaction of the oxidation of aluminum: 2 H2O -» 2H2 +- 20 - Q2, said heat required for the electrolysis reaction, which is coming from the oxidation of aluminum, is continuously supplied as aluminum oxide film continues to be destroyed by the electro-hydraulic shock;

- hydrodynamic cavitation occurs during the passage of the shock wave through the holes of electro lyzer's electrodes providing additional energy, said energy contributes to the breaking of hydrogen bonds, w^rherein said electrodes are also cavitators in the cavitation reaction;

- acoustic vibrations of different frequencies: infrasound, sound, ultrasound,

hypersound, caused by the passage of the frontline water wave through the holes in the electrolyzer's electrodes, said holes covering the entire surface of the electrodes and made in three different diameters: 4, 6 and 8 mm respectively;

- frontline water wave pressure passing through holes in the said electrodes creates in micro-environment the heat, ultrasound, hydrodynamic cavitation, turbulence, high- pressure, chemical catalysts, light energy, electrostatic and electromagnetic fields, dramatically increasing the process decomposition of water molecules.

A multifactorial hydrogen reactor in accordance with claim 1 wherein each of seven cartridges comprising:

- frame made of a dielectric material, wherein the process of cavitation occurs due to the seven cartridges, said frame of each cartridge has three sections: two side sections and one center section, wherein two side sections are cavities containing four perforated aluminum plates each;

- all eight aluminum plates arranged parallel to each other;

- central section containing electro-hydraulic electrodes holder;

A multifactorial hydrogen reactor in accordance with claim 1 wherein electro-hydraulic electrodes holder comprising:

- the body of the electro-hydraulic electrodes holder and the lid of the electro-hydraulic electrodes holder, said body connects to the lid by means of the four technological posts of the lid being inserted mto four teclmological openings at the top part of the body respectively;

- wherein the body of electro-hydraulic electrodes holder is made of a dielectric

material, said body having the shape of a parallelepiped, wherein the body of the electro-hydraulic electrodes holder further comprising:

a. one technological rectangular cavity extends across 3/4* of the body of electro- hydraulic electrodes holder, said teclmological rectangular cavity hollowed out along the diagonal of the body of the electro-hydraulic electrodes holder or at an angle of 45 degrees to the bottom surface of the said body;

b. six ports/opening at the top part of the body and six ports/opening at the bottom, said openings are vertical and parallel to each other, wherein length of the ports/openings changing proportionally along the line of the rectangular cavity; c. electrodes are inserted in said ports/openings, wherein six electrodes inserted into the top ports/openings and six electrodes inserted into the bottom ports/openings, wherein six-discharge electrode assembly in the electro4rydraiilic electrodes holder is for alternately inducing electro-hydraulic shock, wherein the electrode heads working in the rectangular cavity should have shapes of hemisphere, thus the charges would not discharge, wherein the distance between the heads-up of electrodes in the center of the rectangular cavity should be 1.5 - 2 mm;

d. six openings of electro-hydraulic electrodes holder with inserted electrodes

multiplied by seven sections of electro lyzer's electrodes with inserted cartridges create forty two (42) micro-volumes; e. minus wire is connected to all six electrodes installed in the openings at the bottom of the body of electro-hydraulic electrodes holder in sequence;

f. in forty two (42) distributed micro-volumes of hydrogen reactor under the effect of the electro-hydraulic shocks forms local micro-cavities with pressures in the hundreds of thousands of atmospheres and a temperature of several thousand degrees, forming plasma;

g. electrodes of the electro-hydraulic electrodes holder implement process of electro- hydraulic shock;

h. oxidation process of aluminum occurs, but the oxidation film formed on the

aluminum plates gets broken by electro-hydraulic shocks, thus, the plates continue to displace hydrogen from water, wherein the whole process continues without interruption until complete oxidation of the aluminum and full release of hydrogen because aluminum plates are not covered by the oxidation film due to oxidation film being continuously broken by electro-hydraulic shocks;

i. wherein due to the electro-hydraulic shock formed when submitting an electrical pulse to the electrodes of electro-hydraulic electrodes holder, there is electro- hydraulic effect that accompanied by the formation of plasma and release of light energy, heat, high pressure and ionization of the liquid;

j. wherein, this powerful electro-hydraulic shock distributed by forty two (42)

electrodes powered by a pulse generator, said forty two distributed micro- volumes achieved by multiplying seven electro-hydraulic electrodes holders inserted into seven cartridges each, wherein said cartridges inserted into seven cells formed by electrolyzer's electrodes by six electrodes in each of seven electro-hydraulic electrodes holders;

k. Due to all the processes occurring in this reactor: the allocation of light energy, heat, high pressure, ionization of the liquid, the acoustic effect, and cavitation, etc. occurs intensive breaking of hydrogen bonds.

- wherein the lid of the electro-hydraulic electrodes holder further comprising; six vertical ports/openings, said ports/openings are parallel to the openings/ports in the body part of the electro-hydraulic electrodes holder; a. electrodes are inserted into these ports/openings, said electrodes are made of conductive material;

b. wires connecting to the electrodes;

c. the bottom part of high voltage multipin connector is located in the middle of the lid, said high voltage multipin connector serves high voltage impulse to the electrodes in several microseconds;

d. technological posts at the bottom pan of the lid for connecting lid to the body of electro-hydraulic electrodes holder;

e. Contact wires, which connected to the electro-impulse dispenser.

A system of electroiyzer of multifactorial hydrogen reactor for generating hydrogen from water decomposition reaction comprising;

a. two spaced-apart negative and positive electrodes, eight perforated aluminum plates of each of seven cartridges, wherein said electrodes put together with gaskets separating them and eight perforated alumimim plates submerged into the water, said electrodes having a shape of rectangular serpentine spring, said electrodes made of perforated titanium sheet, wherein first electrode having the size and shape allowing the second electrode to be inserted into the first one, wherein two electrodes are spaced-apart due to the size of the separating gaskets between them, wherein the entire surface of said electrodes covered with the holes, said holes made in three different diameters: 4, 6 and 8 mm respectively, wherein there is minimum of four separating gaskets on each surface of the electrodes, said separating gaskets are made of dielectric material and having minimum width of 3.8 cm, said width is a prerequisite for intensive decomposition of water molecules;

b. said seven cartridges with the eight perforated aluminum plates each inserted into seven cells formed by the electrodes' shape;

c. a power supply for supplying power to said electrodes, wherein one of them is anode and the other is cathode;

d. said two electrodes also are catalysts in oxidation reaction of the aluminum plates; e. said two electrodes and eight perforated aluminum plates of each cartridge accelerate the oxidation of aluminum and its reaction with water to produce hydrogen; parallel exothermic and endotherniic reactions occurred in the process of electrolysis, wherein the heat required for the electrolysis reaction. Ai + 2H2O -» Ai-OOH + 3/2H2 + Qi is obtained by the reaction of the oxidation of aluminum: 2H?0 -» 2H2 + 20 - Q2, said heat required for the electrolysis reaction, which is coming from the oxidation of aluminum, is continuously supplied as aluminum oxide film continues to be destroyed by the electro-hydraulic shock;

acoustic vibrations of different frequencies: infrasound, sound, ultrasound, hypersound, caused by the passage of the frontline water wave through the holes in the electrolyzer's electrodes, said holes covering the entire surface of the electrodes and made in three different diameters: 4, 6 and 8 mm respectively;

frontline water wave pressure passing through holes in the said electrodes creates in micro-environment the heat, ultrasound, hydrodynamic cavitation, turbulence, high- pressure, chemical catalysts, light energy, electrostatic and electromagnetic fields, dramatically increasing the process decomposition of water molecules.

7. An electro-hydraulic electrodes holder of multifactorial hydrogen reactor for generating hydrogen from water decomposition reaction comprising: the body of the electro-hydraulic electrodes holder and the lid of the electro-hydraulic electrodes holder, said body connects to the lid by means of the four technological posts of the lid being inserted into four technological openings at the top part of the body respectively; wherein the body of electro-hydraulic electrodes holder is made of a dielectric material, said body having the shape of a parallelepiped, wherein the body of the electro-hydraulic electrodes holder further comprising: a. one technological rectangular cavity extends across 3/4^ttl of the body of electro-hydraulic electrodes holder, said technological rectangular cavity hollowed out along the diagonal of the body of the electro-hydraulic electrodes holder or at an angle of 45 degrees to the bottom surface of the said body ;

six ports/opening at the top part of the body and six ports/opening at the bottom, said openings are vertical and parallel to each other, wherein length of the ports/openings changing proportionally along the line of the rectangular cavity;

electrodes are inserted in said ports/openings, wherein six electrodes inserted into the top ports/openings and six electrodes inserted into the bottom ports/openings, wherein six- discharge electrode assembly in the electro-hydraulic electrodes holder is for alternately inducing electro-hydraulic shock, wherein the electrode heads working in the rectangular cavity should have shapes of hemisphere, thus the charges would not discharge, wherein the distance between the heads-up of electrodes in the center of the rectangular cavity should be 1.5 -2 mm;

six openings of electro-hydraulic electrodes holder with inserted electrodes multiplied by seven sections of electrolyzer's electrodes with inserted cartridges create forty two (42) micro-volumes;

minus wire is connected to all six electrodes installed in the openings at the bottom of the body of electro-hydraulic electrodes holder in sequence;

in forty two (42) distributed micro-volumes of hydrogen reactor under the effect of the electro-hydraulic shocks forms local micro-cavities with pressures in the hundreds of thousands of atmospheres and a temperature of several thousand degrees, forming plasma;

electrodes of the electro-hydraulic electrodes holder implement process of electro- hydraulic shock;

oxidation process of aluminum occurs, but the oxidation film formed on the aluminum plates gets broken by electro-hydraulic shocks, thus, the plates continue to displace hydrogen from water, wherein the whole process continues without interruption until complete oxidation of the aluminum and full release of hydrogen because aluminum plates are not covered by the oxidation film due to oxidation film being continuously broken by electro-hydraulic shocks;

wherein due to the electro-hydraulic shock formed when submitting an electrical pulse to the elecfrodes of electro-hydraulic electrodes holder, there is electro-hydraulic effect that accompanied by the formation of plasma and release of light energy, heat, high pressure and ionization of the liquid;

j. wherein, this powerful electro-hydraulic shock distributed by forty two (42) electrodes powered by a pulse generator, said forty two distributed micro-volumes achieved by multiplying seven electro-hydraulic electrodes holders inserted into seven cartridges each, wherein said cartridges inserted into seven cells formed by electrolyzer's electrodes by six electrodes in each of seven electro-hydraulic electrodes holders;

k. Due to all the processes occurring in this reactor: the allocation of light energy, heat, high pressure, ionization of the liquid, the acoustic effect, and cavitation, etc. occurs intensive breaking of hydrogen bonds. wherein the lid of the electro-hydraulic electrodes holder further comprising: six vertical ports/openings, said ports/openings are parallel to the openings/ports in the body part of the electro-hydraulic electrodes holder; a. electrodes are inserted into these ports/openings, said electrodes are made of conductive material;

b. wires connecting to the electrodes;

d. technological posts at the bottom part of the lid for connecting lid to the body of electro- hydraulic electrodes holder;

e. Contact wires, which connected to the electro-impulse dispenser.