David Miles

 Apparatus and method for the production of an acid super oxidation solution and an alkaline solution with independent flows with ORP from aqueous solutions. DESCRIPTION OBJECTIVE OF THE INVENTION The following invention has the purpose of obtaining acid electrolyzed water from a controlled flow and alkaline electrolyzed water from a controlled flow, for the first product the electrolyzed acid water Is used in the diabetic foot treatment obtaining unexpected results of healing in the patients, the application of alkaline electrolyzed water is used widely in diverse health treatments, one of them is the reduction of sugar levels in the blood and these results are obtained with the present invention, that involves the apparatus and method to produce electrolyzed acid water from a controlled flow and alkaline electrolyzed water from a controlled flow, with independent flows from the water solutions, it has the objective of producing acid water from a controlled flow with an oxide reduction potential (ORP with its English initials) of between +1100 mV and +1200 mV and a pH of between 1.5 and 2.9, with stability and shelf life of more than a year. And alkaline electrolyzed water from a controlled flow with a pH between 9.0 – 11.0 and an ORP of between -700 mV to -800 mV with a shelf life of more than a year. From an apparatus that comprehends a catalyzing system of parallel type with two separate flows that are affected by the polarization of the metallic layers that surround them, give off ions that go through a layer of separation of fluids so that when exiting the system a charged flow of positive ions is obtained and another charged with negative ions. BACKROUND The US patent 8,062,500 of the inventor Sumita; Osao (Tokyo-to, JP), a method and apparatus for the electrolytic production of oxide reduction potential of water from aqueous solutions of salts for use in disinfection, sterilization, decontamination, and wound cleaning. The apparatus contains an electrolysis unit that has a cell of three compartments that comprehends a cathode camera, an anode camera, and a saline solution camera between the anode and cathode cameras. Two communicators the membranes separate the three cameras. The central camera includes an entry of fluids flow and the exit and it contains insulating material that guarantees that the potential of continuous tension doesn’t travel through the camera. A supply of water flows through the cathode and the anode cameras in the respective sides of the camera of saline solution. The saline solution flows through the central camera, through the circulation of an aquatic solution previously prepared that contains ionic species, or, alternatively, through the circulation of pure water or an aqueous solution of, for example, aqueous hydrogen chloride and ammonium hydroxide, adding particles surrounded with insulating material a solid electrolyte. The electric current is given to the membranes that separate the communicating cameras, which causes an electrolytic reaction that produces ORP oxidative water (positive) and the reductive (negative). In comparison with the past invention, US8,062,500, our camera presents various significant differences in the process. First, our invention only has two conducts in the system in which the ionic transfer is constant and in both directions, while that in the US8,062, 500 there are three channels in which one works like the donator of electrons or protons towards both flows that act as receptors. On the other hand in our system the electrode and the cell are polarized, which are the metallic walls that function like + or – poles which produce the attraction of the ions, which makes the electron flow continuous, in both directions and through the separating netting: while in the case of the patent US8,062,500 both separation nettings are polarized so that the force of attraction is done over the donating flow of electrons and the electron flow is only in the positive direction towards one of the flows and in negative direction towards the other lateral flow. This is the main difference in the process due to that in our system the ionic transfer is buffed due to the fact that both flows are submitted to both electric poles that makes the ionization capacity of water stronger, strength that gives the product better stability without degrading so much the production materials. The patent US8,323,252, inventors Alimi; Hojabr (Santa Rosa, CA), Gutierrez; Andres (Petaluma, CA) Method for the treatment of skin ulcers with an oxidative reduction potential water solution, a method in the treatment of skin ulcers and the complications related in patients through the administration of an oxidation reduction potential (ORP) of a water solution that is stable during at least 24 hours. This treatment is done with a solution with a pH of around 7.5 with free chlorine residues of 15-35 ppm and a stability of barely 24 hours. One of the products obtained with our electrolysis camera has the same use but better conditions since it doesn’t have residual chlorine and it has a pH of between 2.0-2.5 with a stability of more than a year. The US patent 7,964,068, of Kitaori, et al. in June 21, 2011, mounting electrode-membrane, electrolytic unit using the same apparatus, the electrolytic water of expulsion, and the method of sterilization. This invention gives: a group of electrode-membranes having a first electrode that has the shape of a bar or a cylindrical shape, a diaphragm in the form of a band that covers the periphery of the first electrode, and a second electrode set on a surface of the diaphragm in the form of a band; an electrolytic unit that contains the electrode-membrane group; an apparatus of electrolytic water ejection that contains the electrolytic unit, and a method of sterilization using the electrode-membrane group. This patent permits to obtain ionized water for wound use but doesn’t mention the stability or its parameters, besides that the system to obtain it is based on a system in spiral that surrounds the electrode which reduces the contact surface decreasing the potential of the electrolysis. The US patent 8,298,588 an improved diet supplementation composition and / or therapeutic that comprehends a quantity of an agent of diet supplement and / or therapeutic that has a pH that after the ingest of food or drink that would limit the efficiency of the agent and a sufficient quantity of an additive of alkaline electrolyte is given in combination with the agent to increase the pH of the composition from a level of approximately 8 to approximately 12,5 to increase the use and the function efficiency of the agent, while the composition is in the stomach of the person. The composition of the supplement is designed for the optimum use of an agent of dietary supplement and / or therapeutic when it’s taken orally with food or drink. El Whang (US patent n. Nos- and-), the title stages of the patent that the elimination of acid residues from the body is much greater through the use of alkaline water and alkaline minerals in the form of sodium and potassium bicarbonate additionally, the claims are done to prevent the increase of acidity in diverse systems of the organism through the use of tampons of the blood and to help the pH value of the body from experiencing extreme fluctuations. The toxic acid residues are believed to be the main factor that contributes importantly in some cases of adult degenerates in the body, such as diabetes and renal disease. In the US patent Homack No-, the patent describes and additive for beverages that includes potassium hydroxide and a mix of ions of electrolytes such as the alkaline minerals (sodium, potassium, calcium and magnesium) in diverse ways (hydroxides, chlorides, carbonates, gluconates, bicarbonates, phosphates, sulfates, quelates, di-phosphates, oxides and stearates). Homack additive is said that are useful to increase the normally acid pH of the beverage from a value of 9,5 up to 14,0 in beverages. The previous three patents are about additives designed for the alkalization of different liquids or beverages through the addition of chemical mixes that change the pH of the substances taking it to alkaline levels. Which is beneficial for health, but they forget the ORP levels and other physical-chemical characteristics that can be obtained from the electrolysis of water that not only benefit the health of the person from the pH level, but also from other properties like the solubility hydration and penetration that water can have a structure of molecular cluster the present invention is lower to normal which is between 10-12 molecules of H2O and our invention is between 5-7 molecules. The patent MX-A from inventor Maria Guadalupe Gordillo Camas, Construction of Cameras for the Ionization or Electrolysis with Coaxial System. It involves of an apparatus to do the electrolysis of water and obtain acid water or alkaline that is said to help sick people cleanse of chemicals and acidity. The apparatus is made up of a platinized titanium tube with spokes and bolts, dielectric material lids, separation netting and a platinized cell. The coaxial system consists in introducing a flow of water and another with NaCl solution to the camera so that in its system they are mixed and pass to the electrolysis camera. Obtaining an acid and an alkaline product. The writing is somewhat confusing but there are several differences to identify the present invention. It is mentioned that the tube has spokes to avoid that the membrane sticks to the tube. The present invention doesn’t have spokes, since they are not needed, what it has is a platinized netting stuck to the electrode to increase the contact surface with water and that way increase a little the performance per hour, the netting can be used or not depending of the product desired to be obtained. In the production process of the patent MX- A it is said that this camera for ionization are introduced to the system a flow of water and another a flow of NaCl solution of equal magnitude, that once inside of the lids they are mixed to pass to the electrolysis camera. In our process and apparatus, in the cell the NaCl solution is previously mixed to the water flow to later separate the mixture in two flows that will have the same NaCl content and that way the flows enter the lid, once in the system both flows never mix, leaving the netting of ionic exchange the function of passing the ions produced during the electrolysis. BRIEF DESCRIPTION OF THE FIGURES For a better comprehension of the invention figures of the sequences are shown that the invention comprehends. Figure 1 shows the complete assembly of the electrolysis camera. Figure 2: shows the total components of the apparatus, just as the assembly method. Figure 3: 3 sided diagram of the superior and inferior exterior lids. The indicator (11) is the center of 13 and 14 are deflectors in the form of a non-concentric snail, and (12) is the entry of the fluid. Figure 4: diagram of the interior inferior or superior lids for the division of the flows. (19) Is the top connector, (16) (18) (17) and (19) make up the design of the deflector and regulator of the electrode flow. (Non-concentric snail shape). Figure 5: Shows the smooth platinum electrode. You can see (20) top of the guide of the electrode for symmetric assembly, (21) smooth electrode body, (22) electrode nut that connects. Figure 6: figure of the electrode with netting. You can see (20) top of electrode guide for symmetrical assembly, (21) electrode body with netting, (22) electrode nut that connects. Figure 7: Assembly of the electrode, internal inferior and superior flow conductor with the netting of ionic separation. Figure 8: 71 year old masculine patient treatment. Figure 9: 45 year old masculine patient treatment. DETAILED DESCRIPTION OF THE INVENTION The following invention is made up of the following elements: Electrolysis chamber description The electrolysis camera consists of various pieces assembled that form the apparatus that permits the electrolysis of water, from which products such as acid electrolyzed water of controlled flow through the control are obtained, of the flow, of the conditions like volume, voltage and solids content, to obtain the properties required. The different pieces are designed so that once assembled it gives way to the conformation of an electrolytic camera where the whole production process occurs. The parts that make up this electrolytic camera are, according to how they are seen in figure 1: 1. Superior and inferior exterior flow conductor 2. Plastic O-ring. 3. Superior and inferior interior flow conductor 4. Electrode rod for fastening 5. Electrode 6. Cell 7. Electric contact 8. Fastening nut for electric outlet 9. Plastic wrapping and washer for hermetical sealing 10. Fastening screw 11. Ionic exchange membrane (see figure 7) Parts description. Electrodes: 1. Smooth electrode (figure 5): (figure 2 (5)) regular and smooth titanium cylinder grade 2, which is covered externally, which a layer of metallic material of high conductivity with a metallic rod (figure 2 (4)) on both tips welded perpendicularly in its base to the titanium tube, and on the other extreme ending with a tip with a nut (figure 5 (22)) to fit nuts and washers of fastening. The exits have an inclination of 90º with relation to the flat surface that it is united to, besides that it is concentric with the electrodes cylinder (figure 5 (20)). It’s made up of the same material than the cylinder, the rod’s covering is optional. The electrodes covering can be Platinum or Ruthenium, depending of the type of product to fabricate. If the electrode is covered with platinum, alkaline and acid products can be obtained, while if the covering is based on Ruthenium the electrode will work to obtain acid products only, due to the electric characteristics of Ruthenium. One must take into account that a smooth electrode reduces its contact area so that strong electrolysis are achieved but a little slower in relation to volume of production. Lastly, the protrusion on its near side to the cylinder has a bolt (figure 5 (21)) attached to this, that serves like a guide in the fastening of the flow conductors in the system. 2. Electrode with netting (Figure 6): (figure 2 (5)) smooth and regular cylinder made of grade II Titanium covered with a netting caliber 20 of the same material (figure 6 (21)), which is covered externally, with a layer of metallic material of high conductivity. The metallic netting has the only purpose of increasing the liquid-metal’s contact area. The superior and inferior sides just as the smooth electrode have the same system of rods *figure 6 (4)) with rope (figure 6(22) and bolt (figure 6 (21)) having the same function that in the smooth electrode. Equally for this type of electrode, Platinum or Ruthenium covering can be used depending on what is desired to be produced, taking into account that the netting electrode can process a greater volume of water, for which the speed of production increases, but the electrolysis’ power will decrease a little. The considerations for the covering are the same mentioned in the smooth electrode. Cell (figure 2 (6)) Grade 2 titanium metallic cylinder covered with platinum to be able to have the function of double polarity. Its interior diameter 10-20% greater to the exterior diameter of the electrode and length in a 5-1 proportion with respect to the diameter. In the central part of the frontal border they have a ledge with a nut finish (figure 6 (7)), for fastening through a washer and screw (figure 6(8)). The covering should be interior and exterior. From the interior edge, they have a small ledge where the exterior lids meet. Ionic Exchange membrane: see figure 7 The ionic exchange membrane is made up of a polyethylene base of high density interweaved by waved aspersion, that creates a porous layer with an opening of at least one micra and maximum 5 micras. The plate is very flexible and resistant, so that for its use cylinders or tubes are formed of a diameter slightly higher to the fastening edges diameter of the interior lids (Figure 4(23)). The length is of the linear distance of one of the flat faces of the electrode to the end of the exit’s connection ledge of the contrary extreme of the electrode. Exterior flow conductor, inferior and superior (figure 3): The exterior flow conductors, inferiors or superiors, can only be distinguished by the position, since they are the same in form. These lids are made up of GRASS sanitarium nitrite, with an appropriate design and pecuniary (figure 3). These are of cylindrical form with a diameter the same as the cell’s (figure 3 (11)). They have 2 protruding exits that make up a 180 º angle between the two (figure 3 (12)). In the middle of the circle that makes up the cylinder, there is a cylindrical opening (figure 3 (15)) of sufficient diameter to insert through this opening one of the electrode’s rods (figure2 (4)). This opening is surrounded by a plate of the same material that makes a cylinder that determines the top where the packaging and nuts will fasten that hold the electrode to the lid (figure3 (11)). The conductor’s inferior side has an exterior border that is marked a lower prominence that permits to fit and come to the union between the external diffuser (figure3) and the cell (figure2 (6)). To the center a hole is visible where the rod fits (figure3 (15)) of the electrode (figure2 (5)). This circular hole and of sufficient diameter to hold the end of the electrode (figure2 (4)), it’s surrounded by a cylindrical sheet. The right side of the figure and having like a tangent one of the ends, three non concentric cylindrical sheets are formed. The first and closest to the right end, marks the lid in its inferior part and its smaller diameter marks the lid in its inferior (figure3 (14)). The second sheet (figure3 (13)) has the same origin, but its greater diameter is 1:3 in relation with the interior diameter of the first sheet which generates the first flow conductor (figure3 (14)). The third sheet has the same origin but its greater diameter is the same as the lesser diameter of the second sheet (figure3 (15)). The diameter of the third sheet is designed to touch the exterior diameter of the sheet that surrounds the hole to fit the electrode. This third sheet marks the second flow conductor. In relation to the ends (figure3 (12)) of the external flow conductors these work to communicate the two spaces for flow with the exterior, be it for entry or exit of the same, according to the flow direction. The ends have cylindrical form and go through the first sheet in a way they permit the entry and exit of liquid. Internal flow conductors (figure4). The superior part of the internal conductor is flat to then take conic form but leaning to a side since it isn’t concentric in the interior (figure4). In the inferior part of the conic edge there Is a low prominence that is the border where the ionic separation exchange membrane attaches to the lid through a cloth belt covered with sealing material figure4 (23). In the same way the superior side of the internal flow conductor has an exterior diameter (figure4 (18)) big enough to fit in the external diffuser by its inferior side (figure3 (13)). In this cylindrical part there are two holes, one that is the hole to fit one of the ends of the electrode (figure 4 (16)). This is of the same diameter than the central hole of the exterior lid (figure4 (16)). This one is of the same diameter to the central hole of the exterior lid (figure3 (15)) and is located to the center of the lid, so that when uniting the lids they are aligned. The rest of the area covered by the lid’s circle forms a half moon (figure4 (17) where one of the water flows passes. In the interior side the form of an interior cone-shaped diffusor is seen that ends in the exiting cylinder to hold the electrode and the half-moon of liquid pass. The end is divided in the direction of the half-moon (figure4 (19)), so that the electrodes exit bolt fits here with the purpose that the lids are perfectly aligned. Entry and exit piping: Consisting in a flexible plastic hose and of nutritious grade with an external diameter the same as the interior diameter of the entry and exit conduits of the exterior lids. Assembly of the electrolysis camera Electrode (figure2 (5)) – Internal flow conductor (figure2 (3)) – Separation membrane (figure7). 1. A conduit is made with the separation membrane in a way that it can contain the electrode (figure2 (5)) long and wide. The separation membrane is generally a little longer than the electrode to be able to have a maneuvering margin with the material when assembling. 2. One of the electrode’s connection ends is introduced (figure2 (4)) in an internal flow conductor (figure2 (3)) by its inferior view and until reaching the bolt (figure6 or figure 5 (2)) of the electrode with the top of the cylinder of its lid (figure4 (19)), in a way that the flow conductor stays fixed. 3. The electrode is inserted (figure2 (5)) to the separation membrane and one of the ends is attached to the interior lid positioned previously (figure4 (23)). The fastening is done through a nylon belt covered with sealing material. 4. The second interior conduit is introduced to the contrary side of the electrode to the one already fastened. It is fastened in the same way in the bolt (figure5 or figure6 (20)) of the electrode’s exit in a way that it is fastened and aligned with the lid of the other end (figure4 (19)). The electrode is covered in its totality fastening the second end of the separation netting to the fastening border (figure4 (23)), in a way that the electrode’s body is between both interior lids and covered by the separation netting sealed to the borders of the interior lids and the half-moons that are formed in the interior of the interiors lids with the same orientation. ELECTROLISIS CHAMBER 1. An external flow conduit is fitted (figure2 (1)) in the electrode (figure2 (5)) now covered with the netting and the internal conduits (figure2 (3)) in a way that when introducing the electrode’s exit (figure2 (4)) in the exterior conduit (figure2 (1)), the internal conduit (figure2 (3)) ends up in the inferior part of the external conductor. The conductors should be positioned in a way that the pass in form of half-moon of the interior conduit (figure4 (17)) fits in the internal half-moon that is formed in the exterior conduit (figure3 (13)). To guarantee a hermetic separation between the conduits place a plastic wrapping (O-ring) (figure2 (2)) in the circle that surrounds the connection between the conduits (figure3 (13)). 2. The flow conduits are fastened through pressure enforced by a pair of stainless steel metallic pulley and screw (figure2 (9 and 10)) that are fastened at the exit (figure2 (4)) of the electrode (figure2 (5)) that goes through both flow conduits (figure2 (3 and 1)). To guarantee the hermetic quality of the cell plastic wrappings are used (O-ring) underneath the fastening washer and between the electrode’s exit with the lid to avoid liquid leaks of the system (figure2 (9)). 3. The metallic cell (figure2 (6)) is positioned in a way that the electrode fits in it and until fitting with the exterior conduit (figure 2 (1)) that was already fastened to the electrode (figure2 (5)) and interior conduit (figure 2(3)). To seal the cell with the exterior lid and avoid the exit of fluids from the system. 4 To finish, an external flow conduit is positioned (figure2 (1)) at the covered electrode’s missing end (figure 2 (4 and 5)), under the same conditions that were applied for the flow conductors at the other end. 5. To connect the electrolysis camera to the electric current, one of the contacts is positioned at the lateral exit of the metallic cell (figure2 (7)) which will be fastened through a pair of pulley and screw (figure2 (8)). The second contact is connected at the superior end of the cell equally fastened through a pulley and screw (figure2 (4)). The apparatus is assembled as shown in figure1. PRODUCTION METHOD. WATER PREPARATION. 1. Common drinking water is used and is passed through a filtering system that consists of 2 main phases. Solids filter with a particle size of 5 – 10 micras, to eliminate some salts and strange material. Carbon activated filter to eliminate chlorine, smells and undesired flavor. After this step water with a low salts concentration should be obtained, an ORP of +300 mV and a pH close to 7. 2. Additionally an aqueous solution of NaCl usp is prepared, of at least 2%, that will be used like electrolyzing solution rationing it to the main flow according to the technical problem requirement to solve in finished product. 3. To produce controlled flow acid pH super oxidation water or the alkaline solution of controlled flow with alkaline pH, the electrolysis cell should be fed with two flows of water previously mixed with the electrolyzing solution. The proportion of electrolyzing solution that is mixed to the main flow will vary depending on the electrolysis conditions which are desired and of external factors that affect it, for which reason it could vary between 5 to 35 ml for every 100 ml of water flow. The flows should be continuous, without air bubbles and should have a pressure of at least 8 lb/in2 entering the cell. The maximum pressure will depend of the material with which the piping is made up of and previous connections to the cell. WATER IN THE ELECTROLISIS APARATUS: 1. To perform the electrolysis in a more effective way, it should be aligned in a vertical position. If not the flow pressure should be adjusted to obtain the adequate parameters. 2. The electrolysis cell should be assembled and positioned in a manner that the exit with the contact is in the frontal part and the flow conduits are in a position that the entry and exit of flow 1 is to the right side and flow 2 to the left. 3. The path of flow 1 or exterior is the following: a. Flow 1 or exterior enters the system by the right exit of the external conduit positioned in the inferior part of the system and enter the vault that is formed at the exterior half-moon of the lid. b. This vault gives exit at the conical external side of the inferior conduit for which reason the liquid travels around it. c. When finished the internal lid the liquid will be trapped between the separation membrane and the internal side of the cell, for which reason it will rise in the space formed between these two components along the system. d. When arriving at the superior end of the cell the flow meets another internal conduit and rises through its external face until reaching the other external conduit in the space that is formed in the second and third nitrite sheet. e. Once there, the flow goes to the exit to pass to the next stages of the process. 4. The path of flow 2 is the following: a. Flow 2 or interior passes through the entry to the conductor of external flow on the left side that gives way to the half-moon interior of the driver (conductor). b. Then the flow goes up to the interior lid through the half-moon that forms in its cylindrical part between the external conductor and the internal conductor. This half-moon goes through the conductors and reaches the electrode. c. The flow goes up uniformly around the electrode, but being contained by the separation netting. d. When reaching the superior part of the electrode the liquid is guided through the corresponding cone of the internal conductor, to the half-moon that will guide it to the external conductor that will channel it to its exit. e. When the vault is reached that is made in the internal half-moon of the external conductor the liquid will crash and by pressure is on its way to the exit of the left side that will give exit to the liquid to the corresponding process. 5. Both flows are generated under the application of pressure and should be continuous. 6. The work conditions are the following. a. The entry water shouldn’t have smell or taste and all chlorine that it could contain should be eliminated. b. The electrolysis chamber should be perfectly sealed and shouldn’t have leaks. i. Hermetic seal, through an O-ring the union between the flow conductors and the metallic cell. ii. Pressured sealing in the fastening of the netting to the interior conductors. iii. Pressured sealing in the union of the interior and exterior conductors from each one of the ends of the system. EXAMPLES ELECTROLISIS CHAMBER OPERATION In order to make super oxidation acid water with acid pH with the electrolytic camera, certain characteristics are required in the materials used. 1. The metallic cell shouldn’t have any leaks or breakage in all of its structure. Also the covering should be complete and uniform along the entire piece. 2. The exterior and interior nitrite flow conductors shouldn’t have fissures and all of its forms and prominences should be visible and adequate for the connection of both conductors to the system. 3. The separation netting shouldn’t have fissures or breakage, also that it will be perfectly fastened and sealed to the interior lids. For its better functioning the material of the separation membrane should be permeated during 6 or 7 hours with water flow with a pressure similar to work, so that the cloth of propylene is prepared to induce and aid in making the ionic exchange more efficient. 4. The electrode shouldn’t show cavities on all of its surface and the covering should be complete without splinters. For the acid product a smooth electrode will be used and covered with Ruthenium to improve the potency of the product. 5. The camera should be correctly connected to the contacts that will apply the current. 6. A continuous flow of filtered water and NaCl solution should be guaranteed. FABRICATION METHOD 1. Before the filtered water enters the electrolysis chamber is made to flow with a pressure of approximately 20 lb, to this flow the NaCla solution is added in a proportion of 5-100 to 35 – 100. The pressure will vary according to the requirements of exit of the product and external manufacturing conditions. 2. This water flow and electrolyzing solution, previously mixed, is divided in two equal flows (flow1 and flow2), with an approximate pressure of 10 lb which enter the chamber in its inferior part. Flow 1 enters by the right connection and travels the path previously mentioned, while flow 2 enters by the left connection to do its corresponding travel. 3. Once the flows run in the chamber they are calibrated so that the negative flow (flow1) is greater in a 5-1 ratio than the positive flow (flow2). This is done lowering the areas in the exit conduits until achieving the required proportions and that they water exit volumes remain stable. 4. The electrode and the cell are polarized through the application of direct current through the electrode’s and chamber’s contacts. Being the electrode the negative or cathode and the cell the positive or anode. The potency will vary according the exit parameters that are required and to conditions such as temperature, solids content and water pressure. So that such energy or polarization power should be controllable. 5. The water that runs through flow 1 remains between the cell and the netting of ionic exchange so that it will be in contact with the anode during all its path. In its counterpart flow 2 is in contact with the cathode during the passage in the system. 6. When flow 1 enters the system and contacts the positive pole this one attracts the negative side of the water molecule that in this case is H+. Contrary case to flow 2 in which the electrode would be attracting the positive pole or the H+. 7. Flow 1 will also be under the cathode’s effect so that during its travel the molecule will separate in H+ and OH- maintaining the OH- in flow 1 and passing through the separation membrane the H+ to flow 2. The same effect happens to flow 2 but in contrary direction, this maintains the H+ and gives way to the flow1 through the separation netting the OH-. 8. The exchange rate will depend on the power applied in the cell and electrode, of the reason (rate) of NaCl solution added and on the flow’s speed. 9. The quantity of product obtained will depend mainly of the chamber’s proportions and secondly of the system’s work conditions. 10. The result of the process is in flow2 a solution of acid pH (1.5-3.0) with a high ORP - mV), without free residual chlorine and a high content of chlorides (1600 mg/L), besides other physicochemical characteristics that make it a good disinfectant for many uses in different markets. While that in flow1 an alkaline product will be obtained with a high pH (10-13) and a negative ORP (-800 to -900 mV) besides other characteristics that make it a very strong product for consumption so in order to obtain an adequate alkaline product for consumption, modifications to the process should be done. (Electrode and work conditions) 11. In order to obtain alkaline solution the electrode can be smooth or with netting, depending on the volume that is desired. It will be greater in the electrode with netting. The covering should be strictly of platinum due to that this will guarantee the product is suitable for consumption. 12. In this case the polarity of the cell and the electrode can be maintained like cathode and anode respectively. But it can also be inverted thanks to the double electrical capacity of platinum. So that the result obtained in flows 1 and 2 will depend on this polarization. 13. The entry volume to the system in flows 1 and 2 should be of 3-1. Being the greater by where the alkaline solution will be obtained with a pH of 9-11 and an ORP of between -750 to -800 mV and with physicochemical characteristics that make it adequate for consumption and that give it all of its qualities for use in the health sector. The acid flow that is obtained from this process also has bactericide characteristics, but due to that its parameters are smaller than the previous process it should be applied in lower potency requirement uses. USE EXAMPLES Controlled flow electrolyzed acid water obtained with the previous process has an antiseptic behavior since it has a bactericide function besides having effects in the cellular membrane and tisular tissue. Thanks to the ORP oxide reduction potential makes the microorganisms lose electrons and the capacity to maintain their structure and when absorbing the solution quickly they swell and blow up. For that reason they are applied on tissues damaged by processes: ulcerative, infectious traumatic, ambient exposed wounds etc., where body water could be lost, from the continuity solution, when administering controlled flow electrolyzed acid water the hydrogen bridges are restored which repolarize the tissues which repolarizes the tissues which avoids the dissemination of the infection due to hiperglucemy and to the microbiota that resides on the skin and moves inside the ulcer. Besides that thanks to the process of electrolysis it improves the solutions capacity of cellular hydration and of tissues since it has molecules joined weakly from ionic bridges of high dissociation capacity. On contact it is distributed homogenously without affecting healthy tissues and disinfects modifying the bacterial pH, eradicating microorganisms Gram positive and negative, diminishing fetidness and the injured tissue or necrotic. It removes and eliminates oozes or abscesses when introduced in deep parts. The necrotic tissue and (esfacelado) is oxidized making it of easy removal, degrading the denaturalized fibrin, collagen and elastin. By maintaining the environment humid, it promotes the growth of tissues promoting the (angiogenesis), avoiding drying and aiding the cells hydration. Besides that the apparition of fibroblasts that synthesize collagen is promoted and basic (mucopolisacaridos) for the tissues repair. Due to these characteristics controlled flow electrolyzed acid water can be used in the disinfection of wounds of all type with aerobic or anaerobic bacteria in: Diabetic foot; dry or gaseous gangrene: varicose ulcers, arterials, decubit, neuropathic; (mal perforante plantar); just as in surgically infected wounds. Cell regenerator and infection prevention in burns, viral and bacterial surface wounds. Aids in dermatological treatments against: mycosis, and external skin tuberculosis, acne, atopic and fatty dermatitis, athlete’s foot, feet warts, athlete’s feet and hands, ingrown toenails, (metricetomias). Biological sterilizing for; healing material, surgical instrumentation, operating rooms and medical areas. Modifying the parameters of exit equally can make it have application in fields like the agro food, industrial, veterinarian and others. The bactericide characteristics of controlled flow electrolyzed acid water were tested in the University Center of Exact Sciences and Engineering of the University of Guadalajara, in the Division of Basic Sciences, Department of the Pharmacy, Laboratory of Sanitary Microbiology, where the results shown in the following chart were found: REGISTER CEPA TESTED CONCENTRATION (UFC/ml) TIME TESTED 10 seg 30 seg 60 seg 3 min 5 min 8 min 52014 Enterobacter aerogenes 8.4 x 105     NA   NA NA 52014 Salmonella typhy 7.6 x 106   NA NA NA     52014 Acinetobacter baumannii 2.6 x 105   NA NA NA     52014 Bacillus spp 1.8 x 106   NA NA NA     52014 Klebsiella pneumaniae 6.8 x 106   NA NA NA     52084 Candida albicans 6.8 x 107 NA NA NA       52084 Aspergillus niger 6.1 x 106 NA NA NA       52649 Enterobacter gergoviae 2.4 x 107 ND NA NA       52649 Pseudomona aeruginosa 2.4 x 108 NA NA NA       52649 Salmonella spp 3.2 x 107 NA NA NA       52649 Candida parapsilosis 3.7 x 105 NA NA NA       52649 Lysteria monocytogenes 1.6 x 107 NA NA NA       52649 Enterobacter cloacae 2.2 x 107 NA NA NA       52649 Sthaphylococcus thermophilus 4.6 x 106 NA NA NA       52649 Bacillus cereus 1.6 x 105 NA NA NA       52649 Leuconostc messenteroides 7.1 x 1010 NA NA NA       52649 Lactococcus lactis 7.5 x 107 NA NA NA       52649 Escherichia coli 9.1 x 107 NA NA NA       52649 Staphilococcus aureus 1.2 x 107 NA NA NA       52649 Raoutella terrigena 3.9 x 105 NA NA NA       52649 Vibrio cholerae 7.4 x 105 NA NA NA       52649 Escherichia coli O157:H7 1.3 x 107 NA NA NA       52649 Stenotrophomonas maltophilia 3.5 x 106 NA NA NA       52649 Sacccharomyces cereviciae I 2.7 x 106 NA NA NA       **Results chart of anti microbian effectivity in vitro of the controlled flow electrolized acid solution. University Center of Exact Sciences and Engineering of the University of Guadalajara, in the Division of Basic Sciences Department of the Pharmacology Laboratory of Sanitary Microbiology On the other side the physicochemical characteristics PHYSICOCHEMICAL ANALYSIS PARAMETER RESULT OBTAINED MEXICAN NORM OF ANALISIS NOM-201-SSA1-2002 (maximum permissible limits) Color 1 unit (Pt-Co) NMX-AA-045-SCFI-2001 15 units (Pt-Co) Odor NA NOM-041-SSA1-95 Odorless Flavor NA NOM-041-SSA1-95 Tasteless Turbidity < 1 UTN NMX-AA-038-SCFI-2001 5 U TN Arsenic < 0,002 mg/L NMX-AA-051-SCFI-2001 0,025 mg/L Barium < 0,0098 mg/L NMX-AA-051-SCFI-2001 0,700 mg/L Borium < 0,150 mg/L NMX-AA-051-SCFI-2001 0,300 mg/L Cadmium < 0,0048 NMX-AA-051-SCFI-2001 0,005 mg/L Cyanides < 0,005 NMX-AA-058-SCFI-2001 0,050 mg/L Free Residual Chlorine Not detected NMX-AA-108-SCFI-2001 0,100 mg/L Total Chrome < 0,0052 NMX-AA-051-SCFI-2001 0,050 mg/L Total Coliforms Not detectable NMP/100mL NMX-AA-042-SCFI-1987 < 1,1 N MP/100mL Niguel < 0,012 mg/L NMX-AA-051-SCFI-2001 0,020 mg/L Silver < 0,007 NMX-AA-051-SCFI-2001 0,100 mg/L Nitrates 3,15 mg/L NMX-AA-79-SCFI-2001 10 mg/L Nitrates < 0,010 mg/L NMX-AA-99-SCFI-2001 0,050 mg/L pH < 2,26 units NMX-AA-008-SCFI-2000 6,5 – 8,5 Units Lead < 0,0052 mg/L NMX-AA-051-SCFI-2001 0,010 mg/L Selenium < 0,002 NMX-AA-051-SCFI-2001 0,010 mg/L SAAM < 0,230 mg/L NMX-AA-039-SCFI-2001 0,500 mg/L Total Coliforms Not detectable NMP/10mL NMX-AA-073-SCFI-2001 < 1 N MP/100mL PARTICULAR CONDITIONS PARAMETER RESULT OBTAINED MEXICAN NORM OF ANALISIS Chlorides 1697,6 mg/L NMX-AA-073-SCFI-2001 Mercury <0,0008 mg/L NMX-AA-051-SCFI-2001 Sodium 376,903 mg/L NMX-AA-051-SCFI-2001 Potassium 3,887 NMX-AA-051-SCFI-2001 Calcium 16,662 NMX-AA-051-SCFI-2001 Conductivity 6,29 ms/cm NMX-AA-093-SCFI-2001 Density 0,9989 g/mL The shelf life of controlled flow electrolyzed acid water is one year, this is only achieved when the product is stored in a fresh place and out of direct sunlight reach, since it is photo sensible. Also the container should be complete and adequately closed. Once the container is open the product’s life is reduced to a month due to the loss of effectivity of the electrons or protons depending of the product that is used. All of these characteristics such as: bactericide function, conductivity and oxidation, controlled flow electrolyzed acid water is given the functions of an antiseptic able to aid in the treatment of several wounds thanks to its regenerative capacity, which has been observable in several documented cases following: 71 year old masculine patient, with mellitus diabetic history of 6 years of evolution treated with insulin, hyper tense of 6 years treated with captopril who was presented with a wound caused by a nail, which the surgeon applies a process of (debridacion) and the resulting wound was treated with a double dose of antibiotics and healing done by applying controlled flow electrolyzed acid water every 8 hours. The results are shown in figure 8. 45 year old masculine patient with non-controlled diabetic mellitus clinical history that was presented with an infected wound that is treated with antibiotics and submitted to a process of (debridation). The resulting wound was submitted to healing based on applying controlled flow electrolyzed water every 8 hours. The results are shown in figure 9. On another note, controlled flow electrolyzed alkaline water is water modified in its physicochemical properties that changes the structure of the molecular bunch, pH, free oxygen content, conductivity, ionic chlorides, among others, it has several impacts in the human organism if its consumption is frequent in a proportion of approximately 200 ml every day for every kg of body weight. Some of the beneficial effects of controlled flow electrolyzed water is thanks to its characteristics that neutralize waste substances that are harmful inside our body, restoring the Acid-Alkaline balance, regulating the pH of the majority of the body fluids. It is also a powerful antioxidant. It increases energy since it is a rich source in stable oxygen, it produces an optimum hydration because of its content of ionic chlorides, neutralizing the excess acidity, inhibits excessive fermentation (digestive zone), dissociates and maintains fats in balance, improves the blood pressure, slows cellular aging, increases the assimilation of nutrients and avoids chronic dehydration. These functions of controlled flow electrolyzed acid water make it ideal for the treatment of disease, pains and chronic degenerative aches, including adults disease such as, cancer, diabetes, arthritis, osteoporosis, bad functioning of the kidneys, liver and circulatory system, cardiac problems, asthma, lupus, leukemia, constipation, urthicary, hemorrhoids, indigestion, headaches, etc. The physicochemical characteristics as well as the determination of heavy metals and other characteristics that are shown in the following chart, were determined at the National Polytechnic Institute in the National Biological Sciences school in the Central Laboratory of Instrumentation under the NOM-201-SSAA1-2002. PHYSICOCHEMICAL ANALYSIS PARAMETER RESULT OBTAINED MEXICAN NORM OF ANALISIS NOM-201-SSA1-2002 (maximum permissible limits) Color 1 unit (Pt-Co) NMX-AA-045-SCFI-2001 15 units (Pt-Co) Odor NA NOM-041-SSA1-95 Odorless Flavor NA NOM-041-SSA1-95 Tasteless Turbidity < 1 UTN NMX-AA-038-SCFI-2001 5 U TN Arsenic < 0,002 mg/L NMX-AA-051-SCFI-2001 0,025 mg/L Barium < 0,0098 mg/L NMX-AA-051-SCFI-2001 0,700 mg/L Borium < 0,150 mg/L NMX-AA-051-SCFI-2001 0,300 mg/L Cadmium < 0,0048 NMX-AA-051-SCFI-2001 0,005 mg/L Cyanides < 0,005 NMX-AA-058-SCFI-2001 0,050 mg/L Free Residual Chlorine Not detected NMX-AA-108-SCFI-2001 0,100 mg/L Total Chrome < 0,0052 NMX-AA-051-SCFI-2001 0,050 mg/L Total Coliforms Not detectable NMP/100mL NMX-AA-042-SCFI-1987 < 1,1 N MP/100mL Niguel < 0,012 mg/L NMX-AA-051-SCFI-2001 0,020 mg/L Silver < 0,007 NMX-AA-051-SCFI-2001 0,100 mg/L Nitrates 3,15 mg/L NMX-AA-79-SCFI-2001 10 mg/L Nitrates < 0,010 mg/L NMX-AA-99-SCFI-2001 0,050 mg/L pH < 2,26 units NMX-AA-008-SCFI-2000 6,5 – 8,5 Units Lead < 0,0052 mg/L NMX-AA-051-SCFI-2001 0,010 mg/L Selenium < 0,002 NMX-AA-051-SCFI-2001 0,010 mg/L SAAM < 0,230 mg/L NMX-AA-039-SCFI-2001 0,500 mg/L Total Coliforms Not detectable NMP/10mL NMX-AA-073-SCFI-2001 < 1 N MP/100mL PARTICULAR CONDITIONS PARAMETER RESULT OBTAINED MEXICAN NORM OF ANALISIS Chlorides 1697,6 mg/L NMX-AA-073-SCFI-2001 Mercury <0,0008 mg/L NMX-AA-051-SCFI-2001 Sodium 376,903 mg/L NMX-AA-051-SCFI-2001 Potassium 3,887 NMX-AA-051-SCFI-2001 Calcium 16,662 NMX-AA-051-SCFI-2001 Conductivity 6,29 ms/cm NMX-AA-093-SCFI-2001 Density 0,9989 g/mL With these analysis it is determined that in the process of electrolysis by controlled flow that is done with the given apparatus under the production conditions already mentioned, gives a product that complies with the required Norm to be able to be consumed and also characteristics that aid in hydration and internal pH control of the organism are obtained, like ionic chlorides content of more than 500 mg/L, sodium of more than 300 mg/L, a conductivity of more than 2.0 ms/cm, pH greater than 9.0 and an ORP greater than -750 mV. The controlled flow electrolyzed acid water has a shelf life of a year, we should mention that this only happens when the product is stored in a fresh place and out of the reach of direct sunlight, since it is photo sensible. Also the container should be in perfect conditions and sealed correctly. Once the container is open the products life is reduced to a month due to the loss of the effectivity of the electrons or protons depending of the product in hand. REPEATED BEFORE AS WELL AS THE CHARTS The function of the alkaline solution can spread to several diseases such as liaises. For example, controlled flow electrolyzed alkaline water was given in a treatment in a dose of a liter a day, to a female patient during 30 days, obtaining a complete elimination of the problem. The ultrasounds and diagnostics are shown in the annexes of initial and final diagnosis of the patient. CLAIMS Having described the present invention in a clear and precise manner, I shall mention its features. It has to be mentioned that all of the characteristics of this invention have been registered as my property at this time: We claim: 1. An electrolysis-process chamber composed by (1) a titanium cell covered in platinum material, of cylindrical shape and with borders in its interior for the assembly with the lids, on the exterior part it has a bolt where one of the contacts is placed. (2) A titanium-made cylindrical electrode covered in platinum or ruthenium depending on the type of product desired. The electrode can be smooth or have a 20 caliber netting equally of titanium covered in platinum or ruthenium with the purpose of increasing the contact surface and increase the product’s volume. (3) A separation netting based on high density polyethylene of high density that attached to the interior lids maintains the fluids separated inside the system and works as a medium to perform the ionic exchange. (4) Interior and exterior system of lids on the superior and inferior part for the adequate separation and conduction of fluids. 2. Electrode: according to claim 1 the electrode that is characterized the titanium cylinder covered with either platinum or ruthenium. And that can contain or not a caliber 20 net equally of titanium covered with platinum or ruthenium. The electrode is characterized by having 2 exits, one at each end, at which a bold is found for the proper orientation of the internal lids and the fastening of the external ones. 3. According to claim 2, the type of covering is characterized by determining the type of polarity that the electrode can take, if it is ruthenium it will only work like a cathode (-) and if it is platinum it could work like anode (+) or cathode (-). 4. According to claim 1 the interior and exterior system of lids that is characterized by its design already described that manages, being connected to the electrode and oriented in an axial manner, to maintain flows 1 and 2 separated and they guide them to the correct area in the electrolysis chamber and then to the exterior. 5. According to claim 4, the lids are characterized by being made up of nitrite grade GRASS. 6. According to claim 1, the electrolysis chamber is characterized by possessing la form of a titanium cylinder covered with platinum since it is relevant that the chamber works like an anode or cathode. 7. According to claim 6, the electrolysis chamber is characterized by its design that has interior borders for the placement of the lids and an exterior bolt to work as one of the contacts to apply electricity. 8. A method to produce controlled flow electrolyzed acid water: the present method comprehends the following steps to obtain super oxidized acid water: I. The assembly of the electrolysis chamber with the smooth electrode with ruthenium and the chamber with platinum. II. The liquid is made to flow through the system. Calibrating the exit flows 1 and 2 according to the required exit parameters. Flow 1 always should be greater than flow 2. III. The solution is added to flows 1 and 2. The quantity of NaCl solution will vary depending on the voltage applied. IV. The electrode and the chamber are polarized. V. The voltage levels are adjusted, flow and NaCl solution until the required exit parameters are obtained. VI. Voltage adjustment, volume flow and salt content according to the temperature of entry in the flows. VII. Controlled flow electrolyzed acid water is obtained and another with alkaline characteristics. 9. According to claim 8 in order to produce controlled flow acid electrolyzed water (super oxidation water) that is characterized by adjusting the voltage levels, flow and NaCl solution until obtaining the required exit parameters, that is characterized for having a pH range of at least 1.5 to 2.9 and ORP of at least +1100 mV to +1200 mV. 10. According to claim 8 the process to produce controlled flow acid electrolyzed water (super oxidation water) is characterized by calibrating flows 1 and 2 with a ratio of at least 5-1 to 7-1 respectively. 11. According to claim 8 the process of creating controlled flow acid electrolyzed water (super oxidation water) is characterized by mixing the NaCl solution in a reason of at least 10 to 30 ml of solution for every 1000 ml of water. 12. According to claim 8 the process of creating controlled flow acid electrolyzed water of controlled flow (super oxidation water) is characterized by polarizing the chamber to positive and electrode to negative through the application of direct current with an intensity that is characterized of at least 2 and 6 Amp and a voltage of at least 4 and not greater to 15 V. 13. According to claims 10, 11 and 12 the process to produce controlled flow acid electrolyzed water of controlled flow (super oxidation water) is characterized by the combinations of the calibration of the three parameters (voltage, flow volume and ml of solution of NaCl until obtaining the desired pH and ORP knowing that: (maintaining the rest of the parameters fixed) a. To greater flow volume, less ORP and pH. b. To greater voltage and amperage, greater ORP and pH but greater wear in the electrode and chamber. c. To greater temperature less ORP and pH. d. To greater flow volume less ORP and pH. 14. According to claim 8 the controlled flow acid electrolyzed water product is characterized with a range of at least 1.5 to 2.5 pH and an ORP of at least +1100 to +1200 mV. 15. According to claim 14 the components of controlled flow acid electrolyzed water are the following elements: non detectable residual chlorine, chlorides of at least 1600 mg/L, a conductivity of at least 6.0 ms/cm, pH less than 3, among other features that make it ideal for its external application and guarantee its correct function. 16. According to claim 14 controlled flow acid electrolyzed acid water is characterized for having microbicide functions done with in vitro studies with an effectivity of at least 10 s to 3 min, which causes it to have very good results treating wounds and eliminating them, enumerating the following cepas (types): Enterobacter aerogenes, Salmonella typhy, Acinetobacter baumannii, Bacillus spp, Klebsiella pneumaniae, Candida albicans,Aspergillus niger, Enterobacter gergoviae, Pseudomona aeruginosa, Salmonella spp, Candida parapsilosis, Lysteria monocytogenes, Enterobacter cloacae, Sthaphylococcus thermophilus, Bacillus cereus, Leuconostc messenteroides, Lactococcus lactis, Escherich ia coli, Staphilococcus aureus, Raoutella terrígena, Vibrio cholerae, Escherichia coli O157:H7, Stenotrophomonas maltophilia and Sacccharomyces cereviciae I. 17. According to claim 14 controlled flow electrolyzed water is characterized by possessing a stability in its physicochemical composition of at least a year. 18. Method for elaboration through the method of controlled flow alkaline electrolyzed water. The present method has the following steps for obtaining the alkaline solution: I. Assembly of the electrolysis chamber with the smooth electrode or with netting and the cell, both covered with platinum. II. The liquid is made to flow through the system. Calibrating the exit flows 1 and 2 according to the required exit values. The greater flow will be the exit flow for the acid electrolyzed water. III. The NaCl solution is added to flows 1 and 2. The quantity of NaCl solution varies depending of the voltage to apply. IV. The electrode and the chamber are polarized, being able to give the positive or negative polarity to either component. V. The voltage levels are adjusted, flow and NaCl solution until the required exit parameters are obtained. VI. To maintain the exit parameters the voltage, the flow volume and the salt content should be adjusted. VII. An acid flow and an alkaline flow is obtained. 19. According to claim 18 the process for elaborating alkaline water that is characterized for calibrating the levels of flow volume, voltage and quantity of NaCl solution to elaborate alkaline electrolyzed water with a pH of at least 9.0 to 11 and an ORP of at least -700 mV to -800 mV. 20. According to claim 18 the process for the elaboration of alkaline water that is characterized for calibrating flows 1 and 2 until reaching a ratio in the volume of at least 3-1, where the greater flow will be where the alkaline electrolyzed solution will be obtained. 21. According to claim 18 the process for the elaboration of alkaline water that is characterized by mixing in flows 1 and 2 the NaCl solution in a proportion of at least 10 ml to 30 ml for every 1000 ml of water. 22. According to claim 18 the process for the elaboration of alkaline water that is characterized by polarizing the cell to positive and the electrode to negative or vice versa, through the application of direct current with an intensity that is characterized of at least 2 and 6 Amp and a voltage of at least 4 and not greater to 15 V. 23. According to claim 19, 20 and 21 the process for the elaboration of alkaline water that is characterized by the combinations when calibrating the three parameters (flow volume, voltage and NaCl solution quantity) until obtaining the desired pH and ORP knowing that: (maintaining all the other parameters fixed) a) To greater flow volume, less ORP and pH. b) To greater voltage and amperage, greater ORP and pH but greater electrode and cell wear. c) To greater temperature less ORP and pH. d) To greater flow volume less ORP and pH. 24. According to claim 18 the alkaline electrolyzed water product that is characterized by having a pH of at least 9.0 to 11 and an ORP of at least -700 to -800 mV. 25. According to claim 24 the controlled flow alkaline electrolyzed water that is characterized by comprehending the following parameters: ionic chlorides of at least 500 mg/L, pH of at least 9.5, conductivity of at least 2.4 ms/cm, among others that make alkaline water ideal for drinking complying with the established in the norm NOM-201-SSA-. According to claim 25 the alkaline electrolyzed water that is characterized for possessing a detoxifying and hydrating effect that make it a good aid in the treatment of diabetes, hypertension, and renal insufficiency among other chronic degenerative diseases. 27. According to claim 25 alkaline electrolyzed water is characterized for having a shelf life of more than a year, keeping all of its physicochemical properties. SUMMARY This invention includes the apparatus and method for producing controlled flow acid electrolyzed water and controlled flow alkaline electrolyzed water with independent flows from aqueous solutions, its objective is to produce controlled flow acid water with an oxide reduction potential (ORP for its acronym in English) between +1100 and +1200 mV and a pH between 1.5 and 2.9, with a stability and shelf life of over a year. And controlled flow alkaline electrolyzed water with a pH between 9.0 – 11.0 and an ORP of between -700 mV to -800 mV with a shelf life of more than a year.