Abstract:
The invention relates to a method and apparatus for physically working and/or heating media, in particular liquids. The high expenditure of energy of the known methods can be avoided, with reduced environmental impact, by the hydrodynamically worked medium being exposed to polar and/or ionic electrochemical potentials and electrochemical signals RC AC

Description:
CROSS-REFERENCE TO RELATED APPLICATION  
       [0001]    This application claims the benefit of the priority filing date in PCT/EP2012/001891 filed on MAY 3, 2012 and referenced in WIPO Publication No. WO2012/150031. The earliest priority date claimed is May 4, 2011. 
     
    
     FEDERALLY SPONSORED RESEARCH 
       [0002]    Not Applicable 
       SEQUENCE LISTING OR PROGRAM  
       [0003]    Not Applicable 
       BACKGROUND 
       [0004]    The invention relates to a method for physically processing and/or heating liquids, as generically defined by the preamble to claim  1 , and to an apparatus for performing the method, an excitation device, and its connection to technological processing nodes. 
         [0005]    The pretreatment of liquid and gaseous media in technologies that work with water and with other chemical compounds (methane, alcohol, ethanol, and others), elemental substances (pure hydrogen gas, gaseous helium, and others), homogeneous compounds (air, seawater, aqueous solutions, such as saline solution, copper vitriol solution, and others), colloidal compounds (milk, blood, and others), heterogeneous compounds (suspension, emulsion, foam, aerosols), is known. These excitation devices are used in biochemistry, in petrochemical technologies, in chemical technologies, and others, in which the media are of an organic, inorganic, polar, nonpolar, natural, or synthetic type. 
         [0006]    Present technologies that work with liquid or gaseous media (whether as material to be processed, or as adjuvant material that improves the technological conditions) are defined by energy bonds in the molecule and between the molecules. The magnitude of their decisive properties, such as fluidity, electrical conductivity, surface tension, etc., depends on those energy bonds. Because of their broad application and because they are so numerous, these technologies cannot be specified concretely within the scope of this invention. They involve liquids and gases in the full scope of their molecular composition, such as water, soda, acid, organic and inorganic liquids, hydrocarbons, in particular fuels, crude oil, gasoline, kerosene, mineral oils, liquid fertilizer, and so forth. 
         [0007]    The technologies that have to do with the media listed, such as burning, combustion, heating, cooling, the preparation of solutions and colloids, and segregation, such as distillation, refining, evaporation, sedimentation, and the like, are energy-, time- and material-consuming. 
         [0008]    Present technologies that require a temperature change (heating, cooling) of the medium are implemented by means of solid, liquid and gaseous fuels, electrical energy, sunlight, heat from the earth (geothermia), heat pumps, and so forth. 
         [0009]    The disadvantage of present methods is their high energy consumption. Moreover, in combustion, fuels have adverse effects on the environment. In the case of automotive traffic, air traffic, and ship traffic, the effects are multiplied and worse. 
         [0010]    If water is used as a heating medium or in the production of steam, for instance for driving a turbine, this medium requires complex processing in order to reduce some or all of the elements. Possible ventilation, especially because of the formation of crusts, must also be provided. In this processing, damage occurs to the surface of the technical systems, the functional surfaces of combustion chambers, and the machines, such as radiators, heat exchangers, heating equipment, and heaters. 
         [0011]    In heating with water in accordance with the PCT application WO 2007/045487, the heating is slow, and sometimes unwanted. This reference was the subject of further research, especially because of unexpected interactions in the type of heating, which was directed to changes in the treated medium. The physical changes found led to use in further implementation, such as in distilled water, demineralized water, geothermal water, alcohol, oils, gases, crude oil, gasoline, kerosene, methane, biogas and other media named in the aforementioned application. 
         [0012]    In U.S. Pat. No. 4,427,544, a magneto-electrochemical reactor for water preparation is described, which is located on a nonmagnetic pipeline having an inlet and an outlet. A DC source is mounted on the outside of the pipeline. In the interior, there is a rotating turbine, which is disposed on ferromagnetic rods that are supported in the pipeline. The rotating turbine generates electric current, which acts on the formation of lime in the pipeline and which, in energy equipment and heat exchangers, forms a protective layer that prevents crusts from forming. 
         [0013]    U.S. Pat. No. 5,384,627 shows a method and an apparatus for electrolytic treatment of materials; the material to be treated is stored in an electrolyte on which an electromagnetic field acts. On the surface of the material to be treated, this field triggers electromagnetic and electrokinetic forces, which are capable of generating chemical and physical changes in the material to be treated. This involves, for one thing, a reactor, supplemented with an electrolyte, that has treatment materials, such as ions, acids, bases, and the like, with an optimal pH value, and also has a takeup electrode or a mixing device and a reducer. The reactor has a number of possible embodiments, and the takeup electrode is connected to a cathodic metal. This method is employed for cementing the surfaces of the material to be treated. 
         [0014]    U.S. Pat. No. 4,061,551 shows a method for extracting gallium from alkaline solutions. This involves a method for obtaining gallium from solutions for further use, for instance, as components for semiconductor elements of thermometers and the like. It also involves an apparatus, which comprises a container with an anode and a liquid metal cathode, and the electrolyte contains a gallium solution. An electromagnetic field speeds up the displacement of gallium from alkali electrolytes to the electrodes. 
         [0015]    US Patent Application 2007/0029261 shows a method and an apparatus for water preparation by electromagnetic waves for the sake of removing lime. It involves part of a pipleline with an electromagnetic induction winding, which is connected to the source of the electromagnetic signal. The electromagnetic field is generated in the interior of the pipeline. 
         [0016]    German patent disclosure DE 888537 shows a method for separating solids out of solutions, in order to avert the formation of deposits on the heating and cooling bodies in conjunction with an anode and a cathode. The technology is implemented using the action of magnets, whose magnetic fields, whether DC or AC, are generated or formed by a permanent magnet. In an alternative embodiment, the effect is augmented with a high-frequency field. 
         [0017]    British patent GB 2 433 267 shows an apparatus with an electrostatic electromagnetic field and an induction field. This involves an electrostatic reduction device, with a combined electromagnetic generator that is connected to a winding. The winding is formed on the outside over the entire circumference of a container in which a reactant is disposed. The AC generator is connected in the container to the AC electrode. The AC generator is connected to the base of the container, and the reactant has both a liquid and a solid aggregate state. 
         [0018]    Moldovan patent disclosure MD 4055 shows a method and an apparatus for softening natural mineral water. In the apparatus, there is a separate chamber for affecting water by means of a hollow cathode with a water inlet. The cathode is disposed on a winding, which is connected to a converter, a source of high-frequency magnetic impulses. The water treated by the cathode can be let out through a valve. However, the water can also flow in the opposite direction over the outer circumference of the cathode and be let out via a second, continuous outlet. Between the anode and the cathode is a ceramic membrane; a separate anode chamber has its own inlet and outlet and is connected to the positive pole of a DC source. The negative pole of the DC source is connected to the cathode. This disclosure also describes the parameters for the electrochemical treatment of the mineral water in that apparatus. 
         [0019]    The common objective of all the aforementioned documents is to prevent the formation of a crust on the pipelines by the action of a magnetic or electromagnetic field on the water, in conjunction with static or moving components in the flow direction. A further group of documents relates to the changes upon the takeup of negative and positive ions by electrodes, or the material to be treated with an enrichment of the surface with these elements, with the goal of achieving cementation or the formation of an antioxidation protective layer, or the recovery of elements from the solutions (electrolytes). 
         [0020]    The object of the invention is the processing of a medium, whether in liquid or gaseous form, in order to alter changes in force and energy in the molecule and between the molecule and the medium, changes that are the cause of physical and/or chemical properties of the medium. 
       SUMMARY 
       [0021]    The essence of the invention is that a hydrodynamically processed medium, in a liquid and gaseous state, is subjected to polar and/or ionically electrochemical potentials and to electrochemical signals RC AC. It suffices if at least some of the medium is pretreated, prior to being subject to physical, biological, chemical, biochemical and other technologies. 
         [0022]    In one embodiment, before introduction to physical, biological, chemical, biochemical and other technologies, the entire contents of the medium are processed in an excitation device. The best method for processing provides that the medium is intentionally passed more than once, or multiple times, through the body of the excitation device. The essence of the invention further comprises that in the body of the excitation device, at least one controlled electrode is connected to a frequency source. This frequency source is connected to an energy source. In the direction of the forced flow of the treated medium, or by means of the flow triggered by temperature changes without a forced flow, a polarization and/or ionization chamber follows, which is formed of various electrochemical potentials. Technically, it is simplest if these electrochemical potentials are formed on a body of standard dimensions on its inner circumference and/or on its axis. The advantage of this method for physical processing, and of the excitation device and its connection, is that the physical changes and their control are greater. Moreover, the heating and expansion of the excitation device&#39;s implementation to technologies, in which it brings unexpected effects, is sped up, for instance, if the method is employed as an interactive node for heating. In that case, the excitation device, in conjunction with conventional technologies, speeds up the heating and increases output from the heating devices (boilers) and reduces emissions, which has positive effects on the environment. In combination with other technologies, it acts as a catalyst, especially in the fields of organic and inorganic chemistry, petrochemistry, natural gas, crude oil, fuel processing, papermaking, water purification, energy economy, etc. The effect described is achieved in that the bonds in the molecule and between the molecule and the medium are altered, and in the case of liquids, their fluidity and surface tension change, similar to what happens with gases. They become thinner as a result and have weaker bonds, which lead to a change in their physical and chemical properties (the heat content/enthalpy changes), such as evaporation, heating, cooling, drying, mixing, etc., and to changes in chemical, physical, biological and bioenergetics reactions. 
     
    
     
       DRAWINGS 
         [0023]    The invention will be described in further detail in conjunction with the accompanying drawings. In the drawings: 
           [0024]      FIG. 1  schematically shows an excitation device for liquids and gases; 
           [0025]      FIG. 2  shows an excitation device built into the cleaning module of a pipe system; 
           [0026]      FIG. 3  shows an excitation device with a heat exchanger and a conventional heating module; 
           [0027]      FIG. 4  shows a variant connection of the excitation device to large-diameter pipelines; 
           [0028]      FIG. 5  shows a variant connection of the excitation device to a chamber having a mixer of a redistributor; 
           [0029]      FIG. 6  shows a variant connection of the excitation device to a chamber that has biological, chemical and other technological devices; 
           [0030]      FIG. 7  shows a basic version of the body in which the negative electrode is in contact with the medium; 
           [0031]      FIG. 8  shows a variant in which the negative electrode is disposed on only part of the body; 
           [0032]      FIG. 9  shows a variant with a secondary negative electrode with various potentials; 
           [0033]      FIG. 10  shows a variant with an insulation layer between the negative and the secondary negative electrode; 
           [0034]      FIG. 11  shows a variant with a different negative electrode; 
           [0035]      FIG. 12  shows a variant with the association of the negative electrode with the controlled electrode, which is separate from the positive electrode and the medium; 
           [0036]      FIGS. 13 and 13A  show a large-volume heating device with a controlled electrode and a positive electrode in two variants; 
           [0037]      FIG. 14  shows the lineup of a plurality of excitation devices; 
           [0038]      FIG. 15  is a block diagram of the excitation device in a vehicle, with a conveyor device for the medium; 
           [0039]      FIG. 16  shows a variant of the excitation device of  FIG. 15 ; and 
           [0040]      FIG. 17  shows a variant with a vertical orientation of the electrodes. 
       
    
    
     DESCRIPTION 
       [0041]    The invention will be described in further detail in terms of an exemplary embodiment of an excitation device shown in  FIG. 1 . 
         [0042]    In a body  1 , an excitation device  10  for liquids and gases has at least one controlled electrode  6 , which is connected to a frequency source  62  that is connected to an energy source  63 . 
         [0043]    In the direction of the forced flow of a treated medium  9  or by means of a flow triggered by temperature changes without a forced flow, a polarization and/or ionization chamber that is formed of various electrochemical potentials follows. Technically, it is simplest if, in the body  1  of standard dimensions, these electrochemical potentials are formed on its inner circumference and at its axis. In a hydrodynamic flow of the medium in the body, the excitation device  10  for liquids and gases, according to the invention, processes only a portion, or the entire volume, of the medium  9  by physical means, such as with electrochemical signals RC AC and with different electrochemical potentials in the body in polar and/or non-polar ionic fashion, which determines the type of change in the medium  9 . If the electrochemical potential that is located in the body  1  has an insulation layer such as  3 . 1 ,  2 . 1 , for example in the form of silicate, Teflon, PP-film and PPR film at its surface, or a layer applied in a vacuum, for example, the effect involved is a polarizing effect. If this insulation layer is only part of the electrochemical potential of the electrodes and a portion of its surface is in contact with the treated medium  9 , then the effect involved is an ionizing effect. The activation excitation device  10  for liquids and gases shown is then used in an existing, old pipe system. If there is a change in the flow, a flange is preferably secured retroactively in the curve  1 . 0  from its axis or in the vicinity thereof; a body  1  of insulating material, such as polyethylene, polypropylene, glass, silicate ceramic, or material with a zero electrochemical potential (platinum) is detachably secured in the curve  1 . 0 . through an opening in the body  1 , preferably round in shape, and is closed by a closure plate  1 . 3  of insulating material. At the location of the flow of the medium  9 , the body  1  laterally has an inlet opening  4 , and in its axis it has an outflow opening  5 . On its inner surface, in this specific exemplary embodiment, the body  1  has a negative electrode  3  in the form of a coating film or the like. 
         [0044]    In an alternative embodiment, at least a portion is covered by a peripheral insulation layer  3 . 0 . In the vicinity of the axis of the body  1 , or directly in the axis, in the closure plate  1 . 3  a holder  61  with the controlled electrode  6  is secured in watertight (media-tight) fashion; a transmission device  64  in the form of a rod or spiral is disposed in the electrode and in this way inserted into a silicate, silicon and/or quartz glass pipe. The transmission device  64  is connected by one end detachably or solidly to the frequency source  6 . 2 , which is connected to the energy source  6 . 3 . The energy source  6 . 3  can be designed as a 230 V/50 Hz distributor network, for instance, or as a photovoltaic module, a battery, or the equivalent. The integrated controlled electrode  6  ( FIG. 12 ), on its end, has a positively polarized electrode  2 , for example, which is disposed in the common silicate pipe and is separated from the controlled electrode  6  by an air gap or an insulating material with minimal thermal expansion and/or a nonpolar elastic material. The positively polarized electrode  2  is formed of C, Ag, Au, or the like, for example, or comprises mixtures thereof or compounds with other elements. In an alternative version, there is a coating, a layer  21  of positive and/or negative electrochemical potential, on the silicate pipe of the controlled electrode  6  and or of the positive electrode  2 . In this way, the medium  9  comes into direct contact with the coating, that is, the layer  21 , and is ionized. 
         [0045]    Further versions of the controlled electrode  6 , the positive electrode  2 , and the negative electrode  3  are shown in  FIGS. 7-12 . 
         [0046]    A further version ( FIG. 2 ) of the general provision recited in PCT application WO 2007/045487 provides that at least some of the medium  9  is processed physically in the body  1 , for instance by means of an electrochemical signal RC AC and various electrochemical potentials in the hydrodynamic flow of the medium  9  in its polarizing and/or nonpolarizing effect in the body  1 , which is inserted retroactively, for instance into a dirt filter  1 . 0  which is a component of the pipe system. This is a version in which the technology is implemented in a linear flow of the medium  9 . The excitation device  10  for liquids and gases comprises one chamber of the controlled electrode  6  of the body  1  and one chamber of the positively polarized electrode  2  of the body  1 . The inlet opening  4  is located in the axis of the integrated body  1  of the chamber of the controlled electrode  6 . The chamber of the positively polarized electrode  2  has a lateral outlet opening  5  as well as an auxiliary inlet opening  4 . 1 . The chamber of the controlled electrode  6  and the chamber of the positively polarized electrode  2  are linked to each other in the body  1  via a communication opening  45 . A positively polarized electrode  2  is disposed directly in the axis of the integrated body  1  of the chamber of the controlled electrode  6 , or in a silicate pipe, preferably of technical glass. The body  1  comprises a first body  1 . 1 , which forms the separate chamber of the controlled electrode  6 , and a second body  1 . 2 , which forms the separate chamber of the positively polarized electrode  2 . These chambers communicate with one another through a closure plate  1 . 3 . The transmission device  64  disposed in the silicate pipe is connected solidly and/or detachably to the frequency source  6 . 2 , which is connected to the energy source  6 . 3 . Similarly to the controlled electrode  6 , the positively polarized electrode  2  is also disposed via a holder  2 . 1  on the body  1  in the closure plate  1 . 3 , which is detachably secured to the flange. The body  1  is provided with sludge openings  1 . 4  and an outer closable drain opening  1 . 5 . On the circumference of a body  1  that is so embodied, there is a cylindrical filter  1 . 02 . 
         [0047]    The version for processing the medium  9  with multiple passages through the excitation device  10  with hydraulic and electrical connection, through which heating is achieved, is shown in detail in  FIG. 3 . The body  1  has at least one controlled electrode  6  and at least one positively polarized electrode  2 . In this version, if the body  1  is made of an insulating material, a negative electrode  3  is located on its inner surface. In an alternative polarized version, the body  1  has a peripheral insulation layer  3 . 0  on the inside circumference, or on only a portion thereof (see the right and left parts of the body  1 ). In the interior of the body  1 , there is at least one conventional heating module disposed in watertight fashion, or at least one heat exchanger  17 . The controlled electrode  6  is connected to the frequency source  62 , which is connected to the energy source  63 . The energy source  63  is connected electrically to a conveyor feed device  15  of the medium  9  and a conventional heating module  14  and its equivalents (laser, induction heating, and the like). The conveyor feed device  15  communicates by its outlet with the interior of the body  1 , at points where at least one controlled electrode  6  disposed in the holder  21  is located. The input into the conveyor feed device  15  from the chamber of the body  1  takes place at points where at least one positively polarized electrode  2 , which is disposed in the holder  21 , is located. The interior of the body  21  has a heat exchanger  17  with an inlet opening  17 . 1  and an outlet opening  17 . 2 . These openings can also have a kinematic reversal. They are inlet-outlet openings. In an alternative version, a secondary excitation device  16  can be connected upstream and/or downstream of the conveyor feed device  15 . The body  1  has a closable air/gas exhaust  7  and a closable sludge drain  8 . If the body  1  is placed horizontally, these openings are located on the upper and lower wall of the body  1 . The excitation device  10  mentioned, shown in  FIG. 3  without a hydraulic connection and without a heat exchanger  17  and heating module  14 , can be used for processing the medium, specifically with a single passage of the medium  9  prior to the physical, chemical, biochemical, biological and other technologies. 
         [0048]    A further version of the excitation device  10  is shown in  FIG. 4 . It shows an arrangement on a large-diameter pipeline for carrying large quantities of the medium  9  while minimizing the execution time. The hydrodynamic chamber  55  forms a part of the pipeline  100 , onto which an inlet opening  102  and an outlet opening  101  are fitted in water-tight fashion. It is advantageous to install closing and opening devices  103  and  104  on these openings. The closing and opening device  103  for the medium  9  is disposed on the outlet opening  101 . The conveyor feed device  15  is connected to the inlet of the excitation device  10 , whose outlet pipeline communicates with the inlet opening  102  via the closing and opening device  104 . The electronic frequency source  62  communicates on the one hand with the controlled electrode  106  and the energy source  63  and on the other with the control module  64 . The control module  64  is connected not only to the conveyor feed device  15  but also to a first continuously or incrementally operating electronic closer/opener  65  and a second closer/opener  66 . The frequency source  62  is connected to the energy source  63  for AC or DC. The control module  64  is connected for example to a first measuring instrument T (for temperature, for instance), a second measuring instrument t (for pressure, for instance), and a final measuring instrument z (for conductivity, pH, and the like, for instance). The conveyor feed device  15  is preferably a pump of any kind and its equivalents, but in the case of cases also a suction pump, ventilator, compressor, and equivalents thereof. The variant of the aforementioned connection at a lower technical level does not have any first and second continuously or incrementally operating closers/openers  65 ,  66 . 
         [0049]    A further connection plan with two excitation devices  10  in the heat generation system with a boiler  100  is shown in  FIG. 5 . The first excitation device  10  communicates via a pipeline with the chamber  55 , which in a concrete embodiment forms a mixing device or a pressure regulator or its equivalent. In this way, the conveyor feed device  15  of the medium  9  is connected to the connecting pipeline. An excitation device  10  may, but need not necessarily, be installed upstream of the boiler  100 , but only in the event that the hydrodynamic chamber  55  is disposed at a distance from the boiler  100 . The boiler  100  has an inlet P for the incoming medium  9 , an outlet for the heating medium OM and usually a gas outlet p, as well as a sludge outlet k and an outlet for impurities. The outlet from the boiler  100  communicates with the distributor chamber  56 , whose outlet communicates with a first technical block  57 , such as a heating block. The second outlet communicates with a second technical block  58 , such as a solvate block for an eco-washing and dry cleaning system. A third outlet from the distributor chamber  56  is connected to a third technical block  59 , for instance for heating swimming pool water. The technical blocks  57 ,  58 ,  59 ,  60  etc. are equipped to supply the needs of an entire facility, such as a hotel, office building, factories, and the like. The hydrodynamic chamber  55  and the distributor chamber  56  also have the outlets p and k. The final technical block  60  is the last outlet that communicates with the distributor chamber  56 , and its outlet communicates with the hydrodynamic chamber  55  via a mixing device or its equivalents. 
         [0050]      FIG. 6  shows a general connection of the excitation device  10  to a hydrodynamic chamber  55 , which communicates by one outlet with the boiler  100 . The hydrodynamic chamber  55  communicates by its first outlet with the physical block  71 , by its second outlet with the chemical block  72 , and by its last outlet with the biological block  73 , for example. It is understood that there can also be more of these technical blocks  71 ,  72 ,  73 . If the medium  9  is crude oil, block  71  can be physical, block  72  can be a refinement block, and block  73  can be an evaporation or distillation block, and so forth. The embodiment of the negative electrode  3  can be of any kind, depending on the type of medium (anionic or cationic) being processed, which can be liquid or gaseous. 
         [0051]    The general embodiment forms a layer, a coating, over the entire circumference along the chamber of the body  1  ( FIG. 7 ). 
         [0052]      FIG. 8  shows an embodiment in which at least a part of the body  1  is covered by the electrode  3  or by the positive and/or negative electrochemical potential equal to zero. 
         [0053]    The version of the electrode  3  in which two layers with different electrochemical potentials are in superficial contact with one another is shown in  FIG. 9 . 
         [0054]    In  FIG. 10 , a version identical to  FIG. 9  is shown, except that between the electrochemical potentials there is a peripheral insulation layer  3 . 0 . 
         [0055]      FIG. 11  shows a body  1  with an electrochemical potential equal to zero. The body  1  comprises one part which has an electrochemical potential equal to zero or is of an insulating material, and secondary parts that have a negative or positive electrochemical potential and that simultaneously replace the electrode  3 . 
         [0056]      FIG. 12  shows an integrated controlled electrode  6  and a polarized electrode  2 , which are disposed separately from one another in a common silicate pipe, which on its outer surface has at least one outer coating, the layer  21  with a positive and/or negative electrochemical potential.  FIG. 12  shows other possible exemplary embodiments of the electrode  3 , the layers of which touch each other, are separate from one another, or cover each other. 
         [0057]    The excitation device  10  for liquids and gases in the form of a large-volume heating device is provided, on one side, in the vicinity of the inlet opening  4 , with one or more controlled electrodes  6  and in the vicinity of the outlet opening  5  with one or more polarized electrodes  2 . It is advantageous if the interior of the body  1  has an insulation layer  10 . 2 , preferably whenever the body  1  is formed of a load-bearing, conductive material  10 . 1 . It is advantageous in this case if the body  1 , on its outside, has at least one technical layer in the form of thermal insulation and/or a back-reflector for electromagnetic radiation, for instance in the form of an aluminum foil or the like ( FIGS. 13 ,  13 A). 
         [0058]    The passage of the medium through the excitation device  10  multiple times can be implemented with the aid of the conveyor feed device  15 . A further concrete embodiment can be attained by lining up the excitation devices  10  in succession ( FIG. 14 ). Passing the medium  9  a single time through two excitation devices  10  enhances its technological effects. 
         [0059]    The electrode  3  is anionic or cationic, depending on the type of material with which it ionizes. The physical liquid or the gas as the medium  9  is influenced thereby. In an alternative version, if it polarizes the medium  9 , the electrode  3  has an insulation layer  3 . 0  on the anionic or cationic material. This electrode  3  is the subject of further research. The polarized electrode  2  can have test tubes of anionic or cationic material in the interior of the silicate pipe and is likewise the subject of further research with regard to its interactions with the chemical composition, physical properties, and the like, of the medium  9 . 
         [0060]    The method according to the invention is the subject of further research. At this time, one can draw the conclusion that, if the electrode  3  is of a material with negative electrode potential (negative electrochemical potential—cathode), such as Fe, Al through lithium (−3.04 V) and compounds and mixtures thereof, then reduction processes take place in the medium  9 . These versions have been tested in terms of energy economy. If the electrode  3  is of a material with a positive electrode potential (positive electrochemical potential—anode), such as Cu, Ag through gold (1.55 V) and compounds and mixtures thereof, then oxidation processes occur in the medium  9 . These versions have been tested in technologies for wastewater purification, biogas processing, and the like. The polarized electrodes  2 , and in particular their interactions upon changes in the medium  9 , are likewise the subject of further research. The polarized electrode  2  in the interior of the silicate pipe can have test tubes of anionic or cationic material and is likewise the subject of research with regard to its interactions with the chemical composition of and the physical changes in the medium  9 . 
         [0061]    Novel physical and chemical properties of the embodiment according to the invention have been investigated using the PO method, which is the subject of Slovakian patent SK 279429. The outcome of the investigation is as follows: 
         [0062]    The molecules in the medium, after the treatment according to the invention, are more weakly bound in their molecular and intermolecular structure; the medium has increased fluidity and an altered surface tension; the creation of an electrical double layer in the medium is influenced; the electrical and chemical potential and the changes in the conditions for the electrical equilibrium affect the pH value and thus also the chemical compositions; the properties of the treated medium are dependent on the time of treatment, the thermal content/enthalpy, the absorption, which given the altered properties was measured by the Si occurring in the medium. 
         [0063]    By experimental measurements, differences were found in the rate of evaporation and the rate of heating, as well as a drop in the energy consumption for heating and cooling the same medium. 
         [0064]    In view of the high measured absorption of water that was processed according to the invention, in comparison to water that was not processed, the inventor ascertained the following, after processing for 30 seconds, using a laser (laser pointer and laser battery available on the market): After 110 hours, he performed a comparison of
       distilled water that was not processed,   distilled water that was processed according to the invention, and   distilled water that was processed according to the invention and was affected by the laser.       
 
         [0068]    This involved heating of a standard volume from 50° C. to 60° C. with the following result: distilled water that was not processed with 4.5 MJ/kg, distilled water which was processed according to the invention with 4.1 MJ/kg, and distilled water that was processed according to the invention and was affected by the laser with 3.7 MJ/kg. 
         [0069]    The above was confirmed by experiments during cooling, which confirmed a substantially shorter time until the onset of nucleation for the water processed according to the invention (performed by WSL, Institute for Snow and Avalanche Research SLF, Davos, Switzerland). From the change in the bonds between the molecules and in the molecules, an optimized heat transfer and a change in the thermal conductivity in the medium can be observed. The energy required for freezing can be transmitted faster, or at a lesser temperature gradient. 
         [0070]    Measurements were performed for the use of distilled water, which had been processed according to the invention, for the electrolysis of water; a faster reaction and a drop of 28% in the cost for the power supply were measured. 
         [0071]    Tests with biogas preparation were performed; after the preparation according to the invention, there was an increase of 17% in the calorific value of biogas. 
         [0072]    The tests were performed using an electromagnetic alternating signal and a steadily sinusoidal electromagnetic signal, a continuous signal and an intermittent signal of 100 to 500 MHz; work was done using a 0.1 to 100 W controlled electrode, a polarized electrode of technical glass and oxide ceramic with a filler of Cu, Ag, Al, C, Mg, and an ionized electrode of stainless steel, Zn, Sn, Fe, Cu, C and coatings, layers of W, Cr, Mo, and their carbides, nitrides, silicides, and multilayer structures and connecting structures. 
         [0073]    By means of the method of the invention, the methane gas that was bound in the well water was eliminated, which confirms a weakening of the bonds. 
         [0074]    The possible uses are dictated by the magnitude of the changes in the physical properties of the liquids and gases that flow through the apparatus. The changes are proportional to the number of passages through the electrochemical potentials and using the controlled electrode. This relates to the drinking water and industrial water processing industry, technical waters and wastewater, construction, spas and medicinal springs, dry cleaning and laundry services, the food industry, alcohol production, brewing, the health field, dermatology, ceramics production, heat generation, heat economy, water purification plants, energy economy, water sources, swimming pools, etc. The method for processing liquids can be employed for processing in the crude oil industry and the automotive industry. 
         [0075]    The method according to the invention also interacts and acts on solid substances either intentionally or by their mere presence in liquid or gaseous media in the form of impurities. The method for processing can be employed in a liquid or gaseous state, and from moisture to liquid state, among other things, and may be present in a gaseous state, and in turn, free or bound gas may be present in the liquid. Accordingly, what is involved is the action on a compound of a solid, liquid or gaseous medium, in which the liquid state prevails at some times and the gaseous state at others. This method can be employed in the environmental field, especially in the combustion of solid fuels.