TECHNOLOGY FOCUS - INSTRUMENTATION AND TESTING - Preferred Components: (B) is in the form of parallelepipedic or cylindrical. The electrodes are hollow type (comprises an inlet for gases and a out let for the reforming gas) and constituted a supply conduit of gas to be reformed and oxidizing gas. (I) comprises two metal electrodes (situated face to face) having a pipe and a perforated hollow disc, where the disc is located at the end of the tube opening into (B) and the disc is in contact with the lining of (B) to ensure electrical supply of lining and heating is measured by Joule effect. (C) (has an electrical resistivity of 50xl0-9 -2x10-9 (preferably 90x10-9-200x10-9) ohm-m at 20degreesC in a dense state) is: elements of group VIII of periodic classification (80%) (iron, nickel or cobalt) or alloys (80%) (carbon steels); beads and/or wires with a base comprising an element of group VIII or a metallic oxide (preferably iron or steel); a fiber (having a diameter of 25 microns-5mm (preferably 50 microns-1 mm) and length greater than 10 (preferably greater than 50) times the diameter). (C) is a scales, fibers, filings, marbles, sinters, beads, nails, wires, filaments, wool (made of steel wires mixed with materials of spherical form such as balls made of steel), rods, bolts, nuts, flanges, chips, powders, grains, granules, perforated plates or partially perforated plates (having surface openings of 5-40 (preferably 10-20)%) or soft steel wool. (C) is present in the porous medium, which has: surface volume of more than 400 (preferably 2) m2/m3 of (B); and a porosity index of 0.50-0.98 (preferably 0.6-0.9). The residence time of the reactive is greater than 0.1 (preferably greater than 3) seconds. (B) further comprises non-conducting and/or semi conducting materials and/or electrical insulator (ceramic and alumna), where the electrical insulator is adequately placed in (B) to adjust the total electrical resistance of the lining. The electrodes are exposed within (B), which is equipped with protuberances and/or projections ( in the form of conical (preferably in the needle form)) (having a spacing density greater than 0.5 unit/cm2). The length of the protuberances and/or projections is 0.001-0.1 times the length of (B) and the width of the protuberances and/or projections is 0.001-0.1 times the diameter of the disc of the electrode). The ratio of the cone height to cone diameter is at least 1 (preferably greater than 10). (C) is previously treated (with mineral acid or heat treatment) to increase the specific surface, purity and chemical activity. The supply conduit of gas to be reformed is positioned perpendicularly to the direction of electron flow between the electrodes. The electrical source comprises a current transformer in case of alternative current (AC) power supply or of a current rectifier in case of direct current (DC) power supply (where the power is calculated by the energy needs of the reforming reactions) and the electric source provides a minimum current intensity, which is calculated by the equation I-minimum is equal to lambdaxF (where I-minimum is the minimum current to apply (expressed in A); ~ asterisk is a parameter depends on the geometry of the reactor, type of lining, operating conditions and on the gas to be reformed; and F is molar flow of the gas to be reformed (expressed in mole of gas to be reformed/second)). The perforated electrode has opening with the diameter of more than 25 microns, the holes are uniformly divided by a density of at most 100 000 opening/cm2 of the electrode surface, where the holes having the pressure loss due to the passage of gas through the electrode or the electrodes does not exceed 0.1 atmospheres and the openings are divided on the surface of the perforated electrode to ensure a uniform diffusion of gases in (B). The size of the openings increases in the radial direction of the perforated electrode or the electrodes. In the cylindrical form of (B), where the conduits for supply of gaseous mixture (containing (D) and/or oxidizing gas) is positioned at tangent to the cylindrical wall of (B). The outlet is positioned in (B), which is in opposite direction of (D). (C) comprises a wool made of steel wires mixed with spherical materials of spherical (beads made of steel). (I) is dimensioned to constitute a compact type reactor.    TECHNOLOGY FOCUS - ORGANIC CHEMISTRY - Preferred Components: The oxidizing gas comprises carbon dioxide, carbon monoxide, water, oxygen, nitrogen oxides (NO, N2O, N2O5, NO2, NO3, N2O3) and/or preferably mixtures of carbon dioxide and water. (D) (natural gas) comprises: 1-12C hydrocarbons (having boiling point lower than 200 (preferably lower than 100)degreesC) (optionally substituted by alcohol, carboxylic acid, ketone, epoxy, ether, peroxide, amino, nitro, cyanide, diazo, azide, oxime or halides), which is aliphatic, benzenic and aromatic, preferably methane, ethane, propane, butane, pentane, hexane, heptane, octane, nonane, decane, undecane and/or dodecane. The reforming gas is a natural gas comprising sulfur, which is removed in the prior process, preferably to reduce deca sulfur 0.4 (preferably 0.01) vol.%. The part or entire lining reacts with sulfur present in (D) and the section of the lining is utilized as sacrificial lining. (D) (having a boiling point less than 150degreesC (preferably less than 100degreesC)) is: a biogas (comprising: methane (35-70%), carbon dioxiode (35-60%), hydrogen (0-3%), oxygen (0-1%), nitrogen (0-3%), various gases (sulfurated hydrogen or ammonia) (0-5%) and water vapor) resulting from fermentation of various organic material; or a natural gas (comprising methane (70-99%), ethylene (0-10%), ethane (0-25%), propane (0-10%), butane (0-8%), hydrogen (0-5%), carbon monoxide (0-2%), oxygen (0-2%), nitrogen (0-15%), carbon dioxide (0-10%), water (0-2%) and 5-12C hydrocarbons (0-3%)); an organic compound (methanol and/or ethanol) of molecular structure constituted by carbon and hydrogen such as alcohols, ethers, ethyl oxide, phenols, aldehyde, ketones, acids, amines, amides, nitriles, esters, oxides or oximes or heteroatoms (oxygen and nitrogen); and inert gases of group VIIIA of periodic classification (CAS numbering). The mixture of gas supplied to the reaction chamber comprises oxygen (less than 5 %). The mixture of (D) and oxidizing gas comprises methane (25-60 (preferably 35-50)%), water vapor (0-75 (preferably 20-50)%) and carbon dioxide (0-75 (preferably 20-50) %). The mixture of gas to be reformed and oxidizing gas is constituted by methane (39%), and the oxidizing gas is constituted by water vapor (49%) and carbon dioxide (12%). The atomic molar ratio of carbon/oxygen in the mixture of gases is 0.2:1 (preferably 0.65:1). Preferred Process: The electrical process further comprises: (i) preparing a mixture of (D) and oxidizing gas within or outside the reforming reactor; (ii) contacting the mixture with the lining of (B) preferably by passage in a hollow electrode; (iii) applying an electron flow for making the electrodes active in (B); (iv) heating the lining of (I) by electron flow at a temperature allowing the catalytic transformation of the gaseous mixture; and (v) recuperating the mixture of gas, preferably by passage in another hollow electrode. The steps (iii) and (iv) are carried out before the step (ii). The lining of (B) is pre-heated before (D) and oxidizing gas at 300-1500degreesC under inert atmosphere (nitrogen) before the step (iii). The step (iii) is carried out by AC or DC current, which is modulated by the level of temperature in the reactor (preferably uninterrupted by avoiding stoppages and while applying the changes moderated to the intensity of current). The steps (ii), (iii) and (iv) are carried out at 300-1500 (preferably 700-900)degreesC and at a pressure higher than 0.001 (preferably 0.5-20) atmospheres, which is maintained constant during reforming. The process is carried out continuously or discontinuously (30 minutes). The reforming reaction is catalyzed by micro-arc jumping between the lining particles or by sites activated at the surface of the lining particles by accumulation of charges and/or passage of electrical current. The lining is replaced between two periods of processing. The process of reforming of methane in the presence of carbon dioxide and water vapor in (B) of a volume of 322 cm3 (26.5 liters) comprising (a conducting lining constituted by steel wool (50 g) or steel filaments (with diameter of 0.5 mm) defining a porous medium, which is constituted by an alternation of layers of the steel wool compacted from each other at roughly 1 cm; and two metallic electrodes (made of carbon steel each constituted by a pipe a length of 30.48 cm and a hollow disc of a diameter of 6.35 cm; or rod of length of approximately 50 cm and a disc of a diameter of approximately 15 cm),(the disc is perforated and provided with projections to ensure a good contact with the lining); comprising mixing gaseous reactive (methane, carbon dioxide and water vapor with concentrations of around 39%, 12% and 49% respectively); introducing the mixture into the reaction chamber by injection into the input electrode; contacting the mixture with the lining; applying an electron flow to make the electrodes of the reaction chamber active (the flow is obtained by a continuous electrical current of a intensity of approximately 150 ampere); heating the lining by the electron flow at a temperature of approximately 780degreesC and production of a movement of electrons to facilitate catalysis by supply of an electrical current by the two electrodes; and evacuating and recuperating the gas in the reactor by passage into the outlet electrode (where the gas is constituted by hydrogen, carbon monoxide, oxygen, methane and carbon dioxide with the concentrations of 69 %, 28 %, 0.4 %, 1.7 % and 0.9 % respectively on an anhydrous and normalized base). In the process: the introduction of the mixture into the reaction chamber is by injection at the level of the radial or tangential openings of the reaction chamber; and evacuation and recuperation of gas from the reactor is by axial, tangential or radial flow with the help of axial, tangential or radial openings. In the process of reforming methane, the application of an electron flow to make the electrodes of the reaction chamber active (the flow is obtained by a continuous electrical current of a intensity of approximately 500 amperes).