in a preferred method of implementation , the oxygen and / or ozone molecules that are formed by recombination of the free radicals o . produced in said plasma are re - dissociated . it is thus possible to increase the density of uncharged active species that are distributed over the surface of the strip independently of the electric field , further improving the uniformity of the treatment . this re - dissociation may be carried out by means of uv radiation of suitable wavelength , which allows the ozone produced by recombination away from the cold arcs to dissociate into molecular oxygen and into the radical o . in another preferred method of implementation , a sinusoidal voltage , the frequency of which is between 10 and 100 khz , is applied in order to initiate the discharge . indeed , this type of voltage results in the almost continuous presence of active species in the inter - electrode space , thereby making it possible to achieve high kinetic yields . in another preferred method of implementation , the energy dissipation in the discharge is less than 40 w / cm 2 and the voltage applied in order to initiate the discharge is less than 4 . 4 kv . the present inventors have in fact found that the inhibiting effects due to the polymerization of the oil are greater the higher the applied voltage and that the surface treatment is nonuniform . this is because the oxidation and elimination of the oil take place essentially at the point where the discharges impact on the strip , whereas the oil polymerizes away from these more intense glow channels . increasing the voltage across the terminals of the discharge results in an increase in the energy of the electrons that all the more easily initiate the polymerization of the oil . the process according to the invention may furthermore have the following features , individually or in combination : the voltage applied in order to initiate the discharge is sinusoidal ; the material is in the form of a running strip and the various steps of the process are carried out continuously by means of installations placed in succession along the path of the running strip ; one of the faces of the material is treated followed by the other ; the material to be treated is a metallic material , preferably a carbon steel ; and the process is carried out in order to degrease the surface of metallic materials , prior to a coating being deposited on this surface . a second subject of the invention consists of an installation which comprises at least one module comprising a treatment chamber , means for setting the pressure inside said chamber to a value between 10 mbar and 1 bar , means for making said grounded strip run through said chamber , a series of dielectric - covered electrodes placed so as to face that surface of said strip to be treated , these electrodes being connected to a sinusoidal high - voltage generator , means for supplying said chamber with gas and means for extracting from said chamber the gases resulting from the decomposition of the organic substance coating the strip . in a preferred embodiment , said installation comprises a succession of an even number of said modules , through which said strip runs in succession , exposing in turn one of its faces to the electrodes of said modules . in another preferred embodiment , said installation furthermore includes uv emission lamps placed between said electrodes . the invention will be illustrated by the description of two embodiments given by way of indication , but implying no limitation , with reference to the appended drawings in which : fig1 shows a schematic view of a treatment installation according to the invention ; fig2 shows a schematic view of a treatment installation according to the invention for a successive treatment of the two faces of a material in the form of a running strip ; fig3 a and 3b show two images of surfaces of strip treated in the presence of uv irradiation ( fig3 b ) and without said irradiation ( fig3 a ); fig4 demonstrates the increase in density of the oxygen radicals during the additional application of uv radiation at 253 nm ; fig5 shows the dependence of the oxygen radical density as a function of the intensity i of the current applied in the discharge ; fig6 shows the change in protective oil coating weight present on a strip as a function of the electron dose it / s which is applied to it ; and fig7 shows the auger electron spectrum of the surface of a strip degreased using a discharge involving an electron dose of 21 mc / cm 2 . fig1 shows a diagram of an installation according to the invention for implementing the process according to the invention , in order to treat a metal strip made for example of carbon steel . this installation comprises a module 1 consisting of a treatment chamber 2 in which there is a cooled roll 3 around which the metal strip 4 runs . the roll 3 and the strip 4 are grounded . pumps ( not shown ) allow the pressure inside this chamber 2 to be set to a value between 10 mbar and 1 bar . electrodes 5 a , 5 b , 5 c , 5 d , 5 e , 5 f and 5 g covered with a dielectric ( alumina ) are placed so as to face the strip 4 . these electrodes 5 a , 5 b , 5 c , 5 d , 5 e , 5 f and 5 g are connected to the high voltage supplied by a medium - frequency sinusoidal generator 6 ( the frequencies being between 10 and 100 khz ). the high - voltage electrodes 5 a , 5 b , 5 c , 5 d , 5 e , 5 f and 5 g are also cooled . in order to optimize the energy invested in the discharge , the fixing of the high - voltage electrodes 5 a , 5 b , 5 c , 5 d , 5 e , 5 f and 5 g allows the inter - electrode distance to be varied . the module also includes means for supplying said chamber with gas , and means for extracting from said chamber the gases resulting from the decomposition of the organic substance coating the strip 4 ( these means not being shown ). in this particular embodiment , uv lamps 7 a , 7 b , 7 c , 7 d , 7 e and 7 f are placed between the high - voltage electrodes 5 a , 5 b , 5 c , 5 d , 5 e , 5 f and 5 g so as , on the one hand , to allow the treatment at the discharge to be made uniform and , on the other hand , to allow the ozone , which is formed away from the inter - electrode volume , to dissociate . consequently , the strip 4 may continue to be degreased away from the inter - electrode space by the o . radicals coming from the dissociative absorption of the ozone induced by applying the additional uv ( 253 nm ) radiation . fig2 is a schematic representation of an installation according to the invention that comprises a succession of four modules 10 , 11 , 12 and 13 for carrying out a successive treatment of both faces of a running strip 14 . the four modules 10 , 11 , 12 and 13 are connected together via intermediate components housing the pumping set and the gas injection system , which ensures that the installation is exposed to the stream and therefore ensures that the treatment is uniform , despite the characteristics of the inhomogeneous discharge . trials were carried out on small - sized ( 20 to 25 cm 2 ) strips in static mode , these being coated with a protective oil ( tinnol 200 ® from quaker chemical ) as it was necessary to complete the degrease , in order to simulate a cleaning treatment before coating . the trials were carried out in a dielectric barrier reactor consisting of an electrode covered with a 0 . 7 mm layer of alumina and of a grounded metal electrode over which the strip to be treated is placed . the alumina - covered electrode was connected to the high voltage ( 350 to 4400 v ). the high voltage was delivered by a medium - frequency ( 3 to 30 khz ) sinusoidal generator . the two electrodes were equipped with a cooling system allowing them to remain at temperatures close to ambient temperature during operation of the plasma . the inter - electrode distance may be set between one millimeter and several tens of millimeters . two identical carbon steel strips , coated with a 186 mg / m 2 protective oil layer were treated . the other parameters were identical for the two treatments , namely : 200 mbar of oxygen ; 12 khz sinusoidal voltage ; 3 . 6 kv ; current : 30 ma ; inter - electrode distance : 5 mm . the strip treatments illustrated in fig3 a and 3b differ only by uv radiation being imposed in one case and not in the other . fig3 shows images of the surface of strips treated by a discharge initiated in just oxygen , with ( fig3 b ) and without ( fig3 a ) additional uv ( 253 nm ) irradiation . the dark areas correspond to the non - greased regions where the oil has polymerized . it may be seen that applying uv radiation in addition to the discharge results in less polymerization of the oil , thus allowing better cleaning , in a shorter time . applying uv radiation whose wavelength corresponds to the dissociative absorption of ozone results in the uniform presence of oxygen radicals on the surface of the strip that allow cold combustion of the oil . applying uv radiation in addition to the discharge results not only in a more uniform distribution of the oxygen radicals on the surface of the strip , but it also increases the density of the o radicals , all the discharge parameters ( voltage , frequency of application of the voltage , current , pressure and inter - electrode distance ) remaining constant . fig4 demonstrates the increase in density of the oxygen radicals during application of 253 nm uv radiation by means of optical emission spectroscopy ( oes ). the emission wavelength of the excited oxygen radicals lies at about 777 nm . this figure shows the intensity i 777 of the radiation at 777 nm as a function of time t . the various regions of the graph correspond to the following phases : zone a : no electrical discharge or uv radiation applied . the recorded intensity corresponds to the background noise ; zone b : an electric discharge has been applied in pure oxygen , without uv radiation being applied ; zone c : in addition to the electric discharge , uv radiation at 253 nm has been applied ; zone d : the uv radiation is maintained , but in the absence of electrical discharge ; and zone e : the uv radiation is stopped and the background noise returns . fig5 shows , using optical emission spectroscopy , that the density of active oxygenated species o . varies linearly with the intensity of the current applied in the discharge . the discharge currents plotted in this figure were varied both at constant voltage , by varying the rate of application of the v , and therefore varying the impedance of the dielectric , and at constant frequency by varying the voltage . this fig5 therefore shows that the density of active species depends only on the intensity of the discharge current and is not in any way influenced by the discharge voltage at constant current . this means that it is possible to obtain the same density of active species at power levels that differ only by the imposed voltage , the current remaining constant . however , it has been found that too high a voltage results in polymerization of the oil , which tends to inhibit the rate of oxidation of the organic residues present on the surface of the strip . in addition , industrial application requires the dissipation of a minimal energy density ( less than 40 w / cm 2 · s ) in the discharge . consequently , the discharge conditions needed for degreasing a strip are achieved by maximizing the current for a minimal imposed voltage . the influence of the power of the discharge at constant current on the rate of degreasing is demonstrated in the table below , which combines two tests carried out by varying the frequency of the applied sinusoidal current : discharge percentage frequency power ( w ) voltage ( v ) degreasing ( khz ) 110 3400 83 % 10 55 1720 87 % 20 it may therefore be seen that , at equal discharge current , and for an identical treatment time , the efficiency of the degreasing is better at lower voltage and therefore at lower power . a 20 cm 2 strip covered with 186 mg / m 2 of protective oil was treated by the process according to the invention . in the present case , the discharge was initiated in a stream of oxygen at a pressure of 350 mbar . the oxygen and / or ozone molecules formed from the recombined free radicals o . were not re - dissociated . fig6 shows the change in coating weight of protective oil present on the strip as a function of the electron dose it / s ( i . e . the electron current density multiplied by the treatment time ). application of the stream allows uniform treatment of the strip , which was confirmed by grazing - incidence infrared absorption spectroscopy ( irras ). fig7 shows the auger electron spectrum of the surface of the strip degreased using a discharge involving an electron dose of 21 mc / cm 2 . only the iron and oxygen peaks are present . the absence of a carbon peak around 273 ev confirms that the strip was completely degreased .