in the method according to this invention , the savings of electric energy , which is first generated in a conventional power plant or by means of nuclear or solar energy with an efficiency of between 15 and 35 %, theoretically corresponds to the free formation enthalpy of the reactions which proceed during the electrolysis simultaneously as coupled reactions . the second process step required in the method according to the invention , the thermal dissociation or decomposition , can generally be performed in the temperature range of up to about 900 ° c . this process step can , therefore , also be combined with a high - temperature reactor ( htr ). the advantage of the method according to the invention is , therefore , seen particularly in the reduced use of valuable electric energy and in the separation of materials in the individual steps , which can be simply performed . to increase the conductivity , it is advantageous in the method according to the invention to add , as is done in conventional water electrolysis , an alkali solution or acid to the water , preferably sodium hydroxide or sulfuric acid . besides water thus provided with additional materials , aqueous solutions of other substances may also be used in the method for generating hydrogen according to the invention , particularly solutions of hydrohalogenides or alkali halogenides . the electrolysis of a hydrochloric solution , i . e ., of hydrochloric acid , for example , proceeds according to the following scheme : hydrogen being developed at the cathode and chlorine at the anode . in the electrochemical decomposition of an aqueous sodium chloride solution , the so - called electrolysis of alkali metal chlorides or chlorine alkali electrolysis , the following reaction occurs : these two reactions , therefore , can also serve for the production of chlorine , besides hydrogen ; moreover , in the chlorine alkali electrolysis , sodium hydroxide is additionally produced in the form of soda lye . in the electrolysis of such aqueous solutions , as in the electrolysis of water , there can be utilized , in accordance with the method of the invention , a cathode material which binds hydrogen in the undervoltage range , and the amount of electric energy required can be reduced . in the method according to the invention , hydride - forming metals , preferably tantalum or palladium , and hydride - forming metal alloys , preferably of vanadium - niobium or nickel - titanium , can be used as cathode materials . in principle , however , all metals and alloys can be used which have a negative hydride formation enthalpy , i . e ., which incorporate hydrogen into the lattice while giving off energy ( exotheric reaction ). such substances are , for example : mg , ti , v , nb , u , mg 2 ni , tife , lani 5 and prco 5 . however , a metal which adsorbs hydrogen at the surface while giving off energy may also be used as cathode material . preferred among such metals are platinum or nickel , which is employed preferably in the form of raney nickel . in the system lani 5 / h 2 , for example , a desorption heat of 7 . 2 kcal / mol h 2 must be supplied in the dissociation of hydrogen . by about this amount , the free reaction enthalpy δg of the electrolytic water dissociation will then also be reduced , i . e ., from 56 . 7 kcal / mol to about 50 kcal / mol . this means a gain in electric energy of about 12 %. the gain in electric energy can be still higher , however , i . e ., 30 % and more , as will be shown in the discussion which follows . in the water electrolysis according to the method of this invention , there may further be advantageously employed an anode material which forms an oxide in the corresponding undervoltage range , i . e ., in a range which is more negative than the reversible oxygen potential . in this manner , the amount of electric energy required for the electrolysis can be reduced still further . the oxygen is subsequently split off thermally from the oxide obtained in the electrolysis . metals , particularly silver or mercury , and metal oxides , particularly manganese ( iii ) oxide mn 2 o 3 , may preferably be utilized as anode materials . accordingly , anode materials may be used , for example , in the electrolysis of aqueous hydrogen halides or alkali halides solutions , which form halogenides in the undervoltage range ; these halogenides are then decomposed thermally to give off halogen . the potential range in which the halogenide formation takes place must always be more negative than the reversible oxygen potential which is about + 1 . 23 v , relative to the potential of the reversible hydrogen electrode . in addition , this potential range must also be more negative than the corresponding reversible halogen potential which , in the case of bromide , for example , is + 1 . 07 v and in the case of chlorine , + 1 . 36 v . in the method according to the invention , electrode materials in power form are preferably employed . such materials for the cathode and , optionally also for the anode , have the advantage that they have a large surface and therefore a high storage capacity for hydrogen and oxygen or halogen . the invention is further illustrated with the aid of the following embodiment examples and figure . example 1 cathode material : ta anode material : mn 2 o 3 or mno ( oh ) electrolyte : aqueous naoh . during the electrolytic process , hydrogen atoms are formed at the cathode by cathodic reduction and incorporated in the undervoltage range into the metal lattice of the tantalum . at the anode , manganese ( iv ) oxide i . e ., mno 2 is simultaneously generated at the same time from the manganese ( iii ) oxide through anodic oxidation . the savings of energy in the reversible case over the customary water electrolysis can be taken from the figure . thus , instead of the otherwise required amount of 1 . 23 v , the dissociation voltage of the water is only 0 . 83 v . this corresponds to a reduction of the amount of electric energy required from 237 . 4 kj / mol h 2 o to 160 . 2 kj / mol h 2 o . in the decomposition of the tantalum hydride into tantalum and hydrogen and the decomposition of mno 2 into mn 2 o 3 and o 2 , the difference of 77 . 2 kj / mol must then be supplied as thermal energy . this energy must be supplied in the case of tantalum hydride at about 400 ° c . and for mno 2 , at about 500 ° c . the theoretical savings of electric energy are 32 . 5 %. as a finite reaction rate is desired , higher dissociation voltages must be employed in the practical implementation of the method according to the invention , as is done in conventional electrolysis . in practice , the electrolysis operations are conducted with a voltage of about 2 . 0 to about 2 . 2 v and a current density of about 200 ma / cm 2 . the reason for the large overvoltage is substantially the irreversibility of the oxygen electrode . however , in the method according to the invention , oxygen formation is circumvented and therefore the overvoltage is lower so that the energy savings are still more favorable than is found by the theoretical consideration . in order to obtain high current densities in the electrolysis and to maintain the diffusion paths in the solid body small , it is advantageous to use electrode materials with large surfaces . the following possibilities , in particular , are available for this purpose : ( a ) plates pressed and / or sintered from powdered material , which can be removed from the electrolyte cell after the electrolytic process is completed and , after a washing and drying process , are fed to the thermal regeneration facility ; ( b ) materials in powder form which are placed in the respective electrode space and are made into a sludge with electrolytic liquid ; in the electrolyte chamber , there is additionally provided a metallic conductor for applying the voltage , for example in the form of a sheet of metal in the case of a bipolar arrangement , and a grid plate or a diaphragm for defining the electrolyte chamber . the use of electrode materials in powder form also has the advantage that the electrolysis can be performed continuously . to be regenerated , the electrode material is taken from the cell , washed , dried and fed to the thermal decomposition . the following reactions take place with the above - mentioned electrode materials : the thermal dissociation of the manganese dioxide ( mno 2 ) takes place at about 530 ° c . with a noticeable reaction ; between about 850 ° and 940 ° c ., mn 3 o 4 is formed , while more oxygen is being given off . palladium stores hydrogen atoms in the lattice with an undervoltage of about 50 mv . the voltage remains constant until the conversion into the β - palladium hydride is complete . silver is oxidized to ag 2 o at - 56 mv , as measured against the reversible oxygen potential . hydrogen can be split from the palladium hydride at about 200 ° c . ; the equilibrium dissociation pressure is then 5 bar . oxygen is given off from the ag 2 o above 350 ° c . if a nickel cathode is used , no hydride is formed during the electrolysis , but a superficial coating of the nickel with hydrogen atoms is obtained . in order to achieve a satisfactory charging capacity , a material with a large specific surface is used . such a material is present , for example , in raney nickel , as there is 1 h - atom to 5 ni - atoms . if platinum is utilized as the cathode material , one may also work with an acid solution . the build - up of the cathode hydrogen coating takes place here in the undervoltage range of 100 to 300 mv . the metallic mercury is oxidized to hgo at - 303 mv relative to the reversible o 2 potential , and is then taken to the thermal decomposition facility . cathode material : vnb anode material : mn 2 o 3 electrolyte : aqueous koh . the procedure is as in example 1 . during the electrolysis , the hydride vnbh 3 is formed at the cathode from which hydrogen is separated at 100 ° c . at a pressure of 10 bar . particularly niti 2 is used as cathode material . in the electrolysis , the hydrogen is incorporated into the lattice .