an embodiment of the present invention will be described below using fig1 to fig4 . fig4 shows the structure of a control rod for an advanced boiling water reactor , having an oval metal hafnium tube , that has been subjected to anodizing film treatment , in the embodiment of the present invention . this control rod comprises an upper handle 2 , a tie rod 5 , a sheath 3 , a lower connector plate 6 , and a coupling socket 7 , and is structured with oval tubes of metal hafnium 4 contained inside the sheath 3 . fig1 ( a ) is a horizontal cross section of a region containing the neutron absorber material of the control rod shown in fig4 . each end of the cruciform tie rod 5 is groove shaped , sheaths 3 formed with a u - shaped cross - section are welded to each end of the tie rod 5 , and two oval metal hafnium tubes are contained in each space thus formed . there are cases where the plate thickness of metal hafnium is caused to vary in the direction of the axis of the control rod , and cases where the metal hafnium is further divided into a number of tubes in the axis direction . fig1 ( b ) is an enlarged schematic drawing of the oval tube metal hafnium 4 of the present invention . the oval tubular shape of the metal hafnium is formed by half oval shapes like the members 4 - 1 and 4 - 2 shown in fig1 by subjecting metal hafnium plates to bending , then the members 1 - 4 and 1 - 2 are joined at the ends and fixed by welding . a surface oxide film 4 &# 39 ; is formed on the surface of the oval hafnium tubes by anodizing . fig2 is a flowchart showing the fabrication sequence for metal hafnium , having an oval tube cross section and provided with an anodized film . the raw material is pure metal hafnium having purity of 95 % or more , and material certification is carried out at the time of entering the manufacturing process . next , bending work is carried out using a pressbrake to impart a radius of curvature at both ends of the long plates . machining of the grooves for welding is then carried out . after that , welding inspection certification , and cleaning treatment is carried out . at this stage , the two oval tube half members 4 - 1 and 4 - 2 shown in fig1 have been formed . the two oval halves are joined at the ends , and an oval tube is made by welding them together . machining is then carried out to form cooling holes and fixing holes , etc . in the oval tube , and finishing processing is carried out . at the stage where these processes have been completed , anodizing treatment is carried out in an electrolyte bath . fig3 is a schematic drawing showing equipment for carrying out the anodizing treatment . anode material comprising a stainless steel anode 9 , for anodizing the outer surface of the metal hafnium , integrally formed with a stainless steel anode 9 &# 39 ; for anodizing the inner surface of the metal hafnium tube , is provided in the electrolytic bath 11 , and the electrolytic bath 11 is filled with electrolyte 10 . circular holes 4h for fixing to a control rod structural member is formed in the metal hafnium oval tube , at an end in the longitudinal direction , and the metal hafnium is lowered using these circular holes 4h . a metal hafnium rod having a diameter smaller than the internal diameter of the circular hole 4h is passed through the circular holes 4h , and is connected to positive electrodes of a direct current source 12 by conductors through a raising and lowering device 13 . on the other hand , a conductor is taken out from the anode in the electrolytic bath , and connected to the negative electrode of the direct current source 12 . the metal hafnium pipe suspended from the metal hafnium rod 8 is dipped into the electrolytic bath , by the raising and lowering device 13 , so that the stainless steel anode 9 &# 39 ; having a smaller diameter that the internal diameter of the tube is inserted into the metal hafnium tube . when anodizing treatment is carried out , there is a current density per unit surface area of a cover oxide member at a level necessary to obtain a uniform oxidation film . as a result , in processing material having a fixed area , like the neutron absorber material used in the control rod in one go , there is a possibility that the necessary current level will become large , exceeding the normal usage range . using the raising and lowering mechanism 13 as shown in fig3 the processing region of the cover oxide member is divided into a few areas , to provide processing equipment that can carry out the process with a current level within a practical range . with respect to a necessary current density for anodizing metal hafnium at mass production levels , requirements are determined by additional measurements , but with examined effects for zircalloy having the same crystal lattice interstitial as hafnium and for which characteristics such as oxidation etc . are analogous , current density of about 1a / dm 2 is obtained . if calculations are made based on this , then in controlling processing current to be in a normal household level of 10a , in the case of an oval metal hafnium tube having a length of about 1800 mm and a width of about 50 mm , it can be presumed that it would be appropriate to divide the metal hafnium oval tube into four stages . therefore , at a first stage a quarter of the length of the metal hafnium oval tube is dipped in the electrolytic bath , current flows from the direct current source , and an anodized film is formed . after the anodized film has stabilized , the anodizing treated metal hafnium tube is lowered by the raising and lowering device , and a further quarter of the hafnium tube is dipped in the electrolytic bath , so that half of the tube is now immersed , and anodizing treatment is carried out . subsequently , a stabilized anodized film is formed in third and fourth stages . using the above process , the oval metal hafnium tube that has been provided with an anodized film on the surface is then subjected to inspection , is cleaned , and then normally progresses to control rod assembly processing , which completes the control rod containing neutron absorber material that has been subjected to anodizing treatment . a specific method of providing the anodized film on the surface of the metal hafnium will be described below . short test pieces have been prepared using a hafnium rod having the technical specifications of an actual reactor control rod . because film certification is carried out at a welded portion , weld material was also prepared as a test piece . electrolyte used in the test was ammonium borate [ 1 % ( nh 4 ) 2 o . 5b 2 0 3 ]. as a general electrolyte for use in anodizing treatment , koh or naoh can be used , but as boric oxide ions are larger than ions of metal such as k and na etc ., it is considered that they will have difficulty in sticking to the hafnium rod as impurities , which is why the aforementioned electrolyte is used . the electrolytic bath is filled with the electrolyte , and anodizing treatment is carried out using platinum as a cathode and the hafnium rod as an anode . at room temperature , direct current at fixed voltages of 100v , 200v and 300v is respectively made to flow between the two electrodes . the period of time for which current flow is maintained was five minutes , for the anodized film formed on the test piece to stabilize . with the above described method , visual inspection , corrosion resistance test and hardness test are carried out on the test piece which has been subjected to anodizing treatment . through the visual inspection formation of similar anodized film was observed on test pieces to which direct current having the foregoing values was applied . the surfaces of the welded portion were also no different from the surface of the base material , and it was observed that a favorable anodized film was formed . because of the influence of voltage , the tone of cover films formed at voltages from 100v to 300v varied from dark blue to dark green . this is a variation in the anodized film formed , and the thickness of a cover film can be judged from the tone . fig5 is a drawing showing oxidation weight after corrosion testing of the test piece that has been subjected to anodizing film treatment , under the conditions of a test temperature of 410 ° c . for eight hours and 530 ° c . for 16 hours , pressure of 105 kg / cm 2 , dissolved oxygen of 200 - 400 ppb , and flow rate of 10 liters per hour . the metal hafnium that has been provided with the anodized film was observed to have a tendency toward improved corrosion resistance compared to the base material without the anodized film . fig6 shows the measurement results of a hardness test on the test piece provided with the anodized film , taken using a micro vickers hardness meter . the metal hafnium that has been provided with the anodized film was observed to have a tendency towards increased surface hardness compared to the base material without the anodized film . however , if the compression load was increased , the hardness of the test piece provided with the anodized film tended to decrease , but with this increased load a compression head destroyed the cover film , and it can be considered that the cover film was also affected by the hardness of the internal base material . from the above described tests , it will be understood that an anodized film having excellent corrosion resistance and excellent wear resistance can be provided on the surface of metal hafnium that has welded portions , in a comparatively short time . with a control rod that is actually manufactured , in the case of a hafnium control rod used in an advanced boiling water reactor using metal hafnium oval tubes as a neutron absorber material , in the manufacturing process shown in fig2 there are cases where metal hafnium oval tubes are manufactured . in such a case , the previously described anodizing treatment process is added in the final process shown in fig2 by using equipment for electrolytic treatment as shown in fig3 there will be no significant influence on the manufacturing process , and it is possible to provide a neutron absorber material having excellent corrosion resistance and wear resistance . in the test , using voltage from 100v to 300v , favorable results are obtained in that the corrosion resistance and wear resistance do not differ greatly with different voltages , but in the processing for an actual product , a relationship between stable film formation and voltage or current value should be understood using an actual electrolytic bath , so that production will be carried out under ideal conditions to give high production efficiency .