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6 3 24 •rH a ,, s o z. ^o S >•« 0) (-. 1—< «5 O a «-» anode II to 4-> 0) ft »I «-2 »J »4 • y »4 »7 •J »^ current d e n s i t y ( A / c m 2 ) Fig 1 . 7 Relation of metal removal rate w i t h current d e n s i t y 39 3. 2. 4 Surface Status The surface was smooth and glossy after decontamination, it was much better than that of batch decontamination. It was mainly because that the gap between electrodes was much narrow than that used in batch cleaning, the anode rotated and cathode moved, that ensured the electrolysis uniformity.

ACKNOWLEDGEMENT The main part of this study was financed by the Nuclear Waste Commission of Finnish Power Companies. , Activity inventory of the activated decommissioning waste in the Loviisa nuclear power plant, Nuclear Waste Commission of Finnish Power Companies, Report YJT-89-02 (1989). , Activity inventory of the activated decommissioning waste in the Olkiluoto power plant, Nuclear Waste Commission of Finnish Power Companies, Report YJT-89-12 (1989). , Long-lived activation products in reactor bioshield material, Technical Research Centre of Finland, Reactor Laboratory, Technical Report KÄPÖ/5/89 (1990).

2. 6. The voltage could be estimated with voltage known for certain diameter of pipe. If the voltage needed closes to or exceeds the range of adjustable voltage, suitable cathode should be designed again. 3. 2. 7 showed the metal removal rate at various current density for anode I and II. The results indicated that metal removal rate depended on the electrode separation strongly at the same current density, comparison with batch electropolishing, the metal removal rate was lower by 2 - 5 times.

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