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Mixer settler electroreduction

Today there exist technically mature apparatuses an electroreduction column (17) for the U/Pu separation in the AGNS Plant, Barnwell and an in-situ electro-reduction mixer settler, installed in the 2nd Pu-cycle in the German WAK Plant, Karlsruhe. [Pg.292]

Figure 1. Principle of the electroreduction mixer settler MILLI-EMMA (8) A, mixing chamber B, aqueous phase C, organic phase D, interface E, anode... Figure 1. Principle of the electroreduction mixer settler MILLI-EMMA (8) A, mixing chamber B, aqueous phase C, organic phase D, interface E, anode...
Figure 2. U-Pu separation (Experiment no. 33) concentration profile in the 16-stage electroreduction mixer settler, MILLI-EMMA (8) [HNOs], [N2H5N03] in mol/L [U], [Pu] in g/L [TBP] in vol % flows in mL/hr. Figure 2. U-Pu separation (Experiment no. 33) concentration profile in the 16-stage electroreduction mixer settler, MILLI-EMMA (8) [HNOs], [N2H5N03] in mol/L [U], [Pu] in g/L [TBP] in vol % flows in mL/hr.
Parallel with the electro-reduction mixer settler an electroreduction column with a 10 cm diameter has been developed at Karlsruhe. [Pg.297]

The conversion rate of about 1,3 g U(IV) per Ah, calculated by means of the column concentration profile, hold-up and operating current corresponds to the value found for the electroreduction mixer settler. [Pg.301]

See other pages where Mixer settler electroreduction is mentioned: [Pg.302]   
See also in sourсe #XX -- [ Pg.305 , Pg.306 , Pg.313 ]



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