(374c) Removal of Acetic Acid from a Urex+ Raffinate Stream | AIChE

(374c) Removal of Acetic Acid from a Urex+ Raffinate Stream

Authors 

Mitchell, J. - Presenter, University of Tennessee-Knoxville
Del Cul, G. (. - Presenter, Oak Ridge National Laboratory
Spencer, B. - Presenter, Oak Ridge National Laboratory
Counce, R. M. - Presenter, University of Tennessee-Knoxville
Watson, J. - Presenter, University of Tennessee-Knoxville


In the UREX+ process, acetohydroxamic acid is added to the UREX step to suppress plutonium extraction. Hydrolysis of acetohydroxamic acid (AHA) produces acetic acid and hydroxyl ammonium nitrate (HAN). The capability to remove acetic acid from aqueous process solutions is desirable as UREX+ flowsheets continue to evolve. To enable recycling of the nitric acid solution and to prevent problems in downstream process steps in the nuclear fuel processing plant, acetic acid should be removed from those streams.

After a literature review, solvent extraction was determined to be the most promising approach for removal of acetic acid. The goal was to identify a solvent that is both insoluble in the aqueous phase and will selectively remove acetic acid. Solutions of tributylphosphate (TBP) have been shown to selectively extract acetic acid over nitric acid with sufficiently high distribution coefficients. Extractant solutions tested in this study include TBP in dodecane and TBP in phenyltrifluoromethyl sulfone (FS-13). The two solvents are both compatible with the UREX+ process flowsheets, so selection of the solvent will be based on the placement of the removal step. The location of the removal step within the process is dependent on many factors. Factors considered in this study include avoiding raffinate stream solutions containing quantities of actinides that TBP would extract, interference with acetic acid with each downstream step, and the amount of nitric to acetic acid in each step so the distribution coefficient can be maximized.

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