2015
DOI: 10.1016/j.jhazmat.2015.04.003
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Dialkylmethyl-2-(N,N-diisobutyl)acetamidoammonium iodide as a ruthenium selective ligand from nitric acid medium

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Cited by 9 publications
(4 citation statements)
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References 22 publications
(32 reference statements)
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“…For extraction studies with such extractants, isodecyl alcohol (IDA) is commonly used to enhance the solubility, as well as acting as a phase modifier to suppress the formation of a third phase. 24,25 Therefore, IDA was chosen as a co-solvent to enhance the solubility and 30% IDA in n-dodecane was found to be suitable for making a clear 0.1 M solution of the OTDA 1a and 1b. The time required to attain equilibrium for the extraction of Pu(IV) was determined for 0.1 M OTDA 1a in 30% IDA/n-dodecane at a 4 M feed HNO 3 concentration.…”
Section: Extraction Studies With Otdasmentioning
confidence: 99%
“…For extraction studies with such extractants, isodecyl alcohol (IDA) is commonly used to enhance the solubility, as well as acting as a phase modifier to suppress the formation of a third phase. 24,25 Therefore, IDA was chosen as a co-solvent to enhance the solubility and 30% IDA in n-dodecane was found to be suitable for making a clear 0.1 M solution of the OTDA 1a and 1b. The time required to attain equilibrium for the extraction of Pu(IV) was determined for 0.1 M OTDA 1a in 30% IDA/n-dodecane at a 4 M feed HNO 3 concentration.…”
Section: Extraction Studies With Otdasmentioning
confidence: 99%
“…Many numbers of reports are available on the extraction and recovery of ruthenium from the acidic medium. Similarly, separation of ruthenium from a chloride medium has been well established by several researchers due to the propensity of formation of the anionic chloro complex in a chloride/HCl medium. , Various anion exchangers containing quaternary ammonium halide and trialkylamines as active functional groups were utilized to separate the anionic chloro complexes from the aqueous chloride medium. , Separation of ruthenium from aqueous nitric acid is more difficult, which makes the ruthenium separation very challenging at the nuclear back end cycle where the overall medium is 2–3 M HNO 3 . , Ruthenium tetroxide is found to be soluble in certain organic solvents such as CCl 4 . The removal of ruthenium in the form of ruthenium tetroxide from the PUREX process waste stream has been reported with paraffin oil.…”
Section: Introductionmentioning
confidence: 99%
“…The separation of ruthenium from an alkaline medium is equally important as it is present in substantial quantity (∼2 × 10 –2 –2 mCi/L depending on fuel cooling period) in intermediate level liquid waste. There are many sources of this waste which are as follows: (i) metallic decladding operation of spent nuclear fuel at the reprocessing site, (ii) evaporation and neutralization of process condensate during the evaporation of acidic HLLW to concentrate, and (iii) purification of degraded TBP solvent through carbonate washing. The ruthenium separation from this alkaline waste is more difficult than acidic HLLW because of alkalinity and high salt content. For this reason, very limited literature is available on the Ru separation from alkaline ILLW.…”
Section: Introductionmentioning
confidence: 99%
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