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IGCAR : Annual Report - Indira Gandhi Centre for Atomic Research

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IGC<br />

<strong>Annual</strong> <strong>Report</strong> 2007<br />

IV.A.2. Radiation Stable Resins <strong>for</strong> the Recovery of<br />

Actinides and Palladium<br />

The purification and<br />

concentration of plutonium<br />

from dilute process solutions<br />

are major steps in nuclear spent<br />

fuel reprocessing in current<br />

PUREX plants. Due to its<br />

simplicity, ion exchange<br />

processes have advantages<br />

over the other separation<br />

methods <strong>for</strong> the concentration<br />

and purification of plutonium.<br />

Anion exchange process is<br />

being commonly used by most<br />

of the nuclear plants and<br />

laboratories <strong>for</strong> plutonium<br />

processing and purifications.<br />

The inability of several elements<br />

to <strong>for</strong>m the anionic complexes<br />

in nitric acid solution makes it<br />

possible to get a better<br />

decontamination factor. The<br />

conventional anion exchange<br />

resins have a styrene-DVB<br />

based coplymers matrix.<br />

In India, the purification and<br />

concentration of plutonium is<br />

carried out by conventional<br />

anion exchange. The two major<br />

problems which have been<br />

encountered during plutonium<br />

purification using the anionexchange<br />

process are<br />

i) very slow sorption and<br />

desorption kinetics,<br />

ii) radiation degradation of<br />

the anion-exchange resin in<br />

intense radiationfield.<br />

The use of resin beads with<br />

high porosity and lower bead<br />

size is preferred to overcome<br />

the slow kinetics. The<br />

combination of hostile<br />

conditions such as high<br />

radiation and concentrated<br />

nitric acid can degrade the<br />

resins and various accidents<br />

had been reported during the<br />

anion-exchange process of<br />

plutonium purification. Thus,<br />

anion-exchange resins, which<br />

possess high radiation and<br />

chemical stability, are preferred<br />

<strong>for</strong> the purification of<br />

plutonium. From the literature it<br />

is found that pyridine-based ion<br />

exchangers have the highest<br />

order of radiation stability. This<br />

is because vinylpyridine resins<br />

are less susceptible to<br />

electrophilic attack than the<br />

styrene-based resins. At the<br />

centre, a programme has been<br />

initiated to synthesise and<br />

develop gel-type 4-<br />

vinylpyridine(PVP) resins <strong>for</strong><br />

plutonium processing and<br />

precious metal recovery. The<br />

PVP resins were synthesized by<br />

suspension polymerization<br />

technique and after that resin<br />

was methylated with<br />

iodomethane. Three different<br />

cross-linked (4, 8, and 12%)<br />

gel-type 4-vinylpyridine resins<br />

were characterized, and<br />

evaluated <strong>for</strong> processing and<br />

purification of plutonium and<br />

palladium from nitric acid<br />

medium. For palladium<br />

recovery PVP resin was used as<br />

it is and <strong>for</strong> plutonium<br />

methylated resin was used. The<br />

results were compared with<br />

those obtained with the<br />

conventional anion-exchange<br />

resin namely, Dowex 1X4,<br />

which has been studied<br />

extensively.<br />

Variation of DPu(IV) as a<br />

function of acidity<br />

From Fig.1 its is seen that<br />

D Pu(IV) value of 4% cross-linked<br />

PVP resin is lowest at all<br />

acidities and <strong>for</strong> 8% the D Pu(IV) is<br />

highest. In Dowex 1x4, the<br />

maximum D Pu(IV) value is<br />

attained at 7 - 8 M, whereas <strong>for</strong><br />

PVP resins, the maximum shifts<br />

towards 8 - 10 M nitric acid.<br />

The D Pu(IV) <strong>for</strong> 8% and 12%<br />

crosslinked resins is high as<br />

compared to Dowex 1X4.<br />

Elution studies<br />

The column per<strong>for</strong>mance of<br />

PVP resins was compared with<br />

that of Dowex 1X4 under<br />

similar conditions. Pu(IV) was<br />

loaded from 8 M nitric acid and<br />

FUEL CYCLE 83

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