Evaluation of a novel sorbent for recovery of radio-nuclides –a comparison of batch and column operation

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  • 8/3/2019 Evaluation of a novel sorbent for recovery of radio-nuclides a comparison of batch and column operation

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    actual effluents are in the neutral range therefore in each case the studies has been conducted at

    pH 7 to avoid any conflicts. The research presented here concerned the usefulness of the

    polymeric chelator for targeting uranium from a very low (ppb) concentration with respect to the

    presence of higher concentration of manganese. Our investigations carried out in terms of batch

    and column operation of the effluent. Batch experiment has been carried out in both actual and

    synthetic solution where as column has been operated with synthetic solution. This synthetic

    solution has been prepared targeting the inlet of a uranium mine effluent treatment plant.

    Experimental

    1. Resin Preparation of the resin has been described by initial solution polymerization method

    and later on by conversion of the functional moieties as described in our previous paper (S.

    Mishra et al, 2008). Prior to the experiment, the resin was washed with 0.1(N) HCl to eradicate

    un-reacted materials and to see the compatibility of the resin in that condition and after that

    thoroughly rinsed with de-ionized water.

    2. Feed solution- The feed solutions were prepared to stimulate the same quantity of uranium

    and manganese present in the actual effluent. The pH of the solutions was adjusted with HCl and

    NaOH.

    3. Eluent - 25 ml of 1(N) HCl solution was used for elution of 1 gm of sorbent.

    4. Sample Collection and procedures for the batch experiment:- For the application of this

    polymer in field conditions, the effluent treatment plant inlet sample and uranium tailings

    samples disposed in tailings pond were collected from Jaduguda. These samples were containing

    high concentration of Mn, U as well as other radionuclides and stable elements. Uptake studies

    were carried out by adding 0.5 gm of dried polymer in about 25 ml of treated effluent and

    tailings leachate sample in neutral pH, and also with the synthetic solution of uranium and

    potassium permanganate, whereas elution of the loaded sorbent completed with 1 (N) HCl.

    5. Immobilisation factor - Metal ion Immobilisation of a resin is the act of limiting

    movement or making incapable of movement of the metal ions by trapping or rather

    chelating it with the functional groups of resin, can be caluclated as

    immobilisation factor = (1- Elution factor)

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    6. Uranium loading - Resin (0.5 gm) was packed in a glass column of 1 inch ID, resulting in a

    bed height of 28 ml after equilibration with the desired synthetic solution. The spiked solution

    was adjusted to neutral pH. The spiked solution of uranium (60 ng/ml) and manganese (60

    ug/ml) down flowed at the rate of 4 ml/min at 40 ml effluent intervals and U and Mn

    concentration in the effluent was analyzed to determine break through point.

    7. Instrumentation and sample analysis- The estimation of manganese and uranium in the

    original feed sample ( i.e., before the sorption experiment), the filtrate and eluent obtained after

    the experiments were carried out by flame atomic absorption spectrophotometry using GBC-

    Avanta atomic absorption spectro-photometer and differential pulse adsorptive strripping

    voltammeter, respectively.

    Results and Discussion

    The capacity of the resin for the actual effluent has been presented in Table 1. Uranium and

    manganese in initial feed solution has been determined. The experiments have been conducted in

    duplicate and in static condition with actual (A) and synthetic solution (B) to achieve a

    comparative study.

    From the tabulated results (Table -1 and Table -2) it has been seen that initial uranium

    concentration is in ppb level for both the solutions (A) and (B), whereas manganese is present in

    ppm level. Sorption study was carried out contacting 25 ml of solution with 0.5 gm of resin in

    duplicate. The respective filtrates were tested. The filtrate containing negligible amount of

    uranium (Table -1) compared to manganese indicates the inlet of ETP after treating with sorbent

    can be disposed safely, as seawater having 3ppb level of uranium complex content on average.

    Table 2 also indicates a good percentage of sorption preferably uranium in the actual effluent,

    having a high distribution factor of 1450 ml/gm for uranium compared to manganese (Kd = 111.64

    ml/gm). Even synthetic solution treatment showed a 6 times greater value of uranium distribution factor

    compared to manganese. The elution results (Table -2) show efficient recovery for both (A) and

    (B) solution. It is indicative of the fact that not only it can be entrapped but all trapped uranium

    can be recovered, therefore a possibility of efficient reuse of the sorbent for scale up. When we

    have contacted the sorbent in column mode a good separation has been found, which supports

    the above fact, the sorbent in column rapidly chelated with uranium, still manganese remained

    that indicates time efficiency.

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    Conclusions

    The experimental studies revealed that the sorbent is useful for the uptake of uranium from the

    inlet of uranium mine effluent treatment plant very selectively and although present in very low

    concentration compared to manganese but still has the ability to form the chelates and can be

    recovered efficiently for uranium recovery and out let effluent of the treated sorbent can be

    safely disposed. Similarly we have experimented in column mode and have found 2 hrs are

    approximately sufficient to reach the desired pick up, although a thorough investigation is

    required to set up in pilot scale.

    Acknowledgement

    For procurement and preparation of resin material, help from Mr. Chunu Soren (DD) and for

    analytical sample preparation and analysis Mr. Dilip Kumar Chaudhary (EAD) is acknowledged.

    References

    1. S. Mishra, Sangita Pal, G. G.Pandit, P. K.Tewari and V. D. Puranik, 2008. Use of

    Polymeric Sorbent for the Uptake of Heavy Metals and Radionuclides from DifferentEffluents. Proceedings of the Sixteenth National Symposium on Environment on

    Groundwater Resources: Conservation and Management. pp 161-165.

    2. Sangita Pal, S. Mishra, G.G.Pandit, K.L. Thalor, P. K.Tewari and V. D. Puranik, 2008.

    Potentiality of polymeric sorbent for immobilization and recovery aspect of contaminants

    from nuclear efluents. In Chemcon-2008, under Safety and Hazards Control, Index no ST35, page. 355

    Table 1 Uptake and elution characteristics of uranium and manganese in the inlet of

    Effluent treatment plant (ETP) and synthetic ETP effluent during batch

    experiment

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    Table 2 The characteristic factors of uranium and manganese in the inlet of effluent

    treatment plant (ETP) and synthetic ETP effluent during batch experiments

    Time

    (min)

    Mn

    (ppm)

    U

    (ppb)10 16.4 12.1

    20 10.7 6.3

    30 9.6 4.1

    40 7.5 1.6

    50 6.4 0.5

    60 3.83 0.08

    70 2 0.08

    80 1.415 0.08

    90 1.37 0.08

    100 0.0798 0.08

    110 0.829 0.24

    120 0.828 0.56

    130 0.912 1.2

    140 1.04 1.6

    150 1.33 1.8160 1.45 2.5

    Sample Element Initial

    conc.(C0)

    Amount of

    total uranium

    present (g) in

    25 ml solution

    Metal content in

    the filtrate

    (g)

    Amount of metal

    ion in the elute

    (g)

    ETP inlet

    Actualsolution

    (A)

    U 97.22 6.2

    (ng/ml)

    2.43 0.15 g 0.081 0.008

    (almost same for

    i. and ii.)

    i. 2.18 0.1 g

    ii. 2.39 0.09 g

    Mn 54.96

    (g/ml)

    1374 g i. 425 g

    ii. 413 g

    i. 899 g

    ii. 919.5 g

    ETP inlet

    Synthetic

    solution

    (B)

    U 60 (ng/ml) 1.5 g NIL i. 1.33 0.1 g

    ii. 1.06 0.07 g

    Mn 60 (g/ml) 1500 g i. 7.05 g

    ii. 5.19 g

    i. 1150 g

    ii. 1088.5 g

    Sample Element Absorption %

    (Co-Ce)/Co . 100

    Kd

    (Co-Ce)/Ce . V/m

    Elution % Immobilization

    factor

    ETP inlet Actual

    solution (A)U 96.67 1450 92.8 0.072

    Mn 69.07 111.64 94.7 0.053

    ETP inlet synthetic

    solution (B)

    U 99.93 74950 88.725 0.113

    Mn 99.53 10588.3 77.03 0.23

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    30

    40

    50

    60

    70

    10 30 50 70 90 110

    130

    150

    170

    190

    210

    230

    250

    Time in minutes

    ncentration

    Mn (ppm)

    170 7.8 8.8

    180 15.6 21.2

    190 20.6 24.7200 35.3 36.5

    210 42.3 39.8

    220 48.5 45.5

    230 57.8 55.3

    240 58.2 57.9

    250 58.6 58.6

    260 59.1 59.5

    Figure 1 Column study of the sorbent with synthetic effluents