A Flow System With an Electrochemical Reduction Cell For

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  • Talanta 50 (1999) 247252

    A flow system with an electrochemical reduction cell forspectrophotometric determinations of major constituents in

    Fe:V alloys

    Antonio O. Jacintho a, Luiz F.R. Machado b, Amauri A. Menegario a,Iolanda A. Rufini a, Maria Fernanda Gine a,*

    a Centro de Energia Nuclear na Agricultura, Uni6ersidade de Sao Paulo, A6. Centenario 303, C. Postal 96,13400-970 Piracicaba, Brazil

    b Instituto de Qumica de Sao Carlos, Uni6ersidade de Sao Paulo, Sao Paulo, Brazil

    Received 22 July 1998; received in revised form 29 September 1998; accepted 2 October 1998

    Abstract

    Insertion of an electrochemical cell in a flow injection system to evaluate the on-line reduction of ionic species ispresented. The cell comprised Pt electrodes installed in two sections separated by a Nafion membrane. The samplewas injected into an acidic carrier stream and passed through the cathode compartment of the electrolytic chamberwhere the species were reduced as consequence of an applied DC voltage. The sample solution leaving the cellreceived a confluent reagent stream (1,10-phenanthroline buffered at pH 4.7) and the reacted products were droppedoff in an open tube for gas:liquid separation. Efficiency of the Fe3 to Fe2 reduction in acidic medium wasevaluated in the presence of strongly reducing species of V and Mo by monitoring the Fe(II) colored complex.Interferences from Pb2, Co2, Ni2, Zn2, Cu2, V5 and Mo6 were evaluated. Production of stronglyreducing species of V at the electrolytic cell presented higher efficiency for Fe reduction than the electrolytic chamberitself. Total reduction of Fe3 in solutions containing up to 10 mg l1 Fe plus 100 mg l1 V or 100 mg l1 of Mowas achieved by the electrolytic process at 2 A. The quantitative determination of Fe and V in low silicon Fe:V alloyswas achieved. Accuracy was assessed with the certified Euro-standard 577-1 ferrovanadium alloy produced by theBureau of Analysed Samples Limited and no difference at the 95% confident level was found. 1999 Elsevier ScienceB.V. All rights reserved.

    Keywords: Electrochemical cell; Iron reduction; Flow analysis; Iron alloys

    1. Introduction

    In flow injection analysis reducing columnshave been used for different applications. Acolumn with copperized cadmium filings was em-

    * Corresponding author. Tel.: 55-194-292-4636; fax: 55-194-294-610.

    E-mail address: [email protected] (M.F. Gine)

    0039-9140:99:$ - see front matter 1999 Elsevier Science B.V. All rights reserved.

    PII: S0039 -9140 (99 )00023 -5

  • A.O. Jacintho et al. : Talanta 50 (1999) 247252248

    ployed for reduction of nitrate to nitrite [1]. Sev-eral applications used the Jones reductor of amal-gamated Zn packed in an on-line column toreduce Cr3 to Cr2 [2,3], V4 and V5 to V2

    [2] and U6 to U3 [4]. In these papers, thegeneration of strongly reducing agents in flowsystems which are unstable under atmosphericconditions was demonstrated. The determinationof total Fe and Fe2 was also attained afterreduction in a column with the Jones reductor ina flow system [5].

    Electrochemical reduction of ionic species wasreported for the hydride forming elements [6]. Theapproach was accomplished by using a flow-through electrolytic cell [7,8]. Papers published onthe last years described the electrochemical hy-dride generation (EcHG) of selenides, arsines,stibines and others coupled to different spectrom-eters, atomic absorption with a T-tube atomizers(ETAAS) [7,8] or with graphite furnaces(GFAAS) [9] or atomic emission microwave in-duced plasmas (MIP-AES) [10]. Electrodes of dif-ferent materials: vitreous carbon [7], platinum[7,8,10], lead and pyrolytic graphite [9] weredescribed.

    In the present work the electrochemical ap-proach using a flow-through cell is proposed toreduce Fe3 to Fe2. The spectrophotometricdetection of the ferroine complex was used toestimate the reduction process. The on line pro-duction of reduced species of V and Mo and theeffect on reducing Fe3 was evaluated. The deter-mination of Fe in ferrovanadium alloys and thepossibility of the indirect determination of V ispresented.

    2. Experimental

    2.1. Apparatus

    The flow system comprised a peristaltic pump(mp-13R Ismatec, Zurich, Switzerland) providedwith Tygon pumping tubing, an automatic injec-tor (Model 352, Micronal, Sao Paulo, Brazil) aflow-through electrolytic cell described below, aspectrophotometer (Model 432, Femto, SaoPaulo, Brazil) furnished with a flow cell (10 mm

    optical path, 80 ml inner volume) and a strip-chartrecorder (REC 61, Radiometer, Copenhagen,Denmark). Accessories such as Y-shaped connec-tors, and mixing coils of polyethylene tubing (0.8mm i.d.) were used.

    The electrochemical cell was constructed byassembling layers of Perspex of different thick-ness, with two compartments, (anode 1.6 cm3 andcathode 0.4 cm3) separated by a Nafion mem-brane and electrodes of platinum sheets (3.2 cm2)connected to a home made electrical source,which could be varied from 0.2 to 3.0 A. TheNafion membrane was conditioned by immersingit in hot water 20 min before installing at the cellprotected between two rubber layers.

    The gas phase separator (PS) was constructedfrom a 10 cm5 mm i.d. glass tube, with twolateral exits at opposite sides as described earlier[11].

    2.2. Reagents and solutions

    All reagents were of analytical grade and dis-tilled, de-ionized water was always used. The elec-trolyte solution was 2.0 M H2SO4. The1,10-phenanthroline solution (0.25% w:v) wasprepared weekly by dissolving 0.6250 g of 1,10-phenanthroline hydrochloride in 250 ml of 0.1 MHCl. Acetate buffer solution (pH 4.7) was pre-pared with 1.0 M ammonium acetate plus 1.0 Macetic acid.

    Stock solution containing 1000 mg l1 Fe3

    was prepared from Fe(NO)3 9H2O (Merck,Darmstadt, Germany). Solutions of the individualconcomitants containing 1000 mg l1 Zn2,Co2 and Cr3 from the metals and Ni2 fromNiSO4 6H2O (Johnson and Matthey ChemicalsJMC), Pb2 from Pb(NO3)2, V5 from NH4VO3and Mo6 from (NH4)6MO7O24 4H2O (Merck,Darmstadt, Germany) were prepared. Solutionsused to test interference containing 10.0 mg l1

    Fe3 plus 10.0 and 100 mg l1 of each elementwere used. A freshly prepared solution containing10.0 mg l1 Fe2 was employed to estimate thereduction efficiency.

    Working standard solutions, 0.00, 2.50, 5.00and 10.0 mg l1 Fe3 plus 100 mg l1 of V5,were used to determine Fe in the diluted sample.

  • A.O. Jacintho et al. : Talanta 50 (1999) 247252 249

    Standard solutions, 0.00, 2.00, 5.00 and 10.0 mgl1 V or Mo plus 10.0, 20.0 and 30.0 mg l1 ofFe were prepared. Three synthetic solutions con-taining Fe and V concentrations in different pro-portions (50:50; 60:40 and 40:60 w:w) in 0.25 MHCl, simulating alloy samples with low siliconcontents were analyzed together with the standardreference material Euro-standard 577-1 producedby the Bureau of Analysed Samples Limited(Middlesborough, UK). About 100 mg of thereference alloy were accurately weighted, received10 ml of acqua-regia and were heated in a hotplate until complete dissolution. After cooling toroom temperature 5 ml of perchloric acid (70%v:v) were added and heated until evolution ofwhite fumes. The residual solution was diluted to100 ml [12]. Aliquots of 5.0 ml of this solutionreceived 50 ml of 2.5 M HCl and 50 ml of 1000mg l1 of V before diluting to 500 ml.

    2.3. The flow system

    The electrochemical reduction of Fe3 was per-formed by using the flow set up depicted in Fig. 1.The electrolyte solution was continuously recycled

    through the anode compartment of the elec-trolytic cell (EC). In the situation specified in Fig.1, the sample solution at loop L was carried by Cthrough the EC cathode compartment and themixing coil B1. At the confluent point X, thesample solution received a buffered reagentstream (BR). After passing reaction coil B2 thesolutions was dropped off in an open tube PS toseparate gaseous components. Part of this solu-tion was aspirated from the bottom of the tubetowards the detector D with wavelength adjustedto 512 nm. Moving down the central part of theinjector, L was filled with another sample solutionwhile part of solution at the PS was drained.After 30 s, the injector returned to the positionshown in Fig. 1 and simultaneously the electricalpower at the EC was switched on during 30 s. Theinjector rested in this position during 60 s and thespectrophotometric detection occurred.

    Speciation of Fe2 and Fe3 in acidified watersamples (0.25 M HCl) could be accomplished withthe flow system in Fig. 1. The injection of thesample allowed the direct Fe2 determination andin a second injected sample volume simulta-neously the EC is switched on and the reduction

    Fig. 1. A. Flow diagram for electrochemical reduction of Fe3 to Fe2. The three rectangles at the left represent the injector inthe injection position with sample in loop L. The arrow below represent the displacement of the central part to the alternativeposition. Lines indicate the tubing used for flowing solutions of electrolyte E, carrier C, sample S, reagent R, buffer B, and theresidual W. Numbers in brackets indicate the flow rates in ml min1, and arrows indicate the pumping direction. Theelectrochemical cell (EC) is schematized with the Nafion membrane N and the electrodes connections. Other devices are the mixingand reaction coils B1 and B2 of 25 cm tubing each, the connector X, the phase separator (PS) and the detector D. Dashed line afterthe EC, indicates the optional inlet to introduce the Fe3 solutions.

  • A.O. Jacintho et al. : Talanta 50 (1999) 247252250

    Table 1Regression data obtained with solutions from 0.00 to 10.0 mgl1 Fe3 at electrolytic currents of 1.0, 2.0 and 3.0 A

    Current (A) r2yaxb R.S.D.10Fea

    0.99901.0 0.980.012x0.0022.0 0.018x0.001 0.9999 2.04

    0.026x0.0043.0 0.9990 2.93

    a Relative standard deviations (R.S.D.) for the 10 mg l1 Festandard based on three replications.

    ber. Thus, further experiments were carried out at2 A yielding results characterized by good linear-ity and precision.

    Solutions containing 10.0 mg l1 of Fe3 plus10.0 and 100 mg l1 of Pb2, Co2, Ni2,Zn2, Cu2, V5 and Mo6 were injected usingthe electrolytic current switched on and off toverify the possibility of being interfering either onreduction or on the complexation reaction. Theeffects of concomitant additions are presented inTable 2. Cobalt solutions were colored and raisedthe background at 512 nm. Using a EC with cleanPt electrodes a signal increase of 10% due to Pbaddition was observed. After passing repeatedlythe Pb solution (total mass of 0.1 mg Pb) thesignal stabilized. When the EC was opened, Pbdeposition on the Pt cathode could be observedby naked eyes.

    Addition of V5 and Mo6 increased the sig-nal proportionally to the applied current empha-sizing the formation of strongly reducing species[2].

    The efficiency of reduction was evaluated atdifferent electrolytic currents by comparing ab-sorbances of a 10 mg l1 Fe3 after reductionwith that corresponding to a 10 mg l1 Fe2

    of Fe3 occurred permitting the determination oftotal iron.

    The flow system in Fig. 1 presents an alterna-tive configuration to introduce the Fe3 solutions(dashed line after the cell), to study the effect ofthe reduced species of V and Mo produced at EC.

    3. Results and discussion

    The efficiency of the proposed electrolytic re-duction of Fe3 to Fe2 is dependent on severalparameters such as flow-rates, cell compartmentdimensions, type and electrode surface, sampleacidity and electrolytic voltage. One liter of theelectrolyte solution (2 M H2SO4) was continu-ously pumped at 2.5 ml min1, through the an-ode compartment. This solution was replacedperiodically to maintain its characteristics. UnderDC current the electrolyte solution yielded H3O

    which crossed the Nafion membrane towards thecathode compartment. The temperature at the ECincreased when the current was raised just to 3 A,sample flow rate was lower than 1.0 ml min1

    and the sample acidity was B0.05 M HCl. Underthese conditions a damage of the Nafion mem-brane was observed. On the other hand, afterincreasing the sample acidity beyond 0.25 M HClthe large quantity of gases evolved impaired theFe3 reduction. Therefore, sample solutions at0.25 M HCl flowing at 2.5 ml min1 were em-ployed throughout.

    Effect of raising the electrolytic current at theEC to reduce solutions of Fe3 produced data inTable 1. Despite higher absorbances being at-tained with 3 A data presented poor precisionprobably due to higher gas evolution at the cham-

    Table 2Results after addition of different ionic species to 10 mg l1

    Fe3a

    Added amount (mg l1)Ions Absorbance

    10 0.18890.003Cu2

    100 0.19990.010Ni2 0.18990.00110

    100 0.19190.0010.18990.00310Zn2

    0.18390.0031000.17790.00110Mn2

    100 0.17990.001Co2 0.32090.00310

    100 0.40790.008Cr3 10 0.18990.006

    100 0.19690.009Mo6 10 0.31590.005

    100 0.47290.004V5 10 0.35390.005

    100 0.47190.009

    a The analytical signal related to 10 mg l1 Fe2 was0.18090.004 A (n3).

  • A.O. Jacintho et al. : Talanta 50 (1999) 247252 251

    Fig. 2. Effect of the electrolytic current and the presence ofV5 on Fe3 reduction (a) 10 mg l1 Fe3; (b) 10 mg l1

    Fe3 10 mg l1 V5; and (c) 10 mg l1 Fe3 100 mgl1 V5. A is absorbance. Dashed line indicates the signalobtained by injecting a solution of 10 mg l1 of Fe2.

    The expected probable competition of Fe2

    and V2 for 1,10-phenanthroline [5] was not ob-served even though a diluted solution of thereagent (0.1% w:v) and a concentrated solution ofV5 (100 mg l1) reduced at 2 A was used.

    The quantification of iron in dissolved fer-rovanadium alloys (dilution factor of 105) wasachieved by adding 100 mg l1 V to the samplesand standards, assuming complete reduction ofFe3 (Fig. 2).

    The analytical curves in Fig. 3 were used for Vquantification. The effect of increasing the V con-centrations up to 10 mg l1 in solutions with 10,20 and 30 mg l1 of Fe was characterized bylinear coefficients and slopes depending on theFe3 concentrations following the relationshipA0.018 CFe0.0008 CFeCV. For the dissolvedsamples, the Fe concentration previously deter-mined was used to calculate the V concentration,but this is only valid for V concentrations lowerthan 10 mg l1. When CV10CFe maximumabsorbance was attained (Fig. 2). Thus, the pro-posal is to add Fe to the diluted samples to ensurethe determination of V in the linear analyticalrange (Fig. 3) for samples with a CFeBCV. Theeffect of adding up to 10 mg l1 Mo to solutionsin three different iron concentrations presentedgood correlation (Fig. 3 dashed lines). In thissituation, the slope of the curves were not depen-

    solution injected in the same way. Results arepresented in Fig. 2. No signal was observed forFe3 without current at the EC. Increasing thecurrent up to 3 A the reduction of Fe3 aloneincreased linearly (r0.9968) attaining 55% ofreduction. The effect of reducing 10 mg l1 Fe3

    alone or together with 0.00, 10.0 or 100 mg l1 ofV5 could be appreciated by comparing curves atFig. 2. The addition of 100 mg l1 V5 to Fe3

    provided the best reduction efficiency, attainingtotal reduction after a current of 2 A (curve c,Fig. 2).

    To elucidate the influence of V and Mo reducedspecies on the reduction of iron, an experimentinvolving addition of a Fe3 solution after theEC was performed. Solutions of V5 and Mo6

    were injected instead of the sample and whileflowing through the EC (2 A) produced reducedspecies which merged with the Fe3 solution. Thereduction of 10 mg l1 Fe3 occurred in anextent of 80% with 100 mg l1 V5 and 45% with100 mg l1 Mo6. Therefore, the reduced Vspecies which formed from 100 mg l1 V5 at theEC cell at 2 A allowed the attainment of 80%efficiency on Fe3 reduction, while the efficiencyof the EC alone was 38% (curve a, Fig. 2). Nosignal corresponding to the reduced species of Vand Mo was observed probably due to their oxi-dation until reaching the detector unity.

    Fig. 3. Effect of adding different V (solid lines) and Mo(dashed lines) concentrations to solutions containing 10.0, 20.0and 30.0 mg l1 Fe3. A is absorbance and C is the concen-tration of V or Mo added. Regression curves in bold corre-spond to V and those in italic to Mo.

  • A.O. Jacintho et al. : Talanta 50 (1999) 247252252

    Table 3Results of a reference standard ferrovanadium alloy and Vresults in three synthetic FeV solutions containing 50, 40 and60% w:w V

    Fe (% w:w)Sample V (% w:w)

    Certified valueEURO-ST5771 47.21 50.1690.1347.290.5Found valuea 50.191.8EURO-ST5771

    1 52.191.738.990.9260.590.83

    a Mean9S.D., n3.

    ing both elements, once these elements are deter-mined indirectly by its effect on iron reduction.

    Acknowledgements

    Financial support from FAPESP (Fundacao deAmparo a` Pesquisa do Estado de Sao Paulo) andCNPq (Conselho Nacional de DesenvolvimentoCientfico e Tecnologico) was greatly appreciated.

    References

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    dent on the Fe concentration as found for V.Results for three ferrovanadium synthetic solu-tions and one certified reference material Euro-standard 577-1 are shown in Table 3. The certifiedand found results were not statistically differentfrom each other at the 95% confidence level.

    4. Conclusions

    The proposed electrochemical reduction ap-proach is efficient for on-line reduction of Fe3

    to Fe2 in acid solutions. Addition of V and Moincreased significantly the Fe3 reduction toFe2.

    The proposal suits well for the quantitativedetermination of Fe2 and total Fe, the determi-nation of Fe and V or Fe and Mo in the respec-tive solubilized iron alloys by using theelectrolytic chamber reduction and 1,10-phenan-throline. Application of this approach could notbe used to determine V or Mo in samples contain-

    ..