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    Contribution of free radicals to chlorophenols decomposition

    by several advanced oxidation processes

    F. Javier Benitez *, Jesus Beltran-Heredia, Juan L. Acero, F. Javier Rubio

    Departamento de Ingenieria Quimica y Energetica, Universidad de Extremadura, 06071, Badajoz, Spain

    Received 18 June 1999; accepted 29 October 1999

    Abstract

    The chemical decomposition of aqueous solutions of various chlorophenols (4-chlorophenol(4-CP), 2,4-dichlor-

    ophenol (2-DCP), 2,4,6-trichlorophenol (2,4,6-TCP) and 2,3,4,6-tetrachlorophenol (2,3,4,6-TeCP)), which are envi-

    ronmental priority pollutants, is studied by means of single oxidants (hydrogen peroxide, UV radiation, Fenton's

    reagent and ozone at pH 2 and 9), and by the Advanced Oxidation Processes (AOPs) constituted by combinations of

    these oxidants (UV/H2O2, UV/Fenton's reagent and O3/UV). For all these reactions the degradation rates are evaluated

    by determining their rst-order rate constants and the half-life times. Ozone is more reactive with higher substituted

    CPs while OH radicals react faster with those chlorophenols having lower number of chlorine atoms. The improvement

    in the decomposition levels reached by the combined processes, due to the generation of the very reactive hydroxyl

    radicals, in relation to the single oxidants is clearly demonstrated and evaluated by kinetic modeling. 2000 Elsevier

    Science Ltd. All rights reserved.

    Keywords: Chlorophenols; Hydroxyl radicals; Advanced oxidation processes; UV radiation/hydrogen peroxide; UV radiation/Fenton's

    reagent; Ozone/UV radiation

    1. Introduction

    The chemical oxidation of toxic and hazardous or-

    ganic pollutants, which frequently are present in surface

    waters and wastewaters, is often carried out by using

    single oxidants such as chlorine, ozone, UV radiation,hydrogen peroxide, etc. However, sometimes this de-

    composition by conventional treatments may be dicult

    if these pollutants are present at low concentrations or if

    they are especially refractory to the oxidants. For these

    situations, it has been necessary to develop more eec-

    tive processes for the destruction of such contaminants.

    Among them, some systems based on the generation

    of very reactive and oxidizing free radicals, especially

    hydroxyl radicals, have experimented an increasing in-

    terest due to their high oxidant power. These systems are

    commonly named Advanced Oxidation Processes

    (AOPs), and the production of those radicals is achieved

    by the combinations of ozone, hydrogen peroxide andUV radiation (Glaze et al., 1987; Glaze and Kang, 1989;

    Masten and Davies, 1994); and also, with the combi-

    nation of hydrogen peroxide with ferrous ions in the so-

    called Fenton's reagent (Walling, 1975).

    Chlorophenols (CPs) constitute a group of organic

    substances that are introduced into the environment as a

    result of several man-made activities, such as water

    disinfection, waste incineration, uncontrolled used of

    pesticides and herbicides, etc., and also as byproducts in

    the bleaching of paper pulp with chlorine (Ahlborg and

    Thunberg, 1980). Because of their numerous origins,

    they can be found in industrial wastewaters, soils and

    surface waters, and several of them have been listed

    Chemosphere 41 (2000) 12711277

    *Corresponding author. Tel.: +34-924-289384; fax: +34-

    924-271304.E-mail address: [email protected] (F.J. Benitez).

    0045-6535/00/$ - see front matter 2000 Elsevier Science Ltd. All rights reserved.

    PII: S 0 0 4 5 - 6 5 3 5 ( 9 9 ) 0 0 5 3 6 - 6

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    among the 65 priority pollutants by the US EPA (Keith

    and Telliard, 1979).

    Their conventional destructive technologies include

    biological treatments, incineration, adsorption over ac-

    tivated carbon, air stripping, etc. (Jardin et al., 1997).

    Some of these treatments, like the biological treatments,can be aected by the toxicity of some substances; oth-

    ers, like incineration, present considerable emission of

    other hazardous compounds; and adsorption or air

    stripping requires a post-treatment to remove the pol-

    lutants from the newly contaminated environment.

    Therefore, a promising technology could be the use of

    single chemical oxidants, or the more eective destruc-

    tion by the AOPs, which can provide an almost total

    degradation as has been reported by several authors in

    the decomposition of a wide variety of organic con-

    taminants (Peyton et al., 1982; Guittonneau et al., 1988;

    Legrini et al., 1993).According to these considerations, a research pro-

    gram was designed which focused on the oxidation of

    several chlorophenols (4-chlorophenol (4-CP), 2,4-di-

    chlorophenol (2,4-DCP), 2,4,6-trichlorophenol (2,4,6-

    TCP) and 2,3,4,6-tetrachlorophenol (2,3,4,6-TeCP)) by

    single oxidants and by dierent AOPs. The objectives

    were to provide data about the removal obtained, to

    report values of the rate constants for the global pro-

    cesses, and to compare the eciency of the dierent

    AOPs tested. Also, the enhancements reached in the

    degradation levels in these combined oxidations com-

    pared to the single oxidation processes are determined,

    and the partial contributions of the OH radical pathwayto the global oxidation process are calculated for the

    dierent AOPs studied.

    2. Materials and methods

    Analytical grade 4-CP, 2,4-DCP, 2,4,6-TCP and

    2,3,4,6-TeCP were obtained from Sigma, hydrogen

    peroxide (33% v/v) was purchased from Panreac and

    ferrous sulfate heptahydrate was from Merck. Ozone

    was produced from an oxygen stream in an ozone gen-

    erator (Yemar, mod. HPA), and the radiation sourcewas a Heraeus TQ150 high pressure mercury vapor lamp

    which emitted a polychromatic radiation in the range

    from 185 to 436 nm.

    The reactor used in all the experiments consisted of a

    500 ml cylindrical glass reactor provided with the nec-

    essary elements for the development of the dierent

    processes: photodecomposition, Fenton's reagent oxi-

    dation, ozonation, and the dierent combinations of

    these oxidants. In the photochemical experiments, the

    radiation source was located in the reactor in axial po-

    sition. The reactor was lled with 350 ml of an aqueous

    solution of the selected CP (initial concentration of

    3 104 M in all cases), and the selected pH (2 or 9) was

    obtained by adding orthophosphoric acid and sodium

    hydroxide. The required amounts of ferrous sulfate and

    hydrogen peroxide were added to the reactor in Fenton's

    reagent oxidation experiments and in the photo-Fenton

    experiments, and only the required amounts of hydro-

    gen peroxide in the UV/H2O2 experiments. In theozonation experiments and combined UV/ozone exper-

    iments, the ozoneoxygen mixture was fed to the reactor

    through a porous plate gas sparger located at the bot-

    tom of the reactor. The temperature was kept constant

    at 25C.

    The CPs concentrations in the samples withdrawn

    from the reactor at regular reaction times were analyzed

    by HPLC using a Waters Chromatograph equipped with

    a 996 Photodiode Array Detector and a Nova-Pak C18

    Column. The detection was made at 290 nm with a

    mobile phase composed of a mixture methanolwater

    acetic acid (65/33/2 in volume) and with a ow rate of 1ml/min. Ozone concentration was measured in the gas

    stream iodometrically by bubbling the gas in a potassi-

    um iodide solution. The concentration of H2O2 was

    determined by the colorimetric method proposed by

    Bader et al. (1988).

    3. Results and discussion

    3.1. Decomposition by single oxidants

    In a rst stage, the decomposition of all four selected

    CPs was performed by the action of the following singleoxidants: UV radiation, Fenton's reagent and ozone. A

    previous set of degradation experiments by using hy-

    drogen peroxide alone was also conducted, but no sig-

    nicant CPs degradation was obtained with this oxidant.

    Therefore, it can be concluded that H2O2 does not oxi-

    dize the studied organic compounds, this eect being

    already observed by several authors with some refrac-

    tory pollutants (Masten and Davies, 1994; Benitez et al.,

    1995).

    3.1.1. UV radiation

    The photooxidation of CPs by a polychromatic UVradiation was conducted at pH 2. Fig. 1 shows thedecrease in concentration as a function of irradiation

    time: As can be observed, 4-CP was rapidly degraded;

    decreasing rates are obtained for 2,4-DCP, 2,4,6-TCP,

    and for 2,3,4,6-TeCP. It suggests that the addition of

    substituent chlorine atoms decreases the susceptibility of

    the aromatic ring to be attacked by the photons gener-

    ated by the UV radiation. It can be explained by taking

    into account that during photochemical treatments,

    electronically excited states of polychlorinated phenols

    are generated (Skurlatov et al., 1998). In these excited

    states, the CP molecules undergo intramolecular trans-

    formations and stabilize states with dierent electron

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    distributions, followed by decomposition to radical or

    molecular products. A higher level of chlorine substi-

    tution must bother the formation of the excited state or

    the stabilization of the intermediate state.

    Since reaction mechanisms are complex for thephotodegradation of organic compounds, a rigorous

    kinetic study cannot be performed. However, the shape

    of the lines in Fig. 1 looks like a rst-order reaction with

    respect to CPs degradation. Therefore, an approach to

    this kinetic study can be performed by assuming that the

    photochemical decomposition reaction follows a rst-

    order kinetics, and can be represented by the simple

    expression

    P hm3kpPoxidY 1

    where Poxid symbolizes intermediates and nal products,and kp is the rst-order rate constant. This approach is

    frequently used by several authors in similar studies

    (Sundstron et al., 1989; Shen et al., 1995).

    In order to evaluate these rate constants, the terms ln

    (CP0/CP) are plotted versus reaction time, and after lin-

    ear regression analysis, the rst-order rate constants are

    determined and showed in Table 1 with the correlation

    coecients. Obviously, they follow the trend already

    commented for the degradation rates: 4-CP >2,4-DCP

    >2,4,6-TCP >2,3,4,6-TeCP. Table 1 also summarizes

    another interesting kinetic parameter, the half-life times

    t1a2 or time necessary to reduce the initial concentrationof the CPs in solution by a factor of two. As can be

    observed, these t1a2 increase when the substituent chlo-

    rine atoms also increase, corroborating the sequence

    obtained for the decomposition rates.

    3.1.2. Fenton's reagent

    In a second step, the decomposition of the four se-

    lected CPs was explored by means of the very reactive

    and oxidizing hydroxyl radicals, which are generated by

    Fenton's reagent, a mixture of hydrogen peroxide and

    ferrous ions, according to the reaction (Walling and

    Kato, 1971; Walling, 1975)

    H2O2 Fe2 3 Fe3 OH OHX 2

    The hydroxyl radicals formed attack any organic

    compound P, and thus, cause its chemical decomposi-

    tion

    POH3krPoxidY 3

    where Poxid again symbolizes dierent intermediates and

    nal products of the chain degradation reactions that

    take place, and kr is the rst-order rate constant for the

    reaction of CPs with OH.

    In these experiments, the initial concentrations of

    Fe2 and H2O2 were respectively 1 104 and

    7X5 103 M, and the pH 2. The degradation curvesobtained versus reaction time again suggest that a rst-

    order kinetics perfectly approaches the real kinetics of

    this Fenton's reagent oxidation process. Fig. 2 shows the

    plot of ln (CP0/CP) against reaction time: as can be seenpoints lie satisfactorily around straight lines. After re-

    gression analysis, the results obtained for kr and for the

    half-life times are depicted in Table 1. The sequence of

    oxidation rates is the same as in the photodegradation

    process, that is: 4-CP >2,4-DCP >2,4,6-TCP >2,3,4,6-

    TeCP. Hydroxyl radicals usually attack the aromatic

    ring at the sites which are not occupied by chlorine at-

    oms, and therefore, hydroxylation is the rst elementary

    step which precedes the dissociation of chlorine atoms

    (Tang and Huang, 1996). So, the increase in the chlorine

    atoms number in the aromatic ring decreases the reac-

    tivity towards the hydroxyl radicals, and subsequently,the trend in the t1a2 values is inverse: they increase when

    the substituent chlorine atoms also increase.

    Table 1

    Rate constants and half-life times for the decomposition of CPs by single oxidants

    Compound UV Fenton O3 pH 2 O3 pH 9

    kp 103

    (min1)

    t1a2(min)

    kr 103

    (min1)

    t1a2(min)

    kO3 103

    (min1)

    t1a2(min)

    kO3 103

    (min1)

    t1a2(min)

    4-CP 564 (0.99) 1.1 1877 (0.99) 0.4 17 (0.99) 38.5 239 (0.99) 3.4

    2,4-DCP 38 (0.99) 17.5 209 (0.99) 2.4 24 (0.99) 30.4 315 (0.98) 3.3

    2,4,6-TCP 26 (0.99) 25.2 98 (0.99) 5.1 44 (0.98) 20.6 314 (0.98) 3.1

    2,3,4,6-TeCP 21 (0.99) 30.6 9 (0.98) 49.5 94 (0.98) 10.6 415 (0.99) 1.9

    Fig. 1. CPs decomposition curves by direct photolysis.

    F.J. Benitez et al. / Chemosphere 41 (2000) 12711277 1273

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    3.1.3. Ozone

    Finally, the CPs were oxidized by ozone (with an

    ozone partial pressure in the ozoneoxygen gas streamof 90 Pa) at 25C and in acidic media pH 2. At thispH the decomposition of ozone, which is initiated by the

    action of hydroxide ions (Staehelin and Hoigne, 1982), is

    too low and consequently the formation of hydroxyl

    radicals is limited. This decomposition of organic com-

    pounds by ozone can be represented by a single global

    reaction which follows a rst-order kinetics:

    PO33KO3

    PoxidX 4

    When the four CPs were ozonated, the rate constant kO3for the reaction represented by Eq. (4) was in the fol-lowing decreasing rate of magnitude: 2,3,4,6-TeCP

    >2,4,6-TCP >2,4-DCP >4-CP as can be observed in

    Table 1. Similar results were obtained by Trapido et al.

    (1997) in the ozonation of several CPs. Therefore, it can

    be concluded that the sequence of degradation is the

    inverse to that found in the photodegradation and

    Fenton's reagent processes; that is, the increase in the

    number of chlorine atoms in the aromatic ring provides

    an increase in the degradation rate. The pathways pro-

    posed by Chen and Ni (1998) to describe the complete

    ozonation of 2,4-dichlorophenol were hydroxylation,

    dechlorination and ring-cleavage. According to thismechanism, the presence of more atoms of chlorine

    enhances the dechlorination step, and therefore, the

    degradation is faster.

    Another group of CPs ozonation experiments were

    conducted in basic media (pH 9). In this case, thedegradation curves were very close for all the CPs

    studied, with similar conversions for every CP. Table 1

    also shows the values obtained for the rst-order rate

    constants kO3 and the half-life times which conrm thesmall dierences in the removal of the CPs at this pH.

    However, the most important fact that can be observed

    when comparing the results at pH 2 and pH 9 is thefurther increase in the rate constant (and decrease in the

    half-life time) with increasing the pH. This nding can

    be explained by the faster production of OH radicals at

    basic pH and the dissociation of phenols to phenolate

    ions that are able to react with ozone faster than the

    non-dissociated species (Hoigne and Bader, 1983).

    3.2. Decomposition by advanced oxidation processes

    In the second part of this research, the Advanced

    Oxidation Processes constituted by the combinations of

    UV radiation plus H2O2, UV radiation plus Fenton's

    reagent, and UV radiation plus ozone, have been used

    for the study of CPs decomposition. As was mentioned

    in Section 1, these processes are characterized by the

    generation of free radicals, mainly hydroxyl radicals

    (Glaze et al., 1987; Glaze and Kang, 1989; Peyton et al.,

    1982). Therefore, the objectives of this study are focused

    on the evaluation of the enhancements caused in the

    oxidation reactions by these radicals in comparison to

    the reduction levels reached by the single oxidants at

    similar operating conditions.

    3.2.1. UV/H2O2 system

    Photodegradation experiments of the four selected

    CPs in the presence of hydrogen peroxide (with a H2O2initial concentration of 5 104 M in these experiments)were conducted at 25C and pH 2, and the sequenceof degradation rates achieved was just the same as that

    obtained for the single photochemical process (showed

    in Fig. 1): the degradation rates increase when the

    number of chlorine substituents decreases. This se-

    quence can be observed in Table 2, where the conver-

    sions obtained at three selected reaction times (2.5, 5 and30 min) are summarized, as well as the rst-order rate

    constants for this combined process kt and the half life

    times t1a2. It is seen that these rate constants present a

    Table 2

    Conversions reached, rate constants and half-life times in the decomposition of CPs by UV/H2O2

    Compound X2X5 (%) X5 (%) X30 (%) kt 103 (min1) t1a2 (min) kr 10

    3 (min1)

    4-CP 70 89 a 601 1.0 36

    2,4-DCP 15 25 74 44 14.5 6.9

    2,4,6-TCP 11 18 66 33 19.2 7.2

    2,3,4,6-TeCP 10 21 63 29 20.1 7.9

    a Total conversion reached at 9 min.

    Fig. 2. Determination of rst-order rate constants kr in CPs

    decomposition experiments by Fenton's reagent.

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    moderate higher values than those obtained in the single

    photodecomposition process (see Table 1, values of kp).

    These ndings demonstrate the additional contribution

    to the single photoreaction of the hydroxyl radicals

    generated by the presence of hydrogen peroxide.

    This supplementary contribution can be determinedby considering the mechanism of the combined process.

    Thus, in addition to the direct photoreaction (1), the

    following reactions must be taken into account:

    Direct photolysis of hydrogen peroxide with the for-

    mation of hydroxyl radicals:

    H2O2 hm3 2 OH 5

    Radical reaction between the organic compound and

    the hydroxyl radicals generated in (5), which is given

    by Eq. (3).

    According to this mechanism, the reaction rate for

    the global photodecomposition rT can be proposed as

    the addition of the direct rP (reaction (1)) and radical rR(reaction (3)) reaction rates in the form

    rT

    dCP

    dt

    ! rP rR kp krCP kt CPX

    6

    According to Eq. (6), the rate constants for the radical

    reaction kr are easily deduced by subtracting the previ-

    ously determined kp from kt, and Table 2 also depicts the

    kr obtained. When comparing these values to those of kp

    in Table 1, it is shown that the direct photolysis provides

    a contribution to the total reaction higher than that of

    the radical reaction.

    In order to validate the proposed mechanism which

    allows to calculate the rate constants, Fig. 3 presents the

    theoretically calculated degradation curves of 2,4,6-TCP

    (taken as example, similar results for other CPs) for thesingle radical and photochemical reactions, and for the

    combined UV/H2O2 reaction. These theoretical curves

    were calculated by means of computer simulations by

    using the program ACUCHEM, which solves compli-

    cated systems of chemical reactions (Braun et al., 1988).

    For these calculations, the evaluated rate constants kpand kr have been used, and the global degradation is

    determined as the sum of both contributions. In the

    combined reaction, the experimental concentrations

    obtained are also plotted. The excellent agreement be-

    tween model calculations and experimental data sup-

    ports the proposed mechanism.

    3.2.2. Photo-Fenton system

    Decomposition experiments of the CPs were carried

    out by the simultaneous action of UV radiation and

    Fenton's reagent (with initial concentrations of

    Fe2 1 105 M and H2O2 5 104 M), and the

    same sequence of degradation rates as in the single

    photodecomposition or Fenton's reagent processes, or

    as in the combined UV/H2O2 system was obtained.

    Table 3 depicts the conversions obtained at three

    reaction times, as well as the rst-order rate constants ktand the half-life times. When compared these rate con-

    stants kt to the single photodecomposition rate con-

    stants (kp in Table 1), higher values for kt can be seen

    which again conrm the additional contribution of the

    radical reaction due to the generation of the hydroxyl

    radicals by Fenton's reagent and by the H2O2.

    To evaluate the contribution of OH radical in this

    process, in addition to reactions (1) and (2), corre-

    sponding to the direct photodecomposition and the

    generation of hydroxyl radicals by Fenton's reagent re-

    spectively, another hydroxyl radicals generation reaction

    must be considered due to the photolysis of H2O2 which

    is represented by Eq. (5). According to this mechanism

    described by Eqs. (1), (2), (5) and (3), Eq. (6) can be usedto determine the hydroxyl radicals contribution to the

    global reaction. Table 3 depicts the kr values obtained

    after using Eq. (6) and higher values ofkr for this system

    Fig. 3. Decomposition curves for 2,4,6-TCP in the UV/H2O2system. ( ) theoretical values. (e) experimental values.

    Table 3

    Conversions reached, rate constants and half-life times in the decomposition of CPs by the photo-Fenton system

    Compound X2X5 (%) X5 (%) X20 (%) kt 103 (min1) t1a2 (min) kr 10

    3 (min1)

    4-CP 81 96 a 642 0.9 79

    2,4-DCP 24 39 84 88 7.4 50

    2,4,6-TCP 21 37 79 78 8.5 52

    2,3,4,6-TeCP 16 28 67 58 12.0 37

    a Total conversion reached at 8 min.

    F.J. Benitez et al. / Chemosphere 41 (2000) 12711277 1275

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    in comparison to the AOP UV/H2O2 are observed.

    Furthermore, the contribution to the global reaction of

    the radical reaction is higher than that of the direct

    photodecomposition (comparison between kr of Table 3

    and kp of Table 1), except for 4-CP whose direct pho-

    tolysis is really fast.Similar to the former UV/H2O2 system, Fig. 4 shows

    the theoretical degradation curves for 2,3,4,6-TeCP

    (taken as example), calculated as described above, and

    the experimental concentrations obtained in this com-

    bined system: again a perfect agreement is observed

    between experimental results and model calculations. In

    addition, is also seen the higher degradation rate cor-

    responding to the radical reaction in comparison to the

    direct photolysis.

    3.2.3. O3/UV system

    Finally, degradation experiments of the four CPs bythe combined process UV/O3 were conducted at 25C

    and pH 2. The results obtained for the conversions atthree reaction times (2.5, 5 and 20 min), the global rst-

    order rate constants kt (with correlation coecients

    higher than 0.99 in all cases) and the half-life times t1a2are depicted in Table 4. When comparing these results to

    those of the single photodecomposition or pH 2 oz-onation processes (Table 1), it is observed that this

    combination accelerates the decomposition rate as could

    be expected, with an extremely high rate constant kt for

    4-CP (as a consequence of its extremely high rate for the

    single photolysis), and lower rates for the rest of CPs.

    These remaining CPs (2,4-DCP, 2,4,6-TCP and 2,3,4,6-

    TeCP) present slightly increasing rate constants when

    the substituent chlorine atoms increase, which was the

    sequence observed in the single ozonation.

    As Peyton et al. pointed out (Peyton et al., 1982),

    ozone absorbs UV radiation and produces hydrogenperoxide

    O3 hm3 H2O2 7

    and then, there is a photolysis of hydrogen peroxide to

    generate hydroxyl radicals in the form described by re-

    action (5). In addition, H2O2 accelerates O3 decompo-

    sition into OH radicals (Staehelin and Hoigne, 1982)

    O3 H2O2 3 OHX 8

    These radicals generated by reactions (5) and (8) con-

    stitute the principal active species in the photolytic oz-

    onation. Thus, in the O3/UV process, there is a

    synergistic eect of several individual reactions: direct

    ozonation (reaction (4)), direct photolysis (reaction (1))

    and hydroxyl radical decomposition (reaction (3)).

    However, this synergism cannot be accounted for on the

    basis of an additive eect as in the former cases (UV/

    H2O2 and photo-Fenton), and its magnitude varies from

    substrate to substrate.

    4. Conclusions

    Several single oxidants and combined systems have

    been used for the decomposition of some CPs, like 4-CP,

    2,4-DCP, 2,4,6-TCP and 2,3,4,6-TeCP, being the de-

    gradation rates evaluated by means of rst-order rate

    constants. In the decomposition by single UV radiation

    and Fenton's reagent, 4-CP is the most rapidly degraded

    and 2,3,4,6-TeCP presents the lowest rate, while in the

    single ozonation process the sequence of degradation is

    inverse: 2,3,4,6-TeCP >2,4,6-TCP >2,4-DCP >4-CP,

    with a clear increase in the degradation rate when the

    pH is increased from 2 to 9. Therefore, ozone attacks to

    these CPs with a dierent mechanism than OH radicals,

    being this study the goal of current investigations.In the decomposition experiments by the advanced

    oxidation processes, an enhancement in the degradation

    is observed due to the generation of the hydroxyl radi-

    Fig. 4. Decomposition curves for 2,3,4,6-TeCP in the photo-

    Fenton system. ( ) theoretical values. (h) experimental values.

    Table 4

    Conversions reached, rate constants and half-life times in the decomposition of CPs by O3/UV

    Compound X2X5 (%) X5 (%) X20 (%) kt 103 (min1) t1a2 (min)

    4-CP 78 96 a 644 1.3

    2,4-DCP 3 14 64 65 15.6

    2,4,6-TCP 16 28 73 68 11.8

    2,3,4,6-TeCP 22 37 77 71 9.7

    a Total conversion reached at 7 min.

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    cals. This improvement is moderate in the UV/H2O2system and signicant in the UV/Fenton's reagent sys-

    tem. In the last one, the contribution of the radical re-

    action to the global reaction is higher than that of the

    direct photolysis. In the O3/UV system an improvement

    of the degradation rate is also observed, but in this casethe synergistic eect is not possible to be determined as a

    result of an additive eect.

    Acknowledgements

    Authors wish to thank CICYT of Spain for its -

    nancial support under Project AMB97-339, and Junta de

    Extremadura for its Project IPR98A014. F. Javier Rubio

    also thanks Junta de Extremadura for being granted with

    a PhD Grant.

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