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a Dep. of Agronomy and Center for Bioremediation and Detoxification, The Pennsylvania State Univ., University Park, PA 16802 USA
b Dep. of Soil Science, Univ. of Saskatchewan, Saskatoon, SK, Canada S7N 5A8
jdc7{at}psu.edu
| ABSTRACT |
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Abbreviations: FTIR, Fourier transform infrared DRIFT, diffuse reflectance infrared Fourier transform
| INTRODUCTION |
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Previous research has established that abiotic soil constituents, including manganese and iron (hydr)oxides, react with organic compounds, analogous to enzyme-mediated transformation, yielding humic substances (Shindo and Huang, 1982, 1984; McBride, 1987, 1989a,b; Huang, 1991). Oxidation of aromatic compounds by Mn (hydr)oxide surfaces is thought to result sequentially from (i) bonding of the organic to the surface through phenolic-OH or carboxylic functional groups, (ii) electron transfer from the organic to oxide, and (iii) release of the reduced metal (Stone and Morgan, 1984b). For dihydroxybenzenes (e.g., catechol), semiquinone radicals and quinones are formed prior to further oxidation and/or polymerization. Prevalence of semiquinone radicals increases with increasing pH and their oxidation to quinones is correlated with O2 consumption (McBride, 1989a,b). McBride (1989a) did not observe radical products in birnessitecatechol suspensions buffered at pH 5.4 and O2 consumption over the course of the experiment was insignificant, indicating that Mn(IV) is the primary oxidant in acidic systems.
Recently, it has been shown that there is a complimentary or competing mechanism resulting in aromatic ring cleavage and liberation of CO2 from these non-biological systems (Wang and Huang, 1994; Wang, 1995; Lee and Huang, 1995; Cheney et al., 1996, 1998). Although mineral dissolution and phenolic polymerization have been well documented, the kinetics and mechanisms of the simultaneous release of CO2 remain to be established. In particular, the rate and relative magnitude of 14CO2 release from radiolabeled parent compounds have not been evaluated previously. Therefore, the objectives of this study were (i) to quantify the mass of catechol-derived C in solid, solution, and gas phases as a function of time and (ii) to confirm that CO2 release from the catecholbirnessite system is derived from ring cleavage of catechol. We measured 14CO2 evolution at acidic pH such that Mn(IV) was the primary oxidant. The effect of adding fresh birnessite and/or catechol after a specified reaction time was used to elucidate processes limiting CO2 release.
| Materials and methods |
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-irradiation prior to experiments (Nuclear Reactor Facility, University Park, PA). Reagent grade catechol and uniformly 14C-labeled catechol (98% purity, specific activity of 17.7 mCi mmol-1) were purchased from Sigma (St. Louis, MO) and used in experiments with birnessite. All inorganic chemicals used were reagent grade and all solutions were prepared with filter-sterilized, distilled, deionized water.
Preliminary experiments in low ionic strength NaCl solutions indicated large pH increases resulting from the reaction of catechol and birnessite because of the production of hydroxide ions with 1,2-benzoquinone as shown in Eq. [1]
![]() | (1) |
In the absence of buffer solutions, the increase in pH is accompanied by significant O2 consumption (McBride, 1987). Oxygen consumption may result from autocatalytic oxidation of Mn2+ (favored at alkaline pH) and oxidation of semiquinone radical intermediates by O2. In the latter case, the relative contribution of Mn4+ and O2 to catechol oxidation is not clear. We found that O2 consumption was negligibledecreasing by less than 5% over the first hour of reactionwhen birnessite and catechol were reacted at pH 4 in buffered, closed systems that were initially saturated with lab air (21% O2). Similarly, McBride (1989b) showed that at pH 5.4, surface Mn(IV) is the primary electron acceptor even in oxic conditions. All of our experiments were conducted at pH 4, in 0.1 M Na-acetate buffer solution, to assure that Mn(IV) was the primary electron acceptor. Acetate buffer was selected because it is less reactive with the birnessite surface than alternatives (e.g., phosphate-citrate, Universal) (Stone, 1987). In experimental controls, we confirmed that the buffer alone did not induce measurable dissolution of birnessite.
Experimental Conditions
All experiments were conducted in triplicate for 24 h in aerated, continuously mixed batch reactors. Each reactor consisted of a sealed 250-mL Erlenmeyer flask supplied with air that was stripped of ambient CO2 by bubbling through a series of three test tubes containing 3 mol L-1 NaOH solution. Effluent 14CO2 evolving from the reaction was trapped in a series of three 0.1 mol L-1 NaOH traps placed downstream of the reaction vessel. Nearly all of the 14CO2 was trapped in the first two of the effluent NaOH traps. Continuous aeration was maintained by drawing a vacuum on the effluent end of the air stream. The initial catechol and birnessite concentrations were 2.3 mmol L-1 (13.8 mmol L-1 as C) and 1.0 g L-1, respectively, to give a Mn(IV) to catechol molar ratio of 4.54. Total volume of the suspension was 125 mL. The distribution of 14C among solid, aqueous and gaseous phases was measured as a function of time over 24 h.
To elucidate factors controlling CO2 evolution, three additional treatments were examined. Batch systems were constructed exactly as above for the starting conditions but, after a 5-h reaction time, a second pulse addition (of concentration equal to the first) of birnessite, catechol, or both birnessite and catechol was added. Hereafter, these experiments are referred to as "+B", "+C" and "+BC", respectively. The baseline case (no pulse addition at 5 h) is referred to as "+0".
Unlabeled catechol stock was mixed with uniformly labeled 14C catechol (to give a total catechol concentration of 2.3 mmol L-1 and a 14C concentration of 2.0 x 104 DPM mL-1) prior to addition to pre-mixed aqueous birnessite suspensions. The concentration of 14C in solution, solid and gas (14CO2) phases was measured at six different times over a 24-h reaction period (1, 2, 5, 6, 9, 24 h). At each sampling time, a 10-mL aliquot was removed from the flask through a syringe and centrifuged for 20 min at 12500 g with a Sorvall Superspeed RC2-B centrifuge (Sorvall Instruments - Du Pont Company, Newton, CT). The supernatant solution and pellet were separated for further analysis.
Chemical Analysis
A 0.100-mL sample of the supernatant solution was mixed with 10 mL of Eco-Scint scintillation cocktail (National Diagnostics, Atlanta, GA) and radioactivity was determined by a Beta Trac 6895 liquid scintillation counter (Elk Grove, IL). The pellet was air dried in a vacuum dessicator for at least 24 h prior to combustion in a Harvey Biological Oxidizer OX 600 (Hillsdale, NJ) using Harvey Carbon 14 Cocktail (Hillsdale, NJ) for absorption of 14CO2. Radioactivity of the solid phase was then determined in a Beta Trac 6895 liquid scintillation counter and corrected for contributions due to entrained solution.
Evolution of 14CO2 was monitored by collection in three successive 0.5 M NaOH traps (each 5 mL in volume) in the flow of air leaving the batch reactor and connected by glass tubing. Sodium hydroxide solutions were collected quantitatively at each sampling time and replaced with fresh NaOH. Trap solutions were combined, vigorously mixed, and a 0.5-mL sub-sample was combined with Eco-Scint cocktail for determination of 14CO2. Experiments were conducted in duplicate or triplicate and control reactors (no birnessite added) were used to determine initial radioactivity (
) and any loss of 14C over time.
Aliquots of the supernatant solution were analyzed by HPLC to measure catechol concentration. A 1.0 mL sample of the supernatant solution was filtered through a 0.45 µm membrane filter (Millipore Corp., Milford, MA), followed by 4 mL of water and 5 mL of methanol to a final eluate volume of 10 mL. The filtrate was thoroughly mixed and triplicate aliquots were injected into a Waters Associates HPLC system (Waters Corp., Milford, MA) equipped with two model 510 pumps, model 717 autosampler, and a Lambda Max 440 absorbance detector set at 254 nm. A solvent system of 60% methanol and 40% distilled deionized water was passed isocratically at a flow rate of 0.8 mL min-1 through a 30 cm, hyperchrome reverse phase C-18 Nucleosil column for analyte separation (Supelco, Bellefonte, PA).
Solution samples were analyzed by flame atomic absorption spectrometry (AAS, Thermo Optek Corp., Atlanta, GA) to determine time-dependent changes in Mn concentration. Aliquots were first filtered through a 0.2-µm membrane filter disk (Gelman Science, Fisher Scientific, Pittsburgh, PA) to remove colloidal Mn. Control experiments, conducted in the absence of catechol, confirmed negligible dissolution of Mn in pH 4 acetate buffer over 24 h.
Diffuse Reflectance Infrared Fourier Transform (DRIFT) Spectroscopy
Each pellet was washed twice with 0.01 M NaCl solution to remove entrained solution and then freeze-dried in a Labconco (Lyph-Lock 6) Freeze Dry System (Fisher Scientific, Pittsburgh, PA) prior to analysis by DRIFT spectroscopy on a Nicolet Magna 560 FTIR spectrometer (Nicolet Instrument Corp., Madison, WI). DRIFT samples were prepared by grinding 14 mg of sample with 60 mg KBr for 40 s. An additional 360 mg of KBr were ground with the sample with a Wig-L-Bug (Spex Sample Preparation, Metuchen, NJ), bringing the final concentration of the freeze-dried sample to 3% (w/w). Solid samples from each of the four treatment conditions (+0, +C, +B, +BC) after the 24-h reaction time were analyzed with a minimum of 400 scans and 4 cm-1 resolution. Spectra of birnessite before and after reaction with acetate buffer for 24 h were identical, indicating that interaction with the acetate buffer in the absence of catechol had no FTIR detectable effect on the Mn oxide. Difference spectra of the organic reaction products were obtained following subtraction of the birnessite spectrum.
Selected experiments were conducted under sterile conditions to verify the abiotic nature of the reactions. Glassware and solutions were autoclaved and all aliquots were removed from suspension in a sterile UV hood. Suspension samples were plated on nutrient agar and incubated for 48 h at 35°C to confirm the absence of microbial growth.
| Results |
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Effects of Subsequent Birnessite and Catechol Additions
Selected experiments were conducted in a manner identical to the "baseline" experiment detailed above except that fresh birnessite and/or catechol were added to the reaction vessels immediately after the sample aliquot was taken at 5 h. Figure 2
shows the effects of these pulse additions on the phase distribution of 14C in comparison to the baseline (+0) case. For the first 5 h of reaction, all treatments are identical and a single mean value is shown for all 12 replicates. Mean values are plotted by treatment for reaction times greater than 5 h.
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The addition of fresh birnessite alone after 5 h (+B) had no significant effect on the relatively large pool of solid phase C (Fig. 2b) and the concentration of solution phase C was not altered significantly (Fig. 2a). However, an increase in CO2 evolution was observed for subsequent sampling intervals (Fig. 2c). Whereas the +0, +C and +BC treatments resulted in similar cumulative CO2 evolution at 24 h, CO2 release from the +B case was significantly higher. This new pulse in CO2 evolution upon addition of birnessite alone (+B) indicates that the fresh birnessite surface (+B) was capable of oxidizing reaction products in addition to free catechol. Similarly, Naidja et al. (1998) found that CO2 generation increased with increasing ratio of birnessite to catechol in aqueous suspension. It is important to note that additional CO2 evolution was not observed when catechol was co-added with the birnessite at 5 h. Hence, if residual reaction products are present upon addition of fresh reactants, they appear to effectively sorb or otherwise sequester the newly oxidized materials before mineralization to CO2 occurs.
Manganese Dissolution
Previous work has confirmed that the Mn solubilized by reaction of birnessite and catechol is predominantly in the form of Mn(II) (McBride, 1989a) and that filtration through 0.2-µm nominal pore size filter disks effectively eliminates colloidal Mn(IV) from subsequent analyses (Stone and Morgan, 1984a,b). In our experiments, filtrate Mn in catechol-free controls was not detecable (Majcher, 1998). Therefore, time-dependent increases in soluble Mn result directly from the reduction of solid phase Mn(IV) by catechol.
Figure 3 shows the time-course solution concentration of Mn, following centrifugation and filtration, for each treatment. Prior to any secondary pulse additions to the reactors, measured Mn concentrations increased rapidly in the first hour to between 4.5 and 6 mmol L-1, then stabilized through the fifth hour at approximately 7 mmol L-1. Measured solution-phase concentrations indicate that 65 to 75% of the Mn solids were dissolved over the course of 24 h. The fact that birnessite was not fully consumed during the reaction is supported by DRIFT spectra of reacted samples that showed persistence (at a lower intensity) of the broad peak at 530 to 565 cm-1, which corresponds to Mn (hydr)oxide lattice vibrations.
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Solid Phase Reaction Products
The oxidation of catechol by Mn(VI) solids was found to produce polymeric solid-phase residues, as has been observed previously (Huang, 1991; Naidja et al., 1998). The solubility of these materials was investigated in the present study by extracting the 14C-enriched solids (generated as a function of reaction time) sequentially in solutions of variable polarity and pH (acetate buffer solution, methanol, ethyl acetate and 0.1 M NaOH). Results are presented in Table 1
. Solubility data indicate that reaction rapidly leads to the formation of highly insoluble and refractory organic precipitates. After only 2 h, less than 20% of the total 14C was solubilized by all extractants combined and most of this was extracted in the acetate buffer (Table 1). At 24 h, the 0.1 M NaOH treatment extracted the largest amount of 14C, but since this treatment removed < 10% of the total, most (90%) of the humified materials were retained in the humin fraction as insoluble birnessite complexes. The efficacy of a given solvent to extract solid-phase 14C varied with reaction time (Table 1). This suggests that the polarity of the solid-phase residue was likewise dependent on reaction time.
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stretch in simple and polycyclic aromatics, including quinones (Becker et al., 1963) and/or the asymmetric stretch of COO- (Baes and Bloom, 1989). Peaks at 1370 to 1390 cm-1, which are apparent in the spectra of +0, +B and +BC (and as a shoulder in the +C treatment) may be assigned to C-H bending of aliphatics, in-plane O-H bending or symmetric stretching of -COO- (Baes and Bloom, 1989; Cothup et al., 1990). Bands at 1614 and 1508 cm-1 (
), which are apparent in the +C treatment and also in pure catechol (Naidja et al., 1998), are masked by peak broadening for the other treatments. The C-OH stretch of phenolic groups (1270 cm-1) is also most evident in the +C case which contained more unreacted catechol. In contrast, this peak is reduced to a shoulder in +0 and +BC spectra and eliminated in the +B treatment.
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and/or COO- stretch predominates and the phenolic C-OH stretching vibration is completely eliminated. Hence, the degree of catechol structural transformation as a function of treatment (+B > +0
+BC > +C) is consistent with the higher CO2 evolution measured for the +B case (Fig. 2c) and the lower catechol transformation measured for the +C case (Fig. 2a). The band intensity of the C-OH stretch of phenolic groups (1290 cm-1) apparently follows the sequence of unreacted catechol in the various systems. | Discussion |
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Use of 14C-labeled catechol in kinetic studies of its reaction with birnessite facilitated accounting for its rapid disappearance, the origin and quantity of CO2 evolved and the mass of partially oxidized reaction products. After 24 h in the baseline treatment (+0, no additions at 5 h), 58 to 61% of the catechol-derived C was in strongly bound, insoluble, solid-phase residues whose structure contained aromatic moieties but less phenolic-OH functionalities than unreacted catechol. The remaining C was in soluble reaction products (1617%) or released as CO2 (1011%).
Although 30 to 40% of the added birnessite was not solubilized by reaction with catechol, the reactivity of the Mn(IV) solids remaining after 5-h reaction time was reduced such that when fresh catechol was added at 5 h (+C) most of this catechol remained unreacted in solution for the duration of the experiment. A small amount of catechol was sorbed to the residual organo-mineral complex, but DRIFT spectra indicated that the sorbed material was structurally similar to catechol and no increases in Mn dissolution or CO2 evolution were observed. Therefore, the decrease in CO2 evolution was not simply a result of diminished catechol concentration. Conversely, the oxidation reaction was limited by the availability of reactive birnessite surface. The residual birnessite may have contained a reduced surface layer (McBride, 1989a) or reactive sites may have been buried by catechol oxidation products. When new birnessite was added at 5 h (+B), a significant increase in CO2 evolution was observed, along with a smaller increase in Mn dissolution and a reduction in soluble C. Since catechol was undetectable at 5 h, this increase in CO2 is evidently a result of mineralization of adsorbed catechol and/or residual oxidation products. It is likely that birnessite oxidizes catechol more rapidly than it oxidizes quinone and other initial reaction products and this may affect the extent of CO2 release under various conditions. For example, Stone and Morgan (1984b) found that 1,4-benzoquinone dissolved Mn oxide, but at a rate that was much slower than hydroquinone. Indeed, the increased CO2 evolution for the +B case (Fig. 2c) is a result of further oxidation of these initial reaction products.
The presence of residual products (i.e., organo-mineral complexes) can also serve to sequester materials generated by subsequent reactions. When catechol and birnessite were added together at 5-h reaction time (+BC), there was a large increase in Mn dissolution (Fig. 3) but no significant increase in CO2 evolved relative to the baseline case (Fig. 2c). Despite the presence of fresh substrate and reactive surface, all of the added catechol was rapidly converted into the solid-phase residue (Fig. 2b). Evidently, the residual material remaining from the first 5 h prevented complete oxidation of added catechol by reacting with its initial oxidation products.
On the basis of the results of prior studies (Shindo and Huang, 1982, 1984; Stone, 1987; McBride et al., 1988; McBride, 1989a,b; Wang and Huang, 1994; Naidja et al., 1998) and those reported here, we postulate the following pathway to CO2 evolution from the oxidation of catechol by Mn(IV) oxides. Electron transfer reactions occur at the mineral surface after formation of a coordinative complex between surface Mn(IV) and phenolic-OH groups (Shindo and Huang, 1982, 1984; Stone and Morgan, 1984a, 1987). The C1 or C2 (hydroxylated) carbon atoms of catechol are the sites of oxidation, ring cleavage and CO2 release. Accordingly, a minimum of six moles of electrons must be transferred for every mole of CO2 released, resulting in dissolution of three moles of Mn(II).
As an index of the efficiency of catechol transformation to CO2 under the different treatments, we calculated the ratio of moles of CO2 released to moles of Mn dissolved (CO2/Mn) over time. Assuming (i) a net transfer of 6e- per CO2 released, (ii) all dissolved Mn is Mn(II), and (iii) once reduced, Mn(II) is not reoxidized or adsorbed, then a molar ratio of 0.33 indicates 100% efficiency [i.e., all Mn(II) production contributes to CO2 evolution]. Although these assumptions may not all be met, the calculation still provides a useful relative accounting of electron transfer attributable to the competing oxidation pathways under different conditions. After 24 h, the CO2/Mn ratio for the +B treatment was 0.27 ± 0.02; this suggests that about 80% of the measured Mn dissolution contributed to liberation of CO2.
Efficiency of catechol mineralization decreased in the other treatment conditions as follows: +B (80%) > +0 (72%) > +C (54%) > +BC (3%). The increase in mineralization efficiency for the +B relative to +0 case suggests that mineralization to CO2 is limited by reactive birnessite surface area. Furthermore, when a second dose of catechol (+C) or both catechol and birnessite (+BC) is added to a suspension containing residual organo-mineral complexes, these complexes are highly effective at sequestering the new reaction products (partially oxidized organics) before mineralization to CO2 occurs. With regard to natural soils, the latter point suggests that humic substances (as sequestering agents) would likely reduce the relative proportion of catechol mineralized to CO2.
Received for publication March 12, 1999.
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