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Environmental Processes
Geochemical Stability of Dissolved Mn(III) in the Presence of Pyrophosphate as a Model Ligand: Complexation and Disproportionation Ao Qian, Wen Zhang, Cheng Shi, Chao Pan, Daniel E. Giammar, Songhu Yuan, Hongliang Zhang, and Zimeng Wang Environ. Sci. Technol., Just Accepted Manuscript • DOI: 10.1021/acs.est.9b00498 • Publication Date (Web): 11 Apr 2019 Downloaded from http://pubs.acs.org on April 13, 2019
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Environmental Science & Technology
Geochemical Stability of Dissolved Mn(III) in the Presence of Pyrophosphate as a Model Ligand: Complexation and Disproportionation
Ao Qian1, Wen Zhang2, Cheng Shi3, Chao Pan4, Daniel E. Giammar4, Songhu Yuan1, Hongliang Zhang3, Zimeng Wang2, 5*
1 State
Key Laboratory of Biogeology and Environmental Geology, China University of Geosciences, Wuhan, Hubei, China
2 Department
of Environmental Science and Engineering, Fudan University, Shanghai, China
3 Department
of Civil and Environmental Engineering, Louisiana State University, Baton Rouge, LA, United State
4 Department
of Energy, Environmental and Chemical Engineering, Washington University in St. Louis, St. Louis, MO, United
State 5 Shanghai
Institute of Pollution Control and Ecological Security, Shanghai, China.
* corresponding
author:
[email protected] Phone: +86-21-31248978 Revised Manuscript submitted to Environmental Science & Technology
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Abstract 1
Dissolved Mn(III) species have recently been recognized as a significant form of Mn in redox transition zones,
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but their speciation, stability and reactivity are poorly understood. Besides acting as the intermediate for Mn redox
3
chemistry, Mn(III) can undergo disproportionation producing insoluble Mn oxides and aqueous Mn(II). Using
4
pyrophosphate(PP) as a model ligand, we evaluated the thermodynamic and kinetic stability of Mn(III) complexes.
5
They were stable at circumneutral pH and were prone to (partial) disproportionation at acidic or basic pH. With an
6
initial lag phase, the kinetics of Mn(III)-PP disproportionation was auto-catalytic with the produced Mn oxides
7
promoting the disproportionation. X-ray diffraction and the average Mn oxidation state indicated that the solid
8
products were not pure Mn(IV) oxides but a mixture of triclinic birnessite and -MnO2. Addition of synthetic
9
analogs of the precipitates eliminated the lag phase, confirming their catalytic roles. Thermodynamic calculations
10
adequately predicted the stability regime of Mn(III)-PP. The present results refined the constant for Mn(PP)25-
11
formation, which allows a consistent and quantitative prediction of equilibrium speciation of Mn(III)-Mn(II)-
12
birnessite with PP. A simple and robust model, which incorporated the thermodynamic constraints, autocatalytic
13
rate law, and verified reaction stoichiometry, successfully simulated all kinetic data.
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Environmental Science & Technology
INTRODUCTION
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Manganese (Mn) is the third most abundant transition metal in the Earth’s crust and is important to many
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biogeochemical redox processes.1, 2 In natural aquatic systems, Mn exists in three oxidation states, Mn(II), Mn(III),
17
and Mn(IV), which are present over a wide range of redox conditions in the environment.1 Mn(IV) is insoluble and
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exists as solid phases that can be potent oxidants.3, 4 Mn(II) is thought to be the primary dissolved form of Mn and
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can be abiotically and biotically oxidized to Mn(III)5, 6 and Mn(IV).7, 8 The intermediate oxidation state, Mn(III), is
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unstable in water because it can immediately disproportionate to Mn(II) and Mn(IV).9 Mn(III) forms from both one-
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electron oxidation of Mn(II)5, 6 and from reduction of Mn(IV)10-12, and the reaction between Mn(II) and Mn(IV)
22
could also produce solid phases of Mn(III) through comproportionation.13-15 Dissolved Mn(III) species have been
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underappreciated for a long time in the conventional paradigm of Mn environmental geochemistry.16
24
Recent reports have highlighted the ubiquitous presence of dissolved Mn(III) in a variety of aquatic systems
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including anoxic/suboxic seawaters17, sediment porewaters18-21, oxygenated surface waters17, 22, 23 and engineered
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treatment systems24. The stabilization of dissolved Mn(III) is enabled by complexation with naturally occurring
27
high-affinity ligands that include natural organic matter (and its degradation products)22, 25, biogenic siderophores26,
28
and cell-lysis products.27 The composition of these ligands in natural waters is not well known except for some
29
indirect information about the range of their overall binding strengths falling between those of pyrophosphate and
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desferrioxamine-B.28 Although complexation will lower the redox potential of Mn(III) below its standard value
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(EH°(Mn3+/Mn2+) = 1.56V), Mn(III) is presumably still an important geochemical oxidant from the thermodynamic
32
point of view29-33. For example, we previously demonstrated that UO2(s) was rapidly oxidized to U(VI) and
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subsequently dissolved.34 It was also reported that dissolved Mn(III) did not oxidize Cr(III) unless or until
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disproportionation happened, even though the energetics of the reaction was favored.35, 2
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Therefore, the
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environmental geochemistry of dissolved Mn(III) remains a significant knowledge gap.
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Even in simplified model ligand systems (e.g., pyrophosphate, citrate and desferrioxamine B.37-40), the speciation,
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stability and reactivity of dissolved Mn(III) species are far from quantitatively understood.27, 34 The stability of
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soluble Mn(III) is affected by the strength of complexation with the ligands, the solution pH and the total ligand:Mn
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ratio (which determines the structural configuration of the complexes).41-43 Depending on the binding affinity of the
40
ligands, an excess of ligand is generally needed to maintain the stability of Mn(III) complexes.41, 42, 44 With natural
41
and biogenic occurrences, pyrophosphate (PP) is an inorganic, redox-inert ligand that can form stable complexes
42
with Mn(III) under neutral pH with representative binding affinity in reference to Mn(III) ligands in natural waters.28
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Mn(III)-pyrophosphate complexes disproportionate at alkaline and acidic pH, and at high Mn(III):PP ratios.34, 43
44
Citrate forms complexes with Mn(III) that are metastable with respect to possible disproportionation and to
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reduction of the Mn(III) center by the organic carbon in the citrate.42, 43 Different from citrate, desferrioxamine B
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stabilizes Mn(III) at alkaline pH (7.0 -11.3), but at lower pH Mn(III)-desferrioxamine B complexes decompose by
47
intermolecular electron transfer to yield Mn(II) and oxidized siderophores, and at pH > 11 the complex degrades
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by disproportionation to yield Mn(II) and Mn oxide.41 Nonetheless, those processes involving destabilization of
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Mn(III) complexes lack quantitative kinetic data and models based on well controlled lab experiments.
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With a prolonged lifetime when complexed by ligands, dissolved Mn(III) may be a critical means of transporting
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oxidized Mn across redox interfaces21 and ultimately producing Mn(IV) in redox transition environments45
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Although recent research has advanced our understanding of the formation and stability of dissolved Mn(III)
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complexes,24, 47 less consideration has been specifically given to the process of disproportionation. Traditionally
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Mn(II) and Mn(IV) are considered as the products from the disproportionation of Mn(III).9 Mn(II) exists mainly as
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soluble species and insoluble Mn(IV) quickly hydrolyzes and polymerizes to precipitate as Mn(IV) oxides.46 Both 3
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Mn(III) complexes and dissolved Mn(II) produced by disproportionation have the ability to adsorb to Mn oxides.42,
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48
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complexes are not well understood.
In addition, the mineral phases and properties of Mn oxides produced from disproportionation of Mn(III)
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The objectives of this study were to (i) assess the stabilization and disproportionation of dissolved Mn(III)-PP at
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environmentally relevant pH; (ii) characterize the Mn solids produced from Mn(III)-PP disproportionation; (iii)
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quantify the kinetics of Mn(III)-PP disproportionation and (iv) develop and refine self-consistent thermodynamic
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and kinetic models for the Mn(III)-PP system. In this study, we used pyrophosphate, a dimer of orthophosphate as
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a model Mn(III) ligand because of its representative binding affinity28, redox-inertness and occurrence in natural
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environments from biogenic and synthetic sources.27
65 66
MATERIALS AND METHODS
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Materials. Manganese(III) acetate dihydrate (> 97%), manganese(II) chloride tetrahydrate (> 99%), potassium
68
permanganate (> 99%) and sodium pyrophosphate decahydrate (> 99%) were purchased from Sigma-Aldrich.
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Mn(III)-PP stock solution was prepared following the procedures of Kostka.21 In this procedure sodium
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pyrophosphate decahydrate was first dissolved in ultrapure water (resistivity > 18.2 1OP- ? with a concentration
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of 50 mM and the pH was adjusted to 8.0. Mn(III) acetate dehydrate solid was then added into the sodium
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pyrophosphate solution under vigorous stirring to reach a final concentration of 10 mM Mn(III). Note that previous
73
experience showed that at least 4 times excess of PP relative to Mn(III) was required to maintain the complexes
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against disproportionation.29 The final pH after dissolving the aliquot of Mn(III) acetate was around 7.0. This
75
solution was filtered (0.22 Q polyethersulfone, Tisch Environmental, OH) to remove any possible Mn precipitates.
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It served as the stock solution of Mn(III) for preparation of the experimental solutions summarized in Table 1. The 4
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average oxidation state of the Mn(III)-PP stock solution determined by comparing iodometric titration results and
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total Mn concentrations confirmed the purity of Mn(III) above 98%.49 H2-sparged anoxic ultrapure water was used
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to prepare all solutions. Diluted HNO3 and NaOH were used for pH adjustment.
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The synthesis of R;1 22 and triclinic birnessite followed the procedures described in Villalobos et al.50. Briefly,
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a volume of 320 mL of MnCl2 (0.095 mol) was added to 680 mL of solution containing 0.175 mol NaOH and 0.063
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mol KMnO4. The resulting suspension was stirred for 2 h and then left to settle for 6 h. Following the precipitation
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of the solid, R;1 22 was washed with 1 M NaCl, shaken for 1 h and centrifuged. The supernatant solution was then
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discarded. The NaCl washing procedure was repeated five times. The centrifuged paste was washed with similar
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procedures with DI water for another five times. The suspension was then dialyzed (3500 Da MWCO) in DI water
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until the conductivity of water outside the dialysis bag remained below the detection limit for 12 hours. Triclinic
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birnessite was synthesized as follows: 160 mL of MnCl2 (0.08 mol) was first added to 180 mL of NaOH (1.375
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mol) under stirring to form a pink gel precipitate of Mn(OH)2, and then 160 mL of KMnO4 (0.032 mol) was added
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slowly to the above mixture while stirring vigorously to form a dark gray precipitate. After another hour of stirring,
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the container was covered and placed in an oven at 55 oC for one day. The suspension was centrifuged at room
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temperature and the supernatant solution was discarded. The centrifuged paste was washed with 1 M NaCl for five
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times in the same way as the R;1 22. The centrifuged paste was then resuspended and washed with DI water for
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multiple times until the pH dropped to 9.8. Both R;1 22 and triclinic birnessite were transferred to polypropylene
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bottles as concentrated slurries and stored at 4 °C prior to use in experiments. X-ray powder diffraction (XRD)
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confirmed the success of the syntheses.
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Batch Experiments. Batch experiments on dissolved Mn(III) disproportionation were performed in an anaerobic
97
chamber (Coy Lab Products Inc., MI) where the O2 concentration was controlled below 1 ppmv. Two groups of 5
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batch experiments were conducted: (1) spontaneous dissolved Mn(III) disproportionation and (2) dissolved Mn(III)
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disproportionation with initial addition of different Mn oxide minerals ( -MnO2 or triclinic birnessite). The ratio of
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total PP:Mn(III) was 5 and the excess PP (pKa = 0.9, 2.0, 6.6, 9.4)51 served as a pH buffer that could be effective
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over the pH range of interest.34 Solution pH was first adjusted to the value known to be able to reach the desired
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final pH value (upon trial and error) and then aliquots of Mn(III)-PP stock solution were added to provide an initial
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concentration of 400 QM Mn(III) and 2 mM PP. Those concentrations might appear to be higher than in natural
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waters, but the results and models using PP as a model ligand could be extrapolated to geochemical contexts.
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Addition of concentrated acid or base into the Mn(III) solutions was avoided based on previous experience that
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undesired chemical transformation might happen before the solution became well mixed.34 For the experiments
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with initial seeding of Mn minerals, different amounts of the Mn minerals were added as concentrated slurries into
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the prepared volume (100 mL) of 400 Q1 Mn(III)-PP. No pH shift was observed after the addition of solids. Careful
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and prompt handling of the experimental solutions ensured accurate recording of the time-resolved data. Samples
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were periodically taken from the well-mixed reactors using syringes. Complementary experiments to examine
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comproportionation between Mn(II) and Mn minerals in the presence of pyrophosphate were also conducted. The
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detailed experimental conditions and key results are compiled in Table 1.
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Analysis Methods. Samples from the batch experiments were filtered through a polyethersulfone (PES) filter
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with a pore size of 0.05 Q
Half of the filtrate was preserved in 1% HNO3 for total dissolved Mn analysis by
115
inductively coupled plasma mass spectrometry (ICP-MS, PerkinElmer ELAN DRC II). The other half was
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immediately analyzed for the concentration of dissolved Mn(III)-PP complexes using a widely adopted method29,
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34, 52
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Lambda XLS, S258nm > 6000 M-1cm-1, detection limit < 5 Q1? Selected solid samples were collected on a filter and
based on the solution’s absorbance at 258 nm measured with a UV-vis spectrophotometer (PerkinElmer-
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then freeze dried. They were characterized by X-ray diffraction (XRD, Cu KU radiation Bruker d8 Advance X-ray
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diffractometer) to identify the mineralogical composition. Iodometric titration was used to determine the average
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Mn oxidation state (AOS) of the solid products.49, 50 Hydrodynamic diameter and zeta potential of the precipitating
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solids were measured on a Zetasizer Nano (Malvern). For dynamic light scattering analysis, disproportionation was
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occurred with in the cuvette that was continuously measured in the instrument to generate time resolved results.
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Thermodynamic and Kinetic modeling. The thermodynamic calculations of the Mn(III)-PP system were based
125
on critically selected equilibrium constants for relevant reactions in the literature and new experimental data
126
observed in the present study. The pe-pH diagrams were generated with the Act2 subprogram of Geochemist’s
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Workbench (GWB, V.11.0.8, Aqueous Solution LLC, IL). The general thermodynamic database used in the
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calculations was the “thermo_ladder” file published by Bethke et al.53, a reliable source where the Mn redox
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equilibrium was critically crafted. PP4- was added as a basis component species with multiple protonated species
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with different pKa values. Redox and hydrolysis reactions of PP species were ignored in the calculations, but the
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acid-base speciation of PP at various pH was considered. Choices of solid phases to include or suppress in the
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calculations were made based on low-temperature environmental relevance and experimental observation (details
133
in discussions). With the predominant species identified, calculations of the energetics and speciation of the
134
controlling equilibrium reactions were enabled by the Rxn subprogram of GWB, and a single equilibrium constant
135
for the dominant Mn-PP complex were optimized to simulate equilibrium Mn(III) concentrations in the present
136
experiments. Based on rational assumptions and experimental evidence, a set of differential equations were solved
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to model the kinetic behaviors of Mn(III) disproportionation where rate constants were optimized to simulate the
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time series datasets. Models were calibrated by minimizing the residual sum of squares (RSS) between the
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experimental and predicted values using a spreadsheet solver.54 7
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RESULTS AND DISCUSSIONS
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Effect of pH on the Stability of Mn(III)-PP Complexes. The stability of Mn(III)-PP complexes with respect to
142
disproportionation was sensitive to the solution pH (Figure 1a). At pH 6, 7, 8 and 8.3, Mn(III)-PP was very stable
143
and no loss of Mn(III)-PP from the solution was observed throughout the 60-hour experiment. It was consistent
144
with the literature that Mn(III)-PP complexes were stable at neutral pH for over two months under anaerobic
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conditions.29, 44 This observed range of pH for Mn(III) stability overlaps with the pH range of common groundwaters
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and surface waters. However, pH values outside of this range (i.e., 5.0, 8.6, 8.8 and 9.0) induced decreases in the
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Mn-PP concentrations. The solution changed from clear pink to turbid brown, and the final solution after the brown
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precipitates settled out still exhibited a light pink color, suggesting remaining Mn(III)-PP complexes, consistent
149
with the measured plateau of dissolved Mn(III) concentration.34 The total dissolved Mn concentration measured by
150
ICP-MS, which included dissolved Mn(III) and Mn(II), followed a similar trend. (Figure S1).
151
The time series of dissolved Mn(III) concentrations for the experiments with disproportionation suggested an
152
autocatalytic reaction in which the formation of an initial amount of Mn(IV)-containing solid accelerated
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subsequent Mn(III) disproportionation. Mn(III) concentration declined slowly during the initial period followed by
154
a much more dramatic decrease (Figure 1b). The duration of the lag phase was shorter for those experiments with
155
a higher extent of Mn(III) disproportionation. The final dissolved Mn(III) concentration plateaued at various levels
156
at different pH. The production of Mn(II) could not be responsible for the autocatalytic effect given its much lower
157
affinity to PP,9 and this was confirmed by a control experiment with initially added Mn(II) (Figure S2).
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Autocatalysis of aerobic Mn oxidation has been well known55, and Mn(III) disproportionation under anaerobic
159
conditions showed similar kinetics, suggesting a catalytic role of the produced Mn oxides.
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Evolution of the Particle Size and Zeta Potential. The time resolved monitoring of the average hydrodynamic
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diameter of the precipitates upon disproportionation at pH 5 and pH 9 suggested different production and growth
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behaviors of the Mn oxide particles (Figure 2). Despite the substantial noise of the DLS data with dynamic particle
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generation and growth, moving average results identified significantly different features. The DLS data could not
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provide concentration values of the colloidal system (the number concentration may be estimated using the Mn(III)
165
and total dissolved Mn concentration data), but it could assess the average particle size as the reaction proceeded.
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Both colloidal systems had very negative zeta potential, as expected for phyllomanganate minerals56, 57, at which
167
particle aggregation should be negligible and the particles would presumably nucleate and grow individually. Steric
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effects caused by ligand complexation on the Mn oxide surface may further stabilize the colloidal system. At pH 5,
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the DLS hydrodynamic diameter showed an initial growth period that was consistent with the lag phase of the loss
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of dissolved Mn(III) concentration, suggesting that relatively slower disproportionation was taking place with the
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growing Mn oxides precipitates as catalytic surfaces to destabilize dissolved Mn(III). At low pH with slower rates
172
(i.e., higher activation energy), dissolved Mn(III) may prefer to catalytically disproportionate on existing Mn oxide
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particles than in the bulk solution, resulting in the growing feature of the DLS particle size. At pH 9, no distinct
174
growing phase was observed, consistent with the faster disproportionation observed in the solution chemistry data.
175
The particle size at pH 9 was generally smaller than at pH 5, although the total number concentration at pH 9 was
176
much higher.
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Characterization of the precipitates. X-ray diffraction results suggested that the precipitates produced during
178
Mn(III) disproportionation were a mixture of triclinic birnessite and -MnO2 (Figure 3). No peak corresponding to
179
pure Mn(III) (manganite or bixbyite) was present, excluding non-redox precipitation of Mn(III). The XRD pattern
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of -MnO2 shows two predominant diffraction peaks at 37.3° (2.4 Å) and 66.4° (1.4 Å) Z and a broad feature 9
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between them, which are characteristic of poorly crystalline phyllomanganates.58, 59 The precipitates produced by
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spontaneous Mn(III) disproportionation exhibited higher crystallinity and the solid products harvested at 13 hours
183
and 56 hours showed similar XRD patterns. Four peaks at 12.4°, 24.9°, 42.0°, and 50.0° matched triclinic birnessite,
184
and the two at 12.4° (7.2 Å) and 24.9° (3.6 Å) Z can be attributed to the (001) and (002) reflections.60 The two
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peaks around 37° and 66° indicated the presence of -MnO2. When 100 Q1 of -MnO2 was initially added, the final
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products of disproportionation still showed evidence of triclinic birnessite, while the relative abundance of the two
187
Mn oxides were different. Iodometric titration of the spontaneous disproportionation products (Exp. 8) gave an
188
average Mn oxidation state (AOS) of 3.4, whereas the values for synthetic -MnO2 and triclinic birnessite were 3.8
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and 3.4, respectively. Even considering the possible amount of sorbed Mn(II), the AOS number suggested that the
190
products may more closely resemble triclinic birnessite than -MnO2. While the ideal stoichiometry of Mn(III)
191
disproportionation presumes a solid product of pure Mn(VI),9 our results suggest that the products (including those
192
produced after both 13 hours and 55 hours) still contained a substantial amount of Mn(III).
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Based on the limited XRD results it was a challenge to unravel the in-situ and initial mineralogical transformation
194
pathways when disproportionation, mineral growth, adsorption of Mn(II) and structural migration of Mn(III) were
195
happening simultaneously. It is reported that the presence of Mn(II) can promote transformation of hexagonal
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birnessite to triclinic birnessite in alkaline pH through comproportionation between Mn(II) and Mn(IV).13,
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Conversely, triclinic birnessite can transform to hexagonal birnessite via either Mn(III) migration into the interlayers
198
or Mn(III) disproportionation to Mn(IV) and Mn(II) at acidic pH.62 Our solid characterization results shed light on
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the possibility that the final products of Mn(III) disproportionation are controlled by chemical equilibrium as will
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be discussed in a later section on modeling.
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Disproportionation with Pre-added Mn Oxides. Knowing that the precipitates produced upon spontaneous
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disproportionation were a mixture of -MnO2 and triclinic birnessite as suggested by XRD results, experiments with
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addition of pre-synthesized precipitates indicated that both -MnO2 and triclinic birnessite can indeed act as the
204
catalysts for disproportionation (Figures 4, S3). We also note that for the most stable Mn(III)-PP solution (e.g, pH
205
7, Exp. 3) Mn oxides still did not induce disproportionation when -MnO2 or triclinic birnessite was added (Figure
206
S4). At pH 9, the 2-hour lag phase was eliminated when -MnO2 or triclinic birnessite was added at the beginning
207
of the experiments. Nevertheless, the dissolved Mn(III) concentration for all experiments at a given pH with
208
different amounts of solid present plateaued at the same level, suggesting an equivalent thermodynamic equilibrium
209
that was only governed by pH (comparing Figures 1, 4, S3 and S4, considering the activity of solids as a constant).
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For the same concentration (Mn atom normalized) of the two Mn oxides, -MnO2 appeared to be a stronger catalyst
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than triclinic birnessite with respect to promoting Mn(III) disproportionation. Partial disproportionation of dissolved
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Mn(III) complexes when the produced Mn oxides remained in the system was reported previously and could be
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interpreted as the concurrent comproportionation between Mn oxides and Mn(II) and subsequent stabilization of
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Mn(III) by PP.34, 43 Such comproportionation reaction has been previously investigated in ligand-free systems, and
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the produced Mn(III) resided in solid phases such as feitknechtite and manganite.14,
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experiments reacting aqueous Mn(II) and -MnO2 or triclinic birnessite in the presence of PP (Figure S5) confirmed
217
that comproportionation could occur in a time scale of hours as a mechanism to maintain residual dissolved Mn(III)
218
in the experiments just discussed. The experimental data above allowed us to develop thermodynamic and kinetic
219
models to describe the dynamic behaviors of dissolved Mn(III).
220 221
Thermodynamic Modeling.
15, 63-65
Complementary
Despite the lack of understanding of Mn(III) environmental speciation, there are
a few studies in the chemistry literature that reported the equilibrium constants of Mn(III)-PP complexes.66-70 We 11
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compiled each set of those constants (Table S1) and calculated the corresponding pe-pH diagrams for each set of
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constants and reactions. The selection of Mn oxide mineral phases was based on the likelihood of natural presence
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in low temperature soil and groundwater systems; consequently, pyrolusite, bixbyite and todorokite were suppressed
225
in the calculations.71, 72 The equilibrium constants related to Mn mineralogy were from Bethke et al.53 It should be
226
noted that the thermodynamic calculations here utilized birnessite (Mn8O19H10(s)) in the database, which was a good
227
analog of the disproportionation product for its mineralogy and average valance state of Mn (+3.5) noted previously.
228
Three sets of Mn(III)-PP equilibrium constants retrieved from the literature turned out to predict predominance of
229
dissolved Mn(III) only at highly acidic pH and above the stability limit of water (Figures S6, S7). This was
230
reasonable as previous studies of Mn(III) complexation used to determine these constants were performed at very
231
low pH. However, they could not predict the observed stability of Mn(III) at circumneutral pH.
232
The only exception was the set of equilibrium constants from Gordienko et al.66 in which a Mn(PP)25- species
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was predicted to be stable over an environmentally relevant regime (Figure 5). Multiple calculations were performed
234
by varying the total PP to total Mn ratio, and the magnitude of the equilibrium constant for Mn(PP)25-. While the
235
prevalence regime shrinks with lower PP to Mn ratio, as long as the equilibrium constant is large enough, Mn-PP
236
can maintain its thermodynamic stability at circumneutral pH. At higher or lower pH beyond its predominance
237
regime, Mn(II) or Mn(IV) oxides are more favorable and thermodynamics drives disproportionation of Mn(III)
238
complexes. Mn(III)-PP speciation calculations with redox decoupled showed that non-redox decomplexation of
239
Mn-PP complex occurred only below pH 3, confirming that the observed Mn(III) loss should be attributed to
240
disproportionation (Figure S8).
241
While they could determine the predominant species, pe-pH diagrams could not quantify the equilibrium
242
concentration of each species that may co-exist. Given that our experimental results suggested that equilibrium was 12
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approached (plateau of the residual Mn(III)), they can be used to verify or refine the equilibrium constants. We
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consider a controlling equilibrium reaction with the predominant species at specific pH as below.
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2Mn(PP)25- + 19/6 H2O + 4/3 H+ = 1/6 Mn8O19H10(s) + 2/3 Mn2+ + 4 H2PP2- , 2.0 < pH < 6.6
(1)
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2Mn(PP)25- + 19/6 H2O = 1/6 Mn8O19H10(s) + 2/3 MnPP2- + 10/3 HPP3- + 4/3 H+, 6.6 < pH < 9.4
(2)
247
2Mn(PP)25- + 19/6 H2O = 1/6 Mn8O19H10(s) + 2/3 MnPP2- +10/3 PP4- + 14/3 H+, pH > 9.4
(3)
248
The stoichiometric relationships and a stability constant of Mn(PP)25- could predict the equilibrium Mn speciation
249
for a given water chemistry condition, including the cases with partial disproportionation (Figure 6). It was
250
remarkable that a single stability constant of Mn(PP)25- with a logK of 28.9, which is lower than the value of 30.9
251
from the literature66, was able to quantitatively predict the final equilibrium concentration of Mn(III) with partial
252
disproportionation at alkaline pH. The experiment duration (60 h) at pH 5 did not capture an unambiguous plateau
253
so that the pH 5 results were not used to constrain the stability constant of Mn(PP)25-. Nevertheless, the logK of
254
28.9 predicted the favorability of disproportionation at pH 5 but not at pH 6 (Figures 1 and 6), which was consistent
255
with our observations. The fact that initial addition of pre-synthesized Mn oxides did not change the final
256
equilibrium Mn(III) concentration (Figures 1, 4, S3 and S4) was in line with the thermodynamic calculations above.
257
These calculations and their consistency with the experimental data suggest that the commonly observed co-
258
existence of Mn(II)-Mn(III)-Mn(IV) species14, 15, 34, 43 over a wide range of pH might be predominantly governed
259
by thermodynamics.
260
Kinetic Modeling. With the final equilibrium Mn(III) concentrations at each pH constrained by thermodynamics,
261
we developed a mathematical model to describe the kinetics of Mn(III) disproportionation using formulations for
262
autocatalysis analogous to Mn(II) oxidation by dissolved oxygen as by Morgan.73, 74 Several assumptions were made
263
to simplify the model: (1) the homogenous disproportionation rate of Mn(III) was first order; (2) the surface 13
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catalyzed disproportionation rate was first order with respect to dissolved Mn(III) and first order with respect to Mn
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oxide concentration; (3) the reaction followed the stoichiometry defined in Reactions 1-3 for the respective pH,
266
ignoring surface associated Mn(II) and Mn(III); (4) both homogenous and heterogeneous disproportionation were
267
constrained by the thermodynamic equilibrium. We acknowledge that the current model could be further refined by
268
considering surface and aqueous speciation, but with only two fitting parameters, the relative importance of various
269
processes could be quantified as below
270
Mn(III)]
=
(1
[Mn(III)] [Mn(III)]eq
)[Mn(III)] (1
[Mn(III)] [Mn(III)]eq
)[Mn(III)][MnO ]
(4)
271
where k is the homogenous disproportionation rate constant (M-1·s-1), k’ is the surface-catalyzed disproportionation
272
rate constant (M-2·s-1), and [Mn(III)]eq is the equilibrium Mn(III) concentration based on the preceding
273
thermodynamic analysis. The third assumption allows the growing value of the concentration of the Mn-containing
274
solid product birnessite (quantified on the basis of Mn atoms) to be expressed by [Mn(III)] based on the
275
stoichiometric mass balance, such that
276
Mn(III)]
=
(1
[Mn(III)] [Mn(III)]eq
)[Mn(III)] (1
[Mn(III)] [Mn(III)]eq
)[Mn(III)]
2 3([Mn(III)]0
[Mn(III)]) (5)
277
where [Mn(III)]0 denotes the initial concentration. Numerical solution of Eq. 5 should reproduce the experimental
278
data of Mn(III) lost during disproportionation at various pH as shown in Figure 1. As the [Mn(III)]eq as a function
279
of pH was determined by the thermodynamic model, the kinetic model only had k and k’ as parameters to be
280
determined by finding the best fit to the data. The model calibrated using dissolved Mn(III) time series data provided
281
an excellent fit to the total dissolved Mn concentration (Figures S1, S3), suggesting that the model assumption of
282
the reaction stoichiometry, i.e., Reaction 2, (the average valence state of Mn and the quantity of dissolved Mn(II)
283
production) was acceptable. Slight underestimation of total dissolved Mn loss might be due to unaccounted
284
adsorption of Mn(II). Despite the success of the model with the assumption of a single Mn(PP)25- species in 14
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285
simulating the present disproportionation data, the real stoichiometry and protonation states of Mn(III)-PP
286
complexes may vary with water chemistry conditions and thus exhibit different kinetic behaviors.
287
The kinetic model framework, upon a change of the initial Mn oxide concentration, could simulate the
288
elimination of the initial lag phase when synthetic pure Mn oxide (triclinic birnessite or R;1 22) was added at the
289
beginning of the experiments (Figures 4 and S3). The homogenous disproportionation rate constant (k) was kept
290
intact at the value obtained from the spontaneous disproportionation experiments and the surface catalyzed
291
disproportionation rate constants (k’) were adjusted to provide an optimal fit of the kinetic data of Mn(III) loss.
292
Model calibration selected the time window of the initial first hour, before the accumulation of the
293
disproportionation products would make the solids a mixture. Comparing the extrapolation of the model to longer
294
durations with the experimental data over the full duration provided information about how different the in-situ
295
formed precipitate was from the initially seeded solids with respect to their catalytic properties. The k’ obtained
296
from the spontaneous disproportionation was higher than that determined from the experiments with addition of
297
pre-synthesized triclinic birnessite, and it was lower than that with R;1 22 addition. These observations are
298
consistent with the fact that the precipitates from spontaneous disproportionation were a mixture of the two Mn
299
oxides. As k’ was expressed by molar concentration on the basis of Mn, the larger value for R;1 22 might be
300
attributed to its larger specific surface area that would provide more catalytic sites per unit mass of solid.50 The
301
model calibrated with the first hour of Mn(III) data with R;1 22 overestimated later Mn(III) loss (Figures 4a, S3a),
302
suggesting that the precipitating products (likely the mixture mentioned above) were overall less reactive than pure
303
R;1 22 for catalyzing Mn(III) disproportionation . In contrast, the quality of the model fits for triclinic birnessite
304
was better over the entire experimental duration (Figures 4a, S3c). Combining these observations with the
15
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comparison of the k’ values for those experiments (Exp. 8-14), it appeared that the products might behave more
306
analogously to triclinic birnessite.
307
As discussed in previous sections, the autocatalytic mechanism looked analogous to that of Mn(II) oxidation in
308
which fast adsorption of Mn precursor on Mn oxides lowers the activation energy. Our kinetic model indicated that
309
a majority of the Mn(III) loss was driven by the surface catalyzed process (Figure S9). The identity of the final solid
310
products (mixture of MnIII and MnIV) and Mn(III) loss not accounted for by disproportionation (note the gap between
311
model and data) are in accord with this mechanism, although autocatalytic processes involving Mn often do not
312
yield unequivocal identification of the reaction mechanisms.55
313
Environmental Implications. With the emerging evidence for the presence of dissolved forms of Mn(III) in
314
aquatic environments and their roles in the fundamental mechanisms of Mn redox processes, understanding Mn(III)
315
stability and reactivity become critical to advancing knowledge of Mn environmental biogeochemistry. The aqueous
316
stability of dissolved Mn(III) would significantly enhance the mobility of oxidized Mn species in subsurface porous
317
media in contrast to particulate or colloidal Mn oxides.34, 75, 76 Disproportionation can occur when the solution pH
318
shifts out of its stability regime and when complexing ligands undergo chemical or microbial degradation. The
319
presence of ligands that can form stable aqueous complexes with Mn(III) allows the coexistence of three oxidation
320
states of Mn over a relatively wide pH range. Such coexistence of multiple oxidation states allows dynamic atomic
321
exchange and electron transfer at mineral-water interfaces that can affect the mobility of associated trace elements.63,
322
64, 77
323
The experimental approach using PP as a model ligand may be extended to other Mn(III) complexes. The pH
324
range of stability as well as the equilibrium residual Mn(III) can provide information about the binding affinity of
325
the ligands for Mn(III). Other ligands may be studied using the same approach to overcome the difficulty in 16
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measuring trace concentrations of free Mn(III). Considering the heterogeneity and time scales relevant to subsurface
327
environments, we anticipate that the autocatalytic disproportionation of dissolved Mn(III) could readily reach
328
equilibrium, which could be incorporated in future geochemical models that consider Mn(III) dynamics. Natural
329
organic matter (NOM) may have specific functional groups such as hydroxylamine and catechol groups that can
330
complex with Mn(III).21, 75 It is possible to follow a bottom up approach by using model ligands to individually
331
establish the speciation of Mn(III) complexes and then extrapolate to a continuum mixture of ligands present in
332
NOM. Caution should be taken when extrapolating the results of Mn-PP system to organic ligands because of the
333
potential intramolecular electron transfer from the organic molecules to Mn(III), which is more favorable at acidic
334
pH; in contrast PP cannot reduce Mn(III) itself, but it can undergo hydrolysis and destabilize Mn(III) towards
335
disproportionation. Therefore, consumption of Mn(III) may occur through different pathways for different ligands.
336
Disproportionation of Mn(III) has been recently recognized as a critical step in microbial production of Mn
337
oxides.45,
46
338
“controlled” disproportionation of Mn(III) in the presence of excess complexing ligands. The products of Mn(III)
339
disproportionation may have properties that depend on the disproportionation rates that are affected by the
340
concentration and Mn(III)-complexing affinity of ligands present 47. The reactivity of soluble Mn(III) species as
341
geochemical oxidants warrants detailed investigation to fill the knowledge gaps of environmental occurrence,
342
chemical speciation, redox activity, and biological roles of aqueous Mn(III) complexes. Those knowledge gaps may
343
challenge our current assessments of the relativities of actual environmental Mn oxides based on laboratory studies
344
using synthetic analogs.
The present study highlighted the mixture of triclinic birnessite and R;1 22 as the products of
345 346
ASSOCIATED CONTENT 17
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Supporting Information. The Supporting Information is available free of charge on the ACS Publications website
348
at DOI ---”.
349
Data and models for total dissolved Mn variation with time; additional control experiments; additional data and
350
model simulations for the experiments with initially seeded Mn oxides; complementary experiments for
351
comproportionation, aqueous speciation equilibrium of Mn(III)-PP, additional pe-pH diagram calculations using
352
other sets of equilibrium reactions and constants; model calculated homogenous and surface catalyzed
353
disproportionation rates, and compilation of the model reactions and constants. (PDF)
354 355
ACKNOWLEDGMENTS
356
We respectfully acknowledge insightful suggestions and comments of Profs. James Morgan and Alan Stone.
357
This study received financial support from National Natural Science Foundation of China (21806021, 41807187)
358
and Louisiana Board of Regents (LEQSF(2017-20)-RD-A-07). A.Q.’s participation was sponsored by a visiting
359
student fellowship from China Scholarship Council. Comments and suggestions of Associate Editor Prof. Timm
360
Strathmann and three other anonymous reviewers improved the quality of the manuscript.
361 362
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Environ. Sci. Technol. 2018, 52, (4), 1844-1853. 66. Gordienko, V. I.; Sidorenko, V. I.; Mikhailyuk, Y. I., Amperometric investigation of Mn(III) pyrophosphate complexes. Russ. J. Inorg. Chem 1970, 15, 1241-1244. 67. Martell, A. E.; Smith, R. M.; Motekaitis, R. J., NIST Critically Selected Stability Constants of Metal Complexes. In NIST Standard Reference Database 46, Version 6.0. NIST, Gaitherburg: 2001. 68. Ciavatta, L.; Palombari, R., On the equilibria of complex formation between manganese(III) and pyrophosphate ions. Gazz. Chim. Ital. 1983, 113, 557-552. 69. Kolthoff, I.; Watters, J., Polarographic determination of manganese as tridihydrogen pyrophosphatomanganiate. Ind. Eng. Chem. Anal. Edit. 1943, 15, (1), 8-13. 70. Bogdanovich, N.; Pechurova, N.; Martynenko, L.; Pinnova, V., Reaction of manganese (III) with complexones. Russ. J. Inorg. Chem. 1971, 16, 1337-1339. 71. Wang, Z.; Giammar, D. E., Metal contaminant oxidation mediated by manganese redox cycling in subsurface environment. In Advances in the Environmental Biogeochemistry of Manganese Oxides, Feng, X. H.; Li, W.; Zhu, M.; Sparks, D. L., Eds. American Chemical Society: Washington DC, 2015; Vol. 1197, pp 29-50. 72. Tebo, B. M.; Bargar, J. R.; Clement, B. G.; Dick, G. J.; Murray, K. J.; Parker, D.; Verity, R.; Webb, S. M., Biogenic manganese oxides: Properties and mechanisms of formation. Annu. Rev. Earth Planet. Sci. 2004, 32, (1), 287-328. 73. Morgan, J. J., Kinetics of reaction between O2 and Mn(II) species in aqueous solutions. Geochim. Cosmochim. Acta 2005, 69, (1), 35-48. 74. Morgan, J. J. Chemistry of Aqueous Manganese II and IV: A Thesis. Harvard University, 1964. 75. Li, Q.; Xie, L.; Jiang, Y.; Fortner, J. D.; Yu, K.; Liao, P.; Liu, C., Formation and stability of NOM-Mn (III) colloids in aquatic environments. Water Res. 2019, 149, 190-201. 76. Wang, Z.; Tebo, B. M.; Giammar, D. E., Effects of Mn(II) on UO2 dissolution under anoxic and oxic conditions. Environ. Sci. Technol. 2014, 48, (10), 5546-5554. 77. Hinkle, M. A.; Flynn, E. D.; Catalano, J. G., Structural response of phyllomanganates to wet aging and aqueous Mn (II). Geochim. Cosmochim. Acta 2016, 192, 220-234.
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Table of Content Art
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533 534
Figure 1. Kinetics of Mn(III)-PP disproportionation at various pH. Panel (b) provides a zoom-in view of the
535
initial dynamics of the autocatalytic behavior. Symbols and lines were experimental data and model simulations,
536
respectively. Error bars indicated standard deviation of at least duplicate experiments, some of which might be
537
shown smaller than the size of the symbols. Data points for pH 6.0, 7.0, 8.0 and 8.3 had substantial overlapping.
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Detailed experimental conditions are summarized in Table 1 (Exp. 1-8).
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Figure 3. Mineralogical identification of the disproportionation products by X-ray diffraction (Blue: Exp. 8;
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Green: Exp. 11)
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551
552 553
Figure 4. Kinetics of Mn(III) disproportionation with initially added R;1 22 (Exp. 9) and triclinic birnessite
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(Exp. 12) at different concentrations. Data and models for Exp. 8 (no Mn mineral) were included for a
555
comparison. Panels a and b presents dissolved Mn(III) and total dissolved Mn, respectively. Symbols and lines
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were experimental data and model simulation, respectively. Error bars indicated standard deviation of at least
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duplicate experiments, some of which might be shown smaller than the size of the symbols. Note that the models
558
were calibrated only using the kinetic data in the initial first hour before the solids developed into a mixture of the
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two oxides. Additional data using different dosages of R;1 22 and triclinic birnessite are presented in Figure S3.
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Residual MnIII ( M)
500 400 300 200 100 0 4
6
8 pH
10
12
571 572
Figure 6. Experimentally observed and model predicted final residual Mn(III) concentration at different pH.
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Initial total Mn(III) concentration was 400 Q
574
separate the pH ranges with different equilibrium reactions considered in the model calculations. The
575
experimentally observed Mn(III) concentration profile at pH 5 after 60 hours could not rule out even lower
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equilibrium concentration, as denoted by the downward arrow. The residual concentration value for pH 5 as of 60
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hours might merely be the upper bound and was not included in the optimization of the thermodynamic model.
and the total PP concentration was 2 mM. The vertical dashed lines
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Table 1. Summary of the Experimental Conditions, Key Results and Thermodynamic and Kinetic Model Parameters Exp
582 583 584 585 586 587 588
pH
MnIII
PP
MnII
R;1 22
Tric. Birn.
k (×103)
>Q1? a
(1/s) b
1/(M s)
>Q1?
>Q1?
>Q1?
>Q1?a
k' (×103) b
Measured MnIII
eq
>Q1?
Predicted MnIIIeq >Q1?c
1
5
400
2000
0
0
0
0.09
0.03
N.A. d
57.5
2
6
400
2000
0
0
0
N.A.
N.A.
400
399
3
7
400
2000
0
0
0
N.A.
N.A.
400
400
4
8
400
2000
0
0
0
N.A.
N.A.
400
400
5
8.3
400
2000
0
0
0
N.A.
N.A.
400
381
6
8.6
400
2000
0
0
0
0.92
2.18
297
276
7
8.8
400
2000
0
0
0
0.99
2.75
214
227
8
9
400
2000
0
0
0
2.20
3.30
180
181
9
9
400
2000
0
20
0
2.20
6.37
181
181
10
9
400
2000
0
50
0
2.20
7.29
184
181
11
9
400
2000
0
100
0
2.20
8.51
180
181
12
9
400
2000
0
0
20
2.20
2.04
217
181
13
9
400
2000
0
0
50
2.20
2.10
197
181
14
9
400
2000
0
0
100
2.20
2.12
187
181
15
9
0
2000
200
200
0
N.A.
N.A.
121
N.A.
16
9
0
2000
200
0
200
N.A.
N.A.
76.5
N.A.
a. The concentration of initially seeded R;1 22 and triclinic birnessite was quantified on the basis of Mn atom. b. k and k’ denote the rate constants for homogeneous and surface catalyzed disproportionation pathways. c. Prediction of the final Mn(III) concentrations was enabled by the thermodynamic calculation using the optimized logK for Mn(PP)25-. d. For pH 5, our experimental results up to 60 hours didn’t capture the plateau of the residual Mn(III) concentration approaching the predicted value. The observed residual Mn(III) after 60 hours was not applicable to compare with the calculated value.
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