Journal Pre-proof Sulfidated nano zerovalent iron (S-nZVI) for in situ treatment of chlorinated solvents: A field study Ariel Nunez Garcia, Hardiljeet K. Boparai, Ahmed I.A. Chowdhury, Cjestmir V. de Boer, Chris Kocur, Elodie Passeport, Barbara Sherwood Lollar, Leanne M. Austrins, Jose Herrera, Denis M. O'Carroll PII:
S0043-1354(20)30130-5
DOI:
https://doi.org/10.1016/j.watres.2020.115594
Reference:
WR 115594
To appear in:
Water Research
Received Date: 2 December 2019 Revised Date:
3 February 2020
Accepted Date: 6 February 2020
Please cite this article as: Garcia, A.N., Boparai, H.K., Chowdhury, A.I.A., de Boer, C.V., Kocur, C., Passeport, E., Lollar, B.S., Austrins, L.M., Herrera, J., O'Carroll, D.M., Sulfidated nano zerovalent iron (S-nZVI) for in situ treatment of chlorinated solvents: A field study, Water Research (2020), doi: https:// doi.org/10.1016/j.watres.2020.115594. This is a PDF file of an article that has undergone enhancements after acceptance, such as the addition of a cover page and metadata, and formatting for readability, but it is not yet the definitive version of record. This version will undergo additional copyediting, typesetting and review before it is published in its final form, but we are providing this version to give early visibility of the article. Please note that, during the production process, errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain. © 2020 Published by Elsevier Ltd.
2
Sulfidated Nano Zerovalent Iron (S-nZVI) for In Situ Treatment of Chlorinated Solvents: A Field Study
3 4 5
Ariel Nunez Garcia,1Hardiljeet K. Boparai,1,2 Ahmed I. A. Chowdhury,1,3 Cjestmir V. de Boer,1,4 Chris M.D. Kocur,1,5 Elodie Passeport,2,6 Barbara Sherwood Lollar,7 Leanne M. Austrins,8 Jose Herrera,9 Denis M. O’Carroll*1,10
1
6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40
1
Department of Civil and Environmental Engineering, Western University, 1151 Richmond Rd., London, Ontario, N6A 5B8, Canada 2
Department of Civil and Mineral Engineering, University of Toronto, 35 St. George Street, Toronto, Ontario, M5S 1A4, Canada 3
Institute of Water and Flood Management, Bangladesh University of Engineering and Technology, Dhaka, Bangladesh 4
Netherlands Organization for Applied Research, TNO, Princetonlaan 6, 3584 CB, Utrecht, The Netherlands 5
OHSU-PSU School of Public Health, Oregon Health & Science University, 3181 SW Sam Jackson Park Road, Portland, OR 97239, United States 6
Department of Chemical Engineering and Applied Chemistry, University of Toronto, 200 College Street, Toronto, Ontario, M5S 3E5, Canada 7
Department of Earth Sciences, University of Toronto, 22 Russell Street, Toronto, Ontario, M5S 3B1, Canada 8
Arcadis, 28550 Cabot Dr #500, Novi, 48377, MI, US
9
Department of Chemical and Biochemical Engineering, Western University, 1151 Richmond Rd., London, Ontario, N6A 5B8, Canada 10
School of Civil and Environmental Engineering, Water Research Centre, University of New South Wales, Sydney, NSW 2052 Australia
*Corresponding author School of Civil & Environmental Engineering Water Research Centre Kensington Campus, University of New South Wales Sydney, NSW 2052 Australia Email:
[email protected]
1
41
Abstract
42
Sulfidated nano zerovalent iron (S-nZVI), stabilized with carboxymethyl cellulose (CMC), was
43
successfully synthesized on site and injected into the subsurface at a site contaminated with a
44
broad range of chlorinated volatile organic compounds (cVOCs). Transport of CMC-S-nZVI to
45
the monitoring wells, both downgradient and upgradient, resulted in a significant decrease in
46
concentrations of aqueous-phase cVOCs. Short-term (0 to 17 days) total boron and chloride
47
measurements indicated dilution and displacement in these wells. Importantly however,
48
compound specific isotope analysis (CSIA), changes in concentrations of intermediates, and
49
increase in ethene concentrations confirmed dechlorination of cVOCs. Dissolution from the
50
DNAPL pool into the aqueous phase at the deepest levels (4.0 - 4.5 m bgs) was identifiable from
51
the increased cVOCs concentrations during long-term monitoring. However, at the uppermost
52
levels (~1.5 m above the source zone) a contrasting trend was observed indicating successful
53
dechlorination. Changes in cVOCs concentrations and CSIA data suggest both sequential
54
hydrogenolysis as well as reductive β-elimination as the possible transformation mechanisms
55
during the short-term abiotic and long-term biotic dechlorination. One of the most positive
56
outcomes of this CMC-S-nZVI field treatment is the non-accumulation of lower chlorinated
57
VOCs, particularly vinyl chloride. Post-treatment soil cores also revealed significant decreases in
58
cVOCs concentrations throughout the targeted treatment zones. Results from this field study
59
show that sulfidation is a suitable amendment for developing more efficient nZVI-based in situ
60
remediation technologies.
61 62
Keywords: sulfidation, nano zerovalent iron, dithionite, groundwater, chlorinated VOCs, in situ
63
remediation
2
64
1.
Introduction
65
Sulfidation is a recent development related to the use of zerovalent iron (ZVI) based
66
materials for groundwater remediation (Fan et al. 2017, Li et al. 2017). Though most of the focus
67
in recent years has been on engineered sulfidation of nano ZVI (nZVI), biogenic sulfidation of
68
ZVI has been extensively investigated since the 1990s (Benner et al. 2002, Phillips et al. 2000,
69
Puls et al. 1999, Wilkin et al. 2003). Earlier studies focused on the identification of authigenic
70
mineral phases formed during the application of ZVI permeable reactive barriers (PRBs).
71
Formation of iron sulfides (FeSs) was attributed to the concurrent oxidation of ZVI and
72
generation of sulfides via biogeochemical processes (e.g., microbial reduction of SO42-). These
73
mineral phases were studied in the context of the hydraulic performance of PRBs, noting that the
74
accumulation of FeS precipitates on ZVI surface could contribute to pore clogging, decreased
75
permeability, and slower groundwater flow. However, parallel work on the dechlorination of
76
chlorinated volatile organic compounds (cVOCs) by FeSs (Butler and Hayes 1999, 2000) led to
77
the recognition of these mineral phases as an additional remediant during the operation of PRBs
78
(He et al. 2008, Shen and Wilson 2007). Similar field studies utilized the in situ formation of
79
FeSs to promote abiotic reduction of cVOCs in the Biogeochemical Reductive Dechlorination
80
technology (Kennedy et al. 2006a, 2006b). Investigations on reactive FeSs for remediation
81
purposes is now a thriving field as demonstrated by recent advances on their synthesis,
82
stabilization, and applicability for the removal of contaminants (Gong et al. 2016).
83
In contrast to the biogenic processes described above, abiotic sulfidation can be achieved
84
by modifying the nZVI particles with sulfur compounds; mainly sulfate (Cumbal et al. 2015),
85
dithionite (Cao et al. 2017, Fan et al. 2016, Li et al. 2016, Nunez Garcia et al. 2016, Song et al.
86
2017, Lv et al. 2019), thiosulfate (Han and Yan 2016), and sulfide (Fan et al. 2016, Rajajayavel
3
87
and Ghoshal 2015, Zhao et al. 2019). The resultant sulfidated nZVI (S-nZVI) is more reactive
88
than sulfur-free nZVI for dechlorination of cVOCs (Han and Yan 2016, Jin et al. 2018, Nunez
89
Garcia et al. 2016, Rajajayavel and Ghoshal 2015), adsorption of heavy metals (Cumbal et al.
90
2015, Lv et al. 2019, Zhao et al. 2019), and transformation of organic contaminants (Cao et al.
91
2017, Li et al. 2016, Song et al. 2017). Increased longevity (Nunez Garcia et al. 2016) and higher
92
colloidal stability in suspension (Cao et al. 2017, Song et al. 2017) has also been reported for S-
93
nZVI. To the best of our knowledge, published studies on S-nZVI have been performed solely at
94
the laboratory scale. As such, the field performance of S-nZVI for dechlorination of cVOCs is
95
yet to be evaluated.
96
Multiple pilot- and field-scale studies have been conducted to evaluate the efficacy of
97
nZVI for in situ treatment of contaminated soil and groundwater (Elsner et al. 2010, He et al.
98
2010, Henn and Waddill 2006, Kocur et al. 2014, Qian et al. 2020, Sheu et al. 2016). However,
99
application of nZVI has often faced limitations related to colloidal instability and side oxidation
100
reactions with natural in situ oxidants causing rapid passivation (Fang et al. 2018, Stefaniuk et al.
101
2016). While a significant amount of research has been directed to improve colloidal stability,
102
fewer studies have been dedicated to the minimization of undesirable oxidation reactions.
103
Controlled abiotic sulfidation of nZVI has shown potential to minimize such reactions and
104
improve selectivity towards targeted pollutants (Fan et al. 2016). Such functionality makes S-
105
nZVI more advantageous than nZVI for large-scale applications, as more electron equivalents
106
would hypothetically be directed to the reduction of contaminants, resulting in a more cost-
107
effective treatment.
108
In this study, we have reported results from a field synthesis and injection of
109
carboxymethyl cellulose (CMC) stabilized S-nZVI to remediate groundwater and soil
4
110
contaminated with cVOCs. To assess the effectiveness of CMC-S-nZVI for the in situ
111
transformation of contaminants, Compound Specific Isotope Analysis (CSIA) was used to
112
differentiate
113
transformations (Hunkeler et al. 2009). The specific objectives of the current study were to (1)
114
assess the short- and long-term spatial and temporal variability of cVOCs concentrations in
115
groundwater and soil after injection of CMC-S-nZVI, (2) utilize CSIA as an advanced diagnostic
116
tool to distinguish chemical transformation from physical processes, and (3) to monitor changes
117
in chloride and total boron concentrations to assess dilution and displacement.
between
physical
processes
(dilution
and
displacement)
and
chemical
118 119
2.
Materials and Methods
120
2.1. Site History and Description
121
Located in Sarnia, Ontario, the site was home to cVOCs production facilities, resulting in
122
the accumulation of a multicomponent dense non-aqueous phase liquid (DNAPL) source zone. A
123
description of the site can be found in our previous publication (Nunez Garcia et al. 2020). In
124
short, the study area is composed of a porous, non-native sandy material emplaced along a utility
125
corridor within the native clay. A DNAPL pool is located directly below the treatment zone. Due
126
to the differences in permeability between the backfill and the surrounding clay, DNAPL
127
primarily migrated and accumulated between 4 and 5 m below ground surface (bgs). This was
128
consistent with the appearance of the grey clay, as revealed by the borehole logs, and visual
129
observations of DNAPL in the form of staining or sheening of soil cores. DNAPL was further
130
confirmed by organic vapor monitoring measurements using a photoionization detector (Fig. S1).
131
The wide range of cVOCs production processes on this site contributed to the formation of
132
a complex source zone, with major compounds previously reported as tetrachloroethene (PCE),
5
133
trichloroethene (TCE), and chloroform (Kocur et al. 2015). The distribution and concentrations
134
of the cVOCs in the source zone could have been impacted by past remedial activities as well as
135
natural attenuation. The abundance of typical daughter products from PCE (i.e., dichloroethenes
136
(DCEs) and ethene) and carbon tetrachloride (CCl4) (i.e., chloroform and dichloromethane
137
(DCM)), present in background samples (Fig. S2), supports the hypothesis that transformation of
138
parent compounds has occurred over time. The present study was conducted at the fringes of a
139
previous field trial that took place four years prior to this study, when a total of 620 L of 1 g L-1
140
CMC-nZVI was introduced into four wells (Kocur et al. 2014, 2015, 2016). A plan view of the
141
study area with the sets of wells from both studies is presented in Fig. S3. Evidence of natural
142
attenuation at the site has been previously reported and attributed to the abundance of
143
Dehalococcoides spp. (Dhc) in the background samples prior to the CMC-nZVI injection (Kocur
144
et al. 2015).
145 146
2.2. Monitoring Network
147
Eight multilevel bundle piezometers were installed, six downstream (NA1, NB1, NC1,
148
NA2, NB2, and NA4) and two upstream (NA3 and NB3) of the injection well (Figs. S3-S4). The
149
injection well consisted of a conventional 5 cm well with 0.61 m screen, advanced using hollow
150
stem augers. Bundled piezometers were made up of seven color coded ¼” teflon tubes, mounted
151
on a ¼” steel threaded rod (McMaster-Carr, USA) for stability. The stainless steel screen length
152
of each teflon tube was 0.127 m (100-mesh, McMaster-Carr, USA) and placed 0.305 m vertically
153
apart with fabric mesh pockets holding ¼” coated bentonite pellets (Canpipe, CA) in between in
154
order to target different sampling depths (Figs. S4-S5). Unless otherwise specified, each color
155
denotes the following depths (m bgs) for all wells: Black - 2.90 m, Yellow - 3.20 m, Green - 3.51
6
156
m, Clear - 3.81 m, Blue - 4.12 m, and White - 4.42 m. The Red level (4.73 m bgs) was emplaced
157
within the DNAPL pool and therefore not sampled for cVOCs analysis. Information on bundle
158
piezometers for multilevel sampling can be found in the supplementary material.
159 160
2.3. CMC-S-nZVI Synthesis and Characterization
161
Details on the synthesis procedure and characterization of the CMC-S-nZVI particles were
162
described previously (Nunez Garcia et al. 2020). Briefly, nZVI was synthesized on site by first
163
mixing ferrous sulfate heptahydrate with CMC (90K) and then reducing the mixture using
164
sodium borohydride. Aqueous-solid sulfidation was then carried out by treating the freshly-
165
synthesized CMC-nZVI with sodium dithionite to produce a suspension of 1 g L-1 CMC-S-nZVI,
166
stabilized in 0.77% weight/volume CMC and doped with 22 mM dithionite. A total of 620 L of
167
the suspension was prepared in four distinct batches, 155 L each, and introduced under gravity-
168
feed conditions via the injection well for 16 hours.
169
Transmission Electron Microscopy (TEM) coupled with Energy Dispersive X-ray
170
Spectroscopy (EDS) of CMC-S-nZVI, from synthesis barrels, confirmed the presence of two
171
different types of particles after sulfidation (Nunez Garcia et al. 2020 and Fig. S6). The first type
172
consisted of discrete spherical nZVI-like particles with an average size of ~90±13 nm and iron as
173
their major constituent. Some particles also showed the presence of oxygen and sulfur, indicating
174
the formation of a thin iron oxide/sulfide coating. The second type of particles were larger flake-
175
like structures, with an average particle size of ~505±81 nm. These were relatively fewer in
176
number and were composed of iron and sulfur, suggesting the formation of larger iron sulfide
177
particles. Dynamic light scattering (DLS) also showed a bimodal particle size distribution,
178
further confirming the presence of two types of particles (Nunez Garcia et al. 2020). The size of
7
179
smaller particles in DLS analysis ranged from 357.4 to 438.7 nm that was close to the
180
hydrodynamic diameter of unsulfidated CMC-nZVI particles. The size of larger particles ranged
181
between 881 and 1038 nm. The Fe0 content of CMC-S-nZVI suspension could not be quantified
182
by acid digestion with hydrochloric acid, possibly due to its reaction with the sulfur compounds
183
(e.g., thiosulfate) present in the suspension (Nunez Garcia et al. 2020).
184 185
2.4. Sampling and Analytical Methods
186
Groundwater samples were collected using 40 mL VOA (volatile organic analysis) glass
187
vials, leaving no headspace and preserved with 0.2 grams of sodium bisulfate (NaHSO4).
188
Background samples were collected ~28.5 hours before the injection and are referred as ‘0 day’.
189
cVOCs (PCE, CCl4, tetrachloroethanes (1,1,1,2-TeCA & 1,1,2,2-TeCA), TCE, chloroform,
190
trichloroethanes (1,1,1-TCA & 1,1,2-TCA), and 1,2-dichloroethane (1,2-DCA)) were extracted
191
by transferring 250 µL aliquot to 1 mL hexane and analyzed with a modified EPA 8021 method
192
using an Agilent 7890 Gas Chromatograph (GC) equipped with an Electron Capture Detector
193
(ECD), a DB-624 capillary column, and an autosampler. For hydrocarbons (ethane and ethene)
194
and lower chlorinated VOCs (DCEs, 1,1-DCA, vinyl chloride (VC), chloroethane, and DCM),
195
aliquots of 1 mL were transferred to 2-mL GC vials and allowed to equilibrate for a minimum of
196
one hour before manually sampling 250 µL of the headspace and injecting into the GC. Analysis
197
was carried out using a Flame Ionization Detector (FID) and a GS-Gaspro column. External
198
standards were used for preparing calibration curves for all the cVOCs and hydrocarbons.
199
For cVOCs in soil, background samples were collected during the installation of the wells
200
(25-28 days before CMC-S-nZVI injection), followed by post-injection sampling at 94 and 554
201
days. The soil cores were logged and sub-sampled at either pre-determined depths or targeted
8
202
locations considered to be highly impacted by cVOCs. Post-injection boreholes were located
203
between the locations of the monitoring wells, 0.3-0.6 meters apart, to sample along the CMC-S-
204
nZVI flow path. Bulk soil samples were collected and stored in 60-mL jars, filling the container
205
to the brim and leaving no headspace to minimize losses, in accordance with EPA Method
206
5035A. Jars were stored on ice, transported to the laboratory, and kept in a cold room at 4 °C. In
207
the laboratory, 10 g of soil sample was quickly transferred into pre-weighted vials containing 10
208
mL methanol and the vials were kept on shaker for thirty minutes for the cVOCs extraction. The
209
extractant solution was then diluted with water. Analysis of the cVOCs was performed with a
210
GC-ECD and a GC-FID, as described above.
211
Chloride was analyzed using a high-performance liquid chromatograph equipped with a
212
conductivity detector (Model 432, Waters, Milford, MA), a 4.6 × 50 cm IC-Pak Anion column
213
(#Wat007355) using a 12% water-acetonitrile eluent as mobile phase. For elemental analysis,
214
soil samples were digested using U.S. EPA Method 3051A. Digested samples, as well as total
215
iron and total boron in water, were analyzed as reported previously (Nunez Garcia et al. 2020).
216
Sulfide in monitoring well samples was measured by iodometric titration (APHA 1999).
217 218
2.5. Compound Specific Isotope Analysis
219
Background samples were collected from NB1-White and NB2-White 28.5 hours before
220
injection and preserved in 40 mL VOA vials using NaHSO4. Post-injection samples were also
221
collected from the same wells 17 days after CMC-S-nZVI injection, preserved in 1 mL
222
concentrated hydrochloric acid in 40 mL VOA vials with 5 mL headspace following the method
223
of Elsner et al. (2006). Vials were then covered with aluminum foil and frozen upside down to
224
allow for a gradual freezing process and minimize losses. Headspace sampling and analysis was
9
225
carried out using Gas Chromatograph - Combustion - Isotope Ratio Mass Spectrometer
226
(Finnigan 252 IRMS). Stable carbon isotope values are reported in the δ-notation (‰), relative to
227
the international Vienna Pee Dee Belemnite standard, as follows (Eq. 1):
‰ =
228
.
.
.
−1
.
$
$
229
where "
230
the sample and standard, respectively. All stable carbon isotope values are reported with a 0.5-‰
231
error encompassing both accuracy and reproducibility (Sherwood Lollar et al. 2007). A
232
minimum of a 1 to 2‰ difference between two δ13C values is considered significant (Hunkeler et
233
al. 2009). Background information on CSIA and details on the GC method can be found in the
234
supplementary material.
.
# .
%&'()*
and "
(1)
.
# .
%+&,-&.-
are the ratios of carbon-13 and carbon-12 in
235 236
3.
Results and Discussion
237
3.1. Fate and Transport of CMC-S-nZVI
238
Detailed results for the fate and transport of CMC-S-nZVI suspension at this site were
239
discussed previously (Nunez Garcia et al. 2020). Briefly, the suspension was quite mobile with
240
significant transport to the downgradient wells NB1-White, NC1-White, and NA4-Blue at a
241
distance of 0.86 m, 0.91 m, and 2.7 m, respectively, from the injection well (Fig. 1a-b). Notable
242
migration of the suspension was also found in NA3-White, 1.71 m upgradient from the injection
243
well. In these wells, concentrations of sulfate, sulfur, and total boron often followed a similar 10
244
trend as total iron. CMC-S-nZVI also travelled vertically up to the Black (2.90 m bgs) level of
245
NB1 and Green level (3.51 m bgs) of NB2, as was shown by significant increase in total iron and
246
total boron concentrations, predominantly during the injection period (Nunez Garcia et al. 2020
247
and Fig. 2a-b). A noticeable increase in sulfide concentrations in the monitoring wells also
248
indicated the lateral and vertical transport of the suspension (Fig. S7). TEM analysis of the
249
monitoring well samples, collected during injection and on day 3, confirmed the presence of both
250
nZVI-like particles and larger flaky structures (possibly FeSX), similar to those observed in the
251
synthesis barrels (Nunez Garcia et al. 2020). Moreover, the presence of CMC-S-nZVI
252
suspension was clearly visible from the black color of the monitoring well samples. Significant
253
amounts of total iron, total boron, and sulfide were found in most of these wells up to 17 days
254
(Figs. 1b, 2a-b, and S7) but the concentrations decreased thereafter. Suspended black particles
255
remained in the injection well for several months (>196 days) but visible particles were not
256
found in the monitoring wells during the long-term sampling events (Nunez Garcia et al. 2020).
257 258
3.2. Changes in cVOCs Concentrations Due to Physical versus Chemical Processes
259
The distribution and concentrations of cVOCs in groundwater samples could have changed
260
due to both chemical transformations as well as physical processes such as dilution and
261
displacement. Contaminant transformation can be assessed by CSIA (Elsner et al. 2010),
262
chloride ion generation, and formation of intermediates and end products while dilution can be
263
assessed by investigating changes in the concentrations of conservative species (He et al. 2010).
264 265
3.2.1. Compound Specific Isotope Analysis
11
266
Stable carbon isotope values were measured for PCE, TCE, cis-1,2-DCE, and VC for NB1-
267
White and NB2-White groundwater samples before (day 0) and after (day 17) of CMC-S-nZVI
268
injection (Table 1). These sampling locations were chosen because of their different CMC-S-
269
nZVI breakthroughs though they were roughly on the same flow path, 0.86 (NB1-White) and
270
1.78 m (NB2-White) downgradient from the injection well (Fig. S3). CMC-S-nZVI breakthrough
271
(Nunez Garcia et al. 2020) was greater at NB1-White with a maximum total iron concentration
272
of 1309 µM whereas the maximum total iron concentration detected at NB2-White was 219 µM
273
(Fig. 1b).
274
Before injection, the δ13C values for PCE were very similar (i.e., within ± 0.5 ‰) in NB1-
275
White and NB2-White, suggesting that -26.0 ‰ was a relatively homogenous initial isotope
276
signature for PCE at the site at the time of this study. Compared to NB1-White, TCE was
277
enriched in 13C (-1.2 ‰) whereas cis-1,2-DCE and VC were depleted in 13C by -2.9 and -1.2 ‰,
278
respectively, in NB2-White. These results indicate the occurrence of TCE transformation and
279
generation of cis-1,2-DCE and VC prior to CMC-S-nZVI injection, as previously reported for
280
the adjoining area (Kocur et al. 2015, 2016). These isotopic changes prior to the CMC-S-nZVI
281
injection, however, would not impact the results of the current study as the CSIA method
282
involves determination of absolute changes in isotopic composition before and after injection.
283
After injection, PCE, TCE, and cis-1,2-DCE concentrations decreased at NB1-White on
284
day 17 whereas VC remained constant (Table 1 and Fig. 1f-i). PCE concentration declined from
285
392 to 73.6 µM while its δ13C value increased from -26.0 to -24.6 ‰ (-1.4 ‰ enrichment in 13C)
286
indicating in situ transformation of PCE between days 0 and 17. For TCE, the δ13C value became
287
more depleted in
288
62.6 µM. This suggests that TCE generation from PCE transformation was likely more
13
C (-22.9 to -25.0 ‰) even though its concentration decreased from 91.9 to
12
289
significant than the TCE transformation. In addition, δ13C for TCE was more negative than that
290
for PCE on day 17 indicating incorporation of
291
transformation product of PCE. Past literature has reported that molecules containing exclusively
292
light isotopes (12C) are preferentially transformed leading to an accumulation of
293
molecules (Elsner et al. 2008, 2010). In both NB1-White and NB2-White, cis-1,2-DCE
294
concentrations decreased by approximately 50-60% while getting enriched in
295
22.8 to -20.2 ‰ in NB1-White and from -25.7 to -24.1 ‰ in NB2-White). Such enrichment
296
trends are consistent with the breaking of bonds during transformation (Lojkasek-Lima et al.
297
2012). The δ13C value for cis-1,2-DCE in NB1-White was less negative than that for PCE and
298
TCE on day 17 suggesting that cis-1,2-DCE transformation exceeded its generation as a
299
PCE/TCE transformation product. Contrary to NB1-White, the concentrations and δ13C values
300
for PCE and TCE were relatively constant at NB2-White between days 0 and 17, indicating
301
limited transformation likely due to the very limited CMC-S-nZVI breakthrough at this location.
302
In both wells, VC concentrations remained constant and VC stable carbon isotope signatures did
303
not change significantly. Overall, the CSIA results provided strong evidence for in situ
304
transformation of PCE, TCE, and cis-1,2-DCE in the well with significant CMC-S-nZVI
305
breakthrough (i.e., NB1-White) but limited transformation in the well with limited CMC-S-nZVI
306
breakthrough (i.e., NB2-White).
12
C in TCE, further pointing towards TCE as a
13
12
C in product
C (i.e., from -
307 308 309 310 311
3.2.2. Chloride Analysis The extent of cVOCs transformation is also explored through chloride analysis. Chloride ions are generated via reductive dechlorination of cVOCs (Eq. 2). /0 1 + 3 4 + 5 6 → /0 #6 + 35 + 4 8
(2)
13
312
where RCl represents a generic chlorinated aliphatic compound.
313
The background chloride concentrations in the monitoring wells were in the range of 6597
314
to 32120 µM (Fig. S8) that are much higher than the chloride concentrations (1290-7300 µM) to
315
be generated from the complete dechlorination of all cVOCs in the background samples of these
316
wells. Thus, the changes in chloride concentrations after CMC-S-nZVI injection would not be
317
able to depict a clear picture of the cVOCs dechlorination due to CMC-S-nZVI. For example, the
318
chloride concentrations, calculated based on the generation of daughter products from the
319
dechlorination of parent compounds, account for only ~12% (540 µM) and ~15% (1069 µM) of
320
the total measured chloride in the Black and Yellow levels of NB1 on day 3, respectively (Table
321
S1). The difference between the predicted and the measured chloride could be due to
322
displacement/dilution as well as generation of unmonitored/unidentified dechlorination products.
323
However, some interesting changes in chloride concentrations were observed at various NB1
324
levels that are worth mentioning. For example, higher chloride concentrations were observed at
325
the lower levels of NB1 (3.51 - 4.42 m bgs) before CMC-S-nZVI injection (Fig. 2c). The trend
326
reversed after the injection, with greater chloride concentrations detected at shallower depths (2.9
327
- 3.2 m bgs). Specifically, the concentrations at the Black and Yellow levels increased by ~4550
328
µM and ~7000 µM, respectively, on day 3. On the other hand, concentrations decreased from
329
14621 to 9594 µM at the White level. Chloride concentrations also decreased significantly for
330
Blue, Clear, and Green levels on day 3. During the injection, CMC-S-nZVI suspension first
331
reached the lower levels (White and Blue) and at greater concentrations. This might have pushed
332
the pre-existing well water vertically to the upper levels, resulting in upward displacement of
333
chloride at NB1. On day 17, chloride concentrations further decreased at White and Blue levels
334
of NB1, increased for Green, but remained constant at the uppermost levels. Along with
14
335
displacement, dilution by the CMC-S-nZVI suspension would also have contributed to these
336
changes in chloride concentrations, especially at the lower levels.
337 338
3.2.3. Depth Profiles of cVOCs and Ethene
339
Similar to chloride data, the depth profiles for cVOCs show that the concentrations of all
340
the cVOCs decreased at NB1-White on day 3 (Fig. 2d-j). However, the trend was not the same
341
for other levels. For example, the concentrations of parent compounds PCE and CCl4 decreased
342
noticeably whereas the concentrations of intermediates (e.g. cis-1,2-DCE, VC, chloroform, and
343
DCM) increased significantly at NB1-Black. This clearly indicates the occurrence of
344
dechlorination even if displacement/dilution was happening. Similarly, the increasing-decreasing
345
trend for the cVOCs was not consistent for the various NB1 levels on day 17.
346
Though significant concentrations of ethene were present in the background samples,
347
considerable changes in the ethene concentrations were noticed after the CMC-S-nZVI injection.
348
On day 3, the trend for ethene was also similar to that of the intermediates, with decreased
349
concentrations at the lower levels and increased concentrations at the upper levels of NB1 (Fig.
350
2k). In contrast to chloride data, ethene concentrations increased at all the levels, except Black,
351
from day 3 to day 17, further indicating dechlorination at NB1.
352 353
3.2.4. Boron Analysis
354
To evaluate the extent of dilution, the inorganic conservative constituent boron was
355
analyzed. Total boron at NB1-White, where chloride concentrations decreased after injection,
356
increased approximately seven-fold in comparison to total boron at the Black level (Fig. 2b). To
15
357
make this observation more quantitative, the following relationship (Eq. 3) is used (He et al.
358
2010):
359
9 = 1 −
360
where D is “dilution” factor, Ct is the total boron concentration in the groundwater sample on t =
361
3 or 17 days, and C0 is the total boron concentration in the injected suspension (37.7 mM).
362
Values approaching unity mean little to no dilution of the groundwater by the injected
363
suspension. On day 3, dilution is most noticeable at NB1-White (D = 0.87, Fig. S9a), followed
364
by NC1-White (0.92) and NA4-Blue (D = 0.93, Fig. S9b). All other wells, including upper levels
365
of NB1, had D ≥0.95 indicating lesser dilution. On day 17, D values increased or remained
366
constant for all the wells, except for NC1-White that decreased to 0.90. The presence of total
367
boron, above background concentrations, indicates that the injected suspension was still present
368
in the targeted area on day 3 and to a lesser extent on day 17. This suggests that dilution has also
369
contributed to changes in cVOCs concentrations.
(;)
=(;)
(3)
370 371
3.3. Dechlorination of cVOCs in Groundwater
372
A previous field study in the adjoining area showed significant cVOCs transformation in a
373
three-week period after CMC-nZVI injection, indicating the occurrence of short-term abiotic
374
transformation that was then followed by long-term enhanced biotic transformation (Kocur et al.
375
2015). Thus, the changes in cVOCs concentrations after CMC-S-nZVI injection are presented as
376
short- and long-term changes in the current study.
377 378
3.3.1. Short-Term Changes in Aqueous cVOCs
16
379
Significant CMC-S-nZVI transport was found at 0.86 m (NB1-White), 0.91 m (NC1-
380
White), and 2.7 m (NA4-Blue) downgradient as well as 1.71 m (NA3-White) upgradient of the
381
injection well (Fig. 1b). NB2-White, located at 1.78 m downgradient, observed limited CMC-S-
382
nZVI breakthrough. Of note is that some of these wells retained high total iron concentrations
383
even 17 days after injection. Coincident with the transport of CMC-S-nZVI and associated
384
geochemical changes (Nunez Garcia et al. 2020), considerable changes in concentrations of
385
aqueous cVOCs in these wells were observed (Figs. 1 and S10). Total iron concentrations did not
386
change much at NA2-Blue and NB3-White and the results for these wells are not discussed here.
387
NB1-White showed a noticeable decrease in all the cVOCs on day 3 (Figs. 1 and S10),
388
concurrent with the high concentration of total iron (763 µM). A simultaneous decrease in ethene
389
concentration (244 to 72.8 µM) on day 3 suggests the occurrence of dilution/displacement due to
390
CMC-S-nZVI injection. However, even when total iron concentration decreased to 96.7 µM on
391
day 17, the decrease in cVOCs (except TCE and VC) concentrations continued, indicating
392
dechlorination. Furthermore, increase in TCE concentration from 28.7 µM on day 3 to 62.6 µM
393
on day 17 had resulted from its generation as a dechlorination product of PCE, as indicated by
394
CSIA results (Section 3.2.1.). A significant increase in ethene concentration from 72.8 µM on
395
day 3 to 173 µM on day 17 further confirms dechlorination.
396
CMC-S-nZVI migrated to NA3-White during injection, with total iron concentrations
397
remaining relatively high for an extended period (i.e., 220 µM total iron on day 17). Like NB1-
398
White, NA3-White showed a noticeable decrease in almost all cVOCs concentrations on day 3
399
that continued until day 17 (Figs. 1 and S10). Although this decrease can be partly attributed to
400
dilution/displacement, increase in ethene concentration on day 17 indicates that dechlorination
17
401
also took place. There was also an increase in TCE concentration from 47.7 µM on day 3 to 57.5
402
µM on day 17 that might have generated from PCE dechlorination.
403
NA4-Blue was another well with good CMC-S-nZVI breakthrough during injection. In this
404
well, concentrations of PCE, cis-1,2-DCE, and chlorinated ethanes did not change considerably
405
on day 3 (Figs. 1 and S10). However, TCE concentration decreased from 87.8 to 37.7 µM (~50
406
µM), concurrent with a proportional increase in VC (~11 µM) and ethene (~36 µM)
407
concentrations on day 3, suggesting TCE dechlorination. A significant decrease in concentrations
408
of chlorinated methanes was also observed on day 3. In contrast to NB1-White and NA3-White,
409
the concentrations of all cVOCs rebounded on day 17 at NA4-Blue. Interestingly, the total iron
410
concentration also increased simultaneously in this well. Transport data shows that NA4-Blue is
411
connected to the injection well via preferential flow paths (Nunez Garcia et al. 2020) which
412
might have contributed to cVOCs and iron mobilization to NA4-Blue on day 17. Like NA4-Blue,
413
cVOCs and ethene concentrations at NC1-White also decreased on day 3 but the concentrations
414
rebounded on day 17 with a concurrent increase in total iron concentration.
415
Although limited CMC-S-nZVI migrated to NB2-White during injection, a significant
416
amount of total iron (219 µM) was retained in this well up to day 17. At this location, limited
417
change (<10%) in concentrations of parent compounds PCE, CCl4, and TCE was observed but
418
concentrations of lower chlorinated VOCs continued to decrease noticeably up to day 17. The
419
decrease in ethene concentration on day 3 suggests dilution/displacement, however, its increase
420
on day 17 indicates occurrence of dechlorination.
421
Proximity of the Blue and White levels (4 - 4.5 m bgs) to the DNAPL pool along with the
422
dilution/displacement effects by CMC-S-nZVI injection make it challenging to distinguish
423
between the various processes that govern the changes in cVOCs concentrations. A clearer
18
424
picture of potential dechlorination can be deduced from the changes in cVOCs concentrations at
425
the uppermost level of NB1 (Black level - 2.90 m bgs), positioned approximately 1.5 m above
426
the source zone (Fig. S11). Vertical transport of the CMC-S-nZVI suspension to this location
427
was observed by an increase in the total iron and total boron concentrations in the upper levels of
428
NB1 on day 3 (Fig. 2a-b). PCE concentration decreased from 374 to 272 µM on day 3 but did
429
not change much on day 17 (Fig. S11). Concurrently, cis-1,2-DCE and ethene increased from
430
70.6 to 169 µM and from 96.9 to 145 µM, respectively, on day 3 but decreased to 110 and 101
431
µM on day 17. It is important to note that there was no appreciable accumulation of VC, with
432
cis-1,2-DCE and ethene observed as the main dechlorination products. Similarly, the decrease in
433
CCl4 concentration (from 255 to 166 µM) was accompanied by an increase in chloroform and
434
DCM on day 3. Unlike PCE, CCl4 concentration decreased further to 124 µM on day 17.
435
Decreases in concentrations were also observed for other parent compounds (1,1,1,2-TeCA and
436
1,1,2,2-TeCA) matched by increases in daughter products (i.e., trans 1,2-DCE and 1,1-DCA).
437
As stated above, the short-term changes in cVOC concentrations were influenced
438
simultaneously by dechlorination, dilution, and displacement. Thus, due to the complexity of the
439
system, changes in cVOC concentrations would not yield a straightforward correlation with
440
changes in total iron, total boron, or sulfate (CMC-S-nZVI constituents) concentrations. For
441
example, the concentrations of intermediates (e.g., cis-1,2-DCE) increased in some wells due to
442
their generation from dechlorination of parent compounds (e.g., PCE) but concurrently decreased
443
in other wells due to their own dechlorination. In contrast, ethene would yield a more
444
straightforward correlation since it is an end product of the reductive dechlorination of
445
chlorinated ethenes present at the site. From day 0 to day 3, changes in ethene concentration
446
were negatively correlated with the changes in total iron concentration (Fig. S12a). The total iron
19
447
concentrations increased as a result of CMC-S-nZVI transport to the monitoring wells. Ethene
448
concentrations were also supposed to increase due to its generation as a dechlorination product.
449
However, the simultaneous occurrence of dilution and displacement resulted in decreased ethene
450
concentrations, especially in the lower levels of the monitoring wells. This trend was reversed at
451
the later stage (Fig. S12d). Changes in ethene concentrations from day 3 to day 17 were
452
positively correlated to changes in total iron concentrations from 0 to 3 days. These results show
453
that increase in ethene concentration was relatively much higher in wells with higher total iron
454
breakthrough, presumably due to abiotic dechlorination of cVOCs by the CMC-S-nZVI. Total
455
boron (Fig. S12b & e) and sulfate (Fig. S12c & f) followed the same trend as the total iron.
456 457
3.3.2. Long-Term Changes in Aqueous cVOCs
458
NB1-White and NB1-Black were selected for analysis of long-term dechlorination. NB1-
459
White lies just above the DNAPL pool whereas NB1-Black, the uppermost level located 1.5 m
460
above, is expected to be least affected by the source zone. Short-term monitoring indicated a
461
significant decrease in concentrations of parent compounds (PCE, CCl4, and TeCAs) at both
462
White and Black levels of NB1 (Fig. 3), which was partly due to dechlorination as discussed in
463
sections 3.2.1., 3.2.3., and 3.3.1. There was also a noticeable change in the concentrations of the
464
daughter products on day 17 at both the levels. Overall, the concentration of total cVOCs
465
decreased from 922 µM to 692 µM at NB1-Black (Fig. 3d) and from 1620 µM to 443 µM at
466
NB1-White on day 17 (Fig. 3h). However, the long-term trend was opposite at these locations.
467
For NB1-Black, the concentrations of PCE, CCl4, and TeCAs continued to decline (e.g. ~70% on
468
day 157), showing further dechlorination of these cVOCs (Fig. 3a-c). Concurrently, the
469
concentrations of daughter products (e.g., DCE isomers, chloroform, and 1,2-DCA) increased on
20
470
day 157 but then decreased noticeably for the next sampling rounds. Production of ethene
471
throughout this period confirms the occurrence of dechlorination (Fig. 3d). Total cVOCs
472
concentration decreased to as low as 245 µM at NB1-Black on day 561. In contrast, total cVOCs
473
concentration rebounded at NB1-White on day 157 and continuously increased to 2585 µM on
474
day 561 (Fig. 3h). There was a significant and continued increase in the concentrations of parent
475
compounds as well as the daughter products at this level (Fig. 3e-g). The constant generation of
476
ethene indicates dechlorination (Fig. 3h) although continued dissolution of the DNAPL pool
477
below seems to be the dominant process. Similar trends were observed for long-term cVOCs
478
data at NB2 where a continuous decrease in cVOC concentrations was observed at NB2-Black
479
but cVOCs concentrations at NB2-White increased with time (Fig. S13).
480
Lack of visible black particles and noticeable decrease in total iron and sulfide
481
concentrations in the monitoring well samples, during the long-term sampling events, indicated
482
the absence of injected CMC-S-nZVI suspension. This suggests that CMC-S-nZVI did not play a
483
direct role in the long-term dechlorination of cVOCs. Previous field studies have also shown that
484
abiotic dechlorination (caused by the initial ZVI corrosion) diminishes during long-term
485
monitoring, while biotic dechlorination becomes the primary degradation pathway (He et al.
486
2010, Kocur et al. 2015, 2016). The injected CMC-S-nZVI might have created favorable
487
conditions for the long-term biotransformation of cVOCs, as reported earlier for a CMC-nZVI
488
injection study (Kocur et al. 2016). Moreover, excess dithionite in the injected suspension would
489
also have indirectly contributed to the long-term dechlorination of cVOCs. Dithionite employed
490
in the in situ redox manipulation (ISRM) technology successfully reduces native Fe(III) from
491
aquifer sediments/soils to reactive Fe(II) species, resulting in the transformation of chlorinated
492
organic compounds (Boparai et al. 2006, Szecsody et al. 2004). It even maintains the subsurface
21
493
conditions favorable for reductive degradation up to >3 years (Fruchter et al. 2000). As the soil
494
in the current study area is rich in iron (Fig. S14), the excess dithionite in the suspension is
495
expected to have enriched the subsurface zone with the reactive Fe(II) species, resulting in the
496
abiotic transformation of cVOCs.
497 498
3.4. Possible Reaction Mechanisms
499
It is challenging to determine if changes in cVOCs concentrations were due to abiotic or
500
biotic transformation. While the CSIA results for NB1-White confirmed the chemical
501
transformation of chlorinated ethenes, distinguishing between biotic and abiotic (i.e., via CMC-
502
S-nZVI) processes typically requires comparison of the isotope signatures of the dechlorination
503
products cis-1,2-DCE, VC, acetylene, ethene, and ethane (Elsner et al. 2008). Ethene and ethane
504
were not analyzed by CSIA. Acetylene, which may serve as an indicator for abiotic
505
dechlorination (Butler and Hayes 1999, Elsner et al. 2010), was not detected. The rapid and
506
efficient removal of cVOCs within 17 days suggests that dechlorination was mainly abiotic
507
during this short-term period. A past field study in the adjoining area also showed noticeable
508
reduction of cVOCs within three weeks after CMC-nZVI injection, indicating the occurrence of
509
short-term abiotic dechlorination (Kocur et al. 2015). As the injected CMC-S-nZVI suspension
510
contained excess dithionite, it might have resulted in some short-term abiotic dechlorination.
511
Moreover, the reactive Fe(II) species generated via ISRM might also have contributed to both
512
short- as well as long-term abiotic dechlorination. However, biotransformation is expected to be
513
the major contributor for long-term dechlorination, as reported earlier for the CMC-nZVI
514
injection study (Kocur et al. 2016).
22
515
For short-term dechlorination, CSIA results confirm the generation of TCE as a product of
516
PCE transformation in NB1-White (Table 1). Other wells (e.g. NB1-Black) also showed a
517
temporary increase in the concentrations of intermediates cis-1,2-DCE and VC with concurrent
518
dechlorination of PCE. This indicates hydrogenolysis as the dechlorination mechanism for
519
chlorinated ethenes. However, PCE dechlorination generally exceeded the generation of
520
intermediates and ethene. Similarly, dechlorination of cis-1,2-DCE (e.g. NB1-White and NB2-
521
White) exceeded the formation of VC and ethene. These results suggest that reductive β-
522
elimination was also happening simultaneously. Past research has reported both reductive β-
523
elimination and hydrogenolysis as the dechlorination mechanisms for TCE, treated by S-nZVI,
524
where ethene or acetylene were found as the major dechlorination products (Han and Yan 2016,
525
Rajajayavel and Ghoshal 2015). Experimental conditions, particularly the method of nZVI
526
sulfidation, determine which mechanism would dominate. For example, Han and Yan (2016)
527
reported ethene as the major product, with ethane and acetylene as the minor products, while
528
treating TCE with S-nZVI developed by post-synthesis addition of dithionite (method similar to
529
the one used in this study). In the current study, no acetylene was detected and chloroacetylenes
530
were not analyzed but this does not completely rule out their formation. The quantification of
531
acetylene and chloroacetylenes is challenging in the field as they can quickly volatilize in air.
532
This may be the reason that reductive β-elimination products are rarely reported for the iron-
533
treated field studies. For chlorinated methanes, the formation of chloroform and DCM indicates
534
the transformation of CT via sequential hydrogenolysis, as also reported by Jin et al. (2018).
535
For long-term dechlorination, the formation of intermediates (e.g., DCE isomers,
536
chloroform, and DCM) at NB1-Black and NB2-Black indicate hydrogenolysis as the
537
dechlorination pathway. Significant decrease in cis-1,2-DCE concentrations without equivalent
23
538
production of VC suggest that reductive β-elimination was also happening. Microbial
539
transformation of higher chlorinated ethanes and ethenes often results in partial dechlorination,
540
leading to the accumulation of intermediates such as DCE isomers and VC (He et al. 2010,
541
Kocur et al. 2016). The accumulation of VC, a highly toxic and confirmed human carcinogen
542
(ATSDR 2006), is usually of particular concern due to its poor biodegradability. Past study in the
543
adjacent area reported the generation and accumulation of VC during long-term microbial
544
transformation of PCE and TCE following a CMC-nZVI injection (Kocur et al. 2015, 2016).
545
However, one of the most positive outcomes of this CMC-S-nZVI field treatment is the non-
546
accumulation of lower chlorinated VOCs, particularly VC. CMC-S-nZVI (dithionite sulfidated)
547
injection would result in decreased H2 evolution, formation of FeSs, and significant reduction of
548
native Fe(III) to reactive Fe(II) species whereas CMC-nZVI injection would generate higher
549
amounts of H2 and may not significantly impact the latter two conditions. Thus, there can be two
550
possible reasons for the non-accumulation of VC in this CMC-S-nZVI field study as opposed to
551
the CMC-nZVI field trial. Firstly, differences in geochemical changes, along with the direct
552
interactions between nZVI/S-nZVI and microbes, are expected to result in different
553
inhibitory/stimulatory effects on the microbial communities for the two treatments. Certain
554
classes of bacteria have the ability to intrinsically biodegrade VC in anaerobic aquifers (Bradley
555
et al. 1998, Lorah and Voytek 2004). Although not yet investigated, the geochemical conditions
556
in the subsurface created by CMC-S-nZVI injection might be favorable for the enrichment of
557
these bacteria. Secondly, reactive Fe(II) species from dithionite-reduced sediments would
558
dechlorinate chlorinated ethenes via reductive β-elimination without noticeable production of
559
VC, as reported for TCE (Szecsody et al. 2004).
560
24
561
3.5. Changes in Soil cVOCs
562
Visual observations in the form of staining/sheening of soil cores as well as OVM
563
measurements (Fig. S1) indicated an appreciable amount of cVOCs present as DNAPL and
564
sorbed mass. Soil cVOCs concentrations are considered as a better metric for determining
565
contaminant mass reduction in comparison to aqueous-phase concentrations (Henn and Waddill
566
2006). Thus, changes in soil cVOCs were quantified by analyzing the soil samples collected
567
before and after CMC-S-nZVI injection. Locations for pre- and post-injection soil cores are
568
shown in Fig. S15. In Table S2, the summarized data shows a significant decrease in
569
concentrations of most of the cVOCs in soil samples collected on 94 and 554 days after CMC-S-
570
nZVI injection, with some of them not even detected at many locations. Fig. S16 shows a
571
continuous decline in the total cVOCs concentrations where the background average of 1496
572
µmol/kg decreased to 653 and 125 µmol/kg, respectively, on day 94 and 554 after CMC-S-nZVI
573
injection.
574
Table S2 and Fig. S16 also show that soil cVOCs concentrations were highly variable. For
575
example, PCE concentrations varied between 35.5 and 1759 µmol/kg for the three zones on day
576
94. Thus, the results are also presented as ‘box and whisker’ plots by grouping the data for each
577
sampling event (Fig. 4). Median concentrations of PCE and CCl4 showed some increase on day
578
94 but noticeably decreased on day 554. For all the other cVOCs, except 1,1,2-TCA, there was a
579
continuous downward trend with time. For example, DCM median concentrations decreased
580
from 278 to 8.62 µmol/kg on day 94 and further decreased to 1.55 µmol/kg on day 554. Median
581
concentrations for 1,1,2-TCA remained relatively constant throughout the monitoring period.
582
This shows that the trends among the ten cVOCs analyzed were not always consistent.
583
Quantification of the extent of remediation using soil cores is challenging, in part due to spatial
25
584
variations and highly stratified distribution of contaminants within aquifers. This complexity is
585
exacerbated by the varying sampling depths for different locations and sampling times, not
586
allowing for a systematic depth-by-depth comparison. A correlation analysis, depicted in Table
587
S3, was performed with the purpose of evaluating the overall effectiveness of the CMC-S-nZVI
588
injection on altering the cVOCs concentrations in soil. The ‘r’ values indicate that the cVOCs
589
concentrations correlate better with each other over time, suggesting the treatment was effective
590
in causing a change in the concentrations and distribution of contaminants in the soil. This long-
591
term decrease in soil cVOCs might have occurred partly due to enhanced biological activity after
592
CMC-S-nZVI injection. However, more work needs to be done to investigate the effect of this
593
CMC-S-nZVI formulation on the microbial communities in the treatment zone. Dithionite-
594
reduced structural Fe(II) in the aquifer sediments/soil might also have played an important role in
595
the long-term transformation of soil cVOCs (Paul et al. 2003). These results suggest CMC-S-
596
nZVI is an effective strategy for cVOCs dechlorination in soil.
597 598
4.
Conclusions
599
Results reported herein demonstrate the suitability of CMC-S-nZVI as an effective
600
technology for soil and groundwater remediation at existing contaminated sites. A rapid decrease
601
in cVOCs concentrations was observed in groundwater samples immediately after injection,
602
followed by sustained long-term dechlorination. Although CMC-S-nZVI injection resulted in
603
some dilution and displacement of cVOCs, the changes in intermediate concentrations and an
604
increase in ethene concentrations clearly indicate dechlorination. CSIA serves as another line of
605
evidence, confirming the direct impact of chemical transformation as shown by the changes in
606
stable isotope values of key chlorinated compounds. Proximity to the DNAPL pool resulted in
26
607
mass transfer of non-aqueous constituents into the aqueous phase at the deeper Blue and White
608
levels (4-4.5 m bgs), although, significant ethene generation indicated concurrent dechlorination.
609
In contrast, the uppermost level (Black), which is expected to be least affected by the source
610
zone, observed a continuous decline in cVOCs concentrations accompanied with the generation
611
of ethene, confirming dechlorination. Transformation was not limited to the aqueous phase as
612
concentrations of soil cVOCs also decreased significantly at 94 and 554 days after injection.
613
Presence of dithionite might additionally have resulted in reducing the native Fe(III) to the
614
reactive Fe(II) species which can degrade cVOCs.
615
Long-term success of in situ emplacement of nZVI often relies on the biotransformation
616
that follows the short-term abiotic dechlorination (Kocur et al. 2016) and care must be taken not
617
to inhibit the growth of healthy microbial communities. In this study, the sustained long-term
618
dechlorination points towards biotransformation suggesting that growth of microbial
619
communities was not inhibited. However, the extent to which biotic processes contributed to the
620
transformation of cVOCs is unknown and further characterization of the microbial communities
621
after emplacement of CMC-S-nZVI is required.
622
As fundamental work about synthesis, characterization, and overall mechanisms of CMC-
623
S-nZVI reactivity is ongoing, this study is the first pilot test to upscale the application of
624
abiotically sulfidated CMC-nZVI from laboratory to field. With the growing interest from all
625
sectors of the remediation community, as evidenced by the introduction of new commercial
626
products of sulfidated (n)ZVI (REGENESIS 2018), S-nZVI is likely to become an important In
627
Situ Chemical Reduction technology.
628 629
Acknowledgements
27
630
Financial support for this project was provided by CH2M Canada Limited, Dow Chemical, the
631
Natural Sciences and Engineering Research Council of Canada (NSERC) Remediation
632
Education Network (RENEW) Program, the NSERC Industrial Postgraduate Scholarship to Ariel
633
Nunez Garcia, a NSERC Collaborative Research and Development (CRD) Grant (CRDPJ
634
530665 - 18) and NSERC Discovery Grant to Barbara Sherwood Lollar. The authors thank Ka
635
Yee Lam and Georges Lacrampe-Couloume for help with the stable isotope analyses.
636 637
References
638 639 640
Agency for Toxic Substances and Disease Registry (ATSDR). 2006. Toxicological profile for Vinyl Chloride. Atlanta, GA: U.S. Department of Health and Human Services, Public Health Service.
641 642 643
American Public Health Association (APHA). 1999. Standard Methods for the Examination of Water and Wastewater, 20th ed., American Public Health Association, American Water Works Association and Water Environment Federation, Washington DC, pp. 845-860.
644 645 646
Benner, S.G., Blowes, D.W., Ptacek, C.J., Mayer, K.U., 2002. Rates of sulfate reduction and metal sulfide precipitation in a permeable reactive barrier. Appl. Geochem. 17 (3), 301320.
647 648 649
Boparai, H.K., Shea, P.J., Comfort, S.D., Snow, D.D., 2006. Dechlorinating chloroacetanilide herbicides by dithionite-treated aquifer sediment and surface soil. Environ. Sci. Technol. 40 (9), 3043-3049.
650 651 652
Bradley, P.M., Chapelle, F.H., Wilson, J.T., 1998. Field and laboratory evidence for intrinsic biodegradation of vinyl chloride contamination in a Fe(III)-reducing aquifer. J. Contam. Hydrol. 31 (1-2), 111-127.
653 654
Butler, E.C., Hayes, K.F., 1999. Kinetics of the transformation of trichloroethylene and tetrachloroethylene by iron sulfide. Environ. Sci. Technol. 33 (12), 2021-2027.
655 656
Butler, E.C., Hayes, K.F., 2000. Kinetics of the transformation of halogenated aliphatic compounds by iron sulfide. Environ. Sci. Technol. 34 (3), 422-429.
657 658 659
Cao, Z., Liu, X., Xu, J., Zhang, J., Yang, Y., Zhou, J.L., Xu, X.H., Lowry, G.V., 2017. Removal of Antibiotic Florfenicol by Sulfide-Modified Nanoscale Zero-Valent Iron. Environ. Sci. Technol. 51 (19), 11269-11277.
660 661 662
Cumbal, L.H., Debut, A., Delgado, D.A., Jurado, C.B., Stael, C., 2015. Synthesis of Multicomponent Nanoparticles for Immobilization of Heavy Metals in Aqueous Phase. NanoWorld J. 1 (4), 103-109.
28
663 664 665 666
Elsner, M., Chartrand, M., VanStone, N., Lacrampe Couloume, G., Sherwood Lollar, B., 2008. Identifying Abiotic Chlorinated Ethene Degradation: Characteristic Isotope Patterns in Reaction Products with Nanoscale Zero-Valent Iron. Environ. Sci. Technol. 42 (16), 5963-5970.
667 668 669
Elsner, M., Couloume, G.L., Mancini, S., Burns, L., Sherwood Lollar, B., 2010. Carbon Isotope Analysis to Evaluate Nanoscale Fe(O) Treatment at a Chlorohydrocarbon Contaminated Site. Ground Water Monit. Remediat. 30 (3), 79-95.
670 671 672
Elsner, M., Couloume, G.L., Sherwood Lollar, B., 2006. Freezing to preserve groundwater samples and improve headspace quantification limits of water-soluble organic contaminants for carbon isotope analysis. Anal. Chem. 78 (21), 7528-7534.
673 674 675 676
Fan, D., Lan, Y., Tratnyek, P.G., Johnson, R.L., Filip, J., O’Carroll, D.M., Nunez Garcia, A., Agrawal, A., 2017. Sulfidation of Iron-Based Materials: A Review of Processes and Implications for Water Treatment and Remediation. Environ. Sci. Technol. 51 (22), 13070-13085.
677 678 679
Fan, D., O’Brien Johnson, G., Tratnyek, P.G., Johnson, R.L., 2016. Sulfidation of Nano Zerovalent Iron (nZVI) for Improved Selectivity During In-Situ Chemical Reduction (ISCR). Environ. Sci. Technol. 50 (17), 9558-9565.
680 681 682
Fang, Y., Wen, J., Zeng, G., Shen, M., Cao, W., Gong, J., Zhang, Y., 2018. From nZVI to SNCs: development of a better material for pollutant removal in water. Environ. Sci. Pollut. Res. 25 (7), 6175-6195.
683 684 685 686
Fruchter, J.S., Cole, C.R., Williams, M.D., Vermeul, V.R., Amonette, J.E., Szecsody, J.E., Istok, J.D., Humphrey, M.D., 2000. Creation of a subsurface permeable treatment zone for aqueous chromate contamination using in situ redox manipulation. Ground Water Monit. Remediat. 20 (2), 66-77.
687 688
Gong, Y., Tang, J., Zhao, D., 2016. Application of iron sulfide particles for groundwater and soil remediation: A review. Water Res. 89, 309-320.
689 690 691
Han, Y., Yan, W., 2016. Reductive Dechlorination of Trichloroethene by Zero-valent Iron Nanoparticles: Reactivity Enhancement through Sulfidation Treatment. Environ. Sci. Technol. 50 (23), 12992-13001.
692 693 694
He, F., Zhao, D., Paul, C., 2010. Field assessment of carboxymethyl cellulose stabilized iron nanoparticles for in situ destruction of chlorinated solvents in source zones. Water Res. 44 (7), 2360-2370.
695 696 697
He, Y.T., Wilson, J.T., Wilkin, R.T., 2008. Transformation of reactive iron minerals in a permeable reactive barrier (biowall) used to treat TCE in groundwater. Environ. Sci. Technol. 42 (17), 6690-6696.
698 699
Henn, K.W., Waddill, D.W., 2006. Utilization of nanoscale zero-valent iron for source remediation—A case study. Remediat. J. 16 (2), 57-77.
700 701 702
Hunkeler, D., Meckenstock, R.U., Sherwood Lollar, B., Schmidt, T.C., Wilson, J.T., 2009. A Guide for Assessing Biodegradation and Source Identification of Organic Ground Water Contaminants Using Compound Specific Isotope Analysis (CSIA), pp. 1 - 82, U.S. EPA.
29
703 704
Jin, X., Chen, H., Yang, Q., Hu, Y.A., Yang, Z.L., 2018. Dechlorination of Carbon Tetrachloride by Sulfide-Modified Nanoscale Zerovalent Iron. Environ. Eng. Sci. 35 (6), 560-567.
705 706 707
Kennedy, L.G., Everett, J.W., Becvar, E., Defeo, D., 2006a. Field-scale demonstration of induced biogeochemical reductive dechlorination at Dover Air Force Base, Dover, Delaware. J. Contam. Hydrol. 88 (1-2), 119-136.
708 709 710
Kennedy, L.G., Everett, J.W., Gonzales, J., 2006b. Assessment of biogeochemical natural attenuation and treatment of chlorinated solvents, Altus Air Force Base, Altus, Oklahoma. J. Contam. Hydrol. 83 (3-4), 221-236.
711 712 713
Kocur, C.M., Chowdhury, A.I., Sakulchaicharoen, N., Boparai, H.K., Weber, K.P., Sharma, P., Krol, M.M., Austrins, L., Peace, C., Sleep, B.E., O'Carroll, D.M., 2014. Characterization of nZVI Mobility in a Field Scale Test. Environ. Sci. Technol. 48 (5), 2862-2869.
714 715 716 717
Kocur, C.M.D., Lomheim, L., Boparai, H.K., Chowdhury, A.I.A., Weber, K.P., Austrins, L.M., Edwards, E.A., Sleep, B.E., O'Carroll, D.M., 2015. Contributions of Abiotic and Biotic Dechlorination Following Carboxymethyl Cellulose Stabilized Nanoscale Zero Valent Iron Injection. Environ. Sci. Technol. 49 (14), 8648-8656.
718 719 720 721
Kocur, C.M.D., Lomheim, L., Molenda, O., Weber, K.P., Austrins, L.M., Sleep, B.E., Boparai, H.K., Edwards, E.A., O'Carroll, D.M., 2016. Long-Term Field Study of Microbial Community and Dechlorinating Activity Following Carboxymethyl Cellulose-Stabilized Nanoscale Zero-Valent Iron Injection. Environ. Sci. Technol. 50 (14), 7658-7670.
722 723
Li, D., Mao, Z., Zhong, Y., Huang, W., Wu, Y., Peng, P.a., 2016. Reductive transformation of tetrabromobisphenol A by sulfidated nano zerovalent iron. Water Res. 103, 1-9.
724 725 726
Li, J., Zhang, X., Sun, Y., Liang, L., Pan, B., Zhang, W., Guan, X., 2017. Advances in Sulfidation of Zerovalent Iron for Water Decontamination. Environ. Sci. Technol. 51 (23), 13533–13544.
727 728 729 730
Lojkasek-Lima, P., Aravena, R., Shouakar-Stash, O., Frape, S.K., Marchesi, M., Fiorenza, S., Vogan, J., 2012. Evaluating TCE Abiotic and Biotic Degradation Pathways in a Permeable Reactive Barrier Using Compound Specific Isotope Analysis. Ground Water Monit. Remediat. 32 (4), 53-62.
731 732 733 734
Lorah, M.M., Voytek, M.A., 2004. Degradation of 1,1,2,2-tetrachloroethane and accumulation of vinyl chloride in wetland sediment microcosms and in situ porewater: biogeochemical controls and associations with microbial communities. J. Contam. Hydrol. 70 (1), 117145.
735 736 737
Lv, D., Zhou, J., Cao, Z., Xu, J., Liu, Y., Li, Y., Yang, K., Lou, Z., Lou, L., Xu, X. 2019. Mechanism and influence factors of chromium(VI) removal by sulfide-modified nanoscale zerovalent iron. Chemosphere 224, 306-315.
738 739 740
Nunez Garcia, A., Boparai, H.K., de Boer, C.V., Chowdhury, A.I.A., Kocur, C.M.D., Austrins, L.M., Herrera, J., O'Carroll, D.M., 2020. Fate and Transport of Sulfidated Nano Zerovalent Iron (S-nZVI): A Field Study. Water Res 170, 115319.
741 742 743
Nunez Garcia, A., Boparai, H.K., O’Carroll, D.M., 2016. Enhanced Dechlorination of 1,2Dichloroethane by Coupled Nano Iron-Dithionite Treatment. Environ. Sci. Technol. 50 (10), 5243-5251. 30
744 745 746 747
Paul, C.J., Khan, F.A., Puls, R.W., 2003. In Situ Reduction of Chromium-Contaminated Groundwater, Soils, and Sediments by Sodium Dithionite. Chapter 16, Handbook of Groundwater Remediation using Permeable Reactive Barriers. Naftz, D.L., Morrison, S.J., Fuller, C.C., Davis, J.A. (eds), pp. 465-493, Academic Press, San Diego.
748 749 750
Phillips, D.H., Gu, B., Watson, D.B., Roh, Y., Liang, L., Lee, S.Y., 2000. Performance evaluation of a zerovalent iron reactive barrier: Mineralogical characteristics. Environ. Sci. Technol. 34 (19), 4169-4176.
751 752 753
Puls, R.W., Paul, C.J., Powell, R.M., 1999. The application of in situ permeable reactive (zerovalent iron) barrier technology for the remediation of chromate-contaminated groundwater: a field test. Appl. Geochem. 14 (8), 989-1000.
754 755 756
Qian, L., Chen, Y., Ouyang, D., Zhang, W., Han, L., Yan, J., Kvapil, P., Chen, M., 2020. Field demonstration of enhanced removal of chlorinated solvents in groundwater using biochar-supported nanoscale zero-valent iron. Sci. Total Environ. 698, 134215.
757 758
Rajajayavel, S.R.C., Ghoshal, S., 2015. Enhanced reductive dechlorination of trichloroethylene by sulfidated nanoscale zerovalent iron. Water Res. 78, 144-153.
759 760
REGENESIS, 2018. AquaZVI Specification Sheet. https://regenesis.com/wpcontent/uploads/2018/04/AquaZVI_SpecSheet-8-1.pdf (November 19, 2018).
761 762 763
Shen, H., Wilson, J.T., 2007. Trichloroethylene removal from groundwater in flow-through columns simulating a permeable reactive barrier constructed with plant mulch. Environ. Sci. Technol. 41 (11), 4077-4083.
764 765 766 767
Sherwood Lollar, B., Hirschorn, S.K., Chartrand, M.M.G., Lacrampe-Couloume, G., 2007. An Approach for Assessing Total Instrumental Uncertainty in Compound-Specific Carbon Isotope Analysis: Implications for Environmental Remediation Studies. Anal. Chem. 79 (9), 3469-3475.
768 769 770
Sheu, Y.T., Lien, P.J., Chen, K.F., Ou, J.H., Kao, C.M., 2016. Application of NZVI-contained emulsified substrate to bioremediate PCE-contaminated groundwater – A pilot-scale study. Chem. Eng. J. 304, 714-727.
771 772 773
Song, S., Su, Y., Adeleye, A.S., Zhang, Y., Zhou, X., 2017. Optimal design and characterization of sulfide-modified nanoscale zerovalent iron for diclofenac removal. Appl. Catal. B Environ. 201, 211-220.
774 775
Stefaniuk, M., Oleszczuk, P., Ok, Y.S., 2016. Review on nano zerovalent iron (nZVI): From synthesis to environmental applications. Chem. Eng. J. 287, 618-632.
776 777 778
Szecsody, J.E., Fruchter, J.S., Williams, M.D., Vermeul, V.R., Sklarew, D., 2004. In situ chemical reduction of aquifer sediments: Enhancement of reactive iron phases and TCE dechlorination. Environ. Sci. Technol. 38 (17), 4656-4663.
779 780 781
Wilkin, R.T., Puls, R.W., Sewell, G.W., 2003. Long-term performance of permeable reactive barriers using zero-valent iron: Geochemical and microbiological effects. Ground Water 41 (4), 493-503.
782 783 784
Zhao, L., Zhao, Y., Yang, B., Teng, H. 2019. Application of Carboxymethyl Cellulose– Stabilized Sulfidated Nano Zerovalent Iron for Removal of Cr(VI) in Simulated Groundwater. Water, Air, & Soil Pollution 230(6), 113. 31
Table 1. δ13C values for chlorinated ethenes from NB1-White and NB2-White (0.86 and 1.78 m downgradient of the injection well, respectively) before (0 days) and after (17 days) CMC-SnZVI injection.
Location
Time (days)
PCE
TCE
cis-1,2-DCE
VC
[µM]
δ13C (‰)
[µM]
δ13C (‰)
[µM]
δ13C (‰)
[µM]
δ13C (‰)
0
392
-26.0
91.9
-22.9
252
-22.8
39.3
-23.0
17
73.6
-24.6
62.6
-25.0
99.8
-20.2
39.2
-22.0
0
394
-26.3
121
-21.7
461
-25.7
29.1
-24.2
17
416
-26.1
125
-22.6
217
-24.1
33.3
-25.0
NB1-White
NB2-White
Distance (m)
0.8
a) Plan View Interval range: 4 - 4.5 m bgs
500
North
Conc. (µM)
1.0 0.6
NA3-White
0.4 NB1-White
0.2 NA4-Blue
0.0 -0.2 2.8
1500 Conc. (µM)
1200
NB2-White
NC1-White
2.1
0.7 0.0 Distance (m)
1.4
-1.4
17 d
200 100 NA3-W 200
b) Total iron
NB1-W
NC1-W
NB2-W
NA4-B
NB1-W
NC1-W
NB2-W
NA4-B
NB1-W
NC1-W
NB2-W
NA4-B
NB1-W
NC1-W
NB2-W
NA4-B
NB1-W
NC1-W
NB2-W
NA4-B
g) TCE
150 100
600
50
300
0 NA3-W
Conc. (µM)
3d
300
-2.1
0 NB1-W
NC1-W
NB2-W
NA4-B
NA3-W 500
c) CCl4
400
300
h) cis-1,2-DCE
300
200
200 100
100
0
0 NA3-W
300 Conc. (µM)
1d
0 -0.7
900
400
400
0d
f) PCE
NB1-W
NC1-W
NB2-W
NA4-B
NA3-W 50
d) Chloroform
40
200
i) VC
30 20
100
10 0
0 NA3-W
Conc. (µM)
100
NB1-W
NC1-W
NB2-W
NA4-B
NA3-W 400
e) DCM
75
300
50
200
25
100
j) Ethene
0
0 NA3-W
NB1-W
NC1-W
NB2-W
NA4-B
NA3-W
Fig. 1. Short - term changes in cVOC concentrations at five locations representing upstream and downstream conditions. a) Plan View is shown for reference and only relevant wells are presented. The origin (0, 0) represents the location of the injection well. b) Total iron concentrations are shown for the same sampling times, including the peak concentrations measured during active injection (0 – 16 hours).
Depth (m bgs)
2.8
b)
2.8
3.0
3.0
3.2
3.2
3.2
3.4
3.4
3.4
3.6
3.6
3.6
3.8
3.8
3.8
4.0
4.0
4.0
4.2
4.2
4.2
4.4
4.4
4.4
0 150 300 450 600 750 Total iron (µM)
d)
0 2.8
c)
Black (2.90 m)
Green (3.51 m) Clear (3.81 m) Blue (4.12 m) White (4.42 m)
2000 4000 6000 0 Total boron (µM) 2.8
5000 10000 15000 Chloride (µM)
e)
f)
2.8
3.0
3.0
3.0
3.2
3.2
3.2
3.2
3.4
3.4
3.4
3.4
3.6
3.6
3.6
3.6
3.8
3.8
3.8
3.8
4.0
4.0
4.0
4.0
4.2
4.2
4.2
4.2
4.4
4.4
4.4
4.4
150 300 PCE (µM)
2.8
450
h)
0
2.8
25 50 75 100 125 0 TCE (µM) 2.8
i)
3.0
3.0
3.2
3.2
3.2
3.2
3.4
3.4
3.4
3.4
3.6
3.6
3.6
3.6
3.8
3.8
3.8
3.8
4.0
4.0
4.0
4.0
4.2
4.2
4.2
4.2
4.4
4.4
4.4
4.4
300
0
50 100 Chloroform (µM)
150
0
10
20 30 40 VC (µM)
j)
3.0
100 200 CCl4 (µM)
g)
100 200 300 400 0 cis-1,2-DCE (µM) 2.8
3.0
0
0d 3d 17 d
Yellow (3.20 m)
3.0
0
Depth (m bgs)
2.8
3.0
2.8
Depth (m bgs)
a)
20 40 DCM (µM)
60
0
50
k)
100 200 Ethene (µM)
Fig. 2. Depth profiles for a) total iron, b) total boron, c) chloride, d-j) cVOCs, and k) ethene at NB1.
300
NB1- Black 500
e) 1000
400 300
100
200 0 0
3
17 157 247 365 561 TeCAs 1,1,1-TCA 1,1,2-TCA 1,2-DCA trans-1,2-DCE/1,1-DCA
b)
125 100
Conc. (µM)
Conc. (µM)
600 400
0
75 50 25 0
300
0
3
17 157 247 365 561
c)
250
900 800 700 600 500 400 300 200 100 0
1000
CCl4 Chloroform DCM
0
3
17 157 247 365 561
3
17 157 247 365 561
3
17 157 247 365 561
f)
0
g) Conc. (µM)
350 Conc. (µM)
800
200
150
NB1-White
1200
PCE TCE cis-1,2-DCE VC
a)
Conc. (µM)
Conc. (µM)
600
200 150
800 600 400
100 200
50
0
0 Total cVOCs Ethane Ethene
200
1000 800 600
100
400
50
200 0 0
3
17 157 247 365 561 Time (days)
0
3000
h)
150
0
1000
2500
800
2000
600
1500 400
1000
200
500
0
0 0
3
17 157 247 365 561 Time (days)
Fig. 3. Background and long - term post-injection concentrations for a – d) NB1-Black and e – h) NB1-White.
Total cVOCs (µM)
d)
17 157 247 365 561
Ethane/Ethene (µM)
3
Total cVOCs (µM)
Ethane/Ethene (µM)
250
0
Conc. (µmol/kg)
10000
1000
a) PCE
100
100
100
10
10
10
1
1
1
i) 1,1,2,2-TeCA
1
0 Background
1000 Conc. (µmol/kg)
1000
g) 1,1,1,2-TeCA
100
0 94 days
94 days
554 days
10000
Background 1000
b) TCE
e) Chloroform
100
0
0 Background
554 days
100
10
94 days
Background
554 days 1000
h) 1,1,1-TCA
100
100
10
10
1
1
94 days
554 days
j) 1,1,2-TCA
1 1 0
0 Background
94 days
0
0 Background
554 days
94 days
1000
1000 Conc. (µmol/kg)
1000
d) CCl4
554 days
Background
94 days
554 days
Background
94 days
554 days
f) DCM
c) cis-1,2-DCE 100
100 10 10
1 0
1 Background
94 days
554 days
Background
94 days
554 days
Fig. 4. cVOCs concentrations in soil for background and post-injection (94 and 554 days) samples collected between 2.5 and 4.5 m bgs. The box-and-whisker plot shows the median ( ), the interquartile range (box), and the extrema (whiskers). Dash lines are straight connectors between the medians.
Highlights •
CMC-S-nZVI was applied for the first time at a site contaminated with a mixture of cVOCs.
•
Compound specific isotope analysis (CSIA) confirmed the transformation of aqueous cVOCs.
•
Unlike nZVI, there was no accumulation of lower cVOCs, particularly VC, in the longterm degradation.
•
CMC-S-nZVI treatment resulted in significant reduction of sorbed phase cVOCs.
Declaration of interests ☒ The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper. ☐The authors declare the following financial interests/personal relationships which may be considered as potential competing interests: