Liu Willow
Yang
a,
Chenhui
Liu
*ab and
Tao
Yang
*a
aState Key Laboratory for Mineral Deposits Research, School of Earth Sciences and Engineering, Nanjing University, Nanjing 210093, P. R. China. E-mail: cliu@nju.edu.cn; yangtao@nju.edu.cn
bKey Laboratory of Marine Mineral Resources, Ministry of Land and Resources, Guangzhou 510075, P. R. China
First published on 2nd October 2019
Anion exchange membranes (AEMs) are adept at extracting sulfate for sulfur isotope analyses by multiple-collector inductively coupled plasma mass spectrometry (MC-ICP-MS) from natural samples typically with low sulfate concentrations. But up to now, their capability for sulfate extraction is still lacking adequate research. In this study, a series of detailed tests on AEMs for sulfate extraction were developed, which included the tolerance of pH, the effect of competitive anions, and the lowest concentration limit of sulfate uploading. The optimal scope of pH for sulfate exchange is from 3 to 11. Approximately over 90% of sulfate recoveries and reliable sulfur isotope analyses can be achieved when the concentrations of nitrate, chloride, phosphate, carbonate, and bicarbonate are limited in 0.5 mmol per L per cm2 of a piece of AEM. In practice, we suggest that the applicable concentrations are able to increase to 10 times, except for phosphate. The lowest uploading concentration of sulfate that can be adsorbed by the AEM without sulfur isotope fractionation is further detected as 0.5 μmol L−1 though the recovery of sulfate decreases when its concentration is lower than 0.01 mmol L−1. This research offers insight into realizing accurate and precise sulfur isotope analyses for natural freshwater and marine pore water by MC-ICP-MS.
An ion exchange membrane is a polymer or copolymer modified by ionic groups, which can be used for collecting and condensing the ion of interest from sample solutions.18 Comparing with the ion exchange resin traditionally used for chemical purification,2,4,19–24 the ion exchange membrane performs better at low concentration but high sample volume.8,25 Anion exchange membranes (AEMs) were widely applied in field and laboratory sample treatments, and particularly in extracting phosphorus compounds (organic and condensed inorganic phosphorus) from soil-water, rainwater, river, and sediments.26–30 Kwon et al.25 firstly used AEM for soil sulfate collection and found that the existence of competitive anions (e.g., nitrate and chloride) only lowered the sulfate absorption on the resin membranes but almost did not produce sulfur isotope fractionation (< 1‰). Afterward, Hanousek et al.8 developed a more detailed test on matrix separation of AEM and chose MC-ICP-MS for direct analyses of sulfur isotopes in rainwater and soil solutions, which were often low in sulfate concentrations (down to 0.04 mmol L−1) but ample for sample amount. They indicated that some common cations including calcium, potassium, sodium, and lithium could be quantitatively removed during the sulfate exchange, but nitrate and chloride ions would compete with sulfate and decrease its recovery. However, these studies have placed more weight on highlighting the necessity of matrix separation for reliable sulfur isotope analyses rather than evaluating the extent to which change in concentrations of competitive ions could impact on sulfate extraction. Meanwhile, the lowest uploading concentration of sulfate that can be adsorbed by AEM without sulfur isotope fractionation is still not determined.
To solve these two questions, we performed a detailed investigation to evaluate the sulfate extraction capability of AEM in this study. First, the pH tolerance of AEM was determined to provide an optimal pH scope for the subsequent tests. As the common anions accompanied with sulfate in nature, nitrate, chloride, phosphate, carbonate, and bicarbonate were chosen to determine the influence of their competitiveness on sulfate absorption. Afterward, the pure sulfate solution was diluted to detect the lowest concentration limit of sulfate uploading. During these tests, the changes in sulfur isotopic compositions before and after the sulfate extraction were measured by MC-ICP-MS. Finally, two geological applications about sulfur isotope analyses of natural freshwater and marine pore water by MC-ICP-MS were further provided.
(a) A series of 0.3 mmol L−1 sulfate solutions were prepared for pH controlling tests with different pH values ranging from ca. 1.2 to 12.5. High-purity nitric acid and ammonium hydroxide (NH3·H2O) were added to adjust pH values. The pH values were verified by a pH meter (Sartorius PB-10, Germany) after being corrected using a series of standard solutions (pH = 4.00, 7.00, and 10.01).
(b) Six groups of samples were prepared by adding competitive ions, nitrate (NO3−), chloride (Cl−) (Chinese national standard solutions GSB 04-1772-2004 and GSB 04-1770-2004, respectively; 1000 μg mL−1), phosphate (PO43−), carbonate (CO32−), and bicarbonate (HCO3−) (dissolved from analytical reagent solid powders with CAS no. 25447-33-0, 506-87-6, and 1066-33-7, respectively) into 0.3 mmol L−1 sulfate solutions. These anions were added separately in the first five groups at the concentrations of 0.15, 0.3, 1.5, 3, 15, 30, 150, and 300 mmol L−1. In the last group, each solution contained both nitrate and chloride but halved in their concentrations. Afterward, the concentration of sulfate was changed with the sequential addition of nitrate as the competitive ion. These solutions contained 0.03, 0.06, 0.15, 0.3, 0.6, and 1.5 mmol L−1 of sulfate, respectively. For each concentration of sulfate, nitrate was introduced to obtain a constant array of atomic ratio (including 0.4, 1, 2, 4, and 10) of nitrate/sulfate. All prepared solutions were adjusted to neutral by adding ammonium hydroxide, which corresponded to the optimal pH range concluded from the controlling tests (see Section 3.1 below).
(c) Six pure sulfate solutions with decreasing sulfate concentrations (including 0.3, 0.05, 0.01, 0.005, 0.001, and 0.0005 mmol L−1) were made to detect the lowest concentration of sulfate uploading.
Several natural freshwater and seawater samples were also applied to validate the sulfate extraction effects. The natural freshwater samples with low levels of sulfate (roughly below 2 mmol L−1) were collected from the Lake Taihu, China and the surface runoff of Aksu region, Xinjiang, China, respectively (see Table 6 below). These samples were further diluted to sulfate concentration of ca. 0.3 mmol L−1 before AEM treatments. In addition, to simulate the marine pore water with different concentrations of sulfate and chloride, the Atlantic Seawater (OSIL, salinity = 35.0 ± 0.2%) was diluted 100, 200, 500, and 1000 times, respectively.
Sulfate sulfur concentrations before and after extraction procedures were determined using an Element XR single-collector inductively coupled plasma mass spectrometer (Thermo Scientific, Bremen, Germany) with the configuration and operating parameters listed in Table 1. A sequence of standard solutions with sulfate sulfur concentrations of 1, 10, 20, 50, and 100 μg kg−1 (GSB 04-1773-2004(b); 1000 μg mL−1) were diluted to construct the standard curve in linear calibration, which had a correlation coefficient greater than 0.9999 and the relative standard deviation lower than 5%. All measured solutions contained 10 μg kg−1 Rh as the internal normalization reference. The recovery of sulfate was calculated by dividing the concentrations of sulfate before and after extraction procedures.
Mass spectrometer setup | ||
ICP-MS | Thermo Scientific Element XR | Thermo Scientific Neptune Plus |
Cooling gas flow rate | ca. 15 L min−1, argon | ca. 15 L min−1, argon |
Auxiliary gas flow rate | ca. 1.25 L min−1, argon | ca. 1.1 L min−1, argon |
Sample gas flow rate | ca. 1.05 L min−1, argon | ca. 0.95 L min−1, argon |
Extraction lens | ca. −2000 V | ca. −2000 V |
Interface cones | Ni cones | Ni cones |
Analyzer pressure | ca. 10−9 torr | ca. 10−9 torr |
RF forward power | ca. 1175 W | ca. 1200 W |
RF reflect power | ca. 5 W | ca. 2 W |
Data acquisition parameters | ||
Mass resolution mode | Medium resolution (m/Δm > 2500) | Medium resolution (m/Δm ≈ 3500) |
Acquisition mode | Static | Static |
Detection system | Analog | Faraday cups |
Cup configuration | 32S | 32S (C), 33S (H2), 34S (H3) |
Signal analysis protocol | 3 runs and 4 passes | 4.194 s integration per cycle, 40 cycles per block, 1 block |
Wash-out time | ca. 200 s | ca. 200 s |
A Neptune Plus multiple-collector inductively coupled plasma mass spectrometer (Thermo Scientific, Bremen, Germany) was used for sulfur isotope ratio measurement. The signals of sulfur isotopes were acquired on the interference-free plateau in medium-to-high mass resolution mode to eliminate the isobaric interferences from oxygen species (e.g., 16O2+). Standard-sample bracketing (SSB) method was applied to determine the sulfur isotopic composition of the recovered solution after extraction procedures. More detailed parameters of apparatus and operation were illustrated in Table 1. The ammonium sulfate (ibid) at the same sulfur concentration was chosen as the working standard and the sulfur isotope deviation of the recovered solution relative to the standard was defined as:
Δ34S (‰) = (Rsam/Rstd − 1) × 1000 | (1) |
δ34S (‰ VCDT) = Δ34S + δ34Sstd | (2) |
pH | Recoverya/% | Δ 34Sb/‰ |
---|---|---|
a All uploading sample solutions have 0.3 mmol L−1 of sulfate. The volumes of uploading and eluting solutions are both 10 mL. b The calculated internal uncertainties are given as 2SE. n.d. = not detected. | ||
1.17 | 2.0 | n.d. |
2.09 | 79.8 | +0.02 ± 0.04 |
3.05 | 99.5 | −0.11 ± 0.05 |
4.01 | 99.5 | −0.10 ± 0.05 |
5.51 | 100.0 | −0.05 ± 0.05 |
8.51 | 99.8 | +0.12 ± 0.06 |
9.23 | 99.8 | +0.03 ± 0.06 |
10.36 | 97.6 | +0.12 ± 0.05 |
11.20 | 91.6 | +0.02 ± 0.04 |
11.98 | 92.2 | +0.07 ± 0.05 |
12.48 | 94.9 | −0.05 ± 0.04 |
Competitive anion/mmol L−1 | Recoverya/% | Δ 34Sb/‰ | ||||
---|---|---|---|---|---|---|
NO3− | Cl− | PO42− | CO32− | HCO3− | ||
a All uploading sample solutions have 0.3 mmol L−1 of sulfate. The volumes of uploading and eluting solutions are both 10 mL. b The calculated internal uncertainties are given as 2SE. n.d. = not detected. | ||||||
0.15 | 97.3 | +0.03 ± 0.04 | ||||
0.3 | 98.5 | +0.08 ± 0.05 | ||||
1.5 | 98.8 | −0.09 ± 0.04 | ||||
3 | 98.0 | +0.04 ± 0.04 | ||||
15 | 46.9 | +0.02 ± 0.04 | ||||
30 | 11.6 | n.d. | ||||
150 | 0.0 | n.d. | ||||
300 | 0.0 | n.d. | ||||
0.15 | 100.4 | −0.04 ± 0.05 | ||||
0.3 | 99.1 | −0.04 ± 0.05 | ||||
1.5 | 99.9 | −0.01 ± 0.05 | ||||
3 | 95.5 | −0.09 ± 0.04 | ||||
15 | 76.4 | +0.09 ± 0.03 | ||||
30 | 48.3 | +0.03 ± 0.04 | ||||
150 | 10 | n.d. | ||||
300 | 0.0 | n.d. | ||||
0.15 | 89.6 | +0.06 ± 0.07 | ||||
0.3 | 92.4 | +0.03 ± 0.09 | ||||
1.5 | 85.0 | −0.05 ± 0.07 | ||||
3 | 94.6 | −0.12 ± 0.08 | ||||
15 | 73.3 | −0.68 ± 0.08 | ||||
30 | 52.0 | −0.90 ± 0.08 | ||||
150 | 20.0 | n.d. | ||||
300 | 13.3 | n.d. | ||||
0.15 | 98.6 | +0.10 ± 0.07 | ||||
0.3 | 98.0 | +0.02 ± 0.09 | ||||
1.5 | 93.7 | +0.11 ± 0.07 | ||||
3 | 89.6 | +0.08 ± 0.07 | ||||
15 | 61.1 | −0.01 ± 0.09 | ||||
30 | 40.6 | −0.07 ± 0.12 | ||||
150 | 2.6 | n.d. | ||||
300 | 0.0 | n.d. | ||||
0.15 | 100.4 | +0.12 ± 0.09 | ||||
0.3 | 98.6 | −0.13 ± 0.08 | ||||
1.5 | 96.8 | +0.08 ± 0.06 | ||||
3 | 95.9 | −0.10 ± 0.08 | ||||
15 | 90.7 | +0.00 ± 0.09 | ||||
30 | 71.7 | +0.03 ± 0.09 | ||||
150 | 11.1 | n.d. | ||||
300 | 0.0 | n.d. | ||||
0.075 | 0.075 | 97.7 | +0.06 ± 0.04 | |||
0.15 | 0.15 | 97.9 | +0.06 ± 0.04 | |||
0.75 | 0.75 | 96.4 | +0.05 ± 0.04 | |||
1.5 | 1.5 | 98.6 | −0.02 ± 0.05 | |||
7.5 | 7.5 | 55.3 | +0.06 ± 0.04 | |||
15 | 15 | 25.2 | n.d. | |||
75 | 75 | 0.5 | n.d. | |||
150 | 150 | 0.0 | n.d. |
Maximum sulfate recoveries (approximately > 90%) are achieved within the concentration threshold of 3 mmol L−1 for every competitive anion (i.e., 0.5 mmol per L per cm2 of AEM piece), except that the threshold of bicarbonate can extend to 15 mmol L−1. When the anion concentration exceeds this threshold, despite only partial sulfate is exchanged by AEM, there exists negligible Δ34S values (avg. 0.02 ± 0.10‰ (2SD)) as indistinguishable as those of high sulfate recoveries (avg. 0.01 ± 0.15‰ (2SD)) (Table 3 and Fig. 2B). The only exceptions are phosphate-bearing samples. Over 0.6‰ of Δ34S values are observed at the phosphate concentration higher than 15 mmol L−1. Low recoveries of sulfate denote that some phosphate ion can simultaneously be absorbed in the membranes and then be eluted together with sulfate. As a result, such obvious sulfur isotope fractionation could be associated with matrix effects from phosphorus. Thus, for the sulfate sample with nitrate, chloride, carbonate, or bicarbonate, the reliable sulfur isotopic composition can be acquired as long as a sufficient amount of sulfate for measurement (5 μg g−1 of sulfur at least) is recovered. But for the phosphate-bearing sample, equally convincing sulfur isotope measurement is only obtained as its concentration stays within 3 mmol L−1. In practice, the applicable concentrations of these competitive anions can extend to 5 mmol per L per cm2 of AEM piece except for phosphate which should be limited to 0.5 mmol per L per cm2 of AEM piece.
Nitrate is further taken as the competitive ion to evaluate the exchange capacity of AEM. Table 4 shows the recovery and isotopic results tested from six groups of sample solutions, which have different sulfate concentrations but a constant array of the atomic ratio between nitrate and sulfate. When the concentration of sulfate is no more than 0.6 mmol L−1, most data points of the sulfate recovery gather around 90% and the difference among them cannot be clearly identified except for those at the nitrate/sulfate ratio of 10 (Fig. 3A). A distinct decrease in the sulfate recovery with the ratio of nitrate to sulfate is observed at 1.5 mmol L−1 of sulfate. In addition, samples with a sufficient amount of sulfate available for Δ34S analyses (avg. 0.01 ± 0.13‰ (2SD)) verify no detectable sulfur isotope fractionation during extraction procedures (Fig. 3B). When replacing the nitrate/sulfate ratio with the anion equivalent concentration (i.e., the sum of nitrate concentration and two times of sulfate concentration) and still retaining the sulfate recovery as the Y-axis, we find that the data points show a decreasing trend following the same linear function (Fig. 3C). The operating exchange capacity can be defined as the maximum moles of exchanged anions per unit area of AEM piece at the maximum sulfate recovery,33 which is calculated from the anion equivalent concentration (=2.88 mmol L−1) at which the fitting line extends upward to 90% of sulfate recovery. According to this, the operating exchange capacity of the AEM used here is of 4.8 μmol cm−2 (=2.88 mmol L−1 × 10 mL/6 cm2). Conversely, the anion equivalent concentration at the lower intercept of the fitting line at the zero recovery of sulfate represents the total exchange capacity,34 whose value is 38.7 μmol cm−2 (= 23.23 mmol L−1 × 10 mL/6 cm2).
Atomic NO3−/SO42− | NO3−/mmol L−1 | Recoverya/% | Δ 34Sb/‰ |
---|---|---|---|
a The volumes of uploading and eluting solutions are both 10 mL. b The calculated internal uncertainties are given as 2SE. n.d. = not detected. | |||
0.03 mmol L−1 of SO 4 2− | |||
0.4 | 0.012 | 93.3 | n.d. |
1 | 0.03 | 92.4 | n.d. |
2 | 0.06 | 89.1 | n.d. |
4 | 0.12 | 92.8 | n.d. |
10 | 0.3 | 98.3 | n.d. |
0.06 mmol L−1 of SO 4 2− | |||
0.4 | 0.024 | 97.7 | n.d. |
1 | 0.06 | 93.7 | n.d. |
2 | 0.12 | 95.1 | n.d. |
4 | 0.24 | 93.0 | n.d. |
10 | 0.6 | 96.1 | n.d. |
0.15 mmol L−1 of SO 4 2− | |||
0.4 | 0.06 | 95.3 | +0.14 ± 0.06 |
1 | 0.15 | 87.5 | −0.02 ± 0.06 |
2 | 0.3 | 94.4 | +0.04 ± 0.05 |
4 | 0.6 | 91.8 | −0.01 ± 0.07 |
10 | 1.5 | 93.3 | −0.03 ± 0.06 |
0.3 mmol L−1 of SO 4 2− | |||
0.4 | 0.12 | 99.8 | −0.02 ± 0.07 |
1 | 0.3 | 86.9 | −0.06 ± 0.07 |
2 | 0.6 | 93.8 | +0.00 ± 0.06 |
4 | 1.2 | 91.9 | +0.07 ± 0.05 |
10 | 3 | 88.0 | +0.06 ± 0.06 |
0.6 mmol L−1 of SO 4 2− | |||
0.4 | 0.24 | 96.8 | +0.05 ± 0.05 |
1 | 0.6 | 87.4 | +0.03 ± 0.06 |
2 | 1.2 | 89.2 | +0.02 ± 0.06 |
4 | 2.4 | 85.2 | +0.06 ± 0.07 |
10 | 6 | 81.4 | +0.05 ± 0.06 |
1.5 mmol L−1 of SO 4 2− | |||
0.4 | 0.6 | 86.4 | +0.03 ± 0.06 |
1 | 1.5 | 84.6 | −0.06 ± 0.07 |
2 | 3 | 74.3 | −0.03 ± 0.08 |
4 | 6 | 56.8 | −0.16 ± 0.05 |
10 | 15 | 22.7 | n.d. |
Conventionally, collecting and condensing sulfate is performed by column chromatography.2,4,19,24,44 However, for the samples in large volume with low sulfate concentration, this method becomes helpless and powerless.8,25 From our AEM tests above (see Section 3.3), the uploading concentration of sulfate can lower down to 0.5 μmol L−1 and there is negligible sulfur isotope fractionation during extraction procedures. Such concentration value is of the same magnitude as the minimum concentration of the freshwater sulfate. Meanwhile, the amount of competitive anions in natural freshwater samples (e.g., the concentrations of nitrate and chloride normally range from 0.03 to 6300 and 0.13 to 3500 μmol L−1, respectively37–43) would not have a greater impact on the sulfate recovery (see Section 3.2). Therefore, the AEM can provide an effective tool to extract sulfate from natural freshwater for accurate and precise δ34S analysis by MC-ICP-MS.
Three water samples from lake and surface runoff were taken as real applications here. These samples contain only trace amounts of sulfate (≤ 2 mmol L−1). As the major competitive anions, the concentrations of chloride and nitrate are lower than 2.5 mmol L−1 and 0.2 mmol L−1, respectively. In this case, the influence of their competitiveness on sulfate absorption can be ruled out. As shown in Table 6, over 95% of sulfate is extracted after AEM treatment and thus the reliable and accurate δ34S values can be obtained.
Sample IDa | SO42−/mmol L−1 | Cl−/mmol L−1 | NO3−/mmol L−1 | Recovery/% | δ 34Sb/‰ VCDT |
---|---|---|---|---|---|
a Samples S1 and S2 are from the Lake Taihu, China. Sample S3 is from the surface runoff of Aksu region, Xinjiang, China. b The calculated internal uncertainties are given as 2SE. | |||||
S1 | 1.92 | 2.23 | 0.01 | 100.0 | +1.75 ± 0.07 |
S2 | 2.02 | 2.08 | 0.06 | 101.7 | +1.57 ± 0.07 |
S3 | 1.05 | 1.24 | 0.19 | 96.5 | +9.06 ± 0.09 |
Considering that pore water samples have almost the same matrix ions (principally sodium) as seawater while the sulfate concentrations vary with depth, Bian et al.6 proposed a convenient method to determine δ34S values of sulfate in pore water by combining matrix-matching with concentration-matching by MC-ICP-MS. This method requires a 100-times dilution of pore water samples beforehand. In this case, the pore water sample initially containing 5 mmol L−1 of sulfate will be diluted to 0.05 mmol L−1. However, replicate δ34S analyses of 0.05 mmol L−1 of sulfate by MC-ICP-MS may generate a considerable uncertainty.7 This denotes that Bian et al.'s method falls ill with very low sulfate concentrations (< 5 mmol L−1) which may be relative to the process of AOM.
The diluted Atlantic seawater was applied to simulate the samples of marine pore water. For all samples diluted from 100 to 1000 times, the recoveries of sulfate maintain a high level of over 94% and those sulfur isotopic compositions show no difference from the mean δ34S value of seawater (ca. +21.0‰ VCDT55) (Table 7). Within this range of dilution factors, the concentration of sulfate is as low as 0.03 mmol L−1 and the concentration of competitive chloride is generally not higher than 6 mmol L−1 (i.e., 1 mmol per L per cm2 of AEM piece). Based on our AEM tests about the effect of anion competition (see Section 3.2), it will not bring a considerable influence on sulfate recovery. Thus, for the AOM-related pore water samples, the prior extraction of sulfate using AEM is highly recommended for accurate and precise δ34S analysis by MC-ICP-MS.
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