Introduction

Nitrate (NO3 ) contamination of freshwater (such as surface and groundwater) is considered one of the most prevalent global environmental problems and is responsible for freshwater ecosystem deterioration on a worldwide scale (Ding et al. 2014; Mallin et al. 2006; Rabalais 2002; Smith 2003; Xue et al. 2010). In many developed regions of the world, nitrate levels in surface and groundwater have risen substantially because of crop and human N fixation; the latter includes synthetic fertilizer production for agriculture and the incidental generation of N-bearing compounds via the combustion of fossil fuels (Boumans et al. 2004; Burgin and Hamilton 2007; Liu et al. 2013; Michalski et al. 2004; Thorburn et al. 2003; Xue et al. 2010). High levels of nitrate can threaten the health of humans, livestock, and freshwater ecosystems. For instance, ingested nitrates can cause methemoglobinemia (namely the commonly known cyanosis or blue baby syndrome) in infants by the conversion of nitrate to nitrites in their guts causing the decrease of the oxygen-carrying capacity of hemoglobin (Camargo and Alonso 2006; Camargo et al. 2005; Fukada et al. 2003; Liu et al. 2006). In addition, ingestion of nitrate-contaminated water may increase the likelihood of stomach cancer because of the formation of nitrosamines, which are one of the most notorious carcinogens in mammals (Camargo et al. 2005; Panno et al. 2006; Xing and Liu 2011). As a result, a limit of 10 mg NO3 –N L−1 for drinking water has been set by the World Health Organization (WHO) (Xue et al. 2009). Furthermore, elevated concentrations of nitrate can stimulate eutrophication and hypoxia in freshwater ecosystems adversely affecting aquatic species (Camargo and Alonso 2006; Lenihan and Peterson 1998; Liu et al. 2013). In response to these problems, the identification of nitrate sources and implementation of appropriate actions are imperative. However, understanding the sources of nitrate in freshwater ecosystems is a challenging task because nitrate can be derived from multiple sources, such as synthetic fertilizer (Bateman and Kelly 2007; Di and Cameron 2002), manure (Choi et al. 2003, 2007; Wassenaar 1995), sewage (Aravena et al. 1993; Li et al. 2007; Widory et al. 2005), atmospheric deposition (Pardo et al. 2004; Russell et al. 1998; Williard et al. 2001; Zhang et al. 2008), and microbial nitrification processes (Mayer et al. 2001, 2002). Traditionally, identification of nitrate sources can be achieved by investigation of the nitrate concentration in conjunction with discharge data, land use, and the hydrological character of contaminated regions (Chang et al. 2002; Xing and Liu 2011). However, these do not supply accurate and detailed information about nitrate sources. Because of the distinct isotopic characteristics of nitrogen and oxygen in the main sources of nitrate, stable isotopic compositions of nitrate can provide helpful information and are considered a powerful tool to track the source of nitrate in freshwater ecosystems (Deutsch et al. 2006; Li et al. 2010; Xue et al. 2010). Kohl et al. (1971) first introduced nitrogen isotopes to estimate the contribution of fertilizer to the nitrate in the Sangamon River (Illinois, USA), which laid the groundwork for the application of stable isotopes to distinguish the sources of nitrate contamination in freshwater ecosystems. During the last two decades, the dual stable isotope analysis technique, which combines the analysis of δ15N–NO3 and δ18O–NO3 , has drawn substantial attention and has been widely used to track sources of nitrate in freshwater ecosystems (Ahmed et al. 2012a, b; Minet et al. 2011). Currently, two principal analytical techniques are used for the determination of δ15N–NO3 and δ18O–NO3 : the denitrification method (Casciotti et al. 2002; McIlvin and Altabet 2005; Sigman et al. 2001) and the ion-exchange method (Chang et al. 1999, 2002; Minet et al. 2011; Silva et al. 2000). The characteristics of the different methods are presented in Table 1. The denitrification method, which allows the determination of both δ15N and δ18O in nitrous oxide (N2O) resulted from nitrate by chemical (McIlvin and Altabet 2005) or by bacterial method (Casciotti et al. 2002; Rock and Ellert 2007; Sigman et al. 2001), have two disadvantages: (1) The nitrite (NO2 ) presented in water samples would overestimate or underestimate the isotopic composition and (2) the results require mathematical treatments to correct for oxygen exchange and fractionation (Minet et al. 2011; Xue et al. 2009). The ion-exchange method, which allows the determination of both δ15N and δ18O simultaneously in silver or potassium nitrate by an extraction and conversion procedure that involves physical and chemical reactions, has several advantages: (1) the ability to store samples on columns in the field and thereby not need to ship water samples; (2) the ability to preserve samples without hazardous chemicals; (3) the lower start-up cost as compared to the bacterial method; and (4) the lack of the need to continuously propagate the bacteria for the denitrification method (Ahmed et al. 2012b; Silva et al. 2000). For these reasons, the ion-exchange method has been successfully used to track nitrate transformations and sources in freshwater ecosystems such as those in surface water (Battaglin et al. 2001; Chang et al. 1999; Chen et al. 2014; Deutsch et al. 2006; Fukada et al. 2003; Lee et al. 2008; Li et al. 2010; Liang et al. 2013; Liu et al. 2006; Minet et al. 2011; Panno et al. 2006; Xue et al. 2010; Zhang et al. 2014) and in groundwater (Aravena and Robertson 1998; Fukada et al. 2003; Liu et al. 2014; Yuan et al. 2012; Zhang et al. 2014) (Table 2). However, the ion-exchange method designed by Chang et al. (1999) and Silva et al. (2000) still has some disadvantages: It is labor-intensive, time-consuming, and expensive and has thus been modified and improved accordingly.

Table 1 Characteristics of different methods for the determination of δ15N–NO3 and δ18O–NO3
Table 2 Case studies of the use of ion-exchange method for nitrogen and oxygen isotope analysis of nitrate from freshwater ecosystems

In the present article, the principles of the ion-exchange method are first introduced. Factors affecting the ion-exchange method and the corresponding significant improvements are reviewed, and the best procedure now available is concluded. Finally, potential improvements and perspectives for the applicability of this method are also discussed, with suggestions for further research and development drawn from the overall conclusions.

Principles of the ion-exchange method

The ion-exchange method, which can be used to extract nitrate from freshwater for the simultaneous determination of δ15N and δ18O, was first designed by Chang et al. (1999) and Silva et al. (2000) and has been modified accordingly during the past decade (Ahmed et al. 2012b; Chen et al. 2010; Fukada et al. 2003; Huber et al. 2012; Minet et al. 2011; Xing and Liu 2011). As shown in Fig. 1, this method is mainly composed of six steps: sampling and pretreatment, extraction, elution, neutralization, removal of interfering ions, and drying and stable isotope analysis. Since anion-exchange resin with chloride form presents relatively high affinity for nitrate, nitrate can be extracted by passing the water samples through columns prefilled with anion-exchange resin. In this way, nitrate is extracted from water and retained onto resins. After the extraction step, the NO3 can be eluted from the anion-exchange resin by dripping of chloride solutions, such as hydrochloric acid (HCl) and potassium chloride (KCl) solutions. With this approach, the NO3 can be recovered from the anion-exchange resin (Silva et al. 2000). Nitric acid (HNO3) and HCl coexist in the nitrate-bearing eluant from the anion-exchange resin column (Eq. 1) (Ahmed et al. 2012a, b). Because HNO3 is volatile and isotopic fractionation will occur under low-pH conditions, it must be neutralized as soon as possible before the drying process (Ahmed et al. 2012b; Böhlke et al. 2003; Silva et al. 2000). To prevent the loss of nitrate, the eluant can be neutralized by silver oxide (Ag2O) (Eq. 2) or combination of Ag2O and potassium hydroxide, and the nitrate was presented as AgNO3 or KNO3, respectively. To obtain solid AgNO3 salts, the solution obtained after neutralization can be freeze-dried or oven-dried (Fukada et al. 2003; Silva et al. 2000; Xue et al. 2009). Freeze-drying, which can be achieved by putting solutions overnight in a freezer or in liquid nitrogen as soon as possible, is the usual choice for the AgNO3-drying process. To obtain solid KNO3 salts, neutralized solution consisting of KNO3 and KCl was evaporated till complete dryness on a hot plate. The dried salt mix was mixed with activated graphite and finally ground (Ahmed et al. 2012a, b; Aly et al. 2010). In this way, the nitrate is extracted from the water and converted into solid AgNO3 or KNO3 salts, which are subsequently processed for stable isotope analysis by combustion or pyrolyzation method.

Fig. 1
figure 1

Flow diagram depicting the procedure for the ion-exchange method (adapted from Chang et al. 1999)

$$ {\mathrm{R}}^{+} + {{\mathrm{NO}}_3}^{-} + 2\mathrm{H}\mathrm{C}\mathrm{l}\ \to\ {\mathrm{HNO}}_3 + \mathrm{H}\mathrm{C}\mathrm{l} + \mathrm{R}\mathrm{C}\mathrm{l} $$
(1)
$$ \mathrm{H}\mathrm{C}\mathrm{l} + {\mathrm{H}\mathrm{NO}}_3 + {\mathrm{Ag}}_2\mathrm{O}\ \to\ \mathrm{AgCl} + {\mathrm{Ag}\mathrm{NO}}_3 + {\mathrm{H}}_2\mathrm{O} $$
(2)

As to the combustion method for nitrogen isotopic analysis, AgNO3 is transferred to silver capsules and then combusted in a combustion reactor, which is maintained at a high temperature (Li et al. 2010). The resulting nitrogen gas (N2) produced in the oxidation reactor is introduced into an isotope ratio mass spectrometer (IRMS) for δ15N analysis (Fukada et al. 2003; Li et al. 2010; Xing and Liu 2011). For the prepared solid KNO3 samples, a modified catalyst-free technique was used by Aly et al. (2010), who used activated graphite as the reducing agent. The prepared KNO3 samples were mixed with activated graphite, loaded onto a precombusted pyrex glass tubes, combusted at 550 °C for 30 min, and cooled for 2 h. In this way, the KNO3 samples were completely decomposed and the liberated N2 gas was available for nitrogen isotopic analysis by IRMS. As to the combustion method for oxygen isotopic analysis, AgNO3 is combusted with silver cyanide (AgCN) or graphite and converted into CO2 according to Eq. 3 and Eq. 4; the produced CO2 is subsequently cryogenically separated from N2 and analyzed for δ18O by IRMS (Ahmed et al. 2012b; Fukada et al. 2003; Silva et al. 2000; Wassenaar 1995). Compared to AgCN, graphite is a better carbon source because it does not necessitate the disposal of hazardous chemicals. For the prepared solid KNO3 samples, a modified catalyst-free technique was used by Ahmed et al. (2012b). The dried solid KNO3 salt is firstly mixed with activated graphite, and then, the mixture is put into a 20 cm length and 6 mm (optical density (OD)) Pyrex glass tubes which need to be precombusted. After this step, the combustion tubes are evacuated, torch-sealed, combusted, and cooled (Ahmed et al. 2012b). In this way, the KNO3 samples were completely decomposed and the liberated CO2 gas was available for oxygen isotopic analysis by IRMS.

With the development of analysis technique, determination of δ15N and δ18O values simultaneously can also be achieved by pyrolyzation method which uses thermal decomposition without adding oxygen (Deutsch et al. 2006; Kornexl et al. 1999; Li et al. 2010; Minet et al. 2011; Xue et al. 2009). The prepared AgNO3 samples are pyrolyzed in a molybdenum-lined, aluminum oxide reduction tube (filled with glassy carbon and topped with a glassy carbon crucible) which is maintained at a high temperature (1400 °C), and the produced N2 and CO can be separated from by a 1 m gas chromatography (GC) column and analyzed via IRMS for δ15N and δ18O (Xue et al. 2009). In addition, oxygen stable analysis can be also achieved individually although the N2 produced during pyrolysis can trail into the CO sample peak, which makes analyses of δ18O in nitrogen-containing materials, such as nitrates and caffeine, difficult. To eliminate the N2 interference in the CO sample peak, two methods can be adopted. First, CO and the undesirable N2 produced by pyrolysis can be separated by a GC column packed with 5-Å molecular sieves (Li et al. 2010; Minet et al. 2011). In addition, an independent CO-trapping technique can be used and the interfering N2 gas can be prevented from entering the IRMS by diverting to a vent (Qi et al. 2011). Subsequently, the trapped CO is released by means of heat and then diverted to the IRMS for δ18O analysis (Qi et al. 2011).

$$ 2{\mathrm{Ag}\mathrm{NO}}_{3\left(\mathrm{s}\right)}+3{\mathrm{Ag}\mathrm{CN}}_{\left(\mathrm{s}\right)}\to\ 5{\mathrm{Ag}}_{\left(\mathrm{s}\right)}+2.5{\mathrm{N}}_{2\left(\mathrm{g}\right)}+3{\mathrm{CO}}_{2\left(\mathrm{g}\right)} $$
(3)
$$ 2{\mathrm{Ag}\mathrm{NO}}_{3\left(\mathrm{s}\right)}+3{\mathrm{C}}_{\left(\mathrm{s}\right)}\to\ 2{\mathrm{Ag}}_{\left(\mathrm{s}\right)} + {\mathrm{N}}_{2\left(\mathrm{g}\right)}+3{\mathrm{C}\mathrm{O}}_{2\left(\mathrm{g}\right)} $$
(4)

Affecting factors and improvement of the ion-exchange method

Type of anion-exchange resins

The adsorption efficiency of nitrate depends on the type of anion-exchange resin used; different resins differ in their ion-exchange capacities. As evident in Table 3, five different types of anion-exchange resins have been investigated. Among these, the most popular resin is AG1-X8 (Cl form, 200–400 mesh), which exhibits excellent adsorption capacity for nitrate (Fukada et al. 2003; Silva et al. 2000). In addition, the ionic form is also an important factor affecting the adsorption efficiency. The resin in the Cl form has a higher adsorption efficiency than the resin in the OH form (Chen et al. 2010). The adsorption efficiency for anion-exchange resins in the Cl form vary between 97 and 99 %, whereas the adsorption efficiency is less than 90 % for the resin in the OH form under the same experimental conditions (Ahmed et al. 2012b; Chen et al. 2010).

Table 3 Types of anion-exchange resins used in the ion-exchange method

Ratio of the height to the diameter of the resin bed

The height-to-diameter (H/D) ratio of the resin bed in the exchange column is also a major factor affecting the adsorption efficiency of nitrate. Researchers have two types of anion-exchange columns at their disposal: prefilled and lab-made columns. Prefilled exchange resin columns can be purchased from suppliers and are convenient; however, they are relatively expensive. To reduce costs, the resin and column can be purchased separately and the anion-exchange resin column can be constructed according to the field requirements. In addition to the type of anion-exchange resin employed, the H/D ratio of the resin bed is also a key factor for the adsorption of nitrate. As suggested from Table 4, the adsorption efficiency increases with increasing H/D ratio of the resin bed because a higher ratio leads to a longer retention time and more frequent contact between the nitrate and the resin (Ahmed et al. 2012b; Chen et al. 2010; Xing and Liu 2011). The use of the same type of exchange resin column is impractical because the nitrate concentration in freshwater varies from place to place. Therefore, if a detailed relationship between the H/D ratio in the resin bed and the nitrate concentration can be established, then a suitable exchange resin column can be selected for different samples. In this way, the efficiency and costs will be reduced accordingly. From this point of view, lab-made anion-exchange resin columns might be a better choice than those purchased from a supplier.

Table 4 Relationship between the height-to-diameter ratio and the adsorption efficiency of anion-exchange resin columns

Flow rate of extraction

The flow rate also plays a significant role on the adsorption efficiency of nitrate, and a suitable flow rate maintains the extraction of nitrate from freshwater within a precise range. Silva et al. (2000) investigated the relationship between the flow rate and the adsorption efficiency in 87 samples with nitrate concentrations ranging from 17 to 130 mg N L−1; they observed that the average nitrate adsorption efficiency was 99.84 ± 0.16 % when the flow rate was set within a range of 90 to 565 mL h−1. According to the results of statistical analysis, no correlation existed between the extent of nitrate adsorption and flow rate. Ahmed et al. (2012a, b) obtained similar results and observed that nearly all of the nitrate was adsorbed onto the resin when the flow rate was varied from 350 to 1500 mL h−1. Irrespective of how the samples were loaded onto the resin columns—for example, by gravity, air pressing or with the aid of suction—a flow rate range of 500 to 1000 mL h−1 was most common. The flow rate can be adjusted by a rubber stopper in a separatory funnel or by a peristaltic pump (Chang et al. 1999; Silva et al. 2000; Xing and Liu 2011). In addition, a coarser mesh size of the same type of anion-exchange resin can be substituted to change the sample flow rate (Silva et al. 2000).

Type of eluant

Consequently, suitable eluants should maintain the elution of nitrate within a precise range. As previously mentioned, the anion-exchange resin in Cl form exhibited an excellent adsorption capacity for nitrate and is the most commonly used resin in this application. Therefore, chloride solutions, such as hydrochloric acid (HCl) and potassium chloride (KCl) solutions, were observed to be superior as for high nitrate yields, relative selectivity for nitrate, and its relative ease of handling (Chen et al. 2010; Silva et al. 2000). Additionally, Silva et al. (2000) and Chen et al. (2010) investigated strontium chloride (SrCl2), calcium chloride (CaCl2), sulfuric acid (H2SO4), potassium citrate (K3C6H5O7·2H2O), and potassium iodide (KI). However, these candidates were abandoned because of chemical instability or low nitrate yields.

Concentration and volume of eluants

The concentration and volume of eluants are two key factors affecting desorption efficiency, and the former is more important than the latter. As previously noted, both HCl and KCl are suitable eluants for the elution of nitrate from anion-exchange resin columns, especially HCl, which is widely used for this purpose. To achieve complete elution of nitrate from resins and save experimental costs, a proper concentration for eluant is necessary. For instance, the desorption efficiency of nitrate was maintained within a low range (lower than 85 %) along with a large variance and did not improve significantly with an increase in volume when the concentration of HCl was as low as 0.2 mol L−1. The optimum concentration and volume vary from resin to resin. With respect to a 2 mL Dowex 1X8 anion-exchange resin column, 30 mL of 0.5 mol L−1 HCl was considered optimum for the elution of nitrate (Ahmed et al. 2012a, b). As a result, the purpose of saving cost was achieved by the reduction of acid usage. In addition, 12 to 15 mL of 3.0 mol L−1 HCl was most commonly used for 2 mL AG1-X8 anion-exchange resin columns (Fukada et al. 2003; Li et al. 2010; Minet et al. 2011; Silva et al. 2000; Xue et al. 2010). Furthermore, KCl is also a suitable eluant. No significant difference was noted eluted between a 40 mL of 2.0 mol L−1 KCl solution and a 40 mL of 3.0 mol L−1 HCl solution for the same sample. The KCl solution produced a slightly higher efficiency than the HCl solution (Chen et al. 2010).

Methods for eluant addition

The method of eluant addition also affects the desorption efficiency of nitrate. Silva et al. (2000) reported that the mean recovery of nitrate was greater than 95 % with a single 15 mL aliquot of 2.7 mol L−1 HCl but had a large variance, whereas 15 mL of 3 mol L−1 HCl applied in five 3 mL increments consistently recovered more than 98 % of the nitrate. Therefore, the aliquot method was adopted by researchers irrespective of type of eluant. After the eluant was added to the anion-exchange resin column, it passed through the column by gravity. To remove residual eluant, positive air pressure must be applied. As a result, a rubber bung and a peristaltic pump were introduced by Fukada et al. (2003) and Xing and Liu (2011), respectively. With the aid of the peristaltic pump, the elution speed was ten times greater than for gravity dripping when 8 mL of HCl was passed through the same anion-exchange resin column, without causing isotopic fractionation (Xing and Liu 2011).

Type of neutralization reagent

The use of Ag2O as a neutralization reagent has several drawbacks: (1) Silver oxide is a type of costly chemical reagent (1 g Ag2O costs approximately US$4.40); (2) commercially available Ag2O reagent contains nitrate blank (11–75 ppm) and must be pretreated before use; (3) AgNO3 is light sensitive, and its photodegradation will cause fractionation; consequently, all of the steps of elution, neutralization, and drying must be conducted quickly, and the samples must be shielded from light during preparation and during temporary storage (Ahmed et al. 2012b; Minet et al. 2011; Silva et al. 2000). Nevertheless, other alternatives (such as hydroxides, oxides, and metals) have one or more of the following fatal drawbacks: (1) Cations, in particular Na, present in the neutralization reagent react with the quartz combustion tubes during the combustion process and (2) fluffy salt (e.g., potassium chloride) generated during the neutralization process can occupy the whole combustion tube and may negatively affect the reaction products (Ahmed et al. 2012b; Silva et al. 2000). Instead of individual neutralization reagents, a combination of reagents is a better choice for achieving analytical precision. Ahmed et al. (2012b) investigated a mixed two-step neutralization scheme in which Ag2O and KOH were chosen as neutralization reagents. They first used Ag2O to neutralize the eluant until a pH of 1.0 was achieved and subsequently added KOH to complete the neutralization until a pH of 7.0 was reached. During the mixed neutralization procedure, majority of the original Cl was removed by AgCl precipitation in the first step limiting the generation of KCl decreased sharply. In this way, a cost reduction resulted from the decreased use of Ag2O and nitrate was produced as KNO3, which was easier to handle than the light-sensitive AgNO3.

Drying methods

Freeze-drying is time-consuming and requires approximately 30 h to dry AgNO3 (or KNO3) salts (Xing and Liu 2011). To circumvent this time-consuming procedure, Fukada et al. (2003) employed an oven-drying process. They prepared ten replicates of standard solutions for processing and concluded that the oven-drying process is also a better choice for the freeze-drying method to recover AgNO3, although they noted little differences between the laboratory standard process and their process. Xing et al. (2011) also investigated the effect of oven-drying on the precision of the method and observed no significant difference between the effects of oven-drying and freeze-drying on the isotope composition for nitrate tested using different types of samples (laboratory standard solutions and natural samples). Compared to freeze-drying, oven-drying is simpler and saves time (only 6 h of oven-drying at 50–60 °C is necessary to evaporate water) (Xing and Liu 2011).

Interferential anions and compounds

As evident in Table 5, the AG1-X8 anion-exchange resin exhibits a good adsorption-exchange capacity and different relative selectivity for different anions. Therefore, other anions containing in solution may play negative impact on the adsorption of nitrate by anion-exchange resin. Among these anions, chloride and sulfate are the most abundant anions and will cause isotope fractionation for nitrate analysis by competing for the adsorption sites (Silva et al. 2000). For this reason, the potential interferences from chloride, sulfate, and dissolved organic carbon (DOC) were investigated and corresponding methods to eliminate these interferences were developed.

Table 5 Relative selectivity between AG1-X8 resin and different anions (Chen et al. 2010; Silva et al. 2000)

Chloride (Cl)

As previously mentioned, Cl is one of the most abundant anions in natural waters, and its relative selectivity is approximately one third that of NO3 . Both of NO3 displacement and exchange capacity exceeding resulted from Cl interference can lead to incomplete adsorption of NO3 (Silva et al. 2000). From this point of view, Cl is considered as potential interference. Silva et al. (2000) investigated the influence of Cl concentration and sample volume on nitrogen isotope fractionation with Cl-amended NO3 solutions processed through the entire procedure and observed that there is a positive relationship between the extent of nitrate-nitrogen isotope fractionation and Cl concentration and sample volume. However, Aly et al. (2010) also conducted similar research but reported that Cl produced no measurable nitrate-nitrogen isotope fractionation because the significant nitrate loss resulted from the displacement of NO3 by Cl rather than exchange capacity exceeding. In addition to nitrate-nitrogen, Ahmed et al. (2012b) also investigated the effect of the chloride ion concentration on the nitrate recovery efficiency and the nitrate-oxygen fractionation; they reported that there is a negative relationship between the nitrate recovery efficiency and sample volume and chloride concentration. In addition, no significant nitrate-oxygen fractionation was found in spite of the Cl concentration that was as high as 4000 mg L−1 for 100 mL samples (Ahmed et al. 2012b).

Sulfate (SO4 2−) and phosphate (PO4 3−)

SO4 2− and PO4 3− must be removed from water samples for the following reasons: (1) SO4 2− is a typical competing ion because of its divalence and high selectivity and is expected to displace both NO3 and Cl; (2) both SO4 2− and PO4 3− are O-containing compounds and were taken as contaminants during the oxygen isotope analysis of nitrate. Silva et al. (2000) investigated the effect of SO4 2− on nitrate nitrogen isotope fractionation by SO4 2−-amended NO3 solutions processed through the entire procedure and did not observe nitrogen isotope fractionation even though the combined concentrations of NO3 and SO4 2− exceeded the capacity of the anion-exchange resin column. However, to avoid contamination for oxygen isotope analysis, action must be taken to remove SO4 2− and PO4 3−. Both barium chloride (BaCl2) and barium hydroxide monohydrate (Ba(OH)2·H2O) are suitable candidates for the removal of these O-bearing compounds by precipitation (Ahmed et al. 2012b; Minet et al. 2011). In the case of BaCl2, the commonly used concentration is 1 mol L−1 and the volume varies from sample to sample. For example, 4 mL of 1 mol L−1 BaCl2 can precipitate as much as 4 mmol of sulfate (Fukada et al. 2003; Minet et al. 2011; Xue et al. 2010). The step for removal of O-bearing contaminants by precipitation can be performed before the extraction of nitrate or after neutralization. The precipitation (such as BaSO4 and BaPO4) can be removed by filtration after the addition of BaCl2 to the sample solution (Chang et al. 1999; Fukada et al. 2003; Li et al. 2010; Minet et al. 2011). In the case of Ba(OH)2·H2O, the saturated solution of which is added to the sample, left for 30 min, and filtered through nylon membrane filter to remove BaSO4 precipitate (Ahmed et al. 2012b). In this way, the sulfate ions was removed and substituted by hydroxyl ions which lead to lower ion strength of the samples.

Dissolved organic carbon

DOC contains nitrogen and oxygen, and this content accounts for approximately 2 and 30–50 % of the average DOC molecule, respectively (Chang et al. 1999). Although the effect of DOC on the nitrogen isotope analysis of nitrate is negligible, its removal before passing the sample through the anion-exchange resin column is preferable because DOC can potentially interfere with NO3 adsorption onto the anion-exchange resin and may lead to the transfer of DOC oxygen into the sample (Ahmed et al. 2012b; Chang et al. 1999). Therefore, the removal of DOC is a key step for oxygen isotope analysis by the ion-exchange method (Ahmed et al. 2012b; Chang et al. 1999; Fukada et al. 2003; Silva et al. 2000; Wassenaar 1995). From the viewpoints of saving time and money, different alleviation schemes are available according to the DOC and nitrate concentrations in the water sample. For samples containing low to moderate DOC concentrations (0.08–0.8 mmol L−1), a special alleviation scheme to remove DOC is unnecessary because most of the DOC is attenuated by adsorption, precipitation, or volatilization throughout the experimental procedure (Silva et al. 2000). For samples containing a high DOC concentration, DOC removal can be achieved with cation-exchange resins, activated-charcoal adsorption columns, or activated carbon (Ahmed et al. 2012b; Chang et al. 1999; Silva et al. 2000). The use of a cation column prior to an anion column reduces the possibility of anion-exchange resin to retain DOC. However, the removal efficiency varied from resin to resin and would likely vary with the local DOC composition (Ahmed et al. 2012b). In order to remove more DOC, activated charcoal column (coarse grained) and activated carbon can be employed. Compared to an activated charcoal column (coarse grained), activated carbon is effective, convenient to handle, and cheap (Ahmed et al. 2012b). However, activated carbon can adsorb nitrate if applied in an excessively high concentration, and its adsorption efficiency is affected by numerous factors, including the additional amount of activated carbon, the contact time with the water sample, the shaking speed, etc. Therefore, to remove DOC without sacrificing nitrate, proper experimental conditions must be used. The optimum conditions for DOC removal while leaving the nitrate intact were 20 mg Norit G-60 activated carbon per 100 mL water sample and then shaking 20 min (Silva et al. 2000). However, activated carbon and activated charcoal would cause O-18 discrimination for nitrate pool in the mobile phase; this fractionation amounted to −6 and +10 ‰, respectively (Ahmed et al. 2012a, b).

Sample preservation

Before samples are loaded onto an anion-exchange resin column, the samples must be carefully preserved to preserve the nitrate pools. Ahmed et al. (2012b) investigated the effect of single or combined use of chloroform, chilling, and freezing on the nitrate pools of artificial wastewater and observed no significant change in the δ18O values for nitrate in samples treated with chloroform (addition of 0.05 to 1000 mL sample), irrespective of the temperature conditions (chilling, freezing, or room temperature). After the sample was loaded onto an anion-exchange resin column and stored in a moist and refrigerated environment, no significant difference was observed for δ15N values of nitrate between stored and directly processed samples after preservation for 7 months to 2 years (Ahmed et al. 2012b; Silva et al. 2000). After being eluted from the anion-exchange resin column by HCl, the eluant must be quickly neutralized. Otherwise, slight isotope fractionation might occur due to HNO3 evaporation (Silva et al. 2000). Therefore, to avoid isotope fractionation and reduce the use of toxic chemical compounds (e.g., CHCl3 or HgCl2), samples must be processed as soon as possible (Silva et al. 2000).

Best procedure available now for ion-exchange method

Sampling and storage

Water samples are collected from freshwater ecosystems (e.g., streamwater, river) with a depth-integrating sampler according to the United States Geological Survey (USGS) protocols (Battaglin et al. 2001; Chang et al. 2002). To satisfy the requirements for dual isotope analysis (approximately 1.4–2.8 mg N), it is firstly needed to determine NO3 concentrations and then confirm the quantity of water sample for processing (Ahmed et al. 2012b; Silva et al. 2000). In addition, the concentrations of Cl, SO4 2−, PO4 3−, HCO3 , and DOC also need to be determined. Subsequently, the water samples are filtered through a 0.45 μm membrane into precleaned polyethylene bottles to remove particles. Addition of chloroform (99.8 %) with the ratio of 0.25 mL L−1 water sample prevents nitrate isotopic fractionation caused by microbial activities (Ahmed et al. 2012b). The water samples can subsequently be shipped to the laboratory for further processing.

Pretreatment

Sulfate (SO4 2−), phosphate (PO4 3−), and dissolved organic carbon (DOC) are the most abundant materials that will cause isotope fractionation for nitrate analysis by competing for the adsorption sites (Silva et al. 2000). Therefore, water samples must be pretreated before the next step. Addition of saturated Ba(OH)2·H2O to water sample, precipitated for half an hour, and filtered by 0.2 mm nylon filter to remove precipitated BaSO4 and Ba3(PO4)2 (Ahmed et al. 2012b; Fukada et al. 2003). Then, the cation-exchange column packed with resin (such as Bio-Rad AG 50W-X8) can be employed to remove DOC and residual Ba2+ (Panno et al. 2008).

Extraction

In this step, the pretreated water sample was passed through the anion-exchange columns at a flow rate of 500 to 1000 mL h−1 (Fukada et al. 2003). In this way, nitrate is extracted from water and retained onto resins. Because incomplete adsorption leads to nitrate fractionation, the NO3 adsorption efficiency must be verified by determination of the NO3 concentration in the eluant passed through the anion-exchange columns. Extraction requires at least 95 % efficiency to avoid significant fractionation (Battaglin et al. 2001; Silva et al. 2000).

Elution

After the extraction step, the NO3 is stripped from the anion-exchange resin by gravity dripping of 15 mL of 3 mol L−1 HCl in five 3 mL increments and then collected the 15 mL of nitrate-bearing eluant by 50 mL glass beakers at the same time (Silva et al. 2000). To remove residual eluant, a rubber bung can be employed to supply positive air pressure to the column after each HCl addition (Fukada et al. 2003). With this approach, more than 98 % of the nitrate can be recovered from the anion-exchange resin (Silva et al. 2000). With respect to a 2 mL Dowex 1X8 anion-exchange resin column, 30 mL of 0.5 mol L−1 HCl was considered optimum for the elution of nitrate (Ahmed et al. 2012a, b).

Neutralization

Nitric acid (HNO3) and HCl coexist in the nitrate-bearing eluant from the anion-exchange resin column (Eq. 1) (Ahmed et al. 2012a, b). Because HNO3 is volatile and isotopic fractionation will occur under low-pH conditions, it must be neutralized as soon as possible before the drying process (Ahmed et al. 2012b; Böhlke et al. 2003; Silva et al. 2000). To prevent the loss of nitrate, the eluant is neutralized immediately with silver oxide (Ag2O), which must be rinsed to remove any traces of NO3 before use. The beaker containing 15 mL of nitrate-bearing eluant is placed in cold-water bath, and Ag2O (prewashed to remove contaminant NO3 ) is added into the beaker increments to neutralize the HNO3 and HCl until a pH of 1 is achieved in the final solution and subsequently added KOH to complete the neutralization until a pH of 7.0 was reached. At last, the solution was filtered to remove silver chloride precipitate (Ahmed et al. 2012a, b; Silva et al. 2000).

Drying and stable isotope analysis

Nitrogen isotopic analysis

To obtain solid KNO3 salts, neutralized solution consisting of KNO3 and KCl was evaporated till complete dryness on a hot plate. The dried salt mix was mixed with activated graphite (in 1:1 mass ratio to KNO3) and finally ground. Then, the mixture is put into a 20 cm length and 6 mm (OD) Pyrex glass tubes which need to be precombusted, and the combustion tubes are evacuated, torch-sealed, combusted, and cooled (Ahmed et al. 2012b). In this way, the KNO3 samples were completely decomposed and the liberated CO2 gas was available for oxygen isotopic analysis by IRMS (Ahmed et al. 2012a, b; Aly et al. 2010). The nitrogen isotopic ratios (R) are reported as the parts per thousand (or per mil, ‰) deviation from the 15N/14N ratios relative to N2 (air). To verify the analytical accuracy, internationally accepted reference materials supplied by USGS and the International Atomic Energy Agency (IAEA) can be employed for isotope analysis (e.g., USGS25, IAEA-N-1, and IAEA-N-2) (Minet et al. 2011; Zhang et al. 2014).

Oxygen isotopic analysis

Activated carbon should be employed to remove residual DOC, and the optimum conditions for DOC removal while leaving the nitrate intact were 20 mg Norit G-60 activated carbon per 100 mL water sample and then shaking 20 min, filtered by 0.2-μm nylon filter to remove residual SO4 2−. Then, the cation-exchange column packed with resin (such as Bio-Rad AG 50W-X8) can be employed to remove the residual Ba2+ (Panno et al. 2008). After re-neutralized, the solution was dried by hot plate. The dried salt mix was mixed with activated graphite (in 1:1 mass ratio to KNO3) and finally ground. Then, the mixture is put into a 20 cm length and 6 mm (OD) Pyrex glass tubes which need to be precombusted, and the combustion tubes are evacuated, torch-sealed, combusted, and cooled (Ahmed et al. 2012b). In this way, the KNO3 samples were completely decomposed and the liberated CO2 gas was available for oxygen isotopic analysis by IRMS. The oxygen isotopic ratios (R) are reported as the parts per thousand (or per mil, ‰) deviation from the 18O/16O ratios relative to standard mean ocean water (SMOW). To verify the analytical accuracy, internationally accepted reference materials supplied by USGS and the International Atomic Energy Agency (IAEA) can be employed for isotope analysis (e.g., USGS32, USGS34, and IAEA-NO-3) (Minet et al. 2011; Zhang et al. 2014).

Discussion and perspective

To date, the ion-exchange method has been widely employed in the collection of nitrate from freshwater ecosystems for nitrogen and oxygen isotope analysis. However, this method has inherent shortcomings, such as high costs and a negative influence of interfering ions (such as chloride, sulfate, etc.); thus, appropriate modifications must be made to this method. First of all, the uncertainties associated with the method and which step gives large contribution should be understood and paid more attention. According to the uncertainty evaluation performed by Ahmed et al. (2012b), the step of purification and DOC removal contributes the most to the total uncertainty budget, followed by the step of matrix variation effects and sample preservation (Fig. 2). Therefore, in order to improve the overall accuracy of the method, the step of purification and DOC removal need to be paid more attention in the future. In addition, the validation and performance of the modified ion-exchange method should be verified by well-established method by determination of large sample sizes at several laboratories (Ahmed et al. 2012b). Time-consuming is also a drawback of the ion-exchange method. Compared to the procedure for measuring δ15N, it is more time-consuming for measuring δ18O since there is a great need to eliminate the negative impact of oxygen-bearing anions and DOC. According to the method characteristics evaluated by Aly et al. (2010), one sample for δ15N analysis of nitrate requires 1–2 h for complete processing from field to IRMS in a set of five samples. However, it will cost at least 4–6 days for δ18O analysis of nitrate for five samples in triplicate means (Ahmed et al. 2012b). Therefore, removal of interfering ions, such as SO4 2− and DOC, is needed to be improved in the future research. Another drawback to the ion-exchange method is its high costs. Therefore, cost reduction is a key step to encourage the application of the ion-exchange method. How can costs be reduced through modification of the ion-exchange method? The total consumables alone for the ion-exchange method developed by Silva et al. (2000) can cost as much as US$76.9 per sample for nitrogen and oxygen stable isotope analysis in duplicate measurements (Xue et al. 2009). While a reduction of 40 % of the total consumables cost was achieved for a modified ion-exchange method developed by Ahmed et al. (2012b). The cost of the column resins (both cation and anion) and the neutralization reagent (Ag2O) account for more than 60 % of the total cost of consumables (Fig. 3). For the modified method by Ahmed et al. (2012b), the anion and cation exchange column was made by injection syringe and resins rather than commercial columns (about US$9.4 per commercial anion or cation exchange resins column). Taking these factors into account, nearly 90 % of the cost would be paid on the column resins (both cation and anion) and Ag2O. Thus, cost savings can be achieved through modification of the use of these consumables. Self-made resin columns are a good choice to replace commercial prefilled columns. Columns and resin of the same pattern as commercial columns can be purchased separately and used to make columns similar to the prefilled columns (Silva et al. 2000). In addition, a sterile syringe is also an alternative for commercial empty column (Ahmed et al. 2012b; Xing and Liu 2011). These two approaches can save as high as US$26 per sample. Nonetheless, a detailed relationship between the H/D ratio in the resin bed and the nitrate concentration needs to be established; then, a suitable exchange resin column can be selected for different samples. In this way, the efficiency and costs will be reduced accordingly. Regarding another costly consumable, Ag2O, cost savings can be realized in three ways: (1) reducing the amount of Ag2O. Xing and Liu (2011) compared a 1 mL sterile syringe exchange resin column with a commercial prefilled column and observed that 2.5–3.0 g Ag2O could be saved, reducing the cost by US$4.30 per sample; (2) the development of an alternative neutralization reagent. Compared to the use of Ag2O alone, combined neutralization with Ag2O and KOH can also lower the costs (Ahmed et al. 2012b); (3) regeneration of Ag2O. The AgCl waste from the neutralization process can be converted back to Ag2O through a series of chemical reactions (Silva et al. 2000). With this approach, Ag2O is no longer a consumable. Although Silva et al. (2000) did not compare the costs between regenerating and purchasing Ag2O, regenerating Ag2O might be a better choice because Ag is a precious metal, which should be reused instead of disposed of as waste. If the cost can be significantly reduced, more information can be obtained for the same cost. For instance, the ion-exchange method can be employed for long-term monitoring of dual stable changes in freshwater systems and can reveal the characteristics of dynamic changes and the potential driving force in the freshwater system. In addition, will the interaction of interfering ions (such as chloride or sulfate) affect the extraction efficiency of nitrate? Adsorption of nitrate onto anion-exchange resins can be interfered by high concentrations of anions in water samples. The effect of interfering anions (such as chloride or sulfate) on the adsorption of nitrate onto anion-exchange resins has been investigated because they could lead to nitrate isotope fractionation. In these experiments, the influence of each interfering ion on nitrate recovery and isotope fractionation was individually investigated, and the authors concluded that no significant isotope fractionation occurred when the interfering anion concentration was within a particular range. However, these results do not agree with reality because interfering anions coexist in water samples. Therefore, the comprehensive influence of interfering ions on nitrate recovery and isotope fractionation should be investigated in the future; in addition, the extent and order of different types of interfering anions on the analytical results can be fully understood, and corresponding methods to offset their effects can be implemented accordingly. In this case, the ion-exchange method can not only be used for the investigation of clean water samples (e.g., surface water and groundwater) but can also be employed to investigate water samples containing complex constituents (e.g., landfill leachate). Landfill leachate is a complex mixture that contains ammonium nitrogen, nitrate, and heavy metals (Kjeldsen et al. 2002). Because heavy metals affect bacterial cultivation, the bacterial denitrification method is not suitable for stable isotope analysis of nitrate in landfill leachate. The passive diffusion method was used as an alternative method for the determination of δ15N–NO3 in landfill leachates (North et al. 2004). However, the passive diffusion method has some drawbacks, such as being time-consuming, and has uncertainties regarding isotope fractionation and lower analytical accuracy. Therefore, if countermeasures to relieve the interference of high concentrations of anions with the adsorption of nitrate onto anion-exchange resins are available, more information on the fate of nitrate in landfill leachate can be revealed. Finally, in order to verify whether the samples can be archived on the resin columns, Ahmed et al. (2012b) and Silva et al. (2000) conducted nitrogen and oxygen isotope fractionation experiments, respectively. According to their results, no significant isotope fractionation occurred when nitrate was preserved on the anion-exchange resin columns for 7 months (for oxygen) and up to 2 years (for nitrogen). Although nitrogen and oxygen isotope fractionation was not investigated in the same experiment, no significant isotope fractionation was expected after the samples were archived on the resin columns for at least 7 months. Therefore, the ion-exchange method can be used as an alternative sample preservation technique for other analytical techniques for the determination of δ15N–NO3 and δ18O–NO3 , such as the bacterial denitrification method. Nitrate in freshwater samples can be placed onto anion-exchange resins in the field and shipped to the laboratory, where the nitrate can be stripped for further processing. However, the use of Ag2O as neutralizing agent is impractical since the silver ions have antimicrobial activity (Chopra 2007). Under this circumstance, KOH is a suitable alternative for Ag2O to neutralize the eluant till a pH of 7.0 was achieved. In this way, the nitrate is extracted from the resin columns and converted into KNO3 salts, which are subsequently processed for stable isotope analysis by the bacterial denitrification method. As a result, two advantages can be realized: (1) enrichment of nitrate for low-nitrate-containing freshwater samples and (2) elimination of the bias of isotopic composition of N2O produced from NO2 in water samples by the bacterial denitrification method because the relative selectivity of NO2 is approximately one third that of NO3 (Table 5).

Fig. 2
figure 2

Uncertainty contributors to the total uncertainty budget of the ion-exchange method (adapted from Ahmed et al. 2012b)

Fig. 3
figure 3

Cost analysis of consumables for the ion-exchange method (adapted from Ahmed et al. 2012b)

Conclusions

The ion-exchange method is a reliable and precise technique for measuring δ15N and δ18O in NO3 and plays an important role in distinguishing the sources of nitrate contamination for freshwater ecosystems. This review summarizes and presents the principles, affecting factors and corresponding significant improvements of the ion-exchange method. The modification of the method or the development of alternative consumables such as columns, resins, and neutralization reagents is necessary to reduce costs and increase the applicability of this method. In addition, to enlarge the applicable range of this method, the effect of interfering ions on the efficiency of this method and corresponding methods to offset these effects should be investigated and the function of sample preservation for stable analysis needs to be confirmed in the future. In comparison to other analytical techniques for the determination of δ15N–NO3 and δ18O–NO3 , more accurate analysis results can be attained using the anion column technique. These research results will be particularly valuable in revealing dynamic change characteristics and the potential driving forces in freshwater systems and in providing information on the fate of nitrate in other liquid samples, such as landfill leachates.