Abstract
Hydrogen-sulfide (H2S) is a molecule of small dimensions typically present in the odor emissions from different plants. The European Standard EN 13725:2003 set a maximum storage time allowed of 30 hours, during which the sampling bag has to maintain the mixture of odorants with minimal changes. This study investigates the H2S losses through Nalophan bags and it shows that nonnegligible losses of H2S can be observed. The percent H2S loss after 30 hrs with respect to the initial concentration is equal to 33% ± 3% at a relative humidity of 20% and equal to 22% ± 1% at a relative humidity of 60%. The average quantity of adsorbed H2S at 30 h is equal to 2.17 105 at a storage humidity of 20% and equal to 1.79 105 at a storage humidity of 60%. The diffusion coefficients of H2S through Nalophan, for these two humidity conditions tested, are comparable (i.e., 7.5 10−12 m2/sec at 20% humidity and 6.6 10−12 m2/sec at 60% humidity).
1. Introduction
Although odors do not have a direct effect on human health, they are considered one of the main causes of discomfort for the population living in areas impacted by odor emissions. Nowadays, olfactory pollution has become a serious environmental concern because it may be the cause of physiological stress to the population [1]. Concerning olfactory nuisance, different European countries have recently adopted specific regulations. The standard methodology for odor concentration measurement is a sensorial technique, that is, dynamic olfactometry [2], which is commonly applied for testing odors for environmental management purposes [3]. This technique is based on the sensation caused by an odorous sample directly on a panel of human assessors [4].
Performing olfactometric analyses on site presents some difficulties. To overcome these problems, the odorous pollutants are collected and stored in appropriate containers until they are analyzed in an olfactometric laboratory [4–6]. In order to regulate the quality of the olfactometric analysis, the European Standard on dynamic olfactometry [2] defines the requirements for the materials used for sampling equipment. The requirements determined by the EN13725 for the olfactometry materials are as follows: being odorless and being able to minimize the physical or chemical interaction between sample components and sampling materials and having low permeability in order to minimize sample losses caused by diffusion and smooth surface.
The materials allowed by EN13725 for sample containers (i.e., bags) are as follows: tetrafluoroethylene hexafluoropropylene copolymer (FEP); Tedlar™ (polyvinyl fluoride, PVF), and Nalophan (polyethylene terephthalate, PET). Moreover, European Standard set a maximum storage time allowed, during which the sampling bag has to maintain the mixture of odorants with minimal changes.
Since the publication of the Standard in 2003, several studies have been carried out in order to test the characteristics of the materials listed in the EN 13725 [2] and to verify their suitability for olfactometric measurements. In Table 1 literature studies are reported investigating losses of odorous molecules through sampling bags [1, 5–36].
More in detail, in Table 1, beside the author and year, the polymer film studied, the thickness of the film, the pollutant taken into account and the detection system adopted are reported.
The results of the studies reported in Table 1 underline that the chemical pollutants diffused through the polymeric film are mainly small molecules, like ammonia (NH3) and H2S.
Nalophan is generally the most used material for the manufacturing of sampling bags for olfactometric analyses, due to its inert properties and cost-effectiveness. Despite these advantages, it is known in literature that Nalophan allows the diffusion of specific compounds, such as water [15]. Water can diffuse quickly through the Nalophan polymeric film because of its structure [15]. The results of the studies reported in Table 1 showed that the chemical compounds that diffuse through the Nalophan film are water, NH3, and H2S [1, 9, 10, 15, 27]; the last two compounds diffuse easily because these molecules have dimensions similar to water [1, 9, 10, 15, 27].
H2S and NH3 are typically odorous pollutants present in the emissions from several plants such as solid waste and waste water treatment.
In this paper, the attention was focused on H2S, a malodorous compound with smell similar to rotten eggs. H2S is detected by human olfaction at very low concentrations—about 1 ppb [37–39]—and it is typically found in the emissions from different plants, like industry [30], agriculture [16, 31], waste water treatment [7], and waste treatment [21].
Generally, the articles present in literature (Table 1) focus the attention mainly on the H2S loss by determining the H2S recovery in the sampling bag.
The study of the contribution of pollutant losses, such as diffusion and adsorption, is not easy because the diffusion through the polymeric film is influenced by the nature of the polymer as well as by the nature of the diffusing pollutant [1, 40].
More in detail, the polymer characteristics that influence the diffusion processes are as follows: the chemical nature of the polymer, its crystalline structure and orientation, the free volume, the molecular cohesion, the relative humidity, temperature, hydrogen bonding, polarity, solubility parameter, and solvent size and shape [40].
As reported by Klopffer and Flaconneche in 2001 [41], the polymer structure plays an important role in the determination of the transport phenomena through the polymeric film.
It is well known in literature that transport phenomena of small molecules through an amorphous polymer are governed by mechanisms of adsorption and diffusion [40]. Transport phenomena can be decomposed into five successive stages (Figure 3) [40, 41]: (i) the diffusion through the boundary layer of the side corresponding to the higher partial pressure (upstream side); (ii) the adsorption of the gas (by chemical affinity or by solubility) on the polymer; (iii) the diffusion of the gas inside the polymer’s membrane; (iv) the desorption of the gas at the side of lower partial pressure; and (v) the diffusion through the limit layer of the downstream side.
Only few studies in literature [1, 14, 27, 28] have faced the problem of diffusion through the sampling bags by calculating the diffusion coefficient of the inspected chemical compound. Moreover, in most studies, the amount of chemical compound lost due to adsorption on the polymeric film has been neglected. Adsorption can be neglected when high concentrations are considered (e.g., 50000 ppm NH3 by Sironi et al. (2014) [1, 27, 28]), whereas for medium-low concentrations (e.g., in the range of ppb to few ppm) the effect of adsorption becomes significant. In this study, both the effects of diffusion through the polyethylene terephthalate (PET, Nalophan) film and the adsorption on the film are investigated. The experiments described in this paper aim to investigate the relative contributions of the two phenomena causing H2S loss in Nalophan bags, that is, adsorption and diffusion. The evaluations were carried out by calculating the amount of H2S adsorbed in the Nalophan film and the diffusion coefficient relevant to this material. Finally, the influence of physical parameter like relative humidity (RH) on both the diffusion coefficient and the adsorption was evaluated.
2. Materials and Methods
2.1. Materials
The sampling bags studied with capacity of 6 liters are prepared from a tubular film of Nalophan supplied by Tilmmanns S.p.A. and shown in Figure 1. The polymer film consists of a 20-µm thick one-layer foil.
The H2S decay over time was evaluated by measuring the H2S concentration inside the bag over time by means of a high performance miniature sensor able to detect H2S at ppb level. More in detail, the sensor used for the H2S concentration measurement is a CairClip apparatus, developed by Cairpol, a French start-up (Alès Engineer School of Mines), which consists in amperometric detection with a dynamic air sampling system, a special filter, and a high sensitive electronic circuit containing a data logger [42]. The instrument was calibrated by the manufacturer and it has a life-cycle of one year. The accuracy of this instrument declared by the manufacturer is 10 ppb, in a range between 30 and 1000 ppb of H2S and mercaptans.
All the test samples were prepared by filling the Nalophan bags with a gaseous mixture of 800 ppbV of H2S in air, defined as the “test mixture” in the paper. The samples were obtained by withdrawing the H2S from a certified H2S gas cylinder (SAPIO technical gas, Milano, Italy) into Nalophan bags with a volume of 6 liters and a surface of 2580 cm2.
One aspect that had to be considered for the design of the experiment is that the CairClip has steel parts that may interact with the H2S and reduce its concentration, thereby affecting the measurements of the H2S concentration decay through the Nalophan, which is the aim of this paper. Therefore, in order to avoid undesired interactions of the CairClip sensor with the H2S during the sample storage period, the concentration measurements were carried out by moving the gaseous mixture contained in the storage bag into another identical empty bag containing the CairClip sensor (Figure 2). Because of the short time of the measurement, the adsorption/diffusion effect in this bag is assumed to be negligible. In order to evaluate the H2S concentration decay over time, this procedure had to be repeated for different time intervals. A new bag had to be prepared for each tested interval and then its contents transferred to the bag containing the measurement apparatus after the desired time interval (Figure 2).
The H2S concentration after each tested time interval was then compared to the initial H2S concentration in the test mixture (800 ppb) in order to evaluate the H2S loss over time.
During storage, external physical parameters like temperature (i.e., 23°C) and relative humidity (i.e., RH% equal to 20 and 60, resp.) were kept under control using a climatic chamber (Chamber GHUMY by Fratelli Galli, Milano, Italy).
2.2. Methods
In order to evaluate the contribution of adsorption and the diffusion phenomena into the Nalophan bags, several tests had to be performed, and three replications of each condition and time were tested, following the scheme in Figure 2.
After a first test using a bag with a volume of 6 liters and a surface of 2580 cm2 (in the following defined as “B-no film”), other tests were repeated using bags with the same geometrical characteristics (i.e., volume of 6 liters and a surface of 2580 cm2), in which sheet of film of the same material (i.e., a 20 μm thick Nalophan sheet) was inserted. Three different tests were performed by changing the dimensions of the sheet of film inserted inside the bag. This way, besides the “B-no film” with no film in it, three different types of bags were prepared:(i)Nalophan bag with volume of 6 L and surface of 2580 cm2 containing a sheet of film of 1900 cm2 (in the following defined as “B-film 1900”).(ii)Nalophan bag with volume of 6 L and surface of 2580 cm2 containing a sheet of film of 2580 cm2 (in the following defined as “B-film 2580”).(iii)Nalophan bag with volume of 6 L and surface of 2580 cm2 containing a sheet of film of 3520 cm2 (in the following defined as “B-film 3520”).The idea of inserting the sheets of Nalophan of different dimensions inside identical bags had the aim of evaluating the contribution of adsorption of the H2S in the Nalophan film, which is expected to increase with the surface of the Nalophan film the H2S is in contact with.
Table 2 reports the experimental conditions tested.
The tests were conducted by measuring the H2S concentration at different storage time intervals, as explained in the previous paragraph. The time intervals tested were from 0 to 30 hrs, the latter being the maximum storage time allowed by the reference standard EN 13725:2003. All measurements, reported in Table 2, were repeated three times each.
The test temperature of the samples was fixed at 23°C. The role of humidity on the H2S concentration decay inside the bag was evaluated by storing the bags at different external humidity values, of 20% and 60%, respectively.
A suitable procedure had to be adopted in order to normalize the Nalophan films tests in terms of initial conditions of water absorbed. In fact, Nalophan is proven to be water permeable [15], and thus the water adsorption in the film is connected to the external environmental conditions. For this reason, in order to normalize the water content of the tested Nalophan films, all bags were stored for 12 hours at the test conditions using a climatic chamber before the beginning of the tests.
This procedure allows obtaining repeatable results by reducing the measurement errors related to the state of swelling of the polymer matrix.
The comparison of the H2S residual concentration inside the bag after the tested storage time with the initial H2S concentration in the test mixture allowed the evaluation of the H2S loss over time. As already mentioned, the aim of this paper was not only the quantification of the H2S loss over time but also the evaluation of the relative contribution of adsorption and diffusion to this loss. H2S adsorption was evaluated using (12) to (14) (see Calculations), whereas diffusion was calculated based on Fick’s law. To calculate the diffusion coefficient of H2S through Nalophan, (15) to (17) were used (see Calculations). The measurements were performed at different times and the diffusion coefficient was averaged over 30 hours.
2.3. Calculations
The model used to determine the H2S loss, due to both adsorption and diffusion, starts from the method developed in Sironi et al. 2014 [1] by adapting this for H2S. More in detail, the novelty of this work is to separate the two contributions on pollutants loss from the sampling bag: adsorption on polymeric matrix and diffusion through the film.
The diffusion phenomenon through a polymeric film can be described by Fick’s law. Accordingly the specific molar flow is defined aswhere (i) is the specific molar flow (mol/m2/sec),(ii) is the diffusion coefficient of the compound through the film (m2/sec),(iii) is the concentration of the diffusing compound (mol/m3),(iv) is the differential thickness of the polymeric film of the bag.The thickness of polymeric film of the bag can therefore be expressed aswhere is the thickness (m) of the polymeric film of the bag.
Referring to Figure 3, which schematizes the diffusion phenomenon through the thin film that constitutes the sampling bag, it is possible to define the following:(i) is the surface of the polymeric film of the bag (m2).(ii) is the thickness of the polymeric film of the bag (m).(iii) is the concentration in the inside volume (mol/m3).(iv) is the concentration outside the film (mol/m3), and for a single bag it is generally considered negligible ().(v) is the specific molar flow through the polymeric film of the bag (mol/m2/sec), assuming in first approximation constant along the film ().By integrating (1) in between 0 and , the specific molar flow can be expressed aswhere is relevant to an infinitesimal portion of the exchange surface .
Assuming that the internal molar concentration is homogeneous inside the whole internal volume and also the external concentration is constant inside the external volume, then the global flow through the exchange surface can be calculated by integrating as follows:Combining (3) with (5), the molar flow through the surface can be expressed asIf the external concentration is assumed to be equal to zero (), which is the case if the bag is placed in a neutral environment (where the presence of H2S may be considered negligible), (6) can be rewritten asAccording to this model, the concentration decay over time turns out to be a function of the surface area (), the volume of the sampled gas , the film thickness (), the time (), the diffusion coefficient () that depends on the characteristics of the material, and the concentration gradient through the polymeric barrier ().
The boundary conditions considered for the integration of (7) areThe integration of (7) allows computing the concentration trend over time:The H2S loss (percent) through the bag over time can be expressed aswhere is the concentration measured at time and is the initial concentration.
The loss of H2S is due both to adsorption in the Nalophan and to diffusion through the bag walls.
The H2S loss due to these phenomena can be calculated as the difference between the initial amount of H2S () and the amount measured at the time ():In order to evaluate the relative contributions of the two phenomena (adsorption and diffusion) to the H2S loss inside the Nalophan bag, the following system has to be solved:where(i) is the amount of H2S loss at time (µg) measured for the simple Nalophan bag,(ii) is the amount of H2S loss at time (µg) measured for the Nalophan bag with the Nalophan sheets inserted,(iii) is the contribution of the adsorbed H2S (µg/m2),(iv) is the contribution of the diffused H2S (µg),(v) is surface area of the bag (m2),(vi) is surface area of the sheet of film inserted in the bag (m2).The first equation of the system refers to the test condition in which the bag has no additional film inserted in it. On the contrary, the second equation refers to the bags containing the sheets of Nalophan film. Moreover, it is important to notice that using the same thickness of the film (i.e., 20 µm) the data are expressed in terms of surface unit. Therefore, the data obtained are directly correlated to the data expressed in terms of mass unit.
The adsorbed amount per unit of surface (/m2) can be obtained by subtracting the contribution of the diffusion (i.e., ) from the amount of H2S losses at time (i.e., (µg)), according to (12):The adsorbed amount () related to the considered surface can be obtained by multiplying /m2 by the inner film surface (i.e., ):The diffused amount (i.e., ) was calculated as the difference between the H2S amount losses () at time and the adsorbed amount:The diffusion coefficient for each time interval was calculated according to the following equation:where is the time interval and is the concentration diffused at time .
The diffusion coefficient of H2S through Nalophan was finally calculated as the average of the different values of weighted on the corresponding storage time :
3. Results and Discussion
As previously mentioned, the main objective of this study was the estimation of the relative contribution of the two phenomena (i.e., adsorption and diffusion) that are responsible for the H2S concentration decay inside Nalophan bags used for olfactometric sampling.
Table 3 shows the ratio , where is the H2S concentration measured at different time intervals () normalized to the initial concentration (), and the percent loss of H2S (%) with respect to the initial concentration. The storage temperature was fixed at 23°C and the relative humidity was 20% and 60%, respectively. Table 3 reports the results obtained for the simple Nalophan bag (“B-no film”) and the other three bags prepared by inserting sheets of Nalophan of different dimensions inside the bags, that is, 1900 cm2 (“B-film 1900”), 2580 cm2 (“B-film 2580”), and 3520 cm2 (“B-film 3520”), respectively, as described in the Methods.
The percent loss of H2S (%) (Table 3) inside the bag with respect to the initial concentration over time was calculated according to (10). The H2S concentration decay is due to both the adsorption into the Nalophan (i.e., both the bag itself and the inserted film sheet) and the diffusion through the bag walls.
The percent loss of H2S (%) from the simple bag that does not contain the extra Nalophan film sheet in it (“B-no film”) after 30 hr turns out to be equal to about 33% ± 3% at a storage humidity of 20% and equal to 22% ± 1% at a storage humidity of 60%. This trend is coherent with other data reported in the scientific literature dealing with the same subject. As an example, a study by Akdeniz et al. (2011) [7], also dealing with H2S losses through polymeric films (Tedlar and Flex Foil), reports losses of about 20% after 36 hours.
Moreover, it is possible to observe for the single bag how the data show that the trends of the H2S losses (%) are little bit higher decreasing the storage relative humidity. This is due to the presence of water caused by the humidity gradient, as already observed in Sironi et al. () [1, 27].
The data reported in Table 3 show also an increase of the H2S losses (%) increasing the surface of the polymeric film sheet inserted in the bag. The H2S percent loss (%), at a storage humidity of 20%, after 30 hr turns out to be equal to 47% for the bag containing the film sheet with a surface of 1900 cm2, increasing up to 71% for the bag containing the film sheet with a surface of 3520 cm2. The same trend is observed at a storage humidity of 60%: the H2S percent loss (%) after 30 hr turns out to be equal to 46% for the bag containing the film sheet with a surface of 1900 cm2, increasing up to 63% for the bag containing the film sheet with a surface of 3520 cm2.
As said above, the H2S losses (%) inside the bag with respect to the initial concentration are affected by two contributions: adsorption into the Nalophan and diffusion through the Nalophan bag walls. In order to evaluate these two contributions separately, the H2S ratio adsorbed into the Nalophan film was evaluated as the ratio between (estimated according to (14)) and the initial concentration (). Figures 4 and 5 report the adsorbed H2S (%) at specific time intervals at a storage temperature of 23°C and a humidity of 20% and 60%, respectively.
As it is possible to observe in Figure 4 and in Figure 5, the ratio of adsorbed H2S (%) increases by increasing the inner film sheet surface. The adsorbed H2S (%) at a storage humidity of 20% (Figure 4) after 30 hr turns out to be equal to(i)about 15% for the bag containing the film sheet with a surface of 1900 cm2 (“B-film 1900”),(ii)about 20% for the bag containing the film sheet with a surface of 2580 cm2 (“B-film 2580”),(iii)about 34% for the bag containing the film sheet with a surface of 3520 cm2 (“B-film 3520”).The adsorbed H2S (%) at a storage humidity of 60% (Figure 5) after 30 hr turns out to be equal to(i)about 11% for the bag containing the film sheet with a surface of 1900 cm2 (“B-film 1900”),(ii)about 16% for the bag containing the film sheet with a surface of 2580 cm2 (“B-film 2580”),(iii)about 24% for the bag containing the film sheet with a surface of 3520 cm2 (“B-film 3520”).The data reported above show a weak increase of the ratio of adsorbed H2S (%) for the bag stored at low humidity (i.e., 20%). The Nalophan film is made with PET (polyethylene terephthalate) that is known from literature to be water permeable [15]. Therefore, when storing the bag at high humidity (i.e., 60%), the amount of water that can be adsorbed on the film is greater compared to the storage condition at low humidity (i.e., 20%). At a temperature of 23°C and relative humidity of 20% the partial pressure of water is equal to 4 mmHg, whereas at a temperature of 23°C and relative humidity of 60% the partial pressure of water is equal to 13 mmHg. Therefore, in this second condition, it is likely that the water is adsorbed on the polymer matrix instead of the H2S (competitive adsorption).
Figures 6 and 7 illustrate the amount of H2S in terms of cumulative losses (µg) and the two contributions, that is, on one hand the H2S adsorbed on the polymeric film and on the other hand the H2S diffused trough the bag walls. The results are shown in function of the surface area of the Nalophan film sheet inserted inside the test bags at a storage humidity of 20% and 60%, respectively.
As expected, the amount of H2S that is adsorbed increases by increasing the surface of the Nalophan film sheet inserted inside the bag. Also, the contribution of diffusion remains almost constant for the two values of relative humidity tested (i.e., RH 20% and 60%, resp.). This aspect was expected because the film sheet inserted has no internal concentration gradient () (see Fick law (7)).
Moreover, it is possible to observe that diffusion is predominant compared to adsorption, although the latter is not negligible. The only exceptions are observed at a temperature of 23°C and a relative humidity of 20% in the bag containing the Nalophan film sheet with a surface of 3520 cm2 (“B-film 3520”) (Figure 6), since in these conditions the contribution of diffusion is comparable to that of adsorption.
The averaged data of the adsorbed amount per surface unit (/m2) in µg/m2 (see (12)) at specific times (i.e., 3 hr, 24 hr, and 30 hr) are reported in Table 4.
It is possible to observe (Table 4) that the results at 24 hours and 30 hours relevant to both the storage conditions tested present comparable values of /m2. At 3 hr, the value of /m2 is lower. The averaged values relevant to 24 and 30 hr of /m2 are equal to 5.8 µg/m2 (which corresponds to a ratio equal to 2.17 105 ) at a relative humidity of 20% and to 4.8 µg/m2 at a relative humidity of 60% (which corresponds to a ratio equal to 1.79 105 ), respectively. The value of was obtained by combining the value of with the thickness of the film, which is equal to 20 µm, and the density of amorphous PET, which is equal to 1.335 g/cm3 [43].
As already observed, at a storage humidity of 20% the amount of adsorbed H2S is higher than the adsorbed amount at the storage humidity of 60%. This may be due to the fact that to a relative humidity of 60% corresponds a higher amount of water, given that the water can compete with the H2S in the adsorption on the polymeric film. Therefore, it is possible to assert that the adsorption of H2S on the polymeric film is influenced by the storage humidity.
Moreover, the data in Table 4 show that after three hours of storage the polymeric film is not yet saturated. The steady state conditions, at which the polymer film is completely saturated, are reached at 24 hours. The steady state is considered reached when the sorption amount of H2S does not vary with time in analogies with Fick law [41]. Therefore, in order to calculate the diffusion coefficient () only the data acquired at 24 hours and 30 hours were used. The diffusion coefficient was evaluated according to (16).
Table 5 reports the diffusion coefficient for each time interval at a storage temperature of 23°C and a humidity of 20% and 60%, respectively.
The diffusion coefficient of H2S () through Nalophan is finally calculated as the average of the different values of (Table 5) weighted on the corresponding storage time according to (17).
The resulting value for , at a storage humidity of 20%, is equal to 7.5 10−12 m2/sec with a standard deviation equal to 1.2 10−14 m2/sec.
The resulting value for , at a storage humidity of 60%, is equal to 6.6 10−12 m2/sec with a standard deviation equal to 7.9 10−15 m2/sec.
The resulting values for obtained at two different storage conditions (i.e., humidity of 20% and of 60%., resp.) present the same order of magnitude.
4. Conclusions
The H2S losses from the Nalophan bag always turned out to be significant. The H2S loss after 30 hr was equal to 33% at a relative humidity of 20% and equal to 22% at a relative humidity of 60%.
The average value of /m2 turns out to be equal to 5.8 µg/m2 at a storage humidity of 20% and equal to 4.8 µg/m2 at a storage humidity of 60%.
The contribution of the adsorption phenomenon, under the test conditions evaluated, is less significant than the diffusion, though not negligible. When increasing the surface of the film sheet inserted in the bag (i.e., test with “B-film 3520” at a humidity of 20%) then the contribution of adsorption to the H2S loss inside the bag becomes comparable with the contribution of diffusion. Therefore, in the case of medium-low concentrations as it happens for those tests (from few ppb to few ppm), an increase of the polymeric surface produces an increase in the H2S loss due to the adsorption on the polymeric film. As a consequence, in order to reduce the adsorption phenomena on the polymeric film when storing gases like H2S at medium-low concentrations (i.e., in a range of ppb to few ppm), it is better to reduce the contact surface exposed to the gas using small sampling bags and storing the bag at a high relative humidity (i.e., RH% equal to 60%). During sampling of H2S, in order to reduce the odor losses, special care should be taken when the expected H2S concentration is medium or low (e.g., in the range of ppb to few ppm) because the adsorption phenomena on the polymer film in this case are not negligible.
The diffusion coefficients of H2S through Nalophan, for these two humidity conditions tested, are comparable (i.e., 7.5 10−12 m2/sec at 20% humidity and 6.6 10−12 m2/sec at 60% humidity).
Evaluating the two contributions of H2S loss (i.e., adsorption and diffusion) is important to choose the best sampling strategy (i.e., the choice of the bag material), as well as the most proper storage time and conditions.
In order to reduce the diffusion phenomena through the bag, it is possible to use polyethylene terephthalate (i.e., commercial named Nalophan) coupled with foils. Nevertheless, this choice does not solve the problems linked to the loss by adsorption of H2S on the polymeric matrix.
Conflicts of Interest
The authors declare that there are no conflicts of interest regarding the publication of this paper.