Journal topic
Atmos. Meas. Tech., 13, 119–130, 2020
https://doi.org/10.5194/amt-13-119-2020
Atmos. Meas. Tech., 13, 119–130, 2020
https://doi.org/10.5194/amt-13-119-2020

Research article 13 Jan 2020

Research article | 13 Jan 2020

# Towards an understanding of surface effects: testing of various materials in a small volume measurement chamber and its relevance for atmospheric trace gas analysis

Towards an understanding of surface effects: testing of various materials in a small volume measurement chamber and its relevance for atmospheric trace gas analysis
Ece Satar1,2, Peter Nyfeler1,2, Céline Pascale3, Bernhard Niederhauser3, and Markus Leuenberger1,2 Ece Satar et al.
• 1Climate and Environmental Physics, Physics Institute, University of Bern, Bern, Switzerland
• 2Oeschger Centre for Climate Change Research, University of Bern, Bern, Switzerland
• 3Gas Analysis Laboratory, Federal Institute of Metrology METAS, Bern, Switzerland

Correspondence: Ece Satar (ece.satar@climate.unibe.ch)

Abstract

A critical issue for the long-term monitoring of atmospheric trace gases is precision and accuracy of the measurement systems employed. Both measuring and preparing reference gas mixtures for trace gases are challenging due to, for example, adsorption and desorption of the substances of interest on surfaces; this is particularly critical at low amount fractions and/or for reactive gases. Therefore, to ensure the best preparation and measurement conditions for trace gases in very low amount fractions, usage of coated materials is in demand in gas metrology and atmospheric measurement communities. This study focuses on testing potential adsorption and desorption effects for different materials or coatings that are currently used or that may be relevant in the future for the measurements of greenhouse gases. For this study we used small volume chambers designed to be used for adsorption studies. Various materials with or without coatings were loaded into the small cylinder to test their adsorption and desorption behavior. We used the aluminum cylinder as the measurement chamber and glass, aluminum, copper, brass, steel and three different commercially available coatings as test materials. Inserting the test materials into the measurement chamber doubles the available geometric area for the surface processes. The presented experiments were designed to investigate the pressure dependency of adsorption up to 15 bar and its temperature dependency up to 80 C for the test materials placed in the measurement chamber. Here, we focused on the species CO2, CH4, CO and H2O measured by a cavity ring-down spectroscopy analyzer. Our results show that the materials currently used in atmospheric measurements are well suited. The investigated coatings were not superior to untreated aluminum or to stainless steel at the tested pressure ranges, whereas under changing temperature aluminum showed better performance for CO2 (<0.05µmol mol−1 change in measured amount fractions) than stainless steel (>0.1µmol mol−1). To our knowledge, this study is one of the first attempts to investigate surface effects of different materials in such a setup for the abovementioned gases.

1 Introduction

Long-term atmospheric monitoring of trace gases requires great attention to precision and accuracy. In order to achieve a high level of compatibility for data obtained at different sites and/or at different times, the World Meteorological Organization (WMO) has recommended compatibility goals for measurements of trace gases within its Global Atmosphere Watch (GAW) Programme (2016). These challenging limits can be achieved not only by regular calibration with standard gases of known composition, but also by limiting any cause of amount fraction alteration. During their relatively long lifetime, on the order of decades, standard gas cylinders may not be stable due to diffusion, leakage, regulator effects, gravimetric fractionation and surface processes . The latter, which encompass adsorption and desorption, are also dependent on temperature, pressure and surface properties. Currently there exists only limited data and a few attempts to quantify these surface processes for CO2 and CH4 . These studies use adsorption theory and Rayleigh fractionation to explain the enrichment in the amount fractions towards the end of the cylinder lifetime with respect to different flow rates.

Key results of the abovementioned studies point out that the adsorption behavior is pressure- and temperature-dependent. All mentioned studies used larger volume (10, 29.5 or 50 L) cylinders, which were already in use as standard cylinders. Their approach on filling varied from compressing natural air to gravimetric preparation in synthetic air or in nitrogen . In their study, neither nor observed that their passivation treatment for the aluminum cylinder decreased the surface interaction of CO2.

defines adsorption as the time lag between the condensation of a molecule and its evaporation from a surface. The simplest relation which can be linked to adsorption is the pressure dependency. At higher pressures, the gas molecules are pressed to the cylinder walls, where they are adsorbed to the cylinder surface. As the pressure decreases during the lifetime of a cylinder, these molecules are desorbed from the surface and lead to an enhancement in the amount fraction of the gas. Changes in temperature also affect the equilibrium amount fraction of the adsorbed molecules by varying temperature-dependent rate constants of adsorption and desorption.

In this study, we aim at distinguishing these effects among various materials under controlled conditions in a previously characterized measurement chamber . We limited ourselves to a selection of materials ranging from materials frequently used in the atmospheric measurement community to commercially available coatings. Aluminum cylinders are now the state of the art for the measurements of greenhouse gases such as CO2 and CH4 (WMO2018). Although not recommended anymore for the abovementioned species, some steel cylinders may still be in use. Additionally, stainless steel pieces are very commonly used as tubing and in pressure regulators, and they are in contact with the measured gases. Some regulators are made of brass (WMO2018), and copper is commonly used as seals in vacuum applications of atmospheric trace gas measurements . Moreover, commercially available coatings are increasingly interesting for both atmospheric measurement and metrology communities, since with the improvement of experimental techniques, the demand for higher precision and accuracy in trace gas analysis is growing.

The affinity of adsorption and desorption deviates largely for different species on various surfaces. Some coatings may provide inert, corrosion-resistant, or hydrophobic surfaces and enable usage of metals instead of polymers with ambiguous outgassing effects. According to the current literature, surface losses are critical especially for more reactive gases during the preparation of the standards. In the gas metrology community, this issue has already been investigated in more detail, i.e., for species such as ammonia using test tubes with various coatings , for propane and benzene , and for monoterpenes in cylinders . In their study, observed that some of the commercial coatings reduced the adsorption loss on the stainless steel surface by a factor of 10 or more. The atmospheric measurement community makes use of inert coatings of a chemically protective barrier of amorphous silicon (SilcoTek Corporation) in air core applications , where the surface-to-volume ratio is large. Diamond-like carbon (DLC) coatings are not yet commonly used in trace gas analysis but have found their place in many applications in a range varying from wear and corrosion protection of magnetic storage media to biological implantations (Grill1999).

This study contributes to the limited literature on the discussion of surface effects of different materials for the species CO2, CH4, CO and H2O. It is one of the first attempts to systematically investigate the differences among various materials in a reproducible way using a relatively small custom-made aluminum measurement chamber requiring less gas and time for the measurements. In this study, we briefly introduce the setup and the established procedure for the measurements. Then, we proceed with eight material loadings to the measurement chamber and test their response to pressure and temperature variations.

2 Data and methods

## 2.1 Measurement setup and used materials

In order to understand the adsorption and desorption behavior of various materials, high-pressure (up to 130 bar) and small-volume (5 L) cylinders of aluminum and steel were designed. These cylinders served as measurement chambers in which various test materials can be inserted. Since the aluminum cylinder showed smaller effects with respect to surface effects in the previous study , we have chosen to use the aluminum cylinder only for the material experiments in order to minimize the background effect related to the measurement chamber. More information and details on the filling history of the cylinders were previously explained . Here we provide a brief summary: the aluminum cylinder is made of the aluminum alloy AlMg1SiCu (EN AW-6061), and its composition is specifically chosen so that it corresponds to the aluminum commonly used in the atmospheric measurement community. This custom-made cylinder consists of three pieces: a body part in the middle with two caps on the sides (Fig. 1a). These pieces are joined by 12 necked-down bolts on each side, and Inconel X750 seals with a silver coating are placed in the caps. It is equipped with four stainless steel bellows sealed valves (SS-4H from Swagelok), where the wetted surfaces are solely of stainless steel and do not include any polymers. The connections are from stainless steel and all tubing is of electropolished stainless steel with a 0.25 in. outer diameter. At the outlet, the cylinders are equipped with dual-stage pressure regulators made of a stainless steel body with a polychlorotrifluoroethylene (PCTFE) seat (64-3441KA412 from Tescom). Pressure transducers are used at low (PTU-S-AC6-31AC from Swagelok) and high (PTU-S-AC160-31AC from Swagelok) pressure sides of the pressure regulators. Temperature sensors spanning a range from −35 to +100C (AF25.PT100 from Thermokon) are placed on the outer cylinder surfaces. All measured temperature and pressure data were read and logged by a signal converter (midi logger GL820 from Graphtec). On the measurement line between the pressure regulator and the Picarro cavity ring-down spectroscopy analyzer (CRDS) G2401 either an electropolished stainless steel 0.25 in. tubing, a mass flow controller (358 series from ANALYT-MTC) or a multiport valve (EMT2CSD6MWE from VICI AG) was placed.

Figure 1(a) Custom-made cylinder of three pieces. (b) Material loading into the cylinder. The metal blocks are placed on the glass ladder, and two rod-shaped glass pieces support the material from the sides.

The fillings were done using compressed air from high-pressure 50 L aluminum cylinders (LUX3586 and LUX3575). These two cylinders are called the mother cylinders and their air content the mother mixture from here on. A mother cylinder was directly connected to a small expansion volume (0.5 L) made of stainless steel (316L-HDF4-500 from Swagelok). In addition to the mother mixture, another mixture of comparable content and from a cylinder of comparable material and equipment to the mother cylinder was measured to check the stability of the measurement device. This mixture (from cylinder LUX3579) is referred to as the working gas. All three cylinders were filled by Carbagas, Switzerland, with compressed air according to their own protocol. The filling history of the cylinders is known only to the extent that the cylinders were filled with compressed air only. In order to test for higher amount fractions of CO, the mother mixtures were spiked: a known amount of pure CO gas was injected into a known volume (60 mL) and was pushed into the sample cylinder using another compressed air mixture as carrier gas. For example, after spiking the mother mixture, the composition of LUX3575 was 428.59 µmol mol−1, 1083.73 nmol mol−1, 2132.93 nmol mol−1 and <15µmol mol−1 for CO2, CO, CH4 and H2O.

Figure 2Schematic of the experimental setup. The aluminum cylinder is placed in the oven (denoted by the red box). The cylinder is filled through the expansion volume from the mother cylinder. At the outlet of the cylinder, the dashed lines show the three possible paths into the analyzer: through the rotary valve, direct tubing or mass flow controller (MFC). The equipment related to the cleaning procedure is denoted in blue.

Material loadings into the cylinder were conducted as follows: glass pieces were inserted in order to avoid sharp metal–metal contact points between the sample pieces and the cylinder inner surface. These consisted of a ladder and two rod-shaped glass pieces (Fig. 1b). Then, on top of the ladder-shaped glass piece, two metal blocks were placed. Each metal block has the dimensions $\mathrm{100}×\mathrm{74}×\mathrm{50}$ mm and has 24 drill holes of 1 cm in diameter. The two blocks have in total comparable (factor of 1.17) geometric area to the cylinder inner surface. Aluminum (AlMgSi1), copper (CuETP), brass (CuZn39Pb3), steel (316L), and three different commercially available coatings on steel (SilcoNert® 2000, Dursan® , and CERODEM® diamond-like carbon) were used as test materials. Glass pieces and metal blocks without coatings underwent a cleaning procedure consisting of an ultrasonic bath with a diluted solution of a mildly alkaline commercial cleaning agent (Deconex HT1201) and vacuum oven drying at 120 C.

Since the cylinder was exposed to outside air in between loadings of different materials, a specific cleaning procedure was applied to eliminate water vapor. The measurement chamber was first pumped down to 0.05 mbar using a dry piston vacuum pump (EcoDry M15 from Leybold), then filled with 2 bar of N2 and pumped again while heating with a heat gun. After three fill–pump–heat cycles of 30 min each, the cylinder was filled with N2 and left for cooling overnight. During these heating cycles, the surface temperature of the sample cylinder increased up to 60 C. The following morning, the cylinder was pumped down to 0.05 mbar and filled with compressed air through expansion. The desired pressure in the small cylinder was achieved by repeating the expansion step several times. An hour was allowed for equilibration prior to starting the measurements.

## 2.2 Measurement sequence and data collection

Figure 2 shows a scheme of the measurement setup. For each material loading, temperature and pressure experiments were conducted using the same procedure as before . The experiments were conducted using a Picarro G2401 CRDS analyzer enabling measurements of CO2, CO, CH4 and H2O. According to the specification sheet of the analyzer, the 5 min, 1σ standard deviation is <0.2µmol mol−1, <1.5 nmol mol−1, <0.5 nmol mol−1 and <50µmol mol−1 for the species CO2, CO, CH4 and H2O, respectively. In order to investigate the material's pressure dependency, the cylinder was filled through expansion from the mother cylinder to around 15 bar and was evacuated through the Picarro analyzer. Each sample material loading had at least three replicates for both temperature and pressure runs with the exception of the blank cylinder (Table 1). Bracketing each measurement, the working gas cylinder was measured to check the stability of the measurement device. The measurement sequence for an individual loading was established in the following order: the first two runs were pressure experiments. These were followed by three cycles of temperature experiments. Lastly, the cylinder underwent the third pressure experiment. This order enables the detection of any changes in pressure response after heating cycles. Table 1 shows an overview of the experiments presented in this study.

Table 1An overview of data included in this study. The pressure values indicate the pressure in the small cylinder at the beginning of each replicate run.

For the pressure dependency experiments, data analysis was based on . There was no flow regulation after the pressure regulator prior to the analyzer inlet. At the beginning of the experiment the flow rate was 220 mL min−1 (standard temperature and pressure, STP), and towards the end of the experiment it decreased to 15 mL min−1 (STP). The endpoint of the experiments was set to a fixed internal parameter of the measurement device called the “outlet valve”. This value can easily be linked to the outflow from the instrument, which corresponds to about 15 mL min−1 at STP. For better comparability among the measurements, measured amount fractions were subtracted from the mean of the first hour of measurements for each run. In order to eliminate instrumental noise, 5 min means of these differences were calculated. In this study, all reported values are in amount fraction differences (ΔCO2, ΔCH4, ΔCO, ΔH2O).

In order to investigate the temperature dependency, the cylinder was placed into a climate cabinet (Angelantoni ACS Challenge 600) at the Swiss Federal Institute of Metrology (METAS). The temperature of the cabinet was set to −10, 20, 50 and 80, with 30 C increments, heated or cooled within an hour (Fig. 3). The temperature was kept constant for 4 h at each level, of which during the last 35 min the material loaded cylinder was measured. These measurements were bracketed by working gas measurements which had not experienced any temperature changes. A multiport valve was used to switch between the small cylinder and the working gas. A full temperature cycle lasted 34 h. For the data analysis, for each temperature step the first 10 min of the measurements were not included in order to allow time for equilibration; the mean of the remaining 25 min was calculated. Then, differences for each temperature level were calculated with respect to the measurements at 20 C.

Figure 3Temperature cycle set at the climate cabinet.

3 Results

## 3.1 Pressure experiments

In Fig. 4, an overview of all measured species is shown. For each run, we calculated the amount fraction differences with respect to the initial amount fraction and selected the maximal difference. The maximal difference was chosen to highlight the maximum possible effect related to desorption. Since all data were processed using the same criterion, the effects originating from the analyzer are canceled out and we focus on the differences between the materials. We grouped replicate runs of each material loading together and showed the calculated maximal differences in the boxplots. The median is denoted by the horizontal line, whereas the mean is shown by the square. Since for most cases only three replicates are present, the first quartile is the mean of the minimum and the median, whereas the third quartile is the mean of the median and the maximum value. For clarity, data points used for the box plots are also shown and they are denoted by the black points. In Fig. 4a and b, CO2 amount fractions are plotted: Fig. 4a includes all materials, whereas Fig. 4b is a zoomed-in image aiming to distinguish smaller differences among the material loadings. For CO2, we were able to detect significant changes only for Dursan® , where the final amount fraction was about 10 times higher than all other materials. For CO and CH4, the maximum difference in the amount fractions did not exceed 6 and 1 nmol mol−1, respectively. According to the analyzer (Picarro G2401) specification sheet, the 5 min, 1σ precision of the instrument is <1.5 and <0.5 nmol mol−1, whereas the 5 min standard deviation of measured data corresponded to 5 and 0.2 nmol mol−1 for CO and CH4, respectively. Therefore, we have concluded that no significant change was observed in the final amount fractions for any of the materials during the course of the pressure experiments for the species CO and CH4. For H2O, steel with mass flow controller and Dursan® loading showed significantly higher maximal amount fractions, corresponding to about 3-times-higher enhancements than other species.

Figure 4Box plots for all materials for the species (a) CO2, (b) zoomed-in image for CO2, (c) CO, (d) CH4 and (e) H2O. The y axes show the maximal amount fraction difference relative to the initial amount fraction. Horizontal lines in each box plot shows the median, whereas the square in the center of the box is the mean of the maximal amount fractions of the replicates.

Figure 5Amount fraction difference relative to the start of the experiment for (a, b) CO2 and (c) H2O with respect to pressure for all tested materials. (a) shows all materials together, whereas in (b, c) each material is plotted separately. Consistent color codes are used throughout the study.

For CO2 measurements, the amount fraction differences for all materials except Dursan® were less than 0.17 µmol mol−1, with slight differences among the various loadings. Of this difference, 0.05 µmol mol−1 is related to the blank cylinder (background effect). The blank cylinder corresponded to the “14 bar after heating” case presented in . More information on the blank cylinder and its filling history is provided in the abovementioned publication. It is also crucial to consider that, during all material block experiments, glass pieces were also present in the small measurement chamber. When the material runs were compared to the experiments with glass, except the DLC loading, the remaining differences were on the order of 0.02 µmol mol−1, which corresponded to the 5 min standard deviation of the measured data. Moreover, during the evacuation of the measurement chamber with the DLC loading, a slightly increasing trend of −0.004µmol mol−1 bar−1 was observed. For the steel loaded cylinder, the experiments where a multiport valve was upstream of the analyzer showed slightly more variation both for final amount fractions and during the pressure run, whereas the mass flow controller employed did not have a significant effect on the CO2 measurements.

H2O measurements (Fig. 5) showed greater differences than CO2 measurements, corresponding to 19.05±2.84µmol mol−1 for the blank cylinder. Compared to other materials, Dursan® loading and the measurements with the mass flow controller showed significantly higher final amount fractions of 73.71±12.55 and 75.22±14.45µmol mol−1, respectively. The difference observed for the mass flow controller was most probably related to a memory effect combined with Teflon tape, since it was used for humid air prior to these measurements. Similar to the CO2 response of Dursan® loading, the increase in H2O amount fraction is most probably a combination of both desorption of newly adsorbed molecules and desorption from the coated layer. It is unlikely that the enrichment of H2O is related to the mother mixture since all other materials resulted in significantly lower amount fraction differences.

Since CO and CH4 (Fig. 4c–d) showed no distinct differences in amount fractions with decreasing cylinder pressure, we include their analog plots in Fig. A1 for completeness. Under these extreme conditions of cylinder evacuation, the observed effects were minimal for most of the investigated materials. However, the Dursan® loading showing a difference revealed that the measurement chamber and the established procedure were successful in detecting changes.

## 3.2 Temperature experiments

Based on the results of the pressure tests, the temperature experiments were conducted within a pressure range for which no pressure effect should occur, with the exception of Dursan®. In order to graphically distinguish the temperature effect on various materials, data were split into four different groups (Fig. 6): group 1 corresponded to materials showing the least response; group 2 were materials showing a significant temperature response; and group 3 and 4 corresponded to Dursan® and DLC separately, since they showed differences an order of magnitude higher for some of the measured species. Note that all x axes in Fig. 6 correspond to a temperature cycle. Blank cylinder, glass, SilcoNert® 2000 and brass loadings (Fig. 6a) showed the least response to temperature variations between −10 and 80 C. For CO2, the observed mean differences per material were less than 0.05 µmol mol−1. However, this difference was as high as 11 nmol mol−1 for CO. At 80 C, there was a clear change in the amount fractions of CO, whereas this step change was not as clear in CO2 measurements. The reason for this behavior is most probably related to the cylinder itself, which points to an irreversible chemical reaction, since the enhancement in amount fraction remained prominent even when the cylinder was cooled back down to 20 C. For CH4, temperature variations resulted in nonsignificant amount fraction differences, and they stayed in a narrow range from −0.75 to 0.5 nmol mol−1. All material loadings showed an effect with respect to H2O measurements. This effect was reversible: lower H2O amount fractions were observed at colder temperatures and higher amount fractions at higher temperatures. This is an indication of adsorption and desorption, in which at colder temperatures the desorption rate is lower, and the system equilibrates at lower amount fractions in the gas mixture. As the temperature increases, the desorption rate increases, resulting temporally in higher amount fractions in water vapor. For the first group of materials, H2O measurements were within the range of −5 to 5 µmol mol−1. After cooling the cylinder to 20 C, a slight change of 1 µmol mol−1 compared to the initial amount fraction was observed.

Figure 6b shows steel, aluminum and copper. These loadings showed a more significant temperature response compared to group 1. Note that the dashed lines represent the ranges from the first group of materials. For CO2, all materials showed a clear increase when the temperature was increased to 80 C. This increase corresponded to 0.16±0.02, 0.10±0.01 and 0.05±0.02µmol mol−1 for copper, steel and aluminum, respectively. After cooling back to 20 C, the amount fraction increase in aluminum and steel dropped back to less than 0.07 µmol mol−1, whereas for copper the difference persisted and was 0.13±0.02µmol mol−1. For CO, the effects were even more significant. At 80 C, ΔCO for the copper loading increased to 29±1 nmol mol−1, and it was followed by 16±4 and 14±2 nmol mol−1 for aluminum and steel, respectively. Aluminum and steel loadings reached their maximum increase at 50 C after cooling down from 80 C and stayed at that level even with further cooling. The increase in CO amount fraction for the copper loading continued and reached 43±1 nmol mol−1. This might be an indication of an irreversible chemical reaction happening after the threshold of 80 C which uses copper as a catalyst. This is further supported by the fact that the amount fraction enhancement after each temperature cycle was reproducible. Similarly to the first group, CH4 measurements of the second group stayed in the narrow window of −0.75 to 0.5 nmol mol−1. For H2O, group 2 materials showed a slightly greater effect than group 1 materials, with a mean of 7.55±2.88µmol mol−1 at 80 C, and reached 11±1µmol mol−1 for aluminum. After cooling to 20 C, a difference over 2 µmol mol−1 compared to the beginning was observed.

Figure 6Temperature experiments grouped according to temperature response. (a) Group 1 materials are blank cylinder (gray), glass (blue), SilcoNert® 2000-coated steel (pink), and brass (brown). (b) Group 2 materials are aluminum (green), stainless steel (red), and copper (orange). (c) Dursan® (light green) and (d) DLC (purple) coatings on stainless steel. Dashed lines indicate the same ranges for each species. The x axes correspond to the temperature cycles (cf. Fig. 3), and the y axes show the amount fraction differences relative to the first measurement block at 20 C.

Figure 6c–d show Dursan® and DLC on separate panels for each of the measured species. For CO2, Dursan® showed differences as high as 0.64±0.02µmol mol−1. A fraction of this difference was related to the pressure decrease of the cylinder from 15 to 5 bar. However, during most of the temperature cycle including measurements at 80 C, the pressure in the cylinder was over 9.5 bar, corresponding to a pressure effect of less than 0.25 µmol mol−1. Even when this difference was considered, the temperature effect of this material was an order of magnitude greater than group 1 materials at 80 C. Whereas at 20 C at the end of the temperature cycle, the pressure contribution was as high as 0.5 µmol mol−1. CO and CH4 did not show any significant difference in their response compared to group 1 and group 2 materials. H2O measurements were higher than in the other groups but reversible.

The DLC loading clearly showed a different temperature response compared to all other materials, especially with regard to the variability of its replicates. CO2 showed a mean difference of 0.15±0.04µmol mol−1 compared to the beginning of the cycle. For CO and CH4, the differences from the starting amount fractions were 10 and 20 times larger than the differences observed for other tested materials. At each temperature cycle, the measured CO difference at 80 C decreased for the first and last cycle; this difference corresponded to 87 and 51 nmol mol−1, respectively. This feature was observed in CH4 and H2O measurements as well. During the first temperature cycle at 80 C, CH4 and H2O showed an increase of 18 nmol mol−1 and 8 µmol mol−1, whereas during the third temperature cycle CH4 and H2O showed an increase of 6 nmol mol−1 and 3 µmol mol−1, respectively. This behavior in DLC measurements showed that the underlying reason of the enhancement in the amount fractions was the substances on the surface of the DLC coating, which were depleted by repeated heating. According to , thermal relaxation of the DLC film may occur at temperatures as low as 100 C.

Moreover, it should be noted that, during the set of the measurements presented in this study, the aluminum cylinder experienced the temperature cycle 30 times. This presumably resulted in a change of the background effect over the course of the presented analysis in the range of 0.04 µmol mol−1. We measured the blank cylinder at the very beginning and at the end of the material set. The blank cylinder result shown in the Fig. 6a is a mean of the former and latter temperature experiments, which therefore resulted in a higher variation. Due to the observed variation, we did not subtract the background to avoid disturbing other measurements. More detailed information on heating experiments and its consequences were presented in .

4 Discussion

The presented setup enabled the investigation of surface effects under extreme conditions which favored adsorption and desorption. Compared to common usage in the atmospheric measurement and gas metrology communities, our study has differed in cylinder size, geometric-surface-to-volume ratios, and pressure and temperature ranges. Previous studies investigating surface effects in compressed gas cylinders have used (50, 10 or 29.5 L) cylinders. The geometric surface of the small (5 L) aluminum cylinder used in this study is 0.18 m2, which results in a surface-to-volume ratio of 35.7 for the unloaded cylinder. Compared to 29.5 L Luxfer cylinders, the small cylinders are estimated to be more prone to adsorption by 40 %. Inserting material blocks into the aluminum cylinder further increased the surface area. Therefore, the setup allows one to test materials under increased surface-to-volume ratios in which the surface effects should be stronger and dominant. However, despite our efforts of increasing the surface material the effects were minor.

In addition to the properties of the materials, pressure and temperature play a role on surface effects. The following assumption lies behind the pressure experiments: if the material has adsorbed a significant amount of gas while filling the cylinder, this should be desorbed towards the end of the experiments controlled by desorption. The onset of the desorption for all tested materials except Dursan® and partly DLC was observed well below atmospheric pressures.

Increasing temperature is expected to facilitate desorption by providing the required energy to desorb the gas molecules from the surface and mix into the gas phase. On the contrary, cooling the cylinder and its content favor adsorption, and it is expected that this results in a decrease in the measured amount fraction.

Testing pieces cut from the aluminum and steel cylinders commonly used in the community would be a valuable addition to enable direct comparison between the commonly used cylinder materials and the produced material blocks at low pressures and high temperatures. Moreover, in order to observe significant surface effects, materials of very high surface areas can be inserted into the measurement chamber. Some ideas would be using thin metal plates, metal spheres or metal pieces resulting from manufacturing processes (e.g., metal chips).

5 Conclusions

We have presented the pressure- and temperature-dependent response of the species CO2, CH4, CO and H2O with respect to glass, aluminum, copper, brass, steel and three different commercially available coatings on stainless steel (Dursan® , SilcoNert® 2000 and DLC). For the pressure response, under the circumstances of our experimental setup and procedure, within the absolute pressure range varying from 15 bar to 200 mbar, we were only able to detect changes for CO2 in the loading with Dursan®-coated stainless steel reaching 2 µmol mol−1 enrichment in the amount fractions. All other materials showed effects less than 0.17 µmol mol−1 for CO2. Under exposure to temperatures from −10 to 80 C, the responses of glass, brass and SilcoNert® 2000-coated steel were minimal, whereas DLC and Dursan® showed distinctly different temperature effects than all other tested materials. For most materials, including stainless steel, copper, aluminum, DLC and Dursan®, a step change in the measured amount fractions was observed after 80 C.

These experiments show that all coatings do not necessarily enable more passive surfaces and might result in enhancements when exposed to pressure and temperature changes. Materials currently used by the atmospheric measurement community for storing standard gases are well suited under 80 C, which are typical utilization temperatures. Moreover, the materials presented in this study are not only relevant for measurements of standard gases, but also of interest for other gas handling and measuring applications.

Data availability
Data availability.

Appendix A

Figure A1Amount fraction differences compared to the start of the experiment for CO and CH4 for all tested materials.

Author contributions
Author contributions.

ML and ES designed the project. ES performed all measurements and wrote the draft of the paper. CP and BN helped with the selection of gases to be studied and provided access to the laboratories and technical units of METAS. PN helped set up the measurement system and solved technical problems. All were actively involved with the final version of the paper.

Competing interests
Competing interests.

The authors declare that they have no conflict of interest.

Acknowledgements
Acknowledgements.

This project is supported by a research contract (F-5232.30052) between the Swiss Federal Institute of Metrology (METAS) and the University of Bern as well as the SNF project Klima- und Umweltphysik: Isotope im Erdklimasystem (icoCEP)(SNF-200020_172550). The authors would like to thank the workshop of the University of Bern for the production of the cylinders, as well as METAS Gas Analysis Laboratory and METAS workshop for their technical support during this work.

Financial support
Financial support.

This research has been supported by the Federal Institute of Metrology METAS (grant no. F-5232.30052) as well as Isotope im Erdklimasystem (icoCEP; SNF-200020_172550).

Review statement
Review statement.

This paper was edited by Brigitte Buchmann and reviewed by three anonymous referees.

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