Raman Sensor for the Determination of Gas Solubility

: Efﬁcient and environmentally responsible use of resources requires the development and optimization of gas separation processes. A promising approach is the use of liquids that are designed for speciﬁc tasks, e.g., the capture of carbon dioxide or other greenhouse gases. This requires an accurate determination of gas solubilities for a broad range of temperatures and pressures. However, state of the art measurement techniques are often very time consuming or exhibit other pitfalls that prevent their use as efﬁcient screening tools. Here, we show that the application of Raman spectroscopy through a compact measuring system can simplify data acquisition for the determination of gas solubilities in liquids. To demonstrate that this approach is expedient, we determined gas solubilities of carbon dioxide in water for three isotherms T = (288.15, 293.15, 298.15) K over a pressure range from p = (0.5–5) MPa and in three imidazolium-based ionic liquids for one isotherm T = 298.15 K at pressures from p = (0.1–5) MPa. When compared to data in the literature, all results are within the reported uncertainties of the measurement techniques involved. The developed analysis method eliminates the need for a lengthy volume or mass calibration of the sample prior to the measurements and, therefore, allows for fast screening of samples, which can help to advance gas separation processes in scientiﬁc and industrial applications.

An accurate and reliable determination of gas solubility is crucial for many research areas. This includes unprecedented environmental challenges due to an excessive emission of carbon dioxide which leads, for instance, to a decrease in the pH value of seawater, thus affecting the mortality rate of deep-sea organisms [3,17]. Carbon Capture and Storage (CCS) technologies are, therefore, explored thoroughly as one of the many approaches to reduce carbon dioxide emissions [18]. The capture of carbon dioxide from industrial processes is as reliant on solubility measurements as the gas separation processes which are needed for the efficient use of resources and often involve the application of tailormade liquids for the separation of specific gases [7]. Investigations of oxygen transfer processes in sewage water [19] or hydrothermal fluids [20] also benefit greatly from gas solubility measurements, and since specific chemical reactions, such as hydrogenations, require the presence of dissolved gas, a suitable solvent has to be identified prior to the reactions [21][22][23]. However, even state of the art analytical [24] and synthetic [25] methods to measure solubility often have severe disadvantages, thus requiring the development of new measurement techniques. Some of the existing approaches need large amounts of sample [6], extensive sample preparation [8], suffer from long data acquisition times [9] or require frequent sampling and, therefore, disturb the vapor-liquid equilibrium (VLE) [4,6].
Since the first systematic measurements by Bunsen in 1855 [26][27][28], a large variety of approaches has been proposed to determine gas solubilities in liquids. Gravimetric [15] and volumetric [29] methods are used, as well as measurement of the bubble-point pressure [5], calorimetry [9], and gas chromatography [4,6]. Vibrational spectroscopy methods such as Raman spectroscopy have been used for solubility measurements as well, e.g., see [1][2][3][30][31][32][33]. They offer several advantages over other conventional methods, which include the possibility of in-situ measurements during reactions or processes and an on-line monitoring of the investigated sample. Optical methods can be easily applied even in harsh environmental conditions [3], but often require long calibration procedures prior to the measurements.
Here, we present a new application of Raman spectroscopy for solubility measurements of gases in liquids. Our approach enables a comparatively straightforward utilization of a spectroscopic method without the need of extensive calibration routines. Samples of unknown mass or volume can be easily characterized based on the molecular density of both the solvent and the solute. A calibration of the Raman system prior to the actual measurements, e.g., with samples of known carbon dioxide concentration, is not necessary with our method, since the calibration is done in parallel to the determination of the solubility. We utilize a compact and relatively simple Raman system for measurements of carbon dioxide in water and three imidazolium-based ionic liquids. The first results after commissioning of the apparatus were in good agreement with literature data, and thus we have come to the conclusion that this is a new and promising measurement method.

Experimental Setup
The experimental setup is shown in Figure 1. It consists of a custom-made measuring cell fabricated from stainless steel and a compact backscattering Raman setup.  [26][27][28], a large variety of approaches has been proposed to determine gas solubilities in liquids. Gravimetric [15] and volumetric [29] methods are used, as well as measurement of the bubble-point pressure [5], calorimetry [9], and gas chromatography [4,6]. Vibrational spectroscopy methods such as Raman spectroscopy have been used for solubility measurements as well, e.g., see [1][2][3][30][31][32][33]. They offer several advantages over other conventional methods, which include the possibility of in-situ measurements during reactions or processes and an on-line monitoring of the investigated sample. Optical methods can be easily applied even in harsh environmental conditions [3], but often require long calibration procedures prior to the measurements.
Here, we present a new application of Raman spectroscopy for solubility measurements of gases in liquids. Our approach enables a comparatively straightforward utilization of a spectroscopic method without the need of extensive calibration routines. Samples of unknown mass or volume can be easily characterized based on the molecular density of both the solvent and the solute. A calibration of the Raman system prior to the actual measurements, e.g., with samples of known carbon dioxide concentration, is not necessary with our method, since the calibration is done in parallel to the determination of the solubility. We utilize a compact and relatively simple Raman system for measurements of carbon dioxide in water and three imidazolium-based ionic liquids. The first results after commissioning of the apparatus were in good agreement with literature data, and thus we have come to the conclusion that this is a new and promising measurement method.

Experimental Setup
The experimental setup is shown in Figure 1. It consists of a custom-made measuring cell fabricated from stainless steel and a compact backscattering Raman setup. Figure 1. Schematic diagram of the experimental setup, consisting of Braeuer's Raman gun mounted on a 3-axis stage (right), the measuring cell, including the sample holder (middle), and a beam dump (left) to absorb the excessive laser light. The gas outlet is connected to a diaphragm vacuum pump via a valve (both not shown in the diagram); the gas inlet is connected the filling and pressure measurement circuit.
In our experimental setup, signal detection is realized with Braeuer's Raman gun (BRG) mounted on a 3-axis micrometer stage (RB13M/M, Thorlabs, Newton, NJ, USA) in connection with a fiber-coupled spectrometer (QEPro, Ocean Insight, Orlando, FL, USA). The BRG has already been described before [34,35], so only a brief description is given here. It consists of several optical elements that guide the inelastically scattered light from the measuring cell into an optical fiber, which subsequently transfers the signals to the spectrometer. A dichroitic mirror in the center of the Raman gun ensures that collimated light from the excitation laser with a wavelength shorter than λ = 532 nm is reflected into Figure 1. Schematic diagram of the experimental setup, consisting of Braeuer's Raman gun mounted on a 3-axis stage (right), the measuring cell, including the sample holder (middle), and a beam dump (left) to absorb the excessive laser light. The gas outlet is connected to a diaphragm vacuum pump via a valve (both not shown in the diagram); the gas inlet is connected the filling and pressure measurement circuit.
In our experimental setup, signal detection is realized with Braeuer's Raman gun (BRG) mounted on a 3-axis micrometer stage (RB13M/M, Thorlabs, Newton, NJ, USA) in connection with a fiber-coupled spectrometer (QEPro, Ocean Insight, Orlando, FL, USA). The BRG has already been described before [34,35], so only a brief description is given here. It consists of several optical elements that guide the inelastically scattered light from the measuring cell into an optical fiber, which subsequently transfers the signals to the spectrometer. A dichroitic mirror in the center of the Raman gun ensures that collimated light from the excitation laser with a wavelength shorter than λ = 532 nm is reflected into the cell, and inelastically scattered signals with a shifted wavelength that are longer than λ = 544 nm can pass freely. Elastically scattered light is removed by a long-pass filter, which is installed before the fiber that is connected to the spectrometer. The samples are excited with a frequency-doubled Nd:YAG laser with a wavelength of λ = 532 nm and an adjustable power output of P = 400 mW (MSL-FN, PhotonTec, Berlin, Germany). The circular sample holder (dimensions: d o = 11.65 mm, d i = 10.55 mm, h = 7.65 mm) is fabricated from borosilicate glass as are the windows of the measuring cell. The cell is connected to a diaphragm vacuum pump (DIVAC 4,8VT, Leybold, Cologne, Germany) with an ultimate pressure of p ult ≤ 200 Pa. A piezoresisitive pressure transducer (PAA-33X, KELLER AG, Winterthur, Switzerland) with an expanded uncertainty (k = 1.73) of 5 kPa is used to monitor the pressure throughout the measurements.
Temperature regulation of the measuring cell is realized with two temperature controllers. A custom-made temperature controller is connected to four Peltier elements located at the bottom of the measuring cell (thermal stage) and is used for a rough regulation of the temperature. A second temperature controller (TEMP-2200, Fluke, Everett, WA, USA), which is connected to two cartridge heaters (S/HS/PT-8/80/125/230-A, Heinz Stegmeier GmbH, Fridingen, Germany) is used for the fine regulation of the temperature and enables temperature stability of 5 mK. For temperature measurements, a resistance bridge (MKT50, Anton Paar, Graz, Austria) is used in combination with two 100 Ω platinum resistance thermometers (PRTs). Both PRTs were calibrated by comparison in a specific temperature range to ensure ITS-90 compliance. Their resistance is checked regularly at the triple point of water. The uncertainty of the temperature measurement (k = 2) is 45 mK (TEMP-5606-50-B, Fluke, USA) and 85 mK (P-M-1/10-3-50-0-TS-2, Omega Engineering GmbH, Deckenpfronn, Germany), respectively.

Experimental Material
Research-grade chemicals were used for all experiments. They were used as received without any further analysis or purification, except for water. Details of all fluids are described in Table 1. Water was purified with a mixed-bed water demineralizer (DI 2000, Thermo Scientific, Waltham, MA, USA) to reach a water quality of σ = 0.1-20 µS·cm −1 ; this was required to allow a comparison with solubility data of carbon dioxide in de-ionized water found in the literature.

Experimental Procedure
The experimental approach for measurements with ionic liquids and water was very similar in each case, but there were a few key differences regarding the handling of the sample prior to the measurements. The sample holder was placed at the window of the measuring cell to avoid additional Raman signals from the carbon dioxide bulk phase during measurements in the liquid samples. In addition, the BRG was adjusted in such a way that the focus point of the laser was set to the far edge of the sample holder to avoid intensity attenuation given by the Beer-Lambert law. Prior to measurements with ionic liquids, the cell was heated to T = 333.15 K and evacuated for three hours to remove any dissolved gas in the sample. After the cell was cooled down to the temperature of the isotherm investigated, a dark spectrum was recorded to capture the baseline offset. Spectra of each ionic liquid were also recorded in vacuum with an illumination time of t i = 6 s.
Ten recordings were averaged for one spectrum, and five spectra were recorded in total. After acquisition of the Raman spectra, the data were processed with the WiRe 3.4 software (Renishaw, United Kingdom) to subtract the baseline and determine the relevant peak area. This procedure was not possible with water since it would evaporate at the given conditions. In this case, the measuring cell has been flushed five times with helium to remove any other gas before the dark spectrum was recorded.
Spectra were recorded at each investigated (T, p) state point along the isotherms in the same way they were recorded in vacuum. An equilibration time of one hour was allowed before each measurement. For calibration purposes, the spectra of the vapor phase were also recorded at the given (T, p) state point. The position of the BRG was adjusted slightly for the recordings of the vapor phase so the focus point of the laser was above the sample but still within the sample holder to account for a possible influence of the sample holder.

Data Analysis
To calculate the gas solubility x from the measurements performed, it is necessary to calculate the density of dissolved gas molecules in the respective fluid ρ sol and the concentration of the fluid c fl (see Equation (1)).
Calculation of c fl is straightforward (see Equation (2)). The density of the fluid at the respective temperature and pressure is divided by the molecular weight of the sample.
Prior to the data analysis, fluid densities ρ fl can be calculated from an equation of state (EOS) that is implemented in a software like NIST's REFPROP database [36] or in TREND [37]; alternatively, densities must be obtained, e.g., experimentally with an auxiliary device or through literature research. For water, the EOS of Wagner and Pruss [38] was used for density calculations with an uncertainty of 0.001% for each (T, p) state point. The density of the ionic liquids was taken from values found in the literature [39,40] and assumed to be constant throughout the measurements.
A more sophisticated data analysis is required to calculate ρ sol (see Equation (3)).
Here, the corrected intensity from the sample measurements I cor is needed alongside the calibration factor m cal . Vapor phase spectra have to be analyzed to calculate m cal . Since a linear relation between the density of molecules and the intensity of the inelastically scattered light is usually assumed [41], the intensity can be plotted against density values calculated at given temperature and pressure. The slope of the linear regression line then equals the calibration factor m cal . An example is shown in Figure 2.
For the vapor phase, the intensity values I vap can be directly derived from the recorded spectra if a suitable peak can be found. In the case of carbon dioxide, the peak area of the right peak of the Fermi dyad ((1380-1420) cm −1 , center: 1404 cm −1 ) was used for the analysis in this work. A peak is considered to be suitable if it is also easily identifiable in the investigated liquid because the same peak must be used to determine I cor for the determination of ρ sol . Temperature and pressure are recorded throughout the measurements and are used to calculate the density of molecules from an equation of state (EOS). The density for pure carbon dioxide at a (T, p) state point ρ vap was calculated with the EOS by Span & Wagner [42] with an uncertainty of 0.03% within the temperature and pressure range of this work.
Span & Wagner [42] with an uncertainty of 0.03% within the temperature and pressure range of this work.

Figure 2.
Example of an intensity vs. density plot of carbon dioxide at T = 293.24 K. The peak area of the right peak of the Fermi dyad, Ivap, is plotted against density values calculated with an EOS, ρvap. The slope of the linear regression line mcal (y = 20,691x, R 2 = 0.9972) is used to calculate the density of the dissolved gas molecules, ρsol, and is given to 95% of confidence.
In order to calculate Icor, the detected intensity from the sample measurements Iraw,sol must be corrected (see Equation (4)) by the factor kexp which, in turn, is derived from the refractive index of the fluid nfl and the gas nvap (see Equation (5)).
This is due to a discrepancy between the detected intensity of a pure component and its intensity in a mixture, as described by Woodward and George [43]. The refractive index for carbon dioxide was calculated from the dielectric constant given by the EOS at the respective (T, p) state point (see Equation (6)), while nfl was taken from literature [44,45].
After the calculation of Icor, ρsol, and kexp, subsequently, the gas solubility can be determined.

Uncertainty in Measurement
To analyze the uncertainty in measurement, we followed the recommendations of the guide to the expression of uncertainty in measurement (GUM) [46]. For all results, we report the combined expanded uncertainty (k = 2) of the dissolved carbon dioxide in the respective fluid (U(xCO2)), which includes the uncertainties of temperature, pressure and spectroscopic measurements.
The main source of uncertainty originates from the recorded spectra and is tied to their quality. The uncertainty of the calibration slope is about 2 %, but the uncertainty contributed by the recorded spectra in the liquid phase depends on the amount of dissolved carbon dioxide in the respective liquid. It is higher at low pressures (p ≤ 1 MPa) and improves gradually with increasing pressures. The uncertainty contribution of the liquid phase spectra depends, therefore, not only on the pressure, but also on the investigated liquid and its behavior as a solvent. The combined expanded uncertainty is approximately U(xCO2,H2O) = 5% for the measurements in water and U(xCO2,IL) = 3% for the ILs Figure 2. Example of an intensity vs. density plot of carbon dioxide at T = 293.24 K. The peak area of the right peak of the Fermi dyad, I vap , is plotted against density values calculated with an EOS, ρ vap . The slope of the linear regression line m cal (y = 20,691x, R 2 = 0.9972) is used to calculate the density of the dissolved gas molecules, ρ sol , and is given to 95% of confidence.
In order to calculate I cor , the detected intensity from the sample measurements I raw,sol must be corrected (see Equation (4)) by the factor k exp which, in turn, is derived from the refractive index of the fluid n fl and the gas n vap (see Equation (5)).
This is due to a discrepancy between the detected intensity of a pure component and its intensity in a mixture, as described by Woodward and George [43]. The refractive index for carbon dioxide was calculated from the dielectric constant given by the EOS at the respective (T, p) state point (see Equation (6)), while n fl was taken from literature [44,45].
After the calculation of I cor , ρ sol , and k exp , subsequently, the gas solubility can be determined.

Uncertainty in Measurement
To analyze the uncertainty in measurement, we followed the recommendations of the guide to the expression of uncertainty in measurement (GUM) [46]. For all results, we report the combined expanded uncertainty (k = 2) of the dissolved carbon dioxide in the respective fluid (U(x CO2 )), which includes the uncertainties of temperature, pressure and spectroscopic measurements.
The main source of uncertainty originates from the recorded spectra and is tied to their quality. The uncertainty of the calibration slope is about 2 %, but the uncertainty contributed by the recorded spectra in the liquid phase depends on the amount of dissolved carbon dioxide in the respective liquid. It is higher at low pressures (p ≤ 1 MPa) and improves gradually with increasing pressures. The uncertainty contribution of the liquid phase spectra depends, therefore, not only on the pressure, but also on the investigated liquid and its behavior as a solvent. The combined expanded uncertainty is approximately U(x CO2,H2O ) = 5% for the measurements in water and U(x CO2,IL ) = 3% for the ILs (however, it must be noted that the results vary for each IL and each water isotherm; detailed information for the studied (T, p) state point is provided in Appendix A). For comparison, typical uncertainties of other solubility measurement techniques, such as ion chromatography, are in the range of 4%, whereby it is virtually never specified in the literature which uncertainty the authors report (single or combined uncertainty, standard or expanded uncertainty, just twice the standard deviation etc.).

Results for Solubilty of Carbon Dioxide in Water
Solubility measurements of carbon dioxide in water were conducted along three isotherms T = (288.15, 293.15, 298.15) K within the scope of this work. The sensitivity of the Raman setup limited the measurements to a pressure range from p = (0.5-5) MPa. The signal-to-noise ratio at p < 0.5 MPa was insufficient to gather meaningful results due to the low solubility. Also, a slight shift in the investigated peak ((1380-1420) cm −1 , center: 1400 cm −1 ) was observed due to the solvation of carbon dioxide in water, however, this is in agreement with previous reports [47]. As an example, the Raman spectrum of dissolved carbon dioxide in water at T = 288.15 K and p = 4 MPa is given in Appendix C. Although data for comparison was limited, the results show good agreement with the available literature data (see Figure 3) and are within the combined uncertainties of the involved measurement techniques, if available. (however, it must be noted that the results vary for each IL and each water isotherm; detailed information for the studied (T, p) state point is provided in Appendix A). For comparison, typical uncertainties of other solubility measurement techniques, such as ion chromatography, are in the range of 4%, whereby it is virtually never specified in the literature which uncertainty the authors report (single or combined uncertainty, standard or expanded uncertainty, just twice the standard deviation etc.).

Results for Solubilty of Carbon Dioxide in Water
Solubility measurements of carbon dioxide in water were conducted along three isotherms T = (288.15, 293.15, 298.15) K within the scope of this work. The sensitivity of the Raman setup limited the measurements to a pressure range from p = (0.5-5) MPa. The signal-to-noise ratio at p < 0.5 MPa was insufficient to gather meaningful results due to the low solubility. Also, a slight shift in the investigated peak ((1380-1420) cm −1 , center: 1400 cm −1 ) was observed due to the solvation of carbon dioxide in water, however, this is in agreement with previous reports [47]. As an example, the Raman spectrum of dissolved carbon dioxide in water at T = 288.15 K and p = 4 MPa is given in Appendix C. Although data for comparison was limited, the results show good agreement with the available literature data (see Figure 3) and are within the combined uncertainties of the involved measurement techniques, if available. Measurements in the vicinity of the literature data [4][5][6] taken as a reference also show a consistent trend regarding the solubility. As gas solubility depends on the physical and chemical properties of the solvent and the solute, it was expected that the solubility of carbon dioxide would increase with decreasing temperature in water [48], and our measurements confirmed this behavior. However, the determined solubilities have a slight tendency to higher values in comparison to the literature data. This might be due to additional signals from the vapor phase in the measuring cell, which is caused by the measurement procedure presented.
The combined expanded uncertainty for the solubility measurements in water is high for every investigated isotherm due to the low solubility in comparison to the investigated ILs. Since the solubility at T = 298 K is the lowest, it shows also the highest uncertainty U(xCO2,H2O) = (6-7.5)% even at p = 5 MPa. The uncertainty is significantly lower at high pressures and lower temperatures, e.g., U(xCO2,H2O) = 3.7% at p = 5 MPa and T = 293 K. Measurements in the vicinity of the literature data [4][5][6] taken as a reference also show a consistent trend regarding the solubility. As gas solubility depends on the physical and chemical properties of the solvent and the solute, it was expected that the solubility of carbon dioxide would increase with decreasing temperature in water [48], and our measurements confirmed this behavior. However, the determined solubilities have a slight tendency to higher values in comparison to the literature data. This might be due to additional signals from the vapor phase in the measuring cell, which is caused by the measurement procedure presented.
The combined expanded uncertainty for the solubility measurements in water is high for every investigated isotherm due to the low solubility in comparison to the investigated ILs. Since the solubility at T = 298 K is the lowest, it shows also the highest uncertainty U(x CO2,H2O ) = (6-7.5)% even at p = 5 MPa. The uncertainty is significantly lower at high pressures and lower temperatures, e.g., U(x CO2,H2O ) = 3.7% at p = 5 MPa and T = 293 K.

Results for Solubilty of Carbon Dioxide in Ionic Liquids
The solubility of carbon dioxide in three imidazolium-based ionic liquids, namely
Due to the complex peak pattern at the relevant Raman shift (see Figure 4), data analysis had to be changed slightly for all three ILs. For the purpose of this analysis, it was assumed that the solubility spectra are a linear combination of a pure carbon dioxide and a pure IL spectrum. The Raman spectrum of the respective IL in vacuum was therefore subtracted from each spectrum of the solubility measurements. In this way, the Fermi dyad was revealed, and the relevant peak area could be determined. However, since a small bulge could be seen in between the peaks of the Fermi dyad ( Figure 4B), it is possible that the carbon dioxide density was calculated with a larger uncertainty. Again, a shift of the investigated peak ((1380-1420) cm −1 ) was observed. However, the peak shift was dependent on the ionic liquid.

Results for Solubilty of Carbon Dioxide in Ionic Liquids
The solubility of carbon dioxide in three imidazolium-based ionic liquids, namely 1- Tf2N]), was investigated at T = 298.15 K. Literature data for all three ionic liquids is very scarce at p > 1.5 MPa and was not available for [Bmim][OTf] at p < 1 MPa. Measurements were still conducted in a pressure range from p = (0.5-5) MPa for all three ILs to obtain better comparability of the three ILs.

Butyl-3-methyl-imidazolium-trifluormethansulfonat ([Bmim][OTf]), 1-Butyl-3-methylimidazolium-hexafluorophosphat ([Bmim][PF6]), and 1-Butyl-3-methylimidazoliumbis(trifluormethylsulfonyl)imid ([Bmim][
Due to the complex peak pattern at the relevant Raman shift (see Figure 4), data analysis had to be changed slightly for all three ILs. For the purpose of this analysis, it was assumed that the solubility spectra are a linear combination of a pure carbon dioxide and a pure IL spectrum. The Raman spectrum of the respective IL in vacuum was therefore subtracted from each spectrum of the solubility measurements. In this way, the Fermi dyad was revealed, and the relevant peak area could be determined. However, since a small bulge could be seen in between the peaks of the Fermi dyad ( Figure 4B), it is possible that the carbon dioxide density was calculated with a larger uncertainty. Again, a shift of the investigated peak ((1380-1420) cm −1 ) was observed. However, the peak shift was dependent on the ionic liquid.  In contrast to water, solubility measurements of all ILs were possible at p < 0.5 MPa due to a higher solubility of carbon dioxide in ILs and, therefore, a better signal-to-noise ratio was obtained. As a result, measurements could be extended to a broader pressure range. The increased solubility of carbon dioxide in ILs in contrast to water was expected due to the quadrupole moment of carbon dioxide and its interaction with the ILs. Here, dispersion forces are likely to govern the solubility of the gas molecules [16]. Again, our results show good agreement with data found in the literature (see Figure 5) and are within the combined uncertainties of the measurement techniques, if available. A consistent data trend can be recognized for all isotherms. In contrast to water, solubility measurements of all ILs were possible at p < 0.5 MPa due to a higher solubility of carbon dioxide in ILs and, therefore, a better signal-to-noise ratio was obtained. As a result, measurements could be extended to a broader pressure range. The increased solubility of carbon dioxide in ILs in contrast to water was expected due to the quadrupole moment of carbon dioxide and its interaction with the ILs. Here, dispersion forces are likely to govern the solubility of the gas molecules [16]. Again, our results show good agreement with data found in the literature (see Figure 5) and are within the combined uncertainties of the measurement techniques, if available. A consistent data trend can be recognized for all isotherms.
As with water, the solubilities determined tend to higher values in comparison to the literature data. Since the measuring procedure that was applied was almost the same, additional vapor phase signals might be the cause of the offset here. This possible artefact will be studied further within the scope of our ongoing research.  [14,15]. Uncertainty values are not shown for clarity but are provided in Appendix B.
As with water, the solubilities determined tend to higher values in comparison to the literature data. Since the measuring procedure that was applied was almost the same, additional vapor phase signals might be the cause of the offset here. This possible artefact will be studied further within the scope of our ongoing research.
The combined expanded uncertainty for the solubility measurements in ILs was found to be significantly lower than in water; it ranges from U(xCO2,IL2) = (1.7-5)% and decreases with increasing pressure due to the clearer carbon dioxide signal. The uncertainty values determined for each ionic liquid are quite similar and vary mainly because of a difference in calibration. Detailed results for each (T, p) state point are presented in Appendix B.

Conclusion and Outlook
A new sensor for the determination of gas solubility in liquids is presented in this paper. Experimental (p, T, x) data for the solubility of carbon dioxide in water at T = (288. 15, 293.15, 298.15) K in a pressure range from p = (0.5-5) MPa and three ionic liquids at T = 298.15 K and pressures from p = (0.1-5) MPa are provided alongside a description of the experimental setup.
The successful application of Raman spectroscopy to solubility measurements opens the door to a rapid screening method, in particular for tailor-made liquids that can be used for specific gas separation processes. It offers short measurement times without the need for sample calibration prior to the experiments. Its measurement procedure and analysis are highly adaptive and can also be extended to solubility measurements of liquid mixtures in the near future. The measurements can be used to screen the samples even more efficiently when gas mixtures are utilized, since Raman spectroscopy can distinguish different gas species in the spectra. This is a clear advantage over conventional methods such as static methods that rely on gravimetric or volumetric analysis to determine the amount of dissolved gas.
The modular-built system can easily be improved with a different laser that offers a better stability and a high-resolution spectrometer. This would not only reduce the required measurement time but also impact the uncertainty of the measurements, since the quality of the spectra have the biggest impact on the results. An improved sample manifold that allows the flushing of the cell with an inert gas, e.g., helium, before each measurement would also benefit the quality of the results. Further improvements in the  [14,15]. Uncertainty values are not shown for clarity but are provided in Appendix B.
The combined expanded uncertainty for the solubility measurements in ILs was found to be significantly lower than in water; it ranges from U(x CO2,IL2 ) = (1.7-5)% and decreases with increasing pressure due to the clearer carbon dioxide signal. The uncertainty values determined for each ionic liquid are quite similar and vary mainly because of a difference in calibration. Detailed results for each (T, p) state point are presented in Appendix B.

Conclusions and Outlook
A new sensor for the determination of gas solubility in liquids is presented in this paper. Experimental (p, T, x) data for the solubility of carbon dioxide in water at T = (288. 15, 293.15, 298.15) K in a pressure range from p = (0.5-5) MPa and three ionic liquids at T = 298.15 K and pressures from p = (0.1-5) MPa are provided alongside a description of the experimental setup.
The successful application of Raman spectroscopy to solubility measurements opens the door to a rapid screening method, in particular for tailor-made liquids that can be used for specific gas separation processes. It offers short measurement times without the need for sample calibration prior to the experiments. Its measurement procedure and analysis are highly adaptive and can also be extended to solubility measurements of liquid mixtures in the near future. The measurements can be used to screen the samples even more efficiently when gas mixtures are utilized, since Raman spectroscopy can distinguish different gas species in the spectra. This is a clear advantage over conventional methods such as static methods that rely on gravimetric or volumetric analysis to determine the amount of dissolved gas.
The modular-built system can easily be improved with a different laser that offers a better stability and a high-resolution spectrometer. This would not only reduce the required measurement time but also impact the uncertainty of the measurements, since the quality of the spectra have the biggest impact on the results. An improved sample manifold that allows the flushing of the cell with an inert gas, e.g., helium, before each measurement would also benefit the quality of the results. Further improvements in the analysis involve consideration of the effect of dissolved gas on the density of the liquid [49,50], which was so far neglected during the data analysis.