11th International GeoRaman Conference (2014) 5040.pdf Experimental determination of CO2 diffusion coefficient in aqueous solutions under pressure via Raman spectroscopy at room temperature: impact of salinity (NaCl) on dissolved CO 2 diffusivity. C. Belgodere1,2* ,J. Dubessy1**, J. Sterpenich1, J. Pironon1, D. Vautrin3, M.C. Caumon1, P. Robert1, A. Randi1 and J.P. Birat4, 1 Universite de Lorraine, CNRS, Georessources Laboratory, BP 70239, F-54506, Vandoeuvre-LesNancy, France, 2CREGU, BP 70023, 54501, BP 30320, F-57283, Vandoeuvre-Les-Nancy, France, 3 IRCCyN, Ecole Centrale de Nantes, 1 rue de la Noë, 44321, Nantes, France, 4 formerly : ArcelorMittal, now : ESTEP, 172 avenue de Cotenbergh, Bruxelles, Belgique. * :[email protected], ** : [email protected] Introduction: The diffusivity rate of dissolved CO2 in aqueous solutions is a key parameter to predict CO2 migration in reservoirs and leakage through caprock in the context of greenhouse gas geological storage in saline aquifers. [1] [2]. Among the different experimental techniques, in situ Raman Spectroscopy in horizontal Fused Silica Capillary (FSC) is a powerful technique to determine CO2 diffusion coefficients at different pressures and temperatures in the absence of advection contribution [3]. Most of the previous experimental investigations were dedicated to the study of the influence of temperature on CO2 diffusivity, at atmospheric pressure and in pure water. While influence of pressure remains unclear, collection of available data [4] shows unambiguous relationship between temperature and CO 2 diffusivity even at temperatures as high as 100°C [3]. The impact of salinity is poorly documented([5];[6];[7]) but show a decrease of the diffusion coefficient with increasing salinity. Aqueous solution of saline aquifers may display a wide range of salinities from 0 to 7 molNaCl.kg-1 H2O [8]. Considering the scattering of experimental data of CO2 diffusion coefficient versus brine salinity, this study was focused on the salinity (NaCl) dependence of CO2 diffusion over from 0 to 6 molNaCl.kg-1 H2O, using Raman spectra of an aqueous solution loaded in a High-Pressure Optical Cell (HPOC, ([3] [9],[10],) at controlled CO2 pressure. Materials and Methods Pressurization device and Fused Silica Capsules Seven experiments, on the range of salinity from 0 to 6 molNaCl.kg-1 H2O, were performed at 21±1°C and 40 bar, in capillary with infiling length higher than 17 mm [11,12,13]. The capillary was fixed to the x-y micrometric moving stage and horizontally placed under the optical microscope of the spectrometer to record Raman spectra in the liquid phase at different distances to the liquid/vapor interface. Raman spectra acquisition Collection conditions of Raman spectra of the CO2 Fermi resonance dyad and the bending mode of H 2O in the 1200-1900 cm-1 spectral range were the following: Labram-HR spectrometer (® Horiba Jobin-Yvon), exciting radiation (0 = 514.532 nm; W0 = 60 mW), exposition time of 30 s, 4 accumulations. Raman spectra were acquired sequentially over 12 hours. The Raman peak areas of the 2ν2(CO2) and of the ν2(H2O) bands (ACO2/AH2O) are considered to be proportional to dissolved CO2 concentration in the molality scale. Numerical determination of diffusion coefficient CO2 diffusion from vapor / liquid interface to the aqueous phase was treated as a one-dimensional diffusion process and modelled using the Fick’s second law. For convenience, (ACO2/AH2O) are normalized with (ACO2/AH2O)° value at 0.03 mm from the interface and at equilibrium to define the variable Rnorm and results in second Fick’s law: (1) CO2 diffusion coefficients in the aqueous solution were determined fitting experimental data with a numerical solution of the second Fick’s law using the least square method and a finite difference numerical method modified after Lu et al., 2006, 2013([10],[3]). Results Figure 1 shows the evolution of the Raman spectra with time and distance from vapor CO2/ aqueous solution interface in the pure water case. Figure 1: a) Raman spectra collected at different times after silica capillary pressurization by gaseous CO2 (40 bar, 21°C, pure water) at 11.025 ± 0.001 mm from the CO2/H2O interface at t = 0. b) Raman spectra collected at different distances from the CO2/H2O interface at t = 375 min after silica capillary pressurization (pure water). Figure 2 shows the evolution of Rnorm in time and space for the 3 molNaCl.kg-1 H2O solution. The asymptotic shape versus time for a given distance is clearly evidenced even for short diffusion distances. Abstract for 11th GeoRaman International Conference, June 15-19, 2014, St. Louis, Missourri, USA 11th International GeoRaman Conference (2014) 5040.pdf diffusive transport of CO2 through cover rock and its consequence on CO2 storage integrity. Figure 2: Evolution of the normalized ratio Rnorm versus time at different distances from the CO2/H2O interface as - (PCO2=40 bar and T =21±1°C) for the 3 molNaCl.kg-1 H2O solution. Discussion The diffusion coefficient of CO2 in pure water at 21±1°C and 40 bar calculated from the present experimental study is 1.71×10-9m2.s-1, a value in good agreement with previous studies (D°CO2 (20°C, 1 bar) = 1.66 ×10-9m2.s-1 ). The diffusion coefficient linearly decreased with increasing salinity between 0.0 and 6.0 molNaCl.kg-1 H2O (Figure 3) and is in good agreement with the results of name-here[5] and name-here[6] determined at 1 bar. The diffusion coefficient determined in these two studies are slightly higher than in the present work, probably because of a working temperature of 25°C. Moreover, our results agree with the Wilke-Chang ([14]) theoretical model calculated at temperature of 21°C and a pressure of 40 bar. Acknowledgements: This work was carried out as part of Clement Belgodere PhD Thesis supported by ArcelorMittal, CREGU, CNRS, Universite de Lorraine, Nancy, France, and CGSµLab ANR-12-SEED-0001. This work has been performed while the first and fifth author were PhD students at Georessources laboratory/ CREGU/ CNRS/ Universite de Lorraine, Nancy, France and IRccyN, Ecole Centrale de Nantes, Nantes, France, respectively. References: [1] Lindenberg, E. B. and Wessel-Berg, B. (1997) Ener. Conv. Manag., 38, 229–234. [2] Fleury, M. et al., (2011) Ener. Proc., 4,5227-5234. [3] Lu, W. et al., (2013). Geoch. Cosmochim. Acta, 115, 183–204. [4] Mutoru, J. W. et al., (2013). AlChe Journal, 57, 1617– 1627. [5] Ratcliff, G. A. and Holdcroft, J. G., (1963). Trans. Instn. Chem. Engrs., 41, 315–319. [6] Hikita, H. et al., (1979). Chem. Eng. Journ., 17, 77–80. [7] Sell, A. et al., (2013). Env. Sci. Tech., 47, 71–78. [8] Wang, Z. et al., (2013). Env. Sci. Tech., 47, 1407–1415. [9] Chou, I. M. et al., (2005). Adv. High. Tech. Geoph. Appl. Elsevier Amsterdam., pp. 475–485. [10] Lu, W. et al., (2006). Appl. Specrt., 60, 122–129. [11] Chou, I. M. et al., (2008). Geochim. Cosmochim. Acta, 72, 5217 -5231. [12] Ong, A. et al., (2013). Geofluids Journ., 13, 298–304. [13] Caumon, M.C. et al., (2013). Eur. Journ. Min., 13, 935–1221. [14] Wilke, C.R. and Chang, P. (1955). AlChE Journal, 1, 264–270. Figure 3: Comparison of the diffusion coefficient of dissolved CO2 determined in this study with previous literature data. Conclusion The experimental device in this study was adapted from Lu et al., 2006, 2013([10],[3]).and successfully applied to high NaCl concentrated aqueous solutions. It confirms that microfluidic techniques coupled with Raman spectrometry may be a route for studying physical-chemical parameters of fluids. Further analytical calculations will demonstrate the impact of salinity on Abstract for 11th GeoRaman International Conference, June 15-19, 2014, St. Louis, Missourri, USA
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