Abstract
A planar laser-induced fluorescence (PLIF) data treatment taking into account variations of the fluorescence extinction due to pH is presented. It is shown that the proposed method needs to be implemented when the product of extinction coefficient variations, path length travelled by the laser and fluorescence concentration become large as in large tank experiments. The influence of extinction coefficient variations has been evaluated on CO2 concentration measurement for a test case in the wake of a free rising bubble.
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Abbreviations
- δ :
-
Diffusive length scale (m)
- \(\varepsilon\) :
-
Molar extinction coefficient \({\left(\frac{{\text{L}}}{{\text{mol m}}}\right)}\)
- ϕ :
-
Quantum yield of the fluorescence
- A :
-
Fraction of the available light collected
- A sc :
-
Area of a spherical cap bubble (m2)
- a :
-
Semi-width of a bubble, (m)
- C :
-
Carbon dioxide molar concentration \( \left( {\frac{{{\text{mol}}}}{{{\text{m}}^{3} }}} \right) \)
- c :
-
Fluorescein molar concentration \( \left( {\frac{{{\text{mol}}}}{{{\text{m}}^{3} }}} \right) \)
- e :
-
Thickness of the laser beam (mm)
- \(F_{{{\text{CO}}_{2} }}\) :
-
Molecular gas flux \(F_{{{\text{CO}}_{2} }} = K_{{L{\text{CO}}_{2} }} \times (C_{{{\text{sat}}}} - C_{{{\text{CO}}_{2} ({\text{aq}})}} )\;\left( {\frac{{{\text{mol}}}}{{{\text{sm}}^{2} }}} \right)\)
- h :
-
Length of the vertical sides of the region of interest (ROI) (m)
- I 0 :
-
Initial light intensity (U.A.)
- I e :
-
Laser excitation intensity (U.A.)
- I f :
-
Fluoresced intensity (U.A.)
- k dehyd :
-
Dehydration rate of H2CO3 (\(\frac{1}{s}\))
- k hyd :
-
Hydration rate of CO2 (aq) (\(\frac{1}{s}\))
- k l :
-
Mass transfer coefficient (\(\frac{\text{m}}{\text{s}}\))
- L d :
-
Distance between the diverging lens and the camera field of view (m)
- L fluo :
-
Distance traversed by the laser beam in the fluorescent fluid to reach the considered element of the ROI (m)
- L s :
-
Length of the sampling volume along the incident beams (m)
- L w :
-
Width of the camera field of view (m)
- r :
-
Coordinate in the downstream direction along a beam of light (m)
- V b :
-
Bubble rising velocity (\(\frac{\text{m}}{\text{s}}\))
- k :
-
Pixel column position along the laser beam
- l :
-
Pixel column position along the laser beam
- pH:
-
Value of the parameter for a given pH
- ref:
-
Value of the parameter for a reference pH before measurements
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The authors would like to thank Microphyt SAS for funding part of this research.
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Appendices
Appendix 1: Reaction time
As written in Gibbons and Edsall (1963) about CO2 reaction kinetics with water : “although the acid–base equilibrium is essentially instantaneous, the dehydration rate of H2CO3 is relatively slow" implying that time to reach equilibrium for H2CO3 and pH may not be short enough to track CO2 concentration variations [cited in Asher and Litchendorf (2009)]. The kinetic of H2CO3/CO2 reaction has been modeled with the coupled differential equations system (7) where k dehyd is the dehydration rate of H2CO3 and k hyd is the hydration rate of CO2.
In (Asher and Litchendorf 2009), the system has been solved analytically with Maple using the source term \(F_{{{\text{CO}}_{2} }}\)/δ (where \(F_{{{\text{CO}}_{2} }}\) is the molecular gas flux and δ is a diffusive length scale of CO2) considered as a constant and applied during a given time referred to here as exposure time.
In order to find the time for the reaction to reach equilibrium, the system has been solved using the same reaction rates values as in (Asher and Litchendorf 2009). Nevertheless, the initial condition of the CO2 spot has been changed in order to have a more realistic contact with the bubble : The source term \(F_{{{\text{CO}}_{2} }}\) /δ has been modeled as a function of time. It was a shifted cosine of maximum \(F_{{{\text{CO}}_{2} }}\)/δ with a semi-period equal to the exposure time requisite to reach the maximum concentration of CO2 in the wake of the bubble determined from Fig. 7.
It is shown in Fig. 8 that for the used continuous source term, [CO2] t=t_e − [CO2] t=0 is very close to the integral of the source term \(\int_0^{t_e} \frac{F_{\text{CO}_2}(t)}{\delta} dt\) meaning that for initial given concentrations, the corresponding concentration evolutions are mainly related to the evolution of the different source terms. Therefore, the time to reach equilibrium is very close to the exposure time (1 ms). The presented analysis suggests that the reaction has been fully completed between two frames (10 ms).
Appendix 2: Intensity attenuation due to the diverging lens
The decreasing intensity due to the diverging lens has to be corrected during the extinction coefficient variation calibration as a function of pH. Assuming no fluorescent dye and a constant thickness of the laser sheet, and considering light flux conservation, the ratio of intensities (per unit area) received by two pixel columns k and l can be determined geometrically :
where I k and I l are the light intensities received by the pixels of two pixel columns k and l, belonging to the ROI, of respective height h k and h l . L w is the width of the camera observation area, and L d is the distance between this area and the diverging lens, as shown in Fig. (4).
This contribution has been taken into account in Eq. (6). As it is a constant for any pair of pixel columns, it has no influence on the extinction coefficient variations (\(\varepsilon_{\text{ref}} - \varepsilon\)) as a function of pH.
Appendix 3: Data acquisition and data treatment procedures
The data acquisition and data treatment procedures from the acquired fluorescence signal to CO2 concentration maps are presented in the following Fig. 9.
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Valiorgue, P., Souzy, N., Hajem, M.E. et al. Concentration measurement in the wake of a free rising bubble using planar laser-induced fluorescence (PLIF) with a calibration taking into account fluorescence extinction variations. Exp Fluids 54, 1501 (2013). https://doi.org/10.1007/s00348-013-1501-y
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DOI: https://doi.org/10.1007/s00348-013-1501-y