| Literature DB >> 35915214 |
Charles R Carrigan1, Yunwei Sun2, Tarabay Antoun1.
Abstract
Radioactive gas signatures from underground nuclear explosions (UNEs) result from gas-migration processes occurring in the subsurface. The processes considered in this study either drive or retard upward migration of gases from the detonation cavity. The relative importance of these processes is evaluated by simulating subsurface transport in a dual-permeability medium for the multi-tracer Noble Gas Migration Experiment (NGME) originally intended to study some aspects of transport from a UNE. For this experiment, relevant driving processes include weak two-phase convection driven by the geothermal gradient, over pressuring of the detonation cavity, and barometric pumping while gas sorption, dissolution, radioactive decay, and usually diffusion represent retarding processes. From deterministic simulations we found that over-pressuring of the post-detonation chimney coupled with barometric pumping produced a synergistic effect amplifying the tracer-gas reaching the surface. Bounding simulations indicated that the sorption and dissolution of gases, tending to retard transport, were much smaller than anticipated by earlier laboratory studies. The NGME observations themselves show that differences in gas diffusivity have a larger effect on influencing upward transport than do the combined effects of tracer-gas sorption and dissolution, which is consistent with a Sobol' sensitivity analysis. Both deterministic simulations and those considering parametric uncertainties of transport-related properties predict that the excess in concentration of SF[Formula: see text] compared to [Formula: see text]Xe as might be captured in small volumetric samples should be much smaller than the order-of-magnitude contrast found in the large-volume gas samples taken at the site. While extraction of large-volume subsurface gas samples is shown to be capable of distorting in situ gas compositions, the highly variable injection rate of SF[Formula: see text] into the detonation cavity relative to that of [Formula: see text]Xe at the start of the field experiment is the most likely explanation for the large difference in observed concentrations.Entities:
Year: 2022 PMID: 35915214 PMCID: PMC9343667 DOI: 10.1038/s41598-022-16918-5
Source DB: PubMed Journal: Sci Rep ISSN: 2045-2322 Impact factor: 4.996
Figure 1Schematic of the representative elementary volume (REV) conceptualized in the simulations. The volume fraction of liquid and gas phases denotes the porosity while the volume ratio of liquid phase to the porosity is defined as saturation. The mass exchange between gas and solid phases is described by sorption/desorption and that between gas and liquid phases is described by phase equilibrium.
Figure 2Comparison between Henry’s type and Langmuir isotherms of xenon sorption in shale at 0 C. (a) Langmuir isotherm fits well with experimental data in the full concentration range ( [mol m]). (b) Henry’s type isotherm approximates experimental data in the low concentration range ( [mol m]). The solid curve (blue) represents the Langmuir fit while dashed (magenta) and dotted (black) lines are the Henry’s type fit and the linearized Langmuir fit when
Equivalent Henry’s absorption constant (, m kg) of xenon, argon, and SF in various geologic materials.
| Gas | T ( | Shale | Sandstone | Slate | Dolomite | Limestone | Tuff | Mean value |
|---|---|---|---|---|---|---|---|---|
| Xe | 0 | 1.97 × 10 | 5.37 × 10 | 2.30 × 10 | 2.32 × 10 | 3.18 × 10 | 4.91 × 10 | 5.55 × 10 |
| 20 | 1.03 × 10 | 3.89 × 10 | 8.46 × 10 | 1.86 × 10 | 1.01 × 10 | 8.83 × 10 | 2.71 × 10 | |
| Ar | 0 | 2.46 × 10 | 1.93 × 10 | 1.23 × 10 | 1.47 × 10 | 1.02 × 10 | 2.32 × 10 | 1.74 × 10 |
| 20 | 1.26 × 10 | 1.73 × 10 | 1.93 × 10 | 2.10 × 10 | 8.47 × 10 | |||
| SF | 0 | 8.38 × 10 | 3.93 × 10 | 3.51 × 10 | 1.75 × 10 | 4.71 × 10 | 4.46 × 10 | |
| 20 | 2.35 × 10 | 1.95 × 10 | 7.77 × 10 | 2.78 × 10 | 1.96 × 10 |
Figure 3Equivalent Henry’s absorption constant of xenon, argon, and SF in various geological materials at (a) 0 and (b) 20 C. Note that experimental data are unavailable for nonexistent bars.
Figure 4Phase equilibrium coefficient of argon, xenon, and SF as a function of temperature. Experimental data are referred to Ashton et al.[25], Cosgrove and Walkley[26] and Mroczek[28].
Sts that fit Eq. (5).
| Gas | Reference | ||||
|---|---|---|---|---|---|
| He | −41.4611 | 42.5962 | 14.0094 | Clever[ | |
| Ne | −52.8573 | 61.0494 | 18.9157 | Clever[ | |
| Ar | −57.6661 | 74.7627 | 20.1398 | Clever[ | |
| Kr | −66.9928 | 91.0166 | 24.2207 | Clever[ | |
| Xe | −74.7398 | 105.210 | 27.4664 | Clever[ | |
| SF | −126.315 | 170.186 | 50.9080 | 0.4190 | Ashton et al.[ |
| Cosgrove and Walkley[ | |||||
| Mroczek[ |
Figure 5Xenon signatures are delayed by radionuclide decay. (a) Xenon concentration in the source area. (b) Xenon concentration 100 m away from source area with a flow velocity of 2 [m d] and a dispersivity of 1.0 [m d].
Deterministic models with multiple physical processes (including basic processes of geothermal-gradient induced multiphase convection and diffusion).
| Process | Basic process | Delaying process | Driving process | ||
|---|---|---|---|---|---|
| Convection+Diffusion | Sorption | Dissolution | Overpressure | Barometric | |
| Model | (DF) | (SP) | (DS) | (OP) | pumping (BP) |
| ☑ | ☐ | ☐ | ☐ | ☐ | |
| 1 | ☑ | ☑ | ☐ | ☐ | ☐ |
| 2 | ☑ | ☐ | ☑ | ☐ | ☐ |
| 3 | ☑ | ☐ | ☐ | ☑ | ☐ |
| 4 | ☑ | ☐ | ☐ | ☐ | ☑ |
| 5 | ☑ | ☑ | ☑ | ☐ | ☐ |
| 6 | ☑ | ☐ | ☐ | ☑ | ☑ |
| ☑ | ☑ | ☑ | ☑ | ☑ | |
Figure 6Concentration profiles are plotted for (a) Ar, (b) SF, (c) Xe, and (d) Xe at the depth of 0.5 m which include radioactive decay. Single delaying or driving process models (#14) are compared with reference models (#0 and 7). Due to the minor driving effect of diffusion and the retarding effects of sorption and dissolution, concentration curves of all gases of models #0, 1, and 2 are overlapped slightly above x-axis.
Figure 7Using deterministic models, concentration profiles are plotted for (a) Ar, (b) SF, (c) Xe, and (d) Xe at the depth of 0.5 m. Although combined delaying or driving process models (#5, 6) are compared with reference models (#0 and 7), model #5 results are not plotted due to its negligible values.
Figure 8From deterministic models, the contribution of driving and retarding processes to concentration profiles is plotted for (a) Ar, (b) SF, (c) Xe, and (d) Xe at the depth of 0.5 m. The yellow region is the base-model (#0) profile, the red region shows the concentration difference between model #7 and model #6 indicating the effect of retarding processes (sorption and dissolution), and the cyan region shows the concentration difference between model #6 and model #0 indicating the effect of driving force (overpressure and barometric pumping).
Figure 9Probability densities of (a) Ar, (b) SF, (c) Xe, and (d) Xe relative concentrations at ground surface of Barnwell system.
Figure 10Sobol’ total sensitivity of Ar, Xe, and SF signals at ground surface of the Barnwell system. Sobol’ total sensitivities of (a) sorption, (b) dissolution, (c) overpressure, and (d) barometric pumping.
Figure 11Scaled Sobol’ sensitivity of Ar, Xe, and SF signals at ground surface of the Barnwell system. Sobol’ total sensitivities of (a) sorption, (b) dissolution, (c) overpressure, and (d) barometric pumping.