Probabilistic Analysis of Floods from Tailings Dam Failures: A Method to Analyze the Impact of Rheological Parameters on the HEC-RAS Bingham and Herschel-Bulkley Models
Abstract
:1. Introduction
2. Materials and Methods
2.1. Mathematical Rheological Models and Parameterization
2.2. Parameter Intervals and Sampling
2.3. Automation of Sensitivity Analysis in HEC-RAS
2.4. Case Study: The Hydrodynamic Model
Parameters | Data | Froehlich [64] |
---|---|---|
Failure Mode | Overflow | |
Total volume (Vw) (1.000 m3) | 38,276.34 | |
Average breach width (Bm) (m) | 116.27 | |
Minimum breach width (m) | 55.27 | |
Elevation of the dam crest (m) | 272.00 | |
Elevation of the base of the dam (m) | 211.00 | |
Elevation of the bottom of the breach (m) | 211.00 | |
Dam height (m) | 61.0 | |
Height of the breach (Hb) (m) | 61.0 | |
Time of breach formation (h) | 0.54 | |
Left Lateral Slope (H:1V) | 1.0 | |
Right Side Slope (H:1V) | 1.0 | |
Mode of progression | Sine Curve |
3. Results
3.1. Probabilistic Maps Related to Flooded Areas
3.2. Arrival Times and Maximum Depth Variation along the Valley
3.3. Rheological Parameters vs. Simulated Areas
3.4. Rheological Parameters vs. Hmean
4. Discussion
5. Conclusions and Recommendations
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
Appendix A
Parameter [Unit] | Parameter Range | Reference | Tailings | Test/Method | Rheological Model/Fitted Equation |
---|---|---|---|---|---|
Volumetric concentration of solids (Cv) [%] | 21.21–35.78 | [47] | Coal | n.a. | n.a. |
27.98–46.65 | [47] | Copper | |||
36.50–38.62 | [47] | Gold | |||
36.34–44.62 | [47] | Lithium | |||
11.09–19.66 | [47] | Nickel | |||
25.48–31.25 | [47] | Uranium | |||
11.82–50.11 | [47] | Zinc | |||
18.0–52.5 | [7] | Base metal | |||
21.8–55.3 | [48] | Iron | |||
32.5–65.0 | [48] | Iron | |||
9.3–48.4 | [9] | Gold | |||
34.75–57.14 | [49] | Iron | |||
58 | [2] | Iron | |||
47 | [37] | Iron | |||
23 | [52] | Iron | |||
Maximum volumetric concentration of solids (Max Cv) [%] | 61.5 | [53] | - | - | n.a. |
53 | [7] | Base metal | - | ||
49.0–62.0 * | [50] | Copper | [67] ** | ||
59.9–76.5 * | [51] | Iron | [67] ** | ||
57.3–68.0 * | [51] | Gold | [67] ** | ||
Dynamic viscosity (μ) [Pa∙s] | 0.03–0.49 | [7] | Base metal | Viscometer | Bingham |
0.15–2.69 | [48] | Iron | Viscometer | Bingham | |
0.002–0.311 | [9] | Gold | Viscometer | Bingham | |
0.0071–0.4457 | [49] | Iron | Rheometer | Quadrática | |
1.09–1.46 | [8] | Pyrophyllite | Rheometer | Bingham | |
50 | [37] | Iron | Calibration | Bingham | |
30.0–100.0 | [38] | Iron | Calibration | Full Bingham | |
Yield stress (τy) [Pa] | 2.122–48.535 | [47] | Coal | Viscometer | Herschel-Bulkley |
0.641–93.50 | [47] | Copper | Viscometer | Herschel-Bulkley | |
0.6–1.5 | [47] | Gold | Viscometer | Herschel-Bulkley | |
1.048–11.165 | [47] | Lithium | Viscometer | Herschel-Bulkley | |
1.564–37.110 | [47] | Nickel | Viscometer | Herschel-Bulkley | |
2.769–9.411 | [47] | Uranium | Viscometer | Herschel-Bulkley | |
0.652–100.260 | [47] | Zinc | Viscometer | Herschel-Bulkley | |
26.0–638.0 | [7] | Base metal | Viscometer | Bingham | |
19.36–602.82 | [48] | Iron | Viscometer | Bingham | |
59.59–2396.53 *** | [48] | Iron | Slump test | Bingham | |
0.5–181.0 | [9] | Gold | Viscometer | Bingham | |
0.085–118.0 | [49] | Iron | Rheometer | Quadrática | |
12.0–23.0 | [8] | Pyrophyllite | Rheometer | Herschel-Bulkley | |
9.7–251.9 | [27] | Synthetic | Rheometer | Herschel-Bulkley | |
100.0–1000.0 | [37] | Iron | Calibration | Bingham | |
750.0–1000.0 | [38] | Iron | Calibration | Full Bingham | |
a [Pa] | 1 | [7] | Base metal | Viscometer | Exponential |
21.381 | [48] | Iron | Viscometer | ||
0.0065 | [48] | Iron | Slump test | ||
0.08 | [52] | Iron | Calibration | ||
1.00 × 10−7 | [49] | Iron | Rheometer | ||
~0.04–3.40 | [10] | Copper | Rheometer | ||
~0.40–3.45 | [10] | Iron | Rheometer | ||
b [-] | 12.2 | [7] | Base metal | Viscometer | Exponential |
90.874 | [48] | Iron | Viscometer | ||
20.47 | [48] | Iron | Slump test | ||
40 | [52] | Iron | Calibration | ||
39.278 | [49] | Iron | Rheometer | ||
~1.2–5.0 | [10] | Copper | Rheometer | ||
~1.2–5.5 | [10] | Iron | Rheometer | ||
Consistency index (K) [Pa∙sn] | 0.034–6.409 | [47] | Coal | Viscometer | Herschel-Bulkley |
0.008–130.0 | [47] | Copper | Viscometer | ||
0.108–0.221 | [47] | Gold | Viscometer | ||
0.222–1.515 | [47] | Lithium | Viscometer | ||
0.154–2.001 | [47] | Nickel | Viscometer | ||
0.065–0.097 | [47] | Uranium | Viscometer | ||
0.428–14.720 | [47] | Zinc | Viscometer | ||
0.69–1.96 | [8] | Pyrophyllite | Rheometer | ||
Flow behavior index (n) [-] | 0.4–1.0 | [47] | Coal | Viscometer | Herschel-Bulkley |
0.192–1.347 | [47] | Copper | Viscometer | ||
0.705–0.744 | [47] | Gold | Viscometer | ||
0.766–1.020 | [47] | Lithium | Viscometer | ||
0.450–0.602 | [47] | Nickel | Viscometer | ||
0.742–0.913 | [47] | Uranium | Viscometer | ||
0.306–0.577 | [47] | Zinc | Viscometer | ||
0.84–1.14 | [8] | Pyrophyllite | Rheometer | ||
0.50–1.50 | [37] | Teórico | Calibration |
Appendix B
Appendix C
Specification | Bingham | Herschel-Bulkley H-B |
---|---|---|
Model area | 69.8 km2 | |
2D mesh resolution | 40 m on the slope centerline in the embedded valley 100 m in the downstream lake 50 m for the rest of the model | |
Number of template cells | 21,148 | |
Equation | Shallow Water Equations | |
Simulation time frame | 20 h | |
Maximum number of computational iterations | 20 | |
Computational Interval | Adjustable based on Courant: maximum = 1.0; minimum = 0.45 1.0–16.0 s | |
Machine used | Processor AMD Ryzen 7 3700X. 8-Core. 3.6 GHz processing speed (4.4 GHz Turbo). 16 GB DDR4 RAM and 4 GB/s M,2 SSD | AMD Ryzen 3 3200G. 4-Core. 3.6 GHz processing speed. 8 GB DDR4 RAM and 6 GB/s Sata SSD |
Average time per simulation | 3.233 min/simulation | 5.284 min/simulation |
Appendix D
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Rheological Model | Varied Parameters | Literature Value Ranges | Adopted Interval |
---|---|---|---|
Bingham | Cv (%) | 9.3–65.0 | 20.0–60.0 |
Max Cv (%) | 49.9–76.5 | 49.0–61.5 | |
a (Pa) | 0.0000001–3.45 | 0.067–3.450 | |
b | 1.2–40.0 | 1.2–10.359 | |
Herschel-Bulkley (H-B) | Cv (%) | 20.0–60.0 | |
τy (Pa) | 0.6–251.9 | ||
K (Pa∙sn) | 0.008–130.0 | ||
n | 0.192–1.5 |
Results/Parameters | Bingham | Herschel H-B | |||||||
---|---|---|---|---|---|---|---|---|---|
Cv | Max Cv | a | b | Cv | τy | K | n | ||
Hmean | Region A1 | 0.4777 | 0.052 | 0.4357 | 0.6902 | −0.2728 | 0.8255 | 0.4149 | 0.1937 |
Region A2 | 0.4737 | 0.064 | 0.4323 | 0.6896 | −0.2667 | 0.9317 | 0.2096 | 0.0881 |
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Melo, M.; Eleutério, J. Probabilistic Analysis of Floods from Tailings Dam Failures: A Method to Analyze the Impact of Rheological Parameters on the HEC-RAS Bingham and Herschel-Bulkley Models. Water 2023, 15, 2866. https://doi.org/10.3390/w15162866
Melo M, Eleutério J. Probabilistic Analysis of Floods from Tailings Dam Failures: A Method to Analyze the Impact of Rheological Parameters on the HEC-RAS Bingham and Herschel-Bulkley Models. Water. 2023; 15(16):2866. https://doi.org/10.3390/w15162866
Chicago/Turabian StyleMelo, Malena, and Julian Eleutério. 2023. "Probabilistic Analysis of Floods from Tailings Dam Failures: A Method to Analyze the Impact of Rheological Parameters on the HEC-RAS Bingham and Herschel-Bulkley Models" Water 15, no. 16: 2866. https://doi.org/10.3390/w15162866
APA StyleMelo, M., & Eleutério, J. (2023). Probabilistic Analysis of Floods from Tailings Dam Failures: A Method to Analyze the Impact of Rheological Parameters on the HEC-RAS Bingham and Herschel-Bulkley Models. Water, 15(16), 2866. https://doi.org/10.3390/w15162866