| Literature DB >> 33233584 |
Shaobiao Zhang1,2,3, Dayong Xu3,4, Gansu Shen3, Junguo Liu5, Lili Yang2.
Abstract
The mechanism of natural-hazard-triggered technological (Na-tech) cascading disasters is complex, and the extent to which their damage is aggravated by various secondary events is difficult to quantify. This study selected a large oil depot and constructed a full-scale three-dimensional scene model based on the surrounding geographical environment. The discrete element method (DEM), finite element method (FEM) and finite volume method (FVM) were employed to conduct numerical simulations of the process and consequences of the following Na-tech disasters: heavy-rainfall-induced landslide → blocks impacting an oil transportation pipeline and breaking it → oil leaking, spreading and resulting in a vapor cloud explosion. According to the results, the maximum impact of the 1 m3 of sliding mass formed in the landslide on the pipeline was over 7 MN (meganewton), and the pipeline fractured completely when it was loaded with a contact force of only 1.44 MN. The numerical simulation methods revealed the mechanism of Na-tech cascading disasters in a large oil depot and quantified the consequences of each event in the cascading disasters.Entities:
Keywords: cascading disaster; landslide; large oil depot; numerical simulation; vapor cloud explosion
Year: 2020 PMID: 33233584 PMCID: PMC7699817 DOI: 10.3390/ijerph17228620
Source DB: PubMed Journal: Int J Environ Res Public Health ISSN: 1660-4601 Impact factor: 3.390
Figure 1Slope conditions for an oil depot.
Figure 23D scene model of the study site: (a) Top view; (b) Side view.
Figure 3Model of slope and engineering structures.
Analysis of the Cases.
| Block Size Indicator | Case A | Case B | Case C |
|---|---|---|---|
| Maximum size/m3 | 1.42 | 2.40 | 3.70 |
| Minimum size/m3 | 0.18 | 0.38 | 0.37 |
| Mean size/m3 | 0.54 | 1.04 | 1.92 |
Parameters for contact mechanics.
| 1. Rigidity Conditions | |||||
|---|---|---|---|---|---|
| Normal Stiffness | Shear Stiffness | ||||
| kn/GPa | ks/GPa | ||||
| 5.0 | 2.5 | ||||
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| Adhesion C/MPa | Friction angle/o | Tensile strength σt/Mpa | Adhesion C/MPa | Friction angle/o | Tensile strength σt/MPa |
| 0.1 | 30 | 0 | 0 | 15 | 0 |
Figure 4Distribution of blocks at key time points (Case A).
Figure 5Influence of block size on block movement speed.
Figure 6Impact of blocks on pipelines across time: (a) Case A; (b) Case B; (c) Case C.
Figure 7Relationship between maximum impact and block size.
Figure 8Boundary condition and load.
Figure 9Time-history curve of impact.
Figure 10Equivalent stress.
Figure 11Deformation of the pipeline (51 ms).
Figure 12Gas leakage curve.
Grid size of leakage simulation.
| Region | Scale of Region | Grid Size/m | ||
|---|---|---|---|---|
| X | Y | Z | ||
| Inner core | XY: within the firewalls where the leaking pipeline was located (108 × 60 m)Z: 25 m above the ground | 0.5 | 0.5 | 0.3 |
| Outer core | XY: within the radius of 150 m | 1 | 1 | 1 |
| Noncore | Other regions | 5 | 5 | 5 |
Figure 13Process of gasoline leakage. (the photographs below contain a larger area than the upper).
Figure 14Explosion at t = 2.85 s.
Damage of overpressure to human.
| Overpressure/kPa | Area |
|---|---|
| 2–10 | Area of minor injury |
| 10–30 | Area of serious injury |
| ≥30 | Area of death |
Influence of overpressure on buildings and structures (equipment).
| Overpressure/kPa | Damage Description |
|---|---|
| 1.03 | Typical pressure for glass breakage |
| 17.2 | 50% destruction of home brickwork |
| 20.7–27.6 | Breakage of oil storage tanks |
| 34.5–48.2 | Nearly complete destruction of houses |
| 30,000 [ | Breakage of Liquified natural gas (LNG) storage tanks |
Figure 15Cross-section of overpressure distribution: (a) 19-m-altitude horizontal cross-section; (b) North–south cross-section; (c) East–west cross-section.
Figure 16Area of damage by explosion overpressure.