Submitted:
25 September 2024
Posted:
25 September 2024
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Abstract
Keywords:
1. Introduction
2. Methodology
2.1. Analytical Model for Assessment of the Continuous Pipeline Response under Longitudinal PGD
2.2. Deformation Capacity and Performance Limit States for the Steel Pipeline
2.2.1. Normal Operability Limit (NOL) State
2.2.2. The Pressure Integrity Limit (PIL) State
2.3. Validation of the Analytical Model
2.3.1. Finite Element Analysis of the Soil-Pipeline System
2.3.2. Comparison between Numerical and Analytical Solutions
2.4. Critical Soil Displacement (δcr) and Length (Lcr) for the Performance Limit States of the Operating Pipeline
2.5. Uncertainty Analysis
| Parameters | Units | Distribution | Mean or range | COV | |
|---|---|---|---|---|---|
| Pipe | Pressure, P | KPa | Uniform | [0, 5846.4] | |
| Temperature, T | °C | Uniform | [0, 50] | ||
| Yield strength, σy | MPa | Normal | 290 | 0.035 | |
| Cover depth, Hc | m | - | [1, 1.5, 2] | ||
| Soil | Soil friction reaction per unit pipe length, fs | KN/m | Normal | [19.2, 26.8, 34.4] | 0.3 |
| Relative soil-pipe displacement at friction sliding, u0 | mm | Normal | 3 | 0.3 |
- definition of the uncertain input parameters and their probability distributions,
- generation of a sample set of the system random variables, considering their probability distributions,
- evaluation of the pipeline displacement capacities, δt1, δt2, δc1, δc2, equal to the ground displacement level associated with the achievement of the pipeline performance limit states, using Equation (1), and the corresponding values of the critical soil length Lcr = (Ft,max−Fc,max)/fs.
- evaluation of the limit state functions, as the difference between the calculated system capacity (δcr,i, Lcr,i) and demand (δ, Lb) using Equations (5-8),
- evaluation of the indicator functions, I1i(δ, Lb) = (max(gt1) ≤ 0 ∪ max(gc1) ≤ 0), and I2i(δ, Lb) = (max(gt2) ≤ 0 ∪ max(gc2) ≤ 0), that are equal to the unity provided unsatisfactory performance for the normal operability and pressure integrity limit state, respectively, and zero otherwise.
- repetition of the steps (1) to (5) N times, to obtain N sample values of I1i(δ, Lb), I2i(δ, Lb), counting the unsatisfactory performance for the normal operability (NOL), and the pressure integrity limit (PIL) state, respectively,
- evaluation of the probability of exceedance of the normal operability (NOL), and the pressure integrity limit (PIL) state, for a given PGD intensity (δ, Lb), as the ratio between the total sum of I1i(δ, Lb) and I2i(δ, Lb) to the sample size N:
3. Fragility Surfaces

4. Global Sensitivity Analysis
5. Conclusions
Appendix A




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| i | F-interval | ΔL | Pipe axial force F |
|---|---|---|---|
| 1 | |||
| >1 |
| Parameters | Units | |
|---|---|---|
| Pipe diameter, D | 0.508 | m |
| Pipe wall thickness, t | 7.1 | mm |
| Pipe elastic modulus, E | 210 | GPa |
| Poisson's ratio, ν | 0.3 | |
| Pipe yield stress, σy | 290 | MPa |
| Pipe cover depth, Hc | 1.5 | m |
| Soil density, γ | 18.0 | kN/m3 |
| Soil friction angle, ϕ | 40 | ° |
| Pipe-soil interface friction angle, δi | 28 | ° |
| Soil pressure at rest, K0 | 1 | |
| Soil friction reaction per unit pipe length, fs | 26.8 | kN/m |
| Relative soil-pipe displacement at friction sliding, u0 | 3 | mm |
| Analysis method | Normal Operability Limit | Pressure Integrity Limit | |||
|---|---|---|---|---|---|
| Tension | Compression | Tension | Compression | ||
| δt1 (m) | δc1 (m) | δt2 (m) | δc2 (m) | ||
| Pressurized pipeline | numerical | 0.5706 | 0.0996 | 0.7835 | 0.4192 |
| analytical | 0.5710 | 0.1001 | 0.7854 | 0.4226 | |
| % difference | 0.06% | 0.51% | 0.24% | 0.81% | |
| conventional | 0.3440 | 0.2327 | 0.5179 | 0.3988 | |
| % difference | 65.90% | -57.18% | 51.30% | 5.09% | |
| Unpressurized pipeline | numerical | 0.3656 | 0.2200 | 0.5420 | 0.5738 |
| analytical | 0.3655 | 0.2199 | 0.5415 | 0.5773 | |
| % difference | -0.02% | -0.06% | -0.08% | 0.61% | |
| conventional | 0.3511 | 0.2069 | 0.5249 | 0.3917 | |
| % difference | 4.12% | 6.35% | 3.24% | 46.48% | |
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