Best use case
piping-stress is best used when you need a repeatable AI agent workflow instead of a one-off prompt.
Skill for piping system stress analysis per ASME B31
Teams using piping-stress should expect a more consistent output, faster repeated execution, less prompt rewriting.
When to use this skill
- You want a reusable workflow that can be run more than once with consistent structure.
When not to use this skill
- You only need a quick one-off answer and do not need a reusable workflow.
- You cannot install or maintain the underlying files, dependencies, or repository context.
Installation
Claude Code / Cursor / Codex
Manual Installation
- Download SKILL.md from GitHub
- Place it in
.claude/skills/piping-stress/SKILL.mdinside your project - Restart your AI agent — it will auto-discover the skill
How piping-stress Compares
| Feature / Agent | piping-stress | Standard Approach |
|---|---|---|
| Platform Support | Not specified | Limited / Varies |
| Context Awareness | High | Baseline |
| Installation Complexity | Unknown | N/A |
Frequently Asked Questions
What does this skill do?
Skill for piping system stress analysis per ASME B31
Where can I find the source code?
You can find the source code on GitHub using the link provided at the top of the page.
SKILL.md Source
# Piping Stress Analysis Skill
## Purpose
The Piping Stress Analysis skill provides capabilities for analyzing piping system stresses per ASME B31 codes, ensuring code compliance and equipment protection through proper flexibility analysis.
## Capabilities
- Piping flexibility analysis
- Thermal expansion stress calculation
- Support and restraint design
- Nozzle load verification
- Flange leakage assessment
- Code compliance verification (B31.1, B31.3)
- CAESAR II integration
- Piping isometric review
## Usage Guidelines
### ASME B31 Code Overview
#### Code Selection
| Code | Application |
|------|-------------|
| B31.1 | Power piping |
| B31.3 | Process piping |
| B31.4 | Liquid transportation |
| B31.5 | Refrigeration piping |
| B31.8 | Gas transmission |
| B31.9 | Building services |
#### Stress Categories
```
B31.3 Stress equations:
Sustained stress:
S_L = (P*D)/(4*t) + (0.75*i*M_A)/Z <= S_h
Expansion stress:
S_E = sqrt(S_b^2 + 4*S_t^2) <= S_A
Occasional stress:
S_L + S_occ <= k*S_h
Where:
P = pressure
D = outside diameter
t = wall thickness
i = stress intensification factor (SIF)
M_A = sustained moment
Z = section modulus
S_h = hot allowable stress
S_A = allowable stress range
k = occasional load factor
```
### Thermal Expansion Analysis
#### Thermal Movement
```
Linear expansion:
delta_L = alpha * L * (T2 - T1)
Where:
alpha = coefficient of thermal expansion
L = pipe length
T2 - T1 = temperature change
Typical alpha values (in/in/F):
Carbon steel: 6.5 x 10^-6
Stainless steel: 9.5 x 10^-6
Copper: 9.3 x 10^-6
```
#### Flexibility Analysis
```
Key principles:
1. Piping expands when heated
2. Expansion induces stress if restrained
3. Flexibility (bends, loops) reduces stress
4. Over-constrained systems have high stress
5. Under-constrained systems have excessive movement
```
### Stress Intensification Factors
#### Common SIF Values
| Component | i-factor (approx) |
|-----------|------------------|
| Straight pipe | 1.0 |
| Long radius elbow | 0.9/h^(2/3) |
| Short radius elbow | 0.75/h^(2/3) |
| Miter bend (1 cut) | 1.52/h^(5/6) |
| Welding tee | 0.9/h^(2/3) |
| Reinforced fabricated tee | Variable |
| Branch connection | Variable |
```
Flexibility characteristic:
h = t*R/(r^2)
Where:
t = wall thickness
R = bend radius
r = mean radius of pipe
```
### Support Design
#### Support Types
| Type | Restrains | Allows |
|------|-----------|--------|
| Rest (shoe) | Vertical down | Horizontal, vertical up |
| Guide | Lateral | Axial, vertical |
| Anchor | All directions | None |
| Rod hanger | Vertical | Horizontal |
| Spring hanger | Vertical (variable) | Horizontal |
| Constant hanger | Vertical (constant) | Horizontal |
#### Support Spacing
```
Suggested maximum spans (B31.1):
| Pipe Size | Water (ft) | Steam/Gas (ft) |
|-----------|------------|----------------|
| 1" | 7 | 9 |
| 2" | 10 | 13 |
| 4" | 14 | 17 |
| 6" | 17 | 21 |
| 8" | 19 | 24 |
| 12" | 23 | 30 |
```
### Nozzle Loads
#### Equipment Protection
```
Nozzle load limits:
- Equipment vendor provides allowables
- Common standards: API 610, API 617, NEMA SM23
- Consider sustained and thermal loads separately
- Combined loads may use interaction formula
Typical check:
sqrt((F_x^2 + F_y^2 + F_z^2)/(F_allow^2) +
(M_x^2 + M_y^2 + M_z^2)/(M_allow^2)) <= 1.0
```
#### Load Combinations
```
Operating case:
W + P + T + D
Hydrotest case:
W + H + D
Where:
W = Weight
P = Pressure
T = Thermal
D = Displacement
H = Hydrotest pressure
```
### Flange Leakage
#### Assessment Methods
```
ASME B16.5 flange rating:
- Check P-T rating at operating conditions
- Include pressure equivalent from moments
Equivalent pressure method:
P_eq = P + (16*M)/(pi*G^3)
Where:
M = bending moment at flange
G = flange gasket diameter
NC(T)MF method:
Uses ASME VIII Appendix 2 calculations
More accurate for high moment cases
```
### Modeling Guidelines
#### Model Building
```
Key elements:
1. Include all pipe runs
2. Model equipment properly (rigid/flexible)
3. Define support locations accurately
4. Include all branch connections
5. Apply correct operating conditions
6. Model spring hangers if used
```
#### Operating Cases
| Case | Temperature | Pressure | Weight | Use |
|------|-------------|----------|--------|-----|
| Sustained | Ambient | Design | Full | Code check |
| Operating | Operating | Operating | Full | Equipment loads |
| Thermal | Operating-Ambient | None | None | Expansion stress |
| Hydrotest | Ambient | Test | Full + Water | Support design |
## Process Integration
- Related to structural analysis for piping systems
## Input Schema
```json
{
"piping_system": {
"line_number": "string",
"code": "B31.1|B31.3",
"material": "string",
"size": "string (NPS)",
"schedule": "string"
},
"operating_conditions": {
"design_pressure": "number (psig)",
"design_temperature": "number (F)",
"operating_pressure": "number (psig)",
"operating_temperature": "number (F)"
},
"geometry": {
"isometric": "file reference",
"length": "number (ft)",
"elevation_change": "number (ft)"
},
"equipment_connections": [
{
"equipment": "string",
"nozzle": "string",
"allowable_loads": "object"
}
]
}
```
## Output Schema
```json
{
"stress_results": {
"code_compliance": "pass|fail",
"sustained_stress": {
"max_value": "number (psi)",
"allowable": "number (psi)",
"location": "string",
"ratio": "number"
},
"expansion_stress": {
"max_value": "number (psi)",
"allowable": "number (psi)",
"location": "string",
"ratio": "number"
}
},
"nozzle_loads": [
{
"equipment": "string",
"forces": "array [Fx, Fy, Fz]",
"moments": "array [Mx, My, Mz]",
"compliance": "pass|fail"
}
],
"support_schedule": [
{
"location": "string",
"type": "string",
"load": "number (lb)"
}
],
"thermal_movements": {
"max_displacement": "number (in)",
"location": "string"
},
"recommendations": "array"
}
```
## Best Practices
1. Start with proper piping layout for flexibility
2. Verify equipment nozzle allowables early
3. Include all weight loads (insulation, contents)
4. Model actual support conditions
5. Check flange ratings at all operating conditions
6. Document all assumptions and simplifications
## Integration Points
- Connects with Pressure Vessel Design for equipment interface
- Feeds into Support design for structural requirements
- Supports FAI Inspection for as-built verification
- Integrates with Design Review for approvalRelated Skills
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