| name | neqsim-pressure-drop-screening |
| version | 0.1.0 |
| description | Educational single-phase line pressure-drop screening against a recommended pressure-gradient guideline. USE WHEN: a task needs a public, screening-level Darcy-Weisbach pressure-drop estimate and a check against NORSOK P-002 / GPSA style line pressure-gradient guidelines before detailed hydraulic design. |
| last_verified | 2026-06-18 |
| requires | {"python_packages":[],"java_packages":[],"env":[],"network":[]} |
Pressure Drop Screening
Use this skill for public, educational line pressure-drop screening. It estimates a single-phase Darcy-Weisbach pressure gradient and compares it to a recommended pressure-gradient guideline so an agent can flag lines that may exceed standard hydraulic limits before moving to validated line sizing.
When to Use
- When a user asks whether a line pressure drop sits within recommended limits.
- When an agent needs a quick pressure-gradient triage to scope a hydraulic or debottlenecking study.
- When examples must run without confidential piping classes, project line lists, or company piping specs.
Inputs
fluid_velocity: actual flowing velocity in the line in m/s.
mixture_density: flowing mixture density in kg/m3.
viscosity: flowing dynamic viscosity in Pa.s.
pipe_inner_diameter: pipe inner diameter in m.
length: line length used for the total pressure drop in m, default 100.0.
roughness: absolute pipe roughness in m, default 4.6e-5 (commercial steel).
guideline_bar_per_100m: recommended maximum pressure gradient in bar per 100 m, default 0.5.
Outputs
reynolds_number: flow Reynolds number.
friction_factor: Darcy friction factor from laminar or Haaland turbulent form.
dp_per_100m_bar: screening pressure gradient in bar per 100 m.
dp_total_bar: screening total pressure drop over the line length in bar.
guideline_ratio: ratio of the pressure gradient to the recommended guideline.
pressure_drop_warning: ok, watch, or high.
assumptions: public assumptions used by the placeholder model.
Engineering Method
The Python class PressureDropModel uses open, published correlations only:
- the Reynolds number uses the standard
Re = rho v D / mu form.
- the friction factor uses
f = 64 / Re in laminar flow and the public Haaland explicit approximation of the Colebrook equation in turbulent flow.
- the pressure gradient uses the Darcy-Weisbach form
dP/L = f (1/D) (rho v^2 / 2).
- the guideline ratio compares the pressure gradient to a configurable recommended gradient aligned with NORSOK P-002 and GPSA style line pressure-gradient guidelines.
This is educational and screening-only logic. It is not a piping standard, a line sizing method, a vendor method, a two-phase or transient hydraulic method, or a replacement for validated hydraulic design and a qualified process engineering review.
Python Usage Pattern
from pressure_drop_screening import PressureDropModel
model = PressureDropModel()
result = model.evaluate(
fluid_velocity=12.0,
mixture_density=50.0,
viscosity=1.2e-5,
pipe_inner_diameter=0.2,
length=100.0,
)
print(result.pressure_drop_warning)
print(result.dp_per_100m_bar)
print(result.guideline_ratio)
If the optional neqsim Python package is available, the result records that fact so an agent can recommend moving to validated NeqSim hydraulic models (for example PipeBeggsAndBrills) for real pressure-drop calculations. If it is not installed, the example still runs with public placeholder logic.
Related NeqSim Functionality
For validated pressure-drop calculations, redirect to existing NeqSim classes instead of this screening placeholder:
neqsim.process.equipment.pipeline.PipeBeggsAndBrills — Beggs and Brills multiphase pipe flow with elevation, holdup, and friction.
neqsim.process.equipment.pipeline.AdiabaticTwoPhasePipe and neqsim.fluidmechanics flow solvers — rigorous single and two-phase hydraulics.
neqsim.process.mechanicaldesign.heatexchanger.ThermalDesignCalculator — tube-side f L/D (rho v^2 / 2) pressure drop inside exchangers.
This skill is a public triage layer that decides when to invoke those validated models.
Validation Checklist
Common Mistakes
| Symptom | Cause | Fix |
|---|
| Pressure gradient looks too low | Density taken at standard rather than flowing conditions | Evaluate density at line pressure and temperature |
| Friction factor looks wrong near Re 2000 | Mixing laminar and turbulent forms at transition | Treat the transition band as approximate and validate with detailed hydraulics |
| Guideline never triggers | Guideline gradient set too high | Use a service-appropriate gradient per NORSOK P-002 / GPSA style limits |
Limitations
- No proprietary piping classes, project line lists, or company piping specs are included.
- No two-phase, slug, flashing, or transient pressure-drop modelling is performed.
- No fittings, valves, elevation, or acceleration pressure losses are included.
References