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Supercritical CO2 Pipeline Hydraulic Calculator engineering
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Supercritical CO2 Pipeline Hydraulic Calculator

CCUS Infrastructure Engineering: Model non-linear dense-phase supercritical $CO_2$ fluid properties, frictional pressure gradients, and allowable pipeline transmission distance above the critical point.

Pipeline Flow & Sizing

Dense-Phase Operating Conditions

Pipeline Hydraulic Performance Output

Outlet Pressure P_out
-- bar
Total Pressure Drop ΔP
-- bar
Dense Phase Status
SUPERCRITICAL
Flow Velocity V
-- m/s
Dense-Phase Density ρ
-- kg/m³
Booster Station Need
--

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Dense-Phase Supercritical CO2 Pipeline Hydraulics

Long-distance pipeline networks transport captured carbon from emitter clusters to offshore or onshore geological storage hubs.

1. Frictional Gradient & Darcy-Weisbach Formulation

ΔP = f · ( L / D_inner ) · ( ρ · V² / 2 )
Re = ( ρ · V · D_inner ) / μ

2. Operating Pressure Corridor

P_operating > P_critical = 73.77 bar   (Strictly Single-Phase Dense Fluid)
P_max ≤ 0.72 · SMYS · ( 2 · t / D_outer )   (ASME B31.4 Hoop Stress Limit)

Frequently Asked Questions

Why is carbon dioxide transported in dense/supercritical phase in CCUS pipelines?

Gaseous $CO_2$ has low density ($\sim 2\,\text{kg/m}^3$), requiring impractically huge pipeline diameters. At pressures above $73.8\,\text{bar}$ and moderate temperatures ($10^\circ\text{C}-30^\circ\text{C}$), $CO_2$ enters a dense liquid-like supercritical phase with densities between $800$ and $950\,\text{kg/m}^3$ (nearly as dense as water) but maintaining gas-like low viscosity, allowing multi-million ton transport through standard $12$ to $24$-inch pipelines.

What is the danger of dropping below critical pressure in a CO2 pipeline?

If line pressure falls below the saturation envelope ($<73.8\,\text{bar}$), $CO_2$ flashes into two-phase liquid-vapor flow. This triggers severe flow slugging, cavitation in booster pumps, and dramatic Joule-Thomson refrigeration cooling that can drop steel temperatures below $-40^\circ\text{C}$, inducing brittle pipeline fracture.

What determines the spacing between CCUS booster pumping stations?

Booster stations are placed before the frictional pressure loss drops line pressure below the safe design minimum (typically $85\sim 90\,\text{bar}$, providing a $12\,\text{bar}$ safety buffer above the $73.8\,\text{bar}$ critical threshold). In flat terrain with a $135\,\text{bar}$ inlet, booster station spacing is typically 100 to 180 kilometers.