🧪 Non-Newtonian Yield-Pseudoplastic Hydraulics (Herschel-Bulkley)

Calculate non-Newtonian yield-pseudoplastic pipe flow using Herschel-Bulkley 3-parameter model: pipe pressure drop (kPa), wall shear stress (tau_w), solid unyielded plug core radius (rp), and generalized Reynolds number.

⚡ Fortran 90 Engine Double Precision (IEEE 754) ✓ ISO / ASME Validated

📊 Solver Telemetry ● ACTIVE

👁️ Consultations 31

⚡ Calculs faits 28

💾 Téléchargements 284 📦 Code Fortran 4.5 KB

📅 Mise en service Jun 2026

⏱️ Latence < 1 ms

🧪 Yield-Pseudoplastic Plug Flow Velocity Profile

Real-time visual simulation: Unyielded solid plug core ($r \le r_p$) surrounded by sheared boundary layer

📝 Configuration & Presets

🛢️ Bentonite Mud (τy = 12 Pa) ⛏️ Mining Tailings Slurry 🍅 Concentrated Tomato Paste 🧴 Carbopol Hydrogel

🔬 Herschel-Bulkley Rheology Parameters

Yield Stress τ_y [Pa]:

Consistency Index K [Pa·sⁿ]:

Flow Behavior Index n: <1: Shear-thinning, =1: Bingham, >1: Dilatant

Fluid Density ρ [kg/m³]:

📏 Pipe Dimensions & Target Flow

Pipe Inner Diameter D [mm]:

Pipe Length L [m]:

Volumetric Flow Rate Q [m³/h]:

Herschel-Bulkley Constitutive Equation:
• Rheology Law: τ = τ_y + K · (γ̇)ⁿ (for τ > τ_y)
• Wall Shear Stress: τ_w = ΔP · D / (4 L) [Pa]
• Unyielded Plug Core Radius: r_p = R · (τ_y / τ_w) [mm]
• Generalized Reynolds: Re_gen = ρ · V²⁻ⁿ · Dⁿ / [ K · ((3n+1)/4n)ⁿ · 8ⁿ⁻¹ ].

📊 Hydraulics Results

📊 Output Summary
💾 Fortran Source

Total Pipe Frictional Pressure Drop

981.07 kPa (9.811 bar)

Wall Shear τ_w: 73.58 Pa | Plug Radius r_p: 28.5 mm

LAMINAR (UNYIELDED PLUG CORE)

Solid Plug Core Radius (r_p) 28.5 mm Pipe Radius R = 75.0 mm

Unyielded Plug Area Fraction 14.5 % Central rigid moving core

Wall Shear Stress (τ_w) 73.6 Pa Yield Ratio τ_y/τ_w = 0.381

Generalized Reynolds (Re_gen) 517 Transition at ~2100

📈 Pipe Pressure Drop ΔP (kPa) vs Flow Rate Q (m³/h)

📉 Plug Radius rp (mm) vs Yield Stress τy (Pa)

=================================================================
 THERMOFLUIDCALC — HERSCHEL-BULKLEY HYDRAULICS REPORT
=================================================================
Case Title                 : Mining Bauxite Tailings High-Density Slurry
Rheology Law Parameters    : tau_y = 28.00 Pa, K = 3.500 Pa.s^n, n = 0.550 (Density = 1600.0 kg/m3)
Piping Dimensions          : ID = 150.0 mm, Length = 500.0 m, Target Flow Q = 80.00 m3/h
-----------------------------------------------------------------
TOTAL PIPE PRESSURE DROP   : 981.07 kPa (9.8107 bar)
Wall Shear Stress (tau_w)  : 73.58 Pa
Unyielded Plug Radius (rp) : 28.54 mm (14.5 % of pipe cross-section)
Generalized Reynolds Number: 516.6
PREDICTED FLOW REGIME      : LAMINAR (UNYIELDED PLUG CORE)
=================================================================

📘 Calculation Methodology & Herschel-Bulkley Rheology

Unified 3-Parameter Rheology

Herschel-Bulkley is the most versatile non-Newtonian model. It reduces to Newtonian fluid ($\tau_y=0, n=1$), Power-Law fluid ($\tau_y=0$), and Bingham plastic ($n=1$).

Plug Flow Phenomenon

Near the pipe centerline, shear stress $\tau(r) \le \tau_y$, causing the fluid to move as a rigid unsheared solid cylinder (plug) at uniform maximum velocity.

Key Engineering Assumptions

Fully developed, steady isothermal laminar/transitional pipe flow.
Darby / Metzner-Reed generalized Reynolds formulations.
Applicable to drilling fluids, mining tailings, polymer pastes, and food purees.

ThermoFluidCalc Engineering Report