๐งช 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.
โก Fortran 90 Engine
Double Precision (IEEE 754)
โ ISO / ASME Validated
๐ Solver Telemetry
โ ACTIVE
๐๏ธ Views
31
โก Solves
28
๐พ Downloads
374
๐ฆ Fortran Code
4.5 KB
๐
Released
Jun 2026
โฑ๏ธ Latency
< 1 ms
๐งช Yield-Pseudoplastic Plug Flow Velocity Profile
Real-time visual simulation: Unyielded solid plug core ($r \le r_p$) surrounded by sheared boundary layer๐ Configuration & Presets
๐ข๏ธ Bentonite Mud (ฯy = 12 Pa)
โ๏ธ Mining Tailings Slurry
๐
Concentrated Tomato Paste
๐งด Carbopol Hydrogel
Herschel-Bulkley Constitutive Equation:
โข Rheology Law: ฯ = ฯy + K ยท (ฮณฬ)n (for ฯ > ฯy)
โข Wall Shear Stress: ฯw = ฮP ยท D / (4 L) [Pa]
โข Unyielded Plug Core Radius: rp = R ยท (ฯy / ฯw) [mm]
โข Generalized Reynolds: Regen = ฯ ยท V2โn ยท Dn / [ K ยท ((3n+1)/4n)n ยท 8nโ1 ].
โข Rheology Law: ฯ = ฯy + K ยท (ฮณฬ)n (for ฯ > ฯy)
โข Wall Shear Stress: ฯw = ฮP ยท D / (4 L) [Pa]
โข Unyielded Plug Core Radius: rp = R ยท (ฯy / ฯw) [mm]
โข Generalized Reynolds: Regen = ฯ ยท V2โn ยท Dn / [ K ยท ((3n+1)/4n)n ยท 8nโ1 ].
๐ Hydraulics Results
Configure inputs and click Compute to view results.
๐ 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.