๐ŸŒช๏ธ Fluidized Bed Hydrodynamics & Minimum Fluidization

Calculate gas-solid fluidized bed hydrodynamics: minimum fluidization velocity (Umf), terminal free-fall velocity (Ut), Archimedes number, Geldart particle classification, and bed pressure drop.

โšก Fortran 90 Engine Double Precision (IEEE 754) โœ“ ISO / ASME Validated
Fluidized Bed Hydrodynamics & Minimum Fluidization Fluid Mechanics
๐Ÿ“Š Solver Telemetry โ— ACTIVE
๐Ÿ‘๏ธ Views 38
โšก Solves 32
๐Ÿ’พ Downloads 475 ๐Ÿ“ฆ Fortran Code 4.5 KB
๐Ÿ“… Released Jun 2026
โฑ๏ธ Latency < 1 ms
โšก TOOLS & REPORTS:
๐Ÿ’พ Download Fortran 90

๐ŸŒช๏ธ Gas-Solid Fluidized Bed Hydrodynamics & Bubble Eruption

Real-time visual simulation: Gas distributor grid, particle bed expansion, and rising void bubbles

๐Ÿ“ Configuration & Presets

๐Ÿ”ฅ Sand Combustor (Geldart B) โšก FCC Regenerator (Geldart A) ๐Ÿชต Biomass Gasifier (Geldart D) ๐Ÿ’Š Pharma Batch Dryer
๐Ÿ”ฌ Solid Particle Properties
1.0 for spherical beads, ~0.85 for sand
๐Ÿ’จ Fluidizing Gas State & Velocity
๐Ÿ“ Bed Column Dimensions
Wen & Yu / Ergun Fluidization Formulation:
โ€ข Archimedes Number: Ar = dpยณ ยท ฯg ยท (ฯp โˆ’ ฯg) ยท g / ฮผgยฒ
โ€ข Minimum Fluidization Reynolds: Remf = โˆš(33.7ยฒ + 0.0408 Ar) โˆ’ 33.7
โ€ข Minimum Fluidization Velocity: Umf = Remf ยท ฮผg / (ฯg ยท dp) [m/s]
โ€ข Bed Pressure Drop: ฮ”Pbed = (1 โˆ’ ฮตmf) ยท (ฯp โˆ’ ฯg) ยท g ยท Hโ‚€ [kPa].

๐Ÿ“Š Fluidization Results

Configure inputs and click Compute to view results.

๐Ÿ“˜ Calculation Methodology & Fluidization Standards

Geldart Particle Groups

Categorizes gas-solid fluidization behavior into 4 groups: Group A (aeratable catalysts), Group B (sand bubbling), Group C (cohesive fine powders), and Group D (coarse spouting grains).

Constant Pressure Drop Principle

Once fluidization begins ($U_0 \ge U_{mf}$), the total pressure drop across the bed remains constant and equals the apparent buoyant weight of the bed per unit area.

Key Engineering Assumptions

  • Wen & Yu (1966) correlation for $Re_{mf}$ across broad Archimedes numbers.
  • Haider & Levenspiel terminal velocity equation for non-spherical particles.
  • Applicable to CFB boilers, FCC regenerators, biomass gasifiers, and drying beds.