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Ergun equation

Estimate pressure loss through a packed bed by combining viscous and inertial terms scaled by fluid properties, particle size, void fraction, and superficial velocity.

Version
v2 · 2026-09-19 · History
Domain-specific #
1786
Domain group
Natural Sciences
Origin domain
Chemistry & Materials Science
Subdomains
Chemical Engineering, Packed Bed Flow → Chemistry & Materials Science
Aliases
Ergun correlation, Packed-bed pressure-drop equation

Core Idea

The Ergun equation is an empirical correlation for pressure gradient in packed particles. A common form is \(-\Delta P/L=150\mu(1-\varepsilon)^2U/(\varepsilon^3d_p^2)+1.75\rho(1-\varepsilon)U^2/(\varepsilon^3d_p)\), where \(U\) is superficial velocity, \(\varepsilon\) void fraction, \(d_p\) an effective particle diameter, and \(\mu,\rho\) viscosity and density. Sign and length conventions must be stated.

The linear term represents viscosity-dominated resistance and approaches Kozeny–Carman scaling at low particle Reynolds number. The quadratic term represents inertial form drag important at larger flow. Adding them bridges regimes for many approximately uniform beds. Inputs compress pore geometry into voidage and effective diameter, so the equation predicts a bulk gradient rather than resolving local velocities.

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Squeezing Through Marbles

Imagine pushing water through a jar packed full of marbles. The water has to squeeze around them, so you have to push hard. The Ergun equation is a helper rule that guesses how hard you need to push, depending on how fast the water goes and how tightly the marbles are packed.

The Packed-Pile Pressure Rule

When a liquid or gas flows through a pile of small particles, like sand or beads, it loses pressure along the way. The Ergun equation estimates that pressure loss. It adds up two parts. One comes from the fluid's stickiness, which matters most when the flow is slow. The other comes from the fluid bumping and swirling around the particles, which matters more when the flow is fast. It uses how much empty space there is between particles and how big they are. The numbers in it come from experiments, so it is a good guess rather than a perfect law.

Packed-Bed Pressure-Drop Correlation

The Ergun equation is an experiment-based formula for how much pressure drops per length when fluid flows through a packed bed of particles. It adds a viscous term, proportional to velocity U, and an inertial term, proportional to U². The inputs are void fraction ε (the fraction of empty space), an effective particle diameter, and the fluid's viscosity and density. U is the superficial velocity, meaning flow rate divided by the empty tube's area, not the faster speed inside the pores. It predicts the overall gradient, not the detailed flow around each grain. Its coefficients 150 and 1.75 are fitted values, not laws of nature.

 

The Ergun equation correlates the pressure gradient across a packed bed. A common form is −ΔP/L = 150μ(1−ε)²U/(ε³d_p²) + 1.75ρ(1−ε)U²/(ε³d_p). Here U is the superficial velocity, ε the void fraction, d_p an effective particle diameter, and μ and ρ the fluid's viscosity and density. The first term captures viscosity-dominated resistance and reduces to Kozeny–Carman scaling at low particle Reynolds number. The second term captures inertial form drag at higher flow rates. Summing the two bridges the two regimes for reasonably uniform beds. The model collapses all pore geometry into ε and d_p, so it predicts a bulk gradient, not local velocity fields. Its coefficients are calibrated, not universal. Nonspherical or polydisperse particles, wall effects at small bed-to-particle diameter ratios, fluidization, compressible or non-Newtonian fluids, and evolving beds may need modified correlations. Sign and length conventions should be stated, and superficial velocity must not be swapped for interstitial velocity.

Scope of Application

The abstraction is literal wherever practitioners can identify the same constitutive roles, apply the same boundary tests, and obtain the same kind of output. The following habitats are uses of Ergun equation itself, not metaphors based only on resemblance.

  • Packed-bed reactors. Estimating bulk pressure loss across catalyst particles.
  • Adsorption columns. Comparing flow resistance across candidate packings.
  • Filtration. Providing a first bulk model under compatible assumptions.
  • Laboratory correlation. Reducing pressure and flow data to regime comparisons.
  • Scale-up screening. Testing whether pressure loss may become limiting.
  • Model selection. Comparing Darcy, Ergun, and modified correlations.

Clarity

A clear account of Ergun equation must preserve the recognition invariant stated in the Core Idea rather than rely on the title alone. Define superficial velocity, void fraction, effective diameter, and pressure sign. Report shape, size distribution, bed-to-particle ratio, and fluid regime. Keep viscous and inertial contributions visible before simplifying. Treat extrapolation and modified coefficients as model changes. These declarations are not editorial extras: each changes what observations count, which transformations are licensed, and what conclusion can be drawn.

Manages Complexity

Ergun equation manages complexity by replacing a diffuse field of observations or possible operations with a bounded role structure: packed bed supplies a stationary porous assembly supplies distributed resistance.; superficial velocity supplies flow divided by empty tube area sets the standard variable.; void fraction supplies fluid-accessible fraction strongly scales both resistance terms.; effective diameter supplies a declared size convention represents pore-scale geometry.; fluid viscosity supplies viscous momentum transport controls the linear contribution..

Abstract Reasoning

  1. Bound the packed interval and confirm that the bed is stationary.
  2. Choose consistent units and a defensible effective diameter.
  3. Calculate superficial velocity from empty cross-sectional area.
  4. Evaluate linear viscous and quadratic inertial contributions separately.
  5. Sum contributions over the declared bed length.
  6. Check Reynolds regime, wall ratio, compressibility, and property variation.
  7. Compare predictions with measurements or a better-suited correlation.

Knowledge Transfer

The strict upward abstraction is Approximation. Ergun Equation instantiates Approximation because it compresses unresolved packed-bed flow into an empirically calibrated two-term pressure-loss relation. Within packed bed flow, the full mechanism transfers literally when the same roles and boundary tests recur. Beyond that domain, only the parent-level skeleton should travel. Reusing the label Ergun equation after removing its constitutive vocabulary would hide a change of mechanism behind an analogy. The honest transfer rule is therefore two-stage: recognize the domain-specific pattern first, then lift only the parent relation that remains invariant under a substrate change.

Relationships to Other Abstractions

Local relationship map for Ergun equationParents appear above the current abstraction, mutual partners to the right, and children below. Node labels state whether each abstraction is prime or domain-specific; colors identify relation types.Ergun equationDOMAINPrime abstraction: Approximation — is a kind ofApproximationPRIME

Current abstraction Ergun equation Domain-specific

Parents (1) — outgoing typed relations

  • Ergun equation is a kind of Approximation Prime

    Ergun Equation instantiates Approximation because it compresses unresolved packed-bed flow into an empirically calibrated two-term pressure-loss relation.

Hierarchy path (1) — routes to 1 parentless root

Neighborhood in Abstraction Space

Ergun equation sits in a sparse region of the domain-specific corpus (91st percentile for distinctiveness): few abstractions share its structure, so a faithful description tends to retrieve it precisely.

Family — Unclustered & Miscellaneous (2769 abstractions)

Nearest neighbors

Computed from structural-signature embeddings · 2026-10-25