Microfluidic Droplet Generator Parameter Estimator

Estimate starting Qc/Qd flow rates, droplet volume, generation frequency, and Capillary number regime for flow-focusing droplet generators. Free. Client-side.

MicrofluidicsDroplet GenerationClient-Side
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Load example microfluidic droplet parameter estimator data to see the full workflow

⚠️ Estimates only. Squeezing-regime droplet diameter is set by a Garstecki-style correlation (d/w ≈ 1 + Qd/Qc) that is good to ~30%. Always validate with a test run before production. Capillary number is the regime indicator — actual droplet size also depends on chip geometry and surfactant chemistry.

Nozzle Geometry

Phases

Target & Flow

Suggested Starting Point

Continuous phase Qc
100.0 μL/min
Dispersed phase Qd
100.0 μL/min
Flow ratio Qd/Qc
1.00
Droplet volume
523.6 pL
Frequency
3.18 kHz
Capillary number
0.1867
Regime: dripping
Dripping regime (Ca 0.01–0.3): droplet size set by competition between viscous drag and interfacial tension. Most flexible regime; tune flow ratio to fine-tune size.
  • Choosing starting Qc/Qd for a new droplet generation chip
  • Estimating droplet volume and frequency for a reagent budget
  • Checking whether your flow conditions are in the squeezing, dripping, or jetting regime
  • Sizing a chip nozzle to hit a target droplet diameter
  • Teaching the Garstecki scaling law interactively

Don't use for

  • For precise droplet sizing (validate empirically — this is a ±30% starting estimate)
  • For emulsions made by shaking, vortexing, or membrane extrusion
  • For gas-in-liquid (bubble) generators (surface tension and density are different)
  • For double emulsions (requires a two-step model not covered here)

The Garstecki Squeezing-Regime Model

In 2006, Garstecki et al. showed that droplet size in a confined microfluidic channel follows a beautifully simple scaling:

d/w \approx 1 + α\alpha ×\times (Qd/Qc)

where d is the droplet diameter, w is the nozzle width, Qd is the dispersed-phase flow rate, Qc is the continuous-phase flow rate, and α\alpha is a geometry-dependent prefactor of order 1.

The key insight: in the squeezing regime, surface tension dominates over viscous stress, so the droplet length depends only on the flow-rate ratio, not on the absolute flow rates. This makes the squeezing regime extremely predictable and the default for biological applications.

Squeezing, Dripping, Jetting — The Three Regimes

Squeezing (Ca < 0.01): The dispersed phase completely fills the nozzle cross-section. Droplets form when the continuous phase pinches the thread against the channel wall. Size is set by geometry + flow ratio. Monodisperse, low throughput.
Dripping (Ca 0.01–0.3): Viscous drag partially thins the dispersed thread before pinch-off. Droplets are smaller than squeezing at the same Qd/Qc. Most flexible regime for tuning size vs throughput.
Jetting (Ca > 0.3): The dispersed phase forms a thin jet that breaks up downstream by Rayleigh–Plateau instability. High throughput but polydisperse — avoid for applications requiring uniform drops.

Surfactant: The Unsung Hero of Droplet Stability

Surface-active molecules (PFPE-PEG for fluorinated oils, Span 80 for hydrocarbon oils) adsorb to the oil/water interface and lower σ\sigma, which:

1. Prevents coalescence — drops can touch without merging 2. Speeds up drop formation (lower σ\sigma → higher Ca at same velocity) 3. Can reduce drop size (weaker surface tension → earlier pinch-off)

At least 0.5% surfactant is required for stable drops. Below that, any downstream contact — in a delay line, in a storage array, at a detector — causes coalescence and destroys the emulsion.

Frequently Asked Questions