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Microfluidic channel calculator

D_h = 4A / P = 2 × width × height / (width + height)

Enter the internal width and height of a rectangular channel and the volumetric flow rate through it: the tool computes the hydraulic diameter (D_h = 4A/P) and the mean fluid velocity (v = Q/A), the two quantities that govern the flow regime (laminar or turbulent) in a microfluidic chip channel.

Channel width
Channel height
Volumetric flow rate
Reynolds number

Optional: choose the dynamic mode (dynamic viscosity µ + density ρ) or the kinematic mode (kinematic viscosity ν), then fill in the fields of the chosen mode to get the Reynolds number.

No flow regime (laminar, transitional, turbulent) is indicated: no verified bound for a microfluidic channel was found in a primary source (ADR-0012, ADR-0028).

Fluid dynamic viscosity (Pa·s)
Fluid density
Hydraulic resistance and pressure drop

Optional: enter the channel length below, the dynamic viscosity used is the one entered in the "Reynolds number" section (dynamic mode). Without both values, the resistance stays not computed.

Channel length

Resistance not computed: enter the channel length and the dynamic viscosity (Reynolds section, dynamic mode).

Series/parallel network

Optional: enter two hydraulic resistances (in Pa·s/m³) and choose how they are combined to get the equivalent network resistance.

Network not computed: enter R₁ and R₂.

Hydraulic resistance uncertainty

Optional: enter the standard uncertainties on width, height and dynamic viscosity to get the composed uncertainty of the resistance (GUM, first-order propagation). The length is assumed exactly known.

Standard uncertainty on width
Standard uncertainty on height
Standard uncertainty on dynamic viscosity (Pa·s)

Uncertainty not computed: enter the length, the dynamic viscosity and the three standard uncertainties above.

Physical limits of the model

Per-category assessment, without correcting the results: each category is evaluated when the required quantities are available, otherwise it stays explicitly not evaluated.

Entrance effects
not evaluated, missing input, La corrélation (24) exige les quatre grandeurs à la fois : rapport d’aspect, diamètre hydraulique, longueur du canal et nombre de Reynolds.
Compressibility
not evaluated, missing input, Aucun nombre de Mach fourni. Ce moteur ne le calcule pas : il exigerait une vitesse du son, donc une hypothèse sur le fluide qui n’est pas la sienne.
Wall slip
not evaluated, missing input, Aucun nombre de Knudsen fourni. Ce moteur ne le calcule pas : Kn = λ/H exige le libre parcours moyen λ du fluide, que la géométrie seule ne donne pas.
Non-Newtonian fluid
not evaluated, missing input, Aucun comportement rhéologique déclaré. Il n’existe pas de seuil chiffré séparant un fluide newtonien d’un fluide qui ne l’est pas : sans déclaration explicite, cette catégorie reste non évaluée plutôt que supposée newtonienne.
Continuum assumption
not evaluated, missing input, Aucun nombre de Knudsen fourni. Ce moteur ne le calcule pas : Kn = λ/H exige le libre parcours moyen λ du fluide, que la géométrie seule ne donne pas.
Channel cross-section

5000 µm²

Hydraulic diameter

66.6667 µm

Mean velocity

33.3333 mm/s

Formula: D_h = 4A/P = 2(l×h)/(l+h) · v = Q/A

Scientific dossier


What the tool computes, what it assumes, where it stops being valid, and where its data comes from.

Method & formulasD_h = 4A / P = 2 × width × height / (width + height)

D_h = 4A / P = 2 × width × height / (width + height)

v = Q / A

Re = v × D_h / ν = ρ × v × D_h / µ

A is the cross-sectional area (width × height), P its wetted perimeter. The hydraulic diameter generalizes the diameter of a circular tube to a rectangular section: it is this quantity, not the width or height alone. That enters the Reynolds number and pressure-drop correlations of a non-circular channel. The Reynolds number Re is computed either from the kinematic viscosity (ν, in m²/s, kinematic mode) or from the dynamic viscosity (µ, in Pa·s) and density (ρ, in kg/m³, dynamic mode). Never both sets of fields at once.

Hydraulic diameter (D_h)
· diameter of the circular tube equivalent, from a flow standpoint, to the channel's rectangular section.
Mean velocity (v)
· flow rate divided by the cross-sectional area, the velocity a uniform flow would have across the whole section, distinct from the velocity at the channel center.
Full section
· the calculation assumes a channel entirely filled by the fluid across its full height, never a free-surface flow.
Reynolds number (Re)
· ratio of inertial to viscous forces. No flow regime (laminar, transitional, turbulent) is inferred from this value: no verified primary source establishes a regime boundary for a microfluidic channel (ADR-0012, ADR-0028).
AssumptionsThe fluid is Newtonian: its viscosity does not depend on shear rate.
  • The fluid is Newtonian: its viscosity does not depend on shear rate. A polymer solution, blood or a concentrated suspension is not, and these results do not apply to them.
  • The flow is fully developed and laminar, far from the channel inlet. Near the inlet the velocity profile is not yet developed and the real resistance is higher.
  • The fluid sticks to the wall (no-slip condition) and is incompressible. Both assumptions fail at high Knudsen and Mach numbers, the tool flags when those thresholds are crossed.
  • The laminar/turbulent regime thresholds come from a macroscopic pipe. In a microchannel, transition may occur at a different Reynolds number depending on geometry, roughness and inlet shape.
Validity domainThe calculation assumes a constant rectangular section and a fully filled channel: it does not apply to a partially filled channel, to a trapezoidal profile from anisotropic etching, or to a circular or semicircular section.

The calculation assumes a constant rectangular section and a fully filled channel: it does not apply to a partially filled channel, to a trapezoidal profile from anisotropic etching, or to a circular or semicircular section. The Reynolds number is only computed when the fields of the chosen viscosity mode (dynamic: µ and ρ; kinematic: ν) are entered in the advanced controls; without them, only the hydraulic diameter and mean velocity are available. No laminar, transitional or turbulent classification is provided.

SourcesWikipedia (Wikimedia Foundation) · LibreTexts (Physics LibreTexts), remixé par Joshua Halpern · d'après OpenStax University Physics · Elvesys (Elveflow) · Microfluidic reviews + 4 more
  1. Wikipedia (Wikimedia Foundation), Reynolds number, révision consultée : oldid 1362194896.

    Location : Section « Flow in a pipe », formule « Re = uD_H/ν = ρuD_H/µ = ρQD_H/(µA) = WD_H/(µA) », avec (unités SI de la source) : D_H « the hydraulic diameter of the pipe (the inside diameter if the pipe is circular) (m) » ; µ (mu) « the dynamic viscosity of the fluid (Pa·s = N·s/m² = kg/(m·s)) » ; ν (nu) « the kinematic viscosity (ν = µ/ρ) (m²/s) », explicitement DISTINCTE de µ. Jamais substituable sans diviser par ρ ; ρ (rho) « the density of the fluid (kg/m³) » ; u « the mean velocity of the fluid (m/s) ». Diamètre hydraulique défini, pour une section quelconque, par « D_H = 4A/P » (A l’aire de la section, P le périmètre mouillé du canal) : c’est cette définition, pas le diamètre d’un tube circulaire, qui rend la formule applicable à un canal microfluidique non circulaire. La source précise elle-même la limite de cette substitution : « the hydraulic diameter can be substituted for the diameter of a circular duct, with reasonable accuracy, if the aspect ratio AR of the duct cross-section remains in the range 1/4 < AR < 4 ». · accessed 2026-08-02 · Licence CC BY-SA 4.0

  2. LibreTexts (Physics LibreTexts), remixé par Joshua Halpern · d'après OpenStax University Physics, 52.7: The Reynolds Number, consulté 2026-08-02.

    Location : Formule « Re = ρvD/µ » (D « the diameter of the pipe ») et seuils « Re<2000 : laminar flow », « 2000<Re<3000 : transition region », « Re>3000 : turbulent flow ». Contexte d’application exact donné par la source : « a general rule of thumb » pour l’écoulement d’un fluide visqueux dans une conduite (pipe), PAS pour un canal microfluidique (voir MICROCHANNEL_REYNOLDS_REGIME_BOUNDS dans reynoldsChannelSources.ts). · accessed 2026-08-02 · Licence CC BY-NC-SA 4.0

  3. Elvesys (Elveflow) · Microfluidic reviews, Flow Resistance in Microfluidics: Principles, Calculations & Applications, consulté 2026-08-02.

    Location : Section « Introduction to microfluidics and flow resistance », équation « ΔP = QR_H », ΔP la différence de pression [Pa en unités SI], Q le débit volumique [m³/s], R_H la résistance hydraulique [Pa·s/m³]. · accessed 2026-08-02

  4. Molecular Medicine Reports (Spandidos Publications) · Bao X., Li Z., Liu H. et al., Stimulation of chondrocytes and chondroinduced mesenchymal stem cells by osteoinduced mesenchymal stem cells under a fluid flow stimulus on an integrated microfluidic device, vol. 17, n° 2 (2018), p. 2277-2285, version PMC5783459.

    Location : Section « Materials and methods », sous-section « Numerical modeling of the shear stress », « R=[12ηL/(1–0.63(h/w)] × (1/h3w). In this formula, R is the hydraulic resistance of the rectangular microchambers, η the dynamic viscosity of the liquid, L the channel length, h and w (always h < w) the channel height and width, respectively. ». La parenthèse « always h < w » est la convention d'orientation du rapport d'aspect ET le domaine géométrique retenus par ce moteur. Le même paragraphe referme la chaîne sur la loi de Hagen-Poiseuille : « Δp=QR_H ». · accessed 2026-08-02 · DOI 10.3892/mmr.2017.8153 · Licence CC BY-NC-ND 4.0

  5. Bar-Meir, Genick · LibreTexts (Civil Engineering), « Fluid Mechanics », Kinematic Viscosity, consulté 2026-08-02.

    Location : Définition « ν = µ/ρ », dimensions [m²/s] · accessed 2026-08-02 · Licence GNU Free Documentation License 1.3

  6. Sensors (MDPI), Shayor Ahmed Abrar, Kabir Md Emamul, Rifath Md Sartaj Ahamed, Rashid Adib Bin, Oh Kwang W., A Synergistic Overview between Microfluidics and Numerical Research for Vascular Flow and Pathological Investigations, vol. 24, n° 18 (2024), article 5872, version PMC11435959.

    Location : Section 1 « Introduction », « To model the flow of Newtonian fluid via a single microchannel, the Hagen–Poiseuille law may be used. The flow profile throughout the channel is assumed to follow a parabolic shape ». · accessed 2026-08-02 · DOI 10.3390/s24185872 · Licence CC BY 4.0

  7. JCGM / BIPM (Joint Committee for Guides in Metrology), Evaluation of measurement data, Guide to the expression of uncertainty in measurement (GUM), JCGM 100:2008, JCGM 100:2008 (GUM 1995 with minor corrections), première édition septembre 2008.

    Location : §5.1 « Uncorrelated input quantities », « This subclause treats the case where all input quantities are independent » ; §5.1.2, équation (10) : « u_c²(y) = Σ_{i=1}^{N} (∂f/∂x_i)² u²(x_i) », suivie de « Equation (10) […] based on a first-order Taylor series approximation of Y = f(X1, X2, ..., XN), express what is termed in this Guide the law of propagation of uncertainty » ; §5.1.3 nomme c_i = ∂f/∂x_i les coefficients de sensibilité. · accessed 2026-08-02

Scientific validationProvisional · revision 1 · reviewed 2026-08-04

Provisional · Sources and assumptions are declared; the full documentary review is still pending.

Physical model. The result follows the significant figures of the least precise input.

revision 1 · reviewed 2026-08-04

Revision log

  1. revision 1 · 2026-08-04 · source update

    Bloc scientifique renseigné : les sept sources déjà utilisées par le moteur microfluidique sont déclarées, ainsi que les hypothèses du modèle.

    Aucun changement de résultat, aucune valeur. Formule ni seuil n’est modifié.