$v_s = \dfrac{(\rho_p - \rho_f)\,d_p^2\,g\,C_c}{18\mu}$
Cunningham correction
$C_c = 1 + \dfrac{2\lambda}{d_p}\!\left(1.257 + 0.4\,e^{-1.1d_p/2\lambda}\right)$
Diffusion coefficient
$D_p = \dfrac{k_B T\,C_c}{3\pi\mu\,d_p}$
Compute settling velocity, diffusion coefficient, Stokes number, Cunningham correction, aerodynamic diameter, and lung deposition fraction for particles from 0.01 to 100 μm in real time.
The core equation governing gravitational settling for small, spherical particles in a fluid is the Stokes' law, corrected for very small particles where air can no longer be treated as a continuous medium.
$$v_s = \dfrac{(\rho_p - \rho_f)\,d_p^2\,g\,C_c}{18\mu}$$Where $v_s$ is the settling velocity (m/s), $\rho_p$ is particle density (kg/m³), $\rho_f$ is fluid (air) density, $d_p$ is particle diameter (m), $g$ is gravity (9.81 m/s²), $\mu$ is air dynamic viscosity (Pa·s), and $C_c$ is the Cunningham slip correction factor.
The Cunningham correction factor is crucial for particles approaching the mean free path of air molecules (~0.066 µm). It accounts for "slip" at the particle surface, which reduces drag and increases settling speed compared to classic Stokes' law.
$$C_c = 1 + \dfrac{2\lambda}{d_p}\!\left(1.257 + 0.4\,e^{-1.1d_p/2\lambda}\right)$$Here, $\lambda$ is the mean free path of air. For large $d_p$, $C_c$ approaches 1 (no correction). For a 0.01 µm particle, $C_c$ can be >20, meaning it falls over 20 times faster than standard Stokes' law would predict!
Pharmaceutical Inhalers: Drug efficacy depends on particles depositing in specific lung regions. Engineers use these dynamics calculations to design aerosol particles with the perfect size (often 1-5 µm) to maximize lung deposition via sedimentation and minimize exhalation.
Indoor Air Quality & Ventilation: Understanding how fast virus-laden aerosols settle or remain airborne informs ventilation guidelines and safe exposure times. For example, large droplets settle quickly, but sub-micron "aerosol" particles can drift across a room.
Industrial Emission Control: Scrubbers and filters are designed based on the size distribution of emitted particles. The Stokes number determines if a particle will impact on a baffle or follow the gas stream, guiding pollution control device design.
Climate Science: The lifetime of atmospheric aerosols (like sea salt or sulfate particles) in the air before they settle or are washed out by rain is governed by these dynamics. This residence time directly impacts their radiative forcing and effect on climate.
First, there's the common assumption that "the particle density can always be taken as 1 g/cm³, the same as water". This can be quite misleading. For instance, between metal oxide dust (density ~4 g/cm³) and pollen (density ~0.5 g/cm³), the settling velocity for the same 10μm particle can differ by several times. Since deposition behavior in the lungs also changes, researching the actual density of the particles you're dealing with is the essential first step.
Next, there's the tendency to assume "air conditions are fixed at standard state (20°C, 1 atm)". At high altitudes (lower pressure) or in high-temperature environments, the air viscosity μ and density ρ_f change, affecting your calculation results. For example, at an altitude of 2000m, air density is about 80% of sea-level density, reducing buoyancy and slightly increasing the settling velocity. When simulating real-world conditions, remember to adjust the temperature and pressure parameters accordingly.
Finally, beware of the oversimplified interpretation that "a Stokes number (Stk) greater than 1 means the particle immediately falls to the floor". Stk is an indicator of behavior at airflow "bends". Even if a particle has high inertia, if its initial velocity is zero, its settling will be gradual. For example, a large particle (Stk>1) carried by ventilation duct airflow is more likely to impact the wall at a duct bend, whereas the same particle in still air would simply undergo Stokes settling. Get into the habit of considering how each parameter calculated by the tool applies within your specific flow field context.
The calculation logic of this tool is fundamental to powder technology and microscale particle fluid dynamics. Specifically, in the design of dust collection equipment like cyclones and bag filters, the aerodynamic diameter and Stokes number of the target particles are key to determining separation efficiency. Furthermore, in spray drying (the technology of drying droplets into powder), particle dynamics are directly applied by competing the droplet drying rate against its settling velocity to control particle morphology.
It also integrates deeply with CFD (Computational Fluid Dynamics) simulation. After characterizing individual particle properties with a tool like this, it can serve as a pre-processing step for the Lagrangian Particle Tracking method, where millions of such particles are released into a flow domain within CFD software. For instance, it helps generate foundational data for predicting where pollen or PM2.5 might accumulate in automotive cabin airflow simulations.
In a more unexpected area, cleanroom design for semiconductor manufacturing is also a related field. Predicting how fine particles generated by manufacturing equipment are carried by laminar flow clean bench airflows and deposit on wafer surfaces requires essential calculations of diffusion coefficients and settling velocities.
First, I recommend playing with the tool to develop an intuition for "dimensionless numbers". Numbers like the Stokes number (Stk) and Reynolds number (Re) are powerful languages for generalizing and understanding phenomena. For example, vary the particle size and find the threshold where Stk exceeds 1, gaining an intuitive understanding that "from this size onward, the particle can no longer follow airflow turns."
The next step is to follow the derivation of the governing equations. The settling velocity formula calculated by the tool, $$v_s = \dfrac{(\rho_p - \rho_f)\,d_p^2\,g\,C_c}{18\mu}$$, can be simply derived from the force balance on a particle (gravity - buoyancy = Stokes drag). Understanding that the Stokes drag formula $F_d = 3\pi \mu d_p v$ rests on the assumptions of "laminar flow, spherical shape, and very low Reynolds number" reveals its limits of applicability (e.g., different drag laws are needed for large particles or high speeds).
If you wish to go further, mathematically exploring the relationship between "Brownian motion" and the "diffusion coefficient" will broaden your perspective. Einstein's relation $$D = \frac{k_B T C_c}{3\pi \mu d_p}$$ allows you to understand the physical origin of how the diffusion coefficient calculated by the tool depends on temperature T and particle diameter d_p. This is at the core of understanding indoor aerosol dispersion and the mechanisms of fine particle penetration into the deep lung.