Liquid column with two timing marks
Provide a 0.100 m timing distance below the initial settling region.
Determine the dynamic viscosity of a liquid from the terminal speeds of small spheres and the gradient of a speed–radius-squared graph. Explore a virtual apparatus, collect readings and analyse a graph.
Ready for a virtual observation.
Adjust the apparatus, then take a reading.
Timing is generated from the model; a short on-screen trial represents a longer physical interval. Animation is illustrative.
The calculation assumes an isolated rigid sphere in an unbounded, incompressible Newtonian fluid with constant density and viscosity and creeping flow. The illustrated column is a schematic timing gate; its walls exert no modeled correction. Initial acceleration, wall and end effects, bubbles, nonspherical beads and temperature drift are omitted. Timing starts after terminal motion is established. Virtual animation time is accelerated; reported elapsed time is physical model time. A fit error or perfect simulated line is not a complete experimental uncertainty estimate. The Newtonian liquid has a model viscosity of 1.20 Pa s at a fixed temperature. An effectively unbounded liquid is assumed. The simulated Reynolds number stays below 0.004 across the allowed radii. There are no wall/end corrections or temperature changes. Pre-terminal motion is not timed; the displayed fall is accelerated and not to scale.
Provide a 0.100 m timing distance below the initial settling region.
Provide smooth spheres of known density and different measured radii.
Measure sphere diameter and vertical separation of the timing marks.
Record transit time and monitor liquid temperature, which affects viscosity.
Determine the dynamic viscosity of a liquid from the terminal speeds of small spheres and the gradient of a speed–radius-squared graph. Suggested independent settings: 0.3, 0.45, 0.6, 0.75, 0.9 mm.
Record sphere density 2500 kg/m³, liquid density 1260 kg/m³ and g = 9.80665 m/s². In a physical lab also record temperature and confirm the liquid is suitable for a falling-sphere method.
Density difference, gravity and temperature enter the interpretation of terminal speed.
Measure each sphere diameter in several orientations, halve it to obtain radius, and convert to metres before calculating r². Select virtual radii within 0.300–0.900 mm.
The result depends on radius squared, making size measurement especially influential.
Set the vertical mark separation to 0.100 m below the release region. Release the sphere gently away from walls and verify steady motion before the upper mark.
The terminal-speed equation does not apply to timing that includes initial acceleration.
Time the sphere centre between the marks and record radius, r², distance and physical elapsed time. Repeat for several radii; the animation accelerates viewing while retaining modeled physical time.
Consistent crossing definitions and multiple sizes produce comparable observations.
For each row calculate v = H/t. Fit v against r² and inspect the points and intercept. Calculate a trial viscosity and Reynolds number to check the creeping-flow condition.
A model should be checked against its assumptions before interpreting a fitted parameter.
Use the gradient in η = 2(ρs − ρl)g/(9s). State viscosity in Pa·s, report the low Reynolds numbers and discuss temperature, walls, radius and timing as uncertainty sources.
A numerical answer is meaningful only together with the conditions under which it was inferred.
Points are your observations. The fit uses SI x and y values before display scaling.
| # | Sphere radius r (mm) | Time between two gates (s) | Radius squared r² (10⁻⁶ m²) | Terminal speed v (mm s⁻¹) | Remove |
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No readings yet. Take a virtual measurement and record it.