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Calcimator

Viscosity Converter

Dynamic viscosity: cP, cSt (needs fluid density), approximate Saybolt Universal seconds, and rough Engler degrees. Correlations are approximate.

Everything resolves to pascal-seconds, and the density field is the hinge that decides whether it is needed. Centipoise is simply a thousandth of a Pa·s, a dynamic viscosity that stands on its own, so while you are entering cP the density box does nothing at all to the cP and Pa·s rows — it moves only the centistokes column. Kinematic units invert that. Centistokes, Saybolt seconds and Engler degrees all describe how readily a fluid flows under its own weight, which means they carry density inside them and have to be multiplied by it to become dynamic; the 1000 kg/m³ default stands for water, and raising it pushes the centistokes reading down for the same underlying viscosity. Saybolt figures go through cSt = 0.226t − 195/t, the ASTM short-range correlation intended for efflux times between roughly 32 and 100 seconds at 100 °F, and this engine applies it outside that window too rather than switching to the longer-time constants. Engler degrees use the comparable 7.31E − 6.31/E approximation. The absence that swamps all of this is temperature. Viscosity depends on it far more strongly than on any unit choice — water alone runs from about 1.79 cP at freezing to 0.28 cP at boiling — and there is no temperature field on the page, so every figure is implicitly at whatever condition your source measurement was taken. Shear rate is missing too, so paint, blood and ketchup, which thin as they are stirred, have no single viscosity to convert.

Convert

Results

cP
1
Pa·s
0.001
cSt @ ρ
1
SUS (approx.)
31.7
How to Use This Calculator
  1. Enter Value, From, and Centipoise (cP).
  2. Set Centistokes (cSt), Saybolt Universal (SUS), and Engler degrees (°E).
  3. Adjust Fluid density (kg/m³) as needed.
  4. Review the cP result.
  5. Use Pa·s and cSt @ ρ to inform your decision.

How the result changes with Value

ValuecP
0.40.4
1.41.4
2.62.6
3.63.6

What each input means

Value
cP, cSt, SUS, or °E depending on unit.
From
cSt, SUS, and °E use density to get Pa·s.
Fluid density (kg/m³)
For kinematic→dynamic (water ≈ 1000).

How this is calculated

Worked example, using the default values

  1. Identify Input Parameters
    Value = 1, From = 0, Fluid density (kg/m³) = 1000 = 3 input(s) provided
  2. Calculate cP
    cP = paS / 0.001
    1 = 1
  3. Calculate Pa·s
    Pa·s = paS
    0.001 = 0.001
  4. Calculate cSt @ ρ
    cSt @ ρ = (paS / rho) * 1e6
    1 = 1

Engine last updated . Checked against 1 independently-derived test how we verify calculators.

Frequently Asked Questions

Do I have to fill in the fluid density?

Only when a kinematic unit is involved. Entering centipoise leaves the cP and Pa·s rows completely unaffected by whatever density you type, because those are dynamic measures. The centistokes row, being kinematic, changes the moment you alter it.

What is the difference between dynamic and kinematic viscosity?

Dynamic viscosity measures resistance to shear on its own; kinematic viscosity is that same resistance divided by density, describing how a fluid flows under gravity. Two liquids can share a kinematic figure and differ in dynamic terms if one is far heavier.

How reliable are the Saybolt seconds?

Treat them as approximate. The correlation used here was published for efflux times of about 32 to 100 seconds measured at 100 °F, and thicker oils that drain more slowly need a different pair of constants that this engine does not apply.

Why is there no temperature input?

There should arguably be one, because temperature dominates viscosity far more than any conversion factor does. Since none is collected, every result inherits the temperature at which your original measurement was taken, and comparing two figures taken warm and cold is meaningless.

Does this work for paint or blood?

Not properly. Those are non-Newtonian fluids whose viscosity falls as they are stirred or pumped, so a single number cannot describe them without also stating the shear rate. This page has no shear input and assumes ordinary Newtonian behaviour throughout.

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