About the Flow Behavior Index Calculator

This guide provides detailed information on the principles behind our Flow Behavior Index calculator. It covers the what, why, and how of analyzing fluid rheology using the Power Law model, helping users interpret their data and results accurately.

What This Calculator Does

The calculator analyzes experimental data of shear stress (τ) versus shear rate (γ̇) to characterize the flow properties of non-Newtonian fluids. Its primary functions are:

  • Calculate Key Parameters: It determines the Flow Behavior Index (n) and the Consistency Index (K) by applying a linear regression to the logarithmic form of the Power Law model.
  • Classify Fluid Type: Based on the calculated Flow Behavior Index (n), it classifies the fluid as Pseudoplastic (shear-thinning), Newtonian, or Dilatant (shear-thickening).
  • Assess Model Fit: It calculates the Coefficient of Determination (R²), which indicates how well the Power Law model represents the provided experimental data. An R² value close to 1.0 suggests a strong fit.
  • Visualize Data: It generates both arithmetic and log-log plots of the data, visually comparing the experimental points against the fitted Power Law model curve.

When to Use It

This tool is essential for scientists, engineers, and technicians in various fields who need to understand and quantify fluid behavior. Key applications include:

  • Pharmaceuticals: Formulating creams, ointments, and suspensions with desired consistency and spreadability.
  • Food Science: Quality control of products like ketchup, yogurt, and sauces, ensuring consistent texture and flow.
  • Chemical Engineering: Designing pipelines and mixing processes for polymers, slurries, and paints.
  • Cosmetics: Developing lotions, gels, and foundations with specific application properties.
  • Materials Science: Characterizing novel polymers and colloidal suspensions.

Inputs Explained

To use the calculator, you need a set of corresponding measurements from a rheometer or viscometer.

  • Shear Rate (γ̇): This is the rate at which a fluid is sheared or “worked.” It represents the velocity gradient within the fluid flow and is typically measured in reciprocal seconds (s⁻¹). You must enter at least two data points.
  • Shear Stress (τ): This is the force per unit area required to move one layer of fluid relative to another. It’s the fluid’s internal resistance to flow. The calculator accepts common units like Pascals (Pa), dynes per square centimeter (dyn/cm²), and pounds per square foot (psf). Ensure you select the correct unit to match your data for accurate conversion.

Results Explained

After calculation, the tool provides a comprehensive analysis of your fluid’s properties:

  • Flow Behavior Index (n): A dimensionless number indicating the degree of non-Newtonian behavior.
    • n < 1: Pseudoplastic (shear-thinning) fluid. Its viscosity decreases as the shear rate increases (e.g., paint, ketchup).
    • n = 1: Newtonian fluid. Its viscosity is constant regardless of the shear rate (e.g., water, simple oils).
    • n > 1: Dilatant (shear-thickening) fluid. Its viscosity increases as the shear rate increases (e.g., cornstarch-water mixture).
  • Consistency Index (K): A measure of the fluid’s “thickness” or consistency. It is analogous to viscosity for a Newtonian fluid. The units are typically Pa·sⁿ, and they depend on the value of ‘n’. A higher K value indicates a more viscous fluid at a shear rate of 1 s⁻¹.
  • Coefficient of Determination (R²): A statistical measure from 0 to 1 that represents the proportion of the variance in the dependent variable that is predictable from the independent variable(s). In this context, it shows how well the Power Law model fits your data. An R² value above 0.95 is generally considered a good fit.

Formula / Method

The calculator is based on the Ostwald-de Waele relationship, commonly known as the Power Law model:

τ = K * (γ̇)ⁿ

Where:

  • τ = Shear Stress
  • K = Consistency Index
  • γ̇ = Shear Rate
  • n = Flow Behavior Index

To solve for n and K, the equation is linearized by taking the natural logarithm (or any base logarithm) of both sides:

log(τ) = log(K) + n * log(γ̇)

This equation is in the form of a straight line, y = c + mx, where:

  • y = log(τ)
  • c = log(K) (the y-intercept)
  • m = n (the slope)
  • x = log(γ̇)

The calculator performs a linear regression (method of least squares) on the log-transformed data points to find the best-fit line. The slope of this line gives n, and the antilog of the y-intercept gives K.

Step-by-Step Example

Let’s analyze a shear-thinning fluid with the following data (Stress in Pa, Rate in s⁻¹):

Shear Rate (γ̇)Shear Stress (τ)log(γ̇)log(τ)
105.02.3031.609
5015.03.9122.708
10025.04.6053.219
  1. Data Transformation: The natural logarithm of each shear rate and shear stress value is calculated.
  2. Linear Regression: A linear regression is performed on the log-log data pairs (e.g., (2.303, 1.609)).
  3. Determine Slope (n): The regression analysis yields a slope for the best-fit line. For this data, the slope is approximately n = 0.70.
  4. Determine Intercept (log K): The regression also provides the y-intercept, which is log(K). For this data, the intercept is approximately log(K) = 0.005.
  5. Calculate K: The Consistency Index K is found by taking the antilog (eⁿ) of the intercept. K = e0.0051.005 Pa·sⁿ.
  6. Conclusion: Since n (0.70) is less than 1, the fluid is classified as Pseudoplastic (shear-thinning).

Tips + Common Errors

Best Practices & Pitfalls

  • Sufficient Data: While the calculator works with a minimum of two points, using at least 5-7 data points spread across a wide range of shear rates will produce a much more reliable result.
  • Unit Consistency: Always double-check that the units selected in the tool match the units of your raw data. Incorrect unit selection is a common source of error.
  • Zero/Negative Values: The Power Law model is undefined for zero or negative values due to the logarithmic transformation. Ensure all your inputs are positive numbers.
  • Poor R² Value: An R² value significantly below 0.95 suggests that the Power Law model may not be appropriate for your fluid over the tested range. The fluid might exhibit other behaviors, such as a yield stress (like a Bingham plastic) or fit a different rheological model (e.g., Carreau, Cross).

Frequently Asked Questions

The units of K depend on the value of n. The general form is pressure × timeⁿ (e.g., Pa·sⁿ). When n=1 (a Newtonian fluid), K has units of viscosity (Pa·s). Because the units change with n, K values should only be compared for fluids with very similar n values.

Plotting shear stress versus shear rate on a log-log scale is a powerful diagnostic tool. If the data points form a straight line, it visually confirms that the Power Law model is a good fit. The slope of this line is the Flow Behavior Index (n).

For rheological data, an R² value of 0.95 or higher is generally considered a good fit. An R² of 0.99 or higher indicates an excellent fit. If your R² is low, it means the model does not accurately describe the data, and another model may be more appropriate.

No. The Power Law model assumes flow begins at an infinitesimally small stress. Fluids with a yield stress (like toothpaste or mayonnaise) require a certain minimum stress before they start to flow. These are better described by models like the Bingham plastic or Herschel-Bulkley model, which this calculator does not implement.

Temperature has a significant impact. Generally, increasing the temperature decreases the Consistency Index (K), making the fluid less viscous. The effect on the Flow Behavior Index (n) is more complex and material-dependent, but it can also change. Therefore, rheological data is only valid at the temperature at which it was measured.

Pseudoplastic (shear-thinning) behavior is a time-independent decrease in viscosity with increasing shear rate. The viscosity change is instantaneous. Thixotropy is a time-dependent phenomenon where viscosity decreases over time under constant shear and then slowly recovers when the shear is removed. This calculator analyzes time-independent behavior only.

This can happen because the linear regression is performed on the log-transformed data. This method gives equal weight to each data point in logarithmic space. If your data spans several orders of magnitude, the low shear rate data has a larger influence on the fit than it appears to on the arithmetic plot. This is standard practice and generally provides the most physically meaningful fit.

This calculator only characterizes the steady-state shear viscosity (the “viscous” part). It does not provide information about the elastic properties of a material (e.g., storage modulus, loss modulus). To characterize viscoelasticity, you would need oscillatory rheometry and a different set of models.

References

  1. Mezger, T. G. (2020). The Rheology Handbook: For Users of Rotational and Oscillatory Rheometers (5th ed.). Vincentz Network.
  2. Barnes, H. A., Hutton, J. F., & Walters, K. (1989). An Introduction to Rheology. Elsevier.
  3. Schramm, G. (2000). A Practical Approach to Rheology and Rheometry. Gebrueder HAAKE GmbH.
  4. ASTM D2196-20, “Standard Test Methods for Rheological Properties of Non-Newtonian Materials by Rotational (Brookfield type) Viscometer,” ASTM International, West Conshohocken, PA, 2020, www.astm.org.

Disclaimer: This content and its associated calculator are for educational and informational purposes only. They are not intended to be a substitute for professional engineering advice, design, or analysis. Always consult with a qualified professional for any specific engineering or scientific application. The user assumes all risks and responsibilities for any decisions made based on the information provided herein.

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