About This Tool
This Energy Requirement Calculator for comminution provides a comparative analysis of the energy needed to reduce the size of solid materials. It implements three foundational empirical laws in mineral processing and chemical engineering: Kick’s Law, Rittinger’s Law, and Bond’s Law. By inputting particle sizes and material-specific constants, users can estimate and compare the specific energy (e.g., kWh/t) and total power (kW) required for a crushing or grinding operation.
What This Calculator Does
The primary function of this calculator is to quantify the energy consumption for particle size reduction (comminution). It simultaneously computes the energy requirements based on three different theoretical models:
- Kick’s Law: Best for coarse crushing, where energy is proportional to the reduction ratio.
- Rittinger’s Law: Ideal for fine grinding, linking energy to the creation of new surface area.
- Bond’s Law: A widely used intermediate model, which proposes energy is proportional to the new crack length produced, making it versatile for both crushing and grinding applications.
The tool presents results in a table and a visual bar chart, allowing for easy comparison of the three models’ predictions for a given scenario.
When to Use It
This calculator is a valuable tool for process engineers, metallurgists, and students in the fields of mineral processing, cement production, and chemical engineering. Common applications include:
- Preliminary Equipment Sizing: Estimating the power draw for selecting mills and crushers.
- Process Optimization: Evaluating the energy efficiency of existing comminution circuits.
- Feasibility Studies: Predicting operational costs related to energy consumption in new projects.
- Academic and Educational Purposes: Demonstrating the differences and application ranges of the three fundamental comminution laws.
Inputs Explained
| Input Parameter | Description |
|---|---|
| Initial Particle Size (df) | The characteristic size of the material being fed into the comminution equipment. This is often represented by F80, meaning 80% of the feed material passes through this size. |
| Final Particle Size (dp) | The characteristic size of the product material after crushing or grinding. This is often represented by P80, meaning 80% of the product material passes through this size. Must be smaller than df. |
| Mass Flow Rate (m) | (Optional) The throughput of the material being processed, typically in tonnes per hour (t/h). If provided, the calculator will compute the total power requirement (kW or hp). |
| Kick’s Constant (Kk) | An empirical constant specific to the material being crushed, representing its resistance to crushing under Kick’s law. |
| Rittinger’s Constant (Kr) | A material-specific constant representing the energy required to create a unit of new surface area under Rittinger’s law. |
| Bond Work Index (Wi) | The most common parameter, representing the energy (in kWh/short ton) required to reduce a very large feed to a size where 80% of the product is finer than 100 micrometers. It is determined experimentally. |
Results Explained
The calculator provides two key outputs for each of the three laws:
- Specific Energy: This is the energy consumed per unit mass of material processed (e.g., kWh/t). It is a measure of the energy efficiency of the size reduction process. The tool allows you to view this in different units like kWh/t, kJ/kg, or hp·h/short ton.
- Total Power: If a mass flow rate is provided, this is the calculated continuous power draw required by the equipment (e.g., kW or hp). It is calculated by multiplying the specific energy by the mass flow rate.
Comparing the three results helps in understanding which model might be most applicable. Typically, for the same reduction ratio, Kick’s law predicts the lowest energy, Rittinger’s the highest, and Bond’s falls in between.
Formula / Method
The calculations are based on the standard forms of the three comminution laws. The energy (E) is calculated as follows:
Kick’s Law
Energy is proportional to the logarithm of the reduction ratio.
E = Kk * ln(df / dp)
Rittinger’s Law
Energy is proportional to the new surface area created.
E = Kr * (1/dp - 1/df)
Bond’s Law
Energy is proportional to the new crack length formed, representing an intermediate case.
E = 10 * Wi * (1/√dp - 1/√df)
Note: In Bond’s formula, dp and df must be in micrometers (μm), and the Work Index (Wi) is in kWh/short ton. The calculator handles all unit conversions internally to provide a consistent output in kWh per metric tonne (kWh/t).
Step-by-Step Example
Let’s calculate the energy required to crush granite from a feed size of 80 mm to a product size of 2 mm, with a throughput of 250 t/h.
Given Parameters:
- df = 80 mm = 80,000 µm
- dp = 2 mm = 2,000 µm
- m = 250 t/h
- Kk = 1.1 kWh/t (typical for hard rock)
- Kr = 150 kWh·µm/t (typical for hard rock)
- Wi = 15.13 kWh/short ton (for Granite)
Calculations:
- Kick’s Law:
E = 1.1 * ln(80000 / 2000) = 1.1 * ln(40) ≈ 1.1 * 3.689 = 4.06 kWh/t - Rittinger’s Law:
E = 150 * (1/2000 - 1/80000) = 150 * (0.0005 - 0.0000125) = 150 * 0.0004875 = 73.13 kWh/t - Bond’s Law:
First, calculate in kWh/short ton:
E = 10 * 15.13 * (1/√2000 - 1/√80000) ≈ 151.3 * (0.02236 - 0.00354) = 151.3 * 0.01882 = 2.85 kWh/short ton
Then, convert to kWh per metric tonne (1 short ton = 0.907185 metric tonnes):
E = 2.85 / 0.907185 ≈ 3.14 kWh/t - Total Power (Bond’s Law Example):
Power = Specific Energy * Mass Flow Rate = 3.14 kWh/t * 250 t/h = 785 kW
Tips + Common Errors
- Unit Consistency: The most common error is inconsistent units. This tool automatically converts common units, but always double-check that your inputs (e.g., mm, µm, in) are correctly selected.
- Size Convention (F80/P80): Remember that df and dp typically represent the 80% passing size, not the maximum or average particle size.
- Applicability of Laws: Do not treat the laws as universally correct. Kick’s law often underestimates energy for fine grinding, while Rittinger’s can overestimate for coarse crushing. Bond’s law is generally the most reliable for mill design.
- Work Index Source: The Bond Work Index (Wi) is material-specific and should ideally be from laboratory tests on a representative sample. Using values from a lookup table provides an estimate only.
- Feed vs. Product Size: Ensure the initial (feed) particle size df is always larger than the final (product) particle size dp. The calculator will flag an error if this is not the case.
Frequently Asked Questions
Each law is based on a different physical assumption. Kick assumes energy is used to create stress for fracture, proportional to volume. Rittinger assumes energy is used to create new surface area. Bond assumes energy is used to propagate cracks. These different models naturally lead to different predictions, with each being more accurate in a specific particle size range (coarse, fine, or intermediate).
There is no single “most accurate” law for all situations. However, Bond’s Law and its associated Work Index (Wi) have become the industry standard for mill design and power calculation because it performs reliably across a wide range of crushing and grinding applications found in the mineral processing industry.
F80 refers to the “Feed 80%” size, which is the mesh size in micrometers through which 80% of the feed material passes. Similarly, P80 is the “Product 80%” size, the mesh size through which 80% of the ground product passes. These are standard metrics used in the Bond’s Law formula to characterize the size distribution of the material.
The Bond Work Index is determined experimentally using a standardized laboratory procedure called the Bond Ball Mill Grindability Test. A sample of the ore is ground in a calibrated laboratory mill until a target product size is reached, and the energy consumed is measured. The calculator provides a lookup for common materials, but these are average values.
Yes. The Bond Work Index method includes corrections for different grinding conditions. The standard test is for wet grinding. If you are performing dry grinding, the calculated work input should typically be multiplied by a factor of 1.3. This calculator uses the base formula, so for dry grinding, you would need to adjust the results or the input Wi accordingly.
Rittinger’s law is highly sensitive to the product size (dp), as the energy is proportional to 1/dp. For very fine grinding (small dp), this term becomes very large, reflecting the massive increase in surface area. This often leads to a much higher energy prediction than Bond’s or Kick’s laws, which is why it is considered most applicable to fine powder production.
If your specific material isn’t listed, you should seek out data from literature, handbooks, or ideally, have a lab test performed. You can also use the value for a geologically similar material as a rough first-pass estimate, but be aware of the potential for significant error.
No. These laws calculate the theoretical net energy required for the size reduction itself. They do not account for mechanical and electrical inefficiencies of the motor, drive train, or the mill/crusher. The actual power drawn from the grid will be higher. A typical motor and drive efficiency of 90-95% should be considered for total power planning.
References
- Wills, B. A., & Finch, J. A. (2015). Wills’ Mineral Processing Technology: An Introduction to the Practical Aspects of Ore Treatment and Mineral Recovery. Elsevier. (Chapter 6: Comminution).
- Perry, R. H., & Green, D. W. (2008). Perry’s Chemical Engineers’ Handbook (8th ed.). McGraw-Hill. (Section 21: Solid-Solid Operations and Processing).
- Bond, F. C. (1952). The third theory of comminution. Transactions of the American Institute of Mining, Metallurgical, and Petroleum Engineers, 193, 484-494.
- Napier-Munn, T. J., et al. (1996). Mineral Comminution Circuits: Their Operation and Optimisation. Julius Kruttschnitt Mineral Research Centre (JKMRC), The University of Queensland.
Disclaimer
This calculator is intended for educational and preliminary estimation purposes only. The results are based on empirical models and user-provided inputs, which may not fully represent the complexities of a real-world industrial process. Factors such as ore variability, moisture content, circuit efficiency, and equipment type can significantly affect actual energy consumption. For detailed engineering, equipment selection, and process design, always consult with a qualified professional engineer.

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