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www.thecementgrindingoffice.com www.thecementgrindingoffice.com  All rights reserved © 2012-201

 All rights reserved © 2012-2013 The Cement Grinding Office3 The Cement Grinding Office Cement ball mill sizing method explanation

Cement ball mill sizing method explanation

1 Introduction: 1 Introduction:

-

- The Bond method The Bond method is used to size is used to size a cement ball a cement ball mill.mill. -

- Efficiency correcEfficiency correction factors tion factors are applied are applied with the with the Bond equation.Bond equation. -

- The method is The method is valid both for clvalid both for clinker grinding and inker grinding and for raw materials for raw materials grinding.grinding. -

- This method only gives a This method only gives a rough and initial idea for sizing rough and initial idea for sizing a cement ball mill. To go aheada cement ball mill. To go ahead, a deeper study is, a deeper study is necessary with ball mills suppliers or a specialized engineering office.

necessary with ball mills suppliers or a specialized engineering office. -

- Two calculators hTwo calculators have been developed ave been developed for sizing monochamber for sizing monochamber mills and two mills and two compartments mills.compartments mills. 2

2 Bond Bond equation equation and and correction correction factors:factors: -

- The well-known The well-known Bond formula Bond formula used is tused is the following:he following:

ith: ith: E = specific energy in kW E = specific energy in kW h/th/t i = work index in kWh/t i = work index in kWh/t C = correction factor  C = correction factor  P80 = sieve wich has 80%

P80 = sieve wich has 80% of passing in the productof passing in the product F80 = sieve wich has 80% of passing in the feed F80 = sieve wich has 80% of passing in the feed -

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ith:

C1 is a correction for dry grinding, C2 is a correction for open circuit C3 is a correction for mill diameter, C4 is a correction for feed size, C5 is a correction for product fineness.

C6 is a correction for high-efficiency separators. - C1 definition:

- C2 definition:

The graph here below is the basis to get C2:

- C3 definition:

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- C5 definition:

- C6 definition:

www.thecementgrindingoffice.com 3 Define fresh feed characteristics:

- Composition: Percentage of each component, Specific gravity (kg/dm3), Work indes (kWh/t) and F80. - F80 must be a representative average of various sampling campaigns of each component.

4 Define target fineness:

- Blaine fineness (cm2/gr) and/or a residue on a certain sieve

- Specify the P80 of the product. It must be a representative average of various particle size analysis of the product. 5 Define production target:

- Production of the mill in t/h 6 Define efficiency factors:

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installations where the raw mills are working in wet process.

- Determine if it is a closed or open circuit. New installations are 99% in closed circuit.

- To define C3 which is the correction factor for mill diameter, it is indispensable to choose a temporary diameter  (which is in fact an unknown) in meters. An experienced Process Engineer has already a good idea about the future diameter of the mill. Later, he will have to modify this diameter in function of the result given by the calculation. It is an iteration.

- C4 and C5 factors are automatically calculated with the data of point 4. - Determine if it is a High Efficiency separator or not.

7 Define the estimated mill specific energy:

- This calculation is carried out with the main Bond formula. 8 Define the absorbed power required:

- Multiply the estimated energy required E by the target production. The found value is the absorbed power  at the mill shaft, in other words before the transmission.

- Determine the type of transmission to add the inefficiency factor.

- Recalculate the specific energy with the absorbed power required at terminals. 9 Sizing of the ball mill:

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- Multiply this L/D ratio by the diameter to find the usefull mill length. - Define the mill speed respecting usual values as shown below:

www.thecementgrindingoffice.com

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- Multiplying the value found here above by the production target will give the required absorbed power  for chamber 1.

- Specify a working filling degree (volume load) in % for first chamber:

- ith the power formula, we can now calculate the length of chamber 1.

- If a DIN (*) configuration is selected, define a new length closed to the calculated value and verify if the new specific power is OK.

(*) distance of 250mm between bolts on t he length

- A new chamber 1 absorbed power is calculated with the DIN length. - Verify again if the chamber 1 specific power is correct.

- Calculate the second chamber length.

- If a DIN configuration is selected, define a new length closed to the calculated value. - Specify a working filling degree (volume load) in % for second chamber with the table above.

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- Calculate the absorbed power of chamber 2. - Calculate the total absorbed power.

- Iteration starts here comparing the absorbed power calculated just before with the one found in point 8. - A difference of maximum 2% is allowed between both powers. If the difference is higher, modify the mill

diameter, the L/D ratio, the mill speed and the filling degrees in order to decrease the difference but keeping in mind that all usual values are respected. Maybe changing one or two parameters is enough

o get the result.

arning: the method is the same for a monochamber mill. It is even easier because there isn't 1st chamber. 11 Other power correction factors:

- If there is 50% or more slag in the fresh feed,

- If the clinker is for the production of Alumina cement (ciment fondu in french), - If there are retention rings (similar as Danula rings) in the second chamber, - If there are cylpebs in the second chamber,

- If there is a lifting-classifying lining in case of monochamber mill and - If the fresh feed is coal in case of monochamber mill,

- Various corrections factors are applied for first chamber and/or second chamber and for monochamber mill absorbed power.

11 Ball mill final dimensions:

- Specify the width internals: feed end liners, intermediate diaphragm and outlet diaphragm to know the full length length of the mill.

- Calculate the tonnage of balls in function of the volume loads defined before. 12 If necessary, drying chamber (for raw mill):

- Specify the maximum moisture of the fresh feed components. - The required drying chamber volume is automatically calculated.

- Define the diameter which usually is the same than the grinding part of the mill but can also be a bit lower. - The required length is automatically calculated by dividing the volume by the area.

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- The drying chamber absorbed power is calculated. - The total mill absorbed power is calculated. 13 Required installed power:

- e take into consideration a factor of 1,1 to calculate the installed power of the mill but the mill's supplier has to recommend for that (possibility of filling degree increase).

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9.1. The drying chamber:

This chamber helps the drying of the material with the help of lifters. The material is lifted and after falls in the hot gas stream.

Which length must have a drying chamber?

 According to industrial experiences, it is possible to dry a maximum of 

220-230 l/m3.h

of water to be efficient. This figure is generally

accepted to size the drying chamber.

Example:

- Mill diameter: 4.6 m

- Mill output: 230 t/h

- Limestone moisture: 4%

=> quantity of water: 230 * 1000 * 4% = 9200 l/h

=> volume requested: 9200 / 225 = 40.89 m3

=> length of the drying chamber: 40.35 / (p * 4.6

2

/ 4) = 2.46 m (with the transfer diaphragm)

We will take a length of 2.50 m as it is DIN.

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References

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