admin
1156 posts
TimePosted 22/08/2006 10:21:09
admin says

Cement milling Question 10

I want to know what is Roslin Ramler slope and characteristic value forcements? Do they have any relationships and how do you understand the fineness by using them.

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admin
1156 posts
TimePosted 22/08/2006 10:21:09
admin says

Re: Cement milling

The Rosin-Rammler-Sperling-Bennett particle size distribution for cement is found by measuring the residue on various sieves (25,32,45,63,90 micronsetc.) Alternatively you can use laser granulometry or some other method of measuring the residues. You then plot the natural log of the sieve sizes on the x axis (ln(sieve)), against the double natural log of 100 divided by the residue on the y axis (ln(ln(100/Residue))). The reason for using these axes is that for fine powders such as cement the plot approximates to a straight line. The slope of the line gives a measure of the "tightness" of the particle size distribution and varies from 0.8 to 1.1 for cements, dependent on the type of equipment used for grinding. The characteristic grain size is the sieve size where 36.8 per cent of the cement would be retained. This can be calculated from the slope and intercept of the RRSB line and is typically between 20 and 30 microns for cement.

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admin
1156 posts
TimePosted 22/08/2006 10:21:09
admin says

Cement milling Question 11

I have two questions: What is the effect of NOx and SOx in controlling the burning zone temperature and what other parameters like kiln torque, kiln inlet oxygen or if anything else affects the kiln operation.
Secondly, how to improve the ventilation in ball mills, as we observe the coating formation on the balls is on the high side.

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admin
1156 posts
TimePosted 22/08/2006 10:21:10
admin says

Re: Cement milling

The weight of grinding balls in the mill and the power drawn by the mill main motor are directly proportional to one another. Therefore it is possible to reduce the power drawn by the mill by reducing the ball charge. However, this will then result in the output of the mill falling due to less grinding balls being present to grind the clinker and generate surface area. As with all these things there is an optimum ball charge and output which corresponds to the lowest unit energy consumption.

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