admin
1156 posts
TimePosted 22/08/2006 10:21:32
admin says

Raw materials Question 25

NOx control approaches applicable to the cement industry may be grouped in three categories: process modifications, combustion control, and NOx reduction controls. One process modification that can be quantified is the CemStar process, which is a small addition of steel slag to the raw kiln feed. Can you provide more information on CemStar?

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admin
1156 posts
TimePosted 22/08/2006 10:21:32
admin says

Re: Raw materials

TXI have published various papers on their patented Cemstar process. The addition of steel slag or air cooled blast furnace slag boosts the output of the kiln with virtually no increase if fuel consumption as the slags have already effectively been clinkered and contains trace elements that mineralise the combination of the kiln feed into the clinker in the kiln. More product with the same amount of fuel burnt inevitably dilutes the NOx emissions per tonne of clinker produced. The mineralising effect may also lead to lower burning zone temperature, and less thermal NOx formation in the flame. The real crux of the technology is adjusting the chemistry of the kiln feed to maintain the desired clinker mineralogy when the slags are being added t the kiln inlet. With steel slag the iron oxide input is increased and has to be compensated by increasing the alumina and silca modulii. With air cooled blast furnace slag the material is deficient in lime therefore the LSF of the kiln feed has be increased. This inevitably increases the demand for high CaCO3 content in limestone and is often the limiting factor.

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admin
1156 posts
TimePosted 22/08/2006 10:21:32
admin says

Raw materials Question 26

I would like to know how to estimate the quantity of grinding media of each size required for a ball mill using the data; mill size, number of chambers and type of material to be ground. Kindly explain me what formula is to be used.

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admin
1156 posts
TimePosted 22/08/2006 10:21:32
admin says

Re: Raw materials

The total quantity of media required for each chamber is determined by calculating the internal volume of the chambers. A rule of thumb is to change the first chamber to 30 per cent of this volume and the second chamber to 27 per cent. You can use 4.6t/m3 as the density of grinding media. As for the individual ball size gradings this has to be determined by conducting a series of axial tests in the mill while you are building up the media charge.

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