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Process Description 7<br />

2.2.2 Semi-wet processes<br />

Semi-wet cement process<strong>in</strong>g employs grate-kiln methods (Figure 2.3). In <strong>the</strong> semi-wet<br />

cement manufactur<strong>in</strong>g process <strong>the</strong> raw materials prepared by wet process<strong>in</strong>g are first<br />

mechanically dewatered - preferably with filter presses - <strong>and</strong> <strong>the</strong>n fed <strong>in</strong> <strong>the</strong> form of<br />

nodules to a dry<strong>in</strong>g unit. This dry<strong>in</strong>g unit may be <strong>the</strong> third compartment of a travel<strong>in</strong>g grate<br />

preheater. Nowadays, a dispersion dryer or impact dryer is preferably <strong>in</strong>stalled ahead of <strong>the</strong><br />

preheater or precalc<strong>in</strong>er kiln. In cases where former wet kilns have been converted <strong>in</strong>to<br />

one-stage or two-stage preheater kilns on this pr<strong>in</strong>ciple, impact dryers have hi<strong>the</strong>rto been<br />

employed. Advantages of grate-kiln systems <strong>in</strong>clude:<br />

- a controlled feed rate<br />

- no flush<strong>in</strong>g of materials <strong>in</strong>to <strong>the</strong> kiln<br />

- no segregation of raw materials due to differential shapes <strong>and</strong> densities<br />

- avoidance of fluidization of <strong>the</strong> materials<br />

- m<strong>in</strong>imal dust<strong>in</strong>g<br />

- production of uniform cl<strong>in</strong>ker<br />

- low <strong>energy</strong> requirement (70% of that required for modern long wet kiln), <strong>and</strong><br />

- ability to use higher-alkali feeds than many o<strong>the</strong>r process<strong>in</strong>g techniques.<br />

2.2.3 Semi-dry process<br />

In <strong>the</strong> semi-dry process, nodules or pellets (approximately 12% water) formed from raw<br />

meal with <strong>the</strong> aid of water are used. The travel<strong>in</strong>g grate preheater kiln cont<strong>in</strong>ues to be<br />

available as a technically well developed pyro-process<strong>in</strong>g unit. Kilns of this type, however,<br />

suffer from some disadvantages <strong>in</strong>herent <strong>in</strong> <strong>the</strong> system, such as:<br />

- relatively high <strong>in</strong>itial cost <strong>and</strong> operat<strong>in</strong>g expenses associated with kiln outputs,<br />

- specific quality requirements of <strong>the</strong> raw materials (grate process requires nodules to<br />

be consistent <strong>in</strong> size <strong>and</strong> composition which is often very difficult to achieve),<br />

- relatively high overall heat consumption (only <strong>the</strong> exhaust air from <strong>the</strong> cooler is<br />

available for dry<strong>in</strong>g <strong>the</strong> materials dur<strong>in</strong>g gr<strong>in</strong>d<strong>in</strong>g),<br />

- restrictions as to <strong>the</strong> use of low-grade fuels, <strong>and</strong><br />

- <strong>in</strong>ability to apply precalc<strong>in</strong>ation.<br />

Because of <strong>the</strong>se drawbacks, this system has lost <strong>the</strong> weight it once possessed. However it<br />

is reported that several of <strong>the</strong> newer <strong>in</strong>stallations <strong>in</strong> <strong>the</strong> United States do employ grate-kiln<br />

methods (Sell, 1992). Depend<strong>in</strong>g upon <strong>the</strong> local conditions, <strong>in</strong> certa<strong>in</strong> situations, <strong>the</strong>y are<br />

deemed preferable to preheater systems.

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