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Engineering Chemistry S Datta

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420 ENGINEERING CHEMISTRY

may be employed as the collector. A concentration of 0.04 lb per ton of rock suspended in 4 tons

of water has given good results. Frothing aids in separation of desired materials from the

undesired ones.

Manufacturing Procedure

Two methods of manufacture are used:

• Wet process

• Dry process

The wet process was the original one. For a time it was gradually displaced by the dry

process. But the wet process is now being adopted largely for new plants for more accurate

control and mixing of the raw mixture.

In the wet process, the solid material after dry crushing is reduced to a fine state of

division in wet tube or ball mills and passes as a slurry through the bowl classifiers or screens.

The slurry is pumped to correcting tanks where rotating arms make the mixture homogeneous

and allow the final adjustment in composition of raw materials to be made. This slurry is

filtered in a continuous rotary filter and fed into the kiln. The moisture content of the feed is 40%.

The dry process is especially applicable to natural cement rock and to the mixtures of

limestone and shale or slate. In this process, the materials are roughly crushed in jaw crushers

followed by gyratory mills, then dried, sized and more finely ground in tube mills. This dry

powdered material (moisture content 2%) is fed directly to the kiln. Heat is provided by burning

oil, gas or pulverised coal, using preheated air from cooling the clinker. 80-160 lbs of fuel are

necessary per barrel (376 lbs) of cement.

The tendency in recent years has been to lengthen the rotary kiln in order to increase its

thermal efficiency. Dry process kilns may be as short as 150 ft, but in the wet process,

300-500 ft kilns are not uncommon. The internal diameter is usually 8 to 15 ft. The kilns are

rotated at from 1/2 to 2 r.p.m., depending on size. The kilns are slightly inclined so that materials

fed in at the upper end and travel slowly to the lower end, taking from 2-3 hrs (Fig. 19.6).

In order to obtain greater heat economy, unit operations are used for removing the part

of the water from slurry by slurry filters. Waste heat boilers are used to conserve heat.

Because the lining of kiln has to withstand severe abrasion and chemical attack at the

high temperatures in the clinkering zone, the choice of refractory linning is difficult. For this

reason, high alumina bricks and high magnesia bricks are widely used for the lining of the

kiln, although Portland cement clinker itself is satisfactory for the purpose.

Reactions at various temperatures in the kiln

Temperature Reactions Heat change

100°C Evaporation of water (H 2

O↑) Endothermic

> 500°C Al 2

O 3

. SiO 2

. xH 2

O ⎯⎯→ Al 2

O 3

.SiO 2

+ xH 2

O Endothermic

> 900°C CaCO 3

⎯⎯→ CaO + CO 2

↑ Endothermic

900°C *5CaO + 3 Al 2

O 3

⎯⎯→ 5 CaO . 3Al 2

O 3

to 2CaO + SiO 2

⎯⎯→ 2CaO . SiO 2

1200°C 3CaO + SiO 2

⎯⎯→ 2CaO . SiO 2

2CaO + Al 2

O 3

⎯⎯→ 2CaO . Al 2

O 3

U

V

|

3CaO + Al 2

O 3

⎯⎯→ 3CaO . Al 2

O 3 W

|

Exothermic

(Contd...)

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