News Date:2017-04-18 09:09:03
Limestone calcination has been carried out in a highly instrumented pilot-scale rotary kiln. Local gas, solids, and wall temperatures and pct calcination have been measured under a range of operating conditions to determine the influence of limestone type, feed rate, rotational speed, inclination angle, and particle size on calcination and heat flow in the kiln. Thus, it has been found that the local calcination is dependent primarily on the solids temperature and hence on heat transfer. Of the variables studied, the limestone feed rate has the strongest effect on the temperature and calcination fields, whereas inclination angle and rotational speed are relatively less important. The different limestones studied exhibited significant differences in heat-absorption capacity and calcination temperature which may be related to their radiative properties. Increasing particle size over a range of 0.75 to 3.5 mm resulted in an increase in both heat transfer to the bed and calcination.
Rotary kiln 2,5х75 m Performance data
|
Rotary kiln
|
Type
|
Operating type
|
Drum volume (m3)
|
Mass (kg)
|
|
RK 1.6x8
|
Parallel flow
|
continuous
|
16.0
|
12 400
|
|
RK 1.6x10
|
Parallel flow
|
continuous
|
20.1
|
13 500
|
|
RK 1.6x16
|
Parallel flow
|
continuous
|
32.0
|
17 800
|
|
RK 2.2x14
|
Parallel flow
|
continuous
|
52.3
|
33 625
|
|
RK 2.5x75
|
Parallel flow
|
continuous
|
|
|
|
RK 2.8x14
|
Parallel flow
|
continuous
|
84.08
|
48950 – 53 700
|
|
RK 2,8x14
|
Counter flow
|
continuous
|
84.2
|
61 200
|
|
RK 2,8x20
|
Parallel flow
|
continuous
|
120.1
|
72 930
|
|
RK 3,5x27
|
Parallel flow
|
continuous
|
250.0
|
200 000
|
