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    3. Limestone calcination in a rotary kiln

      18 Apr,2017 UTC+8 Views:


       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

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