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Annex 2

                                                     SUMMARY KILN MATERIAL & HEAT BALANCE
Input                                                         Fuel Coal H=27 MJ/kg                                                           210 t/h
Heat consumption                                                                                                                              293 kcal/kg
                                                                                                                                               30 kgcoal/t siderite

                    INPUTS                                       Flow               Temp   Cp                                 Heat
                                              3
                                            Nm /kg      Nm3/h       kg/h kg/kgcal     o
                                                                                      C kcal/kgoC   kcal/kg   Gcal/h      kJ/kg     GJ/t     GJ/h         kW        %
Total Fuel combustion                                                                                293.18    39.17     1,227     1.227    163.95      45.58    76.09
Sensible heat of fuel kiln                                         6,072    0.045     60    0.178      0.49     0.06         2     0.002      0.27       0.08     0.13
Sensible heat of siderit                                         201,600    1.509     20    0.176      5.31     0.71        22     0.022      2.97       0.83     1.38
Water                                                              8,400    0.063     20    0.176      0.22     0.03         1     0.001      0.12       0.03     0.06
Sensible heat of cooling air+false air        0.42     55,518     71,584    0.536    626    0.251     84.31    11.26       353     0.353     47.15      13.11    21.88
Waste Air humidity                            0.01        900        723    0.005    626    0.478      1.62     0.22         7     0.007      0.91       0.25     0.42
Sensible heat of PA                           0.03      3,966      5,113    0.038     20    0.237      0.18     0.02         1     0.001      0.10       0.03     0.05
Waste Air humidity                            0.00         64         52    0.000     20    0.444      0.00     0.00         0     0.000      0.00       0.00     0.00
TOTAL OF INPUTS                               0.45      60,448    293,544   2.197                    385.32    51.48   1,613.26     1.61    215.48      59.90   100.00

                   OUTPUTS
Theoretical heat of reaction                                                                         64.00      8.55       268     0.268     35.79       9.95    16.61
Sensible heat of calcinate                                       133,594    1.000    800    0.218   174.56     23.32       731     0.731     97.62      27.14    45.30
Sensible heat of fly dust                                          2,562    0.019    274    0.190     1.00      0.13          4    0.004      0.56       0.16     0.26
Sensible heat of waste gases                  0.25     32,782     55,851    0.418    274    0.274    31.33      4.19       131     0.131     17.52       4.87     8.13
Sensible heat of material waste gases CO2     0.25     34,027     66,797    0.500    274    0.225    30.83      4.12       129     0.129     17.24       4.79     8.00
Water vapoor                                  0.08     10,460      8,400    0.063    274    0.456    39.29      5.25       164     0.164     21.97       6.11    10.20
Waste air                                     0.15     19,828     25,566    0.191    274    0.243    12.76      1.70         53    0.053      7.13       1.98     3.31
Water vapoor                                  0.01        964        774    0.006    274    0.456     0.72      0.10          3    0.003      0.40       0.11     0.19
Kiln +Preheater radiation                                            -                               30.83      4.12       129     0.129     17.24       4.79     8.00
Other losses and error                                               -                                0.00      0.00          0    0.000      0.00       0.00     0.00
TOTAL OF OUTPUTS                              0.73     98,061    293,544    2.197                   385.32     51.48   1,613.26     1.61    215.48      59.90   100.00
1               2             3           4       5
m                         150             800         1,000          97      20
g                          20             626         1,615         274     144



                                      Temperature evolution-Efficiency 30 kg coal/t
                       1800

                                                                    1,615
                       1600


                       1400


                       1200

    Temperature [oC]                                              1,000
                       1000
                                                                                               Material
                                                800
                        800                                                                    Gases
                                                                597.2289

                        600                               626


                        400
                                                                              274

                                150                                                 144
                        200

                                          20                                              20
                          0                                                  97
                                      1               2               3      4      5

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Summer

  • 1. Annex 2 SUMMARY KILN MATERIAL & HEAT BALANCE Input Fuel Coal H=27 MJ/kg 210 t/h Heat consumption 293 kcal/kg 30 kgcoal/t siderite INPUTS Flow Temp Cp Heat 3 Nm /kg Nm3/h kg/h kg/kgcal o C kcal/kgoC kcal/kg Gcal/h kJ/kg GJ/t GJ/h kW % Total Fuel combustion 293.18 39.17 1,227 1.227 163.95 45.58 76.09 Sensible heat of fuel kiln 6,072 0.045 60 0.178 0.49 0.06 2 0.002 0.27 0.08 0.13 Sensible heat of siderit 201,600 1.509 20 0.176 5.31 0.71 22 0.022 2.97 0.83 1.38 Water 8,400 0.063 20 0.176 0.22 0.03 1 0.001 0.12 0.03 0.06 Sensible heat of cooling air+false air 0.42 55,518 71,584 0.536 626 0.251 84.31 11.26 353 0.353 47.15 13.11 21.88 Waste Air humidity 0.01 900 723 0.005 626 0.478 1.62 0.22 7 0.007 0.91 0.25 0.42 Sensible heat of PA 0.03 3,966 5,113 0.038 20 0.237 0.18 0.02 1 0.001 0.10 0.03 0.05 Waste Air humidity 0.00 64 52 0.000 20 0.444 0.00 0.00 0 0.000 0.00 0.00 0.00 TOTAL OF INPUTS 0.45 60,448 293,544 2.197 385.32 51.48 1,613.26 1.61 215.48 59.90 100.00 OUTPUTS Theoretical heat of reaction 64.00 8.55 268 0.268 35.79 9.95 16.61 Sensible heat of calcinate 133,594 1.000 800 0.218 174.56 23.32 731 0.731 97.62 27.14 45.30 Sensible heat of fly dust 2,562 0.019 274 0.190 1.00 0.13 4 0.004 0.56 0.16 0.26 Sensible heat of waste gases 0.25 32,782 55,851 0.418 274 0.274 31.33 4.19 131 0.131 17.52 4.87 8.13 Sensible heat of material waste gases CO2 0.25 34,027 66,797 0.500 274 0.225 30.83 4.12 129 0.129 17.24 4.79 8.00 Water vapoor 0.08 10,460 8,400 0.063 274 0.456 39.29 5.25 164 0.164 21.97 6.11 10.20 Waste air 0.15 19,828 25,566 0.191 274 0.243 12.76 1.70 53 0.053 7.13 1.98 3.31 Water vapoor 0.01 964 774 0.006 274 0.456 0.72 0.10 3 0.003 0.40 0.11 0.19 Kiln +Preheater radiation - 30.83 4.12 129 0.129 17.24 4.79 8.00 Other losses and error - 0.00 0.00 0 0.000 0.00 0.00 0.00 TOTAL OF OUTPUTS 0.73 98,061 293,544 2.197 385.32 51.48 1,613.26 1.61 215.48 59.90 100.00
  • 2. 1 2 3 4 5 m 150 800 1,000 97 20 g 20 626 1,615 274 144 Temperature evolution-Efficiency 30 kg coal/t 1800 1,615 1600 1400 1200 Temperature [oC] 1,000 1000 Material 800 800 Gases 597.2289 600 626 400 274 150 144 200 20 20 0 97 1 2 3 4 5