Page 528 - Materials Chemistry, Second Edition
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CAT3525_C15.qxd  1/27/2005  12:40 PM  Page 499
                       Incineration of Hazardous Wastes                                            499
                       Properties of the waste constituents are as follows:

                                       Compound     Chemical      Molecular     Heat
                                                    Formula      Weight(MW)    Content
                                                                                (kJ/kg)
                                       Xylene       C H (CH )    106.16         42,989
                                                       4
                                                          3 2
                                                     6
                                       Toluene      C H CH 3      92.13         42,527
                                                     6
                                                       5
                                       Pentane      C H 12        72.14         49,142
                                                     5
                                       Water        H O           18.01             0
                                                     2
                         1. Calculate the total heat release in the incinerator.
                         2. Calculate the percent by volume of each component in the flow gas.
                       SOLUTION
                         1. Heat release in the incinerator:
                             Xylene heat release      0.40 x 42,989   17,196 kJ/kg
                             Toluene heat release     0.35 x 42,527   14,884 kJ/kg
                             Pentane heat release     0.23 x 49,142   11,303 kJ/kg
                             Water heat release       0 kJ/kg
                             Heat release/kg of mixture 43,382 kJ/kg
                             Total heat release in the incinerator
                             550 kg/h   43,382 kJ/h   23,860,100 kJ/h

                         2. Calculate the percent by volume of each component in the flow gas:
                             (a) Xylene: C H   11.5O → 8CO   5H O
                                        8  10      2        2    2
                                Mass of xylene   0.40   550 kg/h   220 kg/h
                                220/106   2.08 mol/h of xylene

                                            Component          MW           mol/h
                                            Xylene             106           2.08
                                            O                   32          23.92
                                             2
                                                                44          16.64
                                            CO 2
                                            H O                 18          10.4
                                             2
                                0.18   23.92   4.31 mol/h of O
                                                          2
                                23.92   4.31   28.32 mol/h of O
                                                           2
                                Note that air is 79% N and 21% O , so 79/21   28.23   106.20 mol N
                                                            2                             2
                             (b) Toluene: C H   9O → 7CO   4H O
                                         7  8    2       2     2
                                Mass of toluene   0.35   550 kg/h   192.5 kg/h
                                192.5/92   2.09 mol/h of toluene
                                            Component          MW           mol/h
                                            Toluene            92            2.09
                                            O                  32           18.81
                                             2
                                            CO                 44           14.63
                                              2
                                            H O                18            8.36
                                             2
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