Page 116 - Chemical engineering design
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96
                             Reactions: C C O 2 ! CO 2
                                            1
                                       H 2 C O 2 ! H 2 O  CHEMICAL ENGINEERING
                                            2
                                Element      kg       kmol      Stoichiometric O 2   kmol, products
                                                                      kmol
                                  C         87.5       7.29           7.29           7.29, CO 2
                                  H 2        8.0       4.0            2.0            4.0, H 2 O
                                  O 2        3.5       0.11                          0.11
                                  N 2        1.0       0.04                          0.04
                                 Total                11.44           9.29

                             O 2 required with 20 per cent excess D 9.29 ð 1.2 D 11.15 kmol.
                             Unreacted O 2 from combustion air D 11.15   9.29 D 1.86 kmol.
                                                           79
                             N 2 with combustion air D 11.15 ð  D 41.94 kmol.
                                                           21
                           Composition of combustion gases:
                                                                   D 7.29 kmol
                                                   CO 2
                                                   H 2 O           D 4.0
                                                        0.11 C 1.86 D 1.97
                                                   O 2
                                                        0.04 C 41.94 D 41.98
                                                   N 2
                             Presentation of data to the program:
                           C p of fuel (component 5), taken as constant,
                                                     A D 1.6,  B D C D D D 0

                             Heat of reaction and latent heat, taken to be values at datum temperature of 298 K.
                             There is no need to convert to kJ/kmol, providing quantities are expressed in kg. For
                           the purposes of this example the dissociation of CO 2 and H 2 O at 1500 K is ignored.

                           Computer print-out
                           Data inputs shown after the symbol (?)
                           RUN
                           HEAT BALANCE PROGRAM, BASIS kmol/h, TEMP K, DATUM 298 K
                           INPUT THE NUMBER OF COMPONENTS, MAXIMUM 10
                           ?5
                           INPUT HEAT CAPACITY DATA FOR EQUATION A+BT+CT^2+DT^3
                           FOR COMPONENT 1 INPUT A, B, C, D, INCLUDING ANY ZERO VALUES
                           ? 19.763, 7.332E-2, -5.518E-5, 1.7125E-8
                           FOR COMPONENT 2 INPUT A, B, C, D, INCLUDING ANY ZERO VALUES
                           ? 32.19, 1.9207E-3, 1.0538E-5, -3.591E-9
                           FOR COMPONENT 3 INPUT A, B, C, D, INCLUDING ANY ZERO VALUES
                           ? 28.06, -3.67E-6, 1.74E-5, -1.0634E-8
                           FOR COMPONENT 4 INPUT A, B, C, D, INCLUDING ANY ZERO VALUES
                           ? 31.099, -1.354E-2, 2.6752E-5, -1.1662E-8
                           FOR COMPONENT 5 INPUT A, B, C, D, INCLUDING ANY ZERO VALUES
                           ?1.6,00, 0,0
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