Page 180 - Chemical engineering design
P. 180

So, O 2 required to oxidise the NO in the inlet to stream to NO 2 , from reaction 4, D
                   15.7 ð  1  D 7.85 kmol.      FLOW-SHEETING                             157
                          2
                     Hence, the “free” oxygen in the inlet stream D 20.0   7.85 D 12.15 kmol.
                     Combining reactions (4) and (5) gives the overall reaction for the absorption of NO 2
                   to produce HNO 3 .
                                     Reaction 6.  4NO 2 C 2H 2 O C O 2 ! 4HNO 3
                   Using this reaction, the oxygen required to oxidise the NO formed in the absorber can be
                   calculated:
                                                                                     1
                           O 2 required to oxidise NO formed Df NO C NO 2   in stream  6 gð
                                                                                     4
                                                        D  48.9 C 15.7  ð  1  D 16.15 kmol
                                                                        4
                   So O 2 required for complete oxidation, in addition to that in inlet gas
                                             D 16.15   12.15 D 4kmol
                   Let the secondary air flow be y kmol. Then the O 2 in the secondary air will be D
                   0.21 y kmol. Of this, 4 kmol react with NO in the absorber, so the free O 2 in the tail
                   gases will be D 0.21 y   4kmol.

                     N 2 passes through the absorber unchanged, so the N 2 in the tail gases D the N 2 entering
                   the absorber from the cooler-condenser and the secondary air. Hence:

                                         N 2 in tail gas D 720 C 0.79 y kmol.
                     The tail gases are essentially all N 2 and O 2 (the quantity of other constituents is
                   negligible) so the percentage O 2 in the tail gas will be given by:
                                                           0.21 y   4 100
                                   O 2 per cent D 3 D
                                                     720 C 0.79 y  C  0.21 y   4
                   from which
                                                  y D 141.6kmol
                   and the O 2 in the tail gases D 141.6 ð 0.21   4 D 25.7kmol
                   and the N 2 in the tail gases D 720 C 111.8 D 831.8kmol.

                     Tail gas composition, the tail gases will contain from 0.2 to 0.3 per cent NO, say 0.2
                   per cent, then:
                                                        0.2
                               NO in tail gas D total flow ð  D  N 2 C O 2   flow ð 0.002
                                                        100
                                           D  831.8 C 25.7 0.002 D 1.7kmol
                     The quantity of the secondary air was based on the assumption that all the nitric oxides
                   were absorbed. This figure will not be changed as it was calculated from an assumed
                   (approximate) value for the concentration of the O 2 in the tail gases. The figure for O 2
                   in the tail gases must, however, be adjusted to maintain the balance.
                     The unreacted O 2 can be calculated from Reactions (4) and (6). 1.7 kmol of NO are not
                                                                                1
                                                                            1
                   oxidised or absorbed, so the adjusted O 2 in tail gases D 25.7 C 1.7  C   D 27.0 kmol.
                                                                            4   2
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