Page 61 - Chemical engineering design
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                             There are three streams, feed, overheads and bottoms, and three independent compo-
                           nents in each stream.        CHEMICAL ENGINEERING
                              Number of variables (component flow rates) D 9
                              Number of independent material balance
                              equations                            D 3
                              Number of variables to be specified for
                              a unique solution                    D 9   3 D 6
                             Three variables are specified; the feed flow and composition fixes the flow of each
                           component in the feed.
                             Number of variables to be specified by designer D 6   3 D 3. Any three component
                           flows can be chosen.
                             Normally the top composition and flow or the bottom composition and flow would be
                           chosen.
                             If the primary function of the column is to separate the benzene from the other compo-
                           nents, the maximum toluene and xylene in the overheads would be specified; say, at
                           5 kg/h and 3 kg/h, and the loss of benzene in the bottoms also specified; say, at not
                           greater than 5 kg/h. Three flows are specified, so the other flows can be calculated.
                             Benzene in overheads D benzene in feed   benzene in bottoms.
                                                    0.6 ð 10,000   5 D 5995 kg/h

                             Toluene in bottoms D toluene in feed   toluene in overheads
                                                    0.3 ð 10,000   5 D 2995 kg/h

                             Xylene in bottoms D xylene in feed   xylene in overheads
                                                    0.1 ð 10,000   3 D 997 kg/h



                                                  2.11. TIE COMPONENTS
                           In Section 2.9 it was shown that the flow of any component was in the same ratio to the
                           flow of any other component, as the ratio of the concentrations of the two components.
                           If one component passes unchanged through a process unit it can be used to tie the inlet
                           and outlet compositions.
                             This technique is particularly useful in handling combustion calculations where the
                           nitrogen in the combustion air passes through unreacted and is used as the tie component.
                           This is illustrated in Example 2.8.
                             This principle can also be used to measure the flow of a process stream by introducing
                           a measured flow of some easily analysed (compatible) material.

                           Example 2.7
                           Carbon dioxide is added at a rate of 10 kg/h to an air stream and the air is sampled at a
                           sufficient distance downstream to ensure complete mixing. If the analysis shows 0.45 per
                           cent v/v CO 2 , calculate the air-flow rate.
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