Page 216 - Chemical engineering design
P. 216

193
                                                FLOW-SHEETING
                            containing around 0.5 per cent w/w MEK, is recycled to the absorption column.
                            The extract, which contains around 20 per cent w/w MEK, and a small amount
                            of butanol and water, is fed to a distillation column.
                         5. A distillation column, which separates the MEK and alcohol from the
                            solvent TCE.
                            The solvent containing a trace of MEK and water is recycled to the extraction
                            column.
                         6. A second distillation column, which produces a pure MEK product from the
                            crude product from the first column. The residue from this column, which
                            contains the bulk of the unreacted 2-butanol, is recycled to the reactor.
                         For a production rate of 1250 kg/h MEK:
                         1. Draw up an information flow diagram for this process.
                         2. Estimate the split-faction coefficients and fresh feeds for each stage.
                         3. Set up the resulting material balance equations, in matrix form.
                         4. Solve the equations using a suitable spread-sheet.
                         5. Adjust the values chosen for the split-fractions and feeds, so the results meet
                            the constraints,
                         6. Draw a flow-sheet for the process.








































                     Postscript: The design problems given in Appendix F provide more problems in flow-sheeting.
   211   212   213   214   215   216   217   218   219   220   221