Page 332 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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334    Chapter 11 Distillation




                (A)     Cooling    Cooling
                        water in   water out
                                     Condenser

              EQUALISER line
                 to condenser
                       shell           Reflex        (B)                           Condenser
                                       line
                                                                                   Cooling Water
                                                                                   3-way valve to
                                                                                   control reflux
                                                                             Distillate
                       Tray
                     column
                                      Distillate                   Vapour        Packed
                                                                                 column
                                                    Steam

                                                  Condensate                 Reboiler
                                           Change
                                           still                     Liquid  Bottoms
                Steam


                               Bottoms
                   Condensate
             FIGURE 11.18
                    Multistage Batch Distillation (A) Tray column above still, (B) Packed column beside still.


             vacuum, the vent is connected often through a surface condenser to the suction of an ‘ejectore
             barometric condenser’ arrangement. The surface condenser upstream of the ejector condenses much of
             the overhead vapour and reduces the vapour load to the ejector. The residual streams (bottoms) is
             usually taken out of the still after the dilatation ends once the still is cooler and safer to drain.
                Instrumentation scheme
                Instrumentation of the process consists of temperature measurements of the liquid in the still,
             vapour entering the condenser and the liquid collected in the accumulator vessel. Pressure is measured
             at the top of the still. This needs to be a compound gauge measuring both vacuum and pressure as
             condensation of vapour after shutdown may lead to vacuum in the system. The accumulator and the
             charge still are provided with level gauge glasses. In small plants these instruments locally indicate the
             readings, whereas in large plants there may be telemetry arrangement along with alarms associated
             with the process parameters. The charge still heat input should be regulated as this decides the start-up
             period and also production rate of distillate. In case of electrical heating the power to the heating
             element is regulated. Opening of the control valve in the heating steam supply line is manipulated to
             control heat input in case of steam heated still. Sudden increase of input heat may lead to large amount
             of vaporisation in the still and carryover of liquid along with distillate vapour. This leads to poorer
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