Page 70 - Coulson Richardson's Chemical Engineering Vol.6 Chemical Engineering Design 4th Edition
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53
                                       FUNDAMENTALS OF MATERIAL BALANCES
                   separated from the recycle stream in the separation units these inerts would accumulate in
                   the recycle stream until the stream eventually consisted entirely of inerts. Some portion
                   of the stream would have to be purged to keep the inert level within acceptable limits. A
                   continuous purge would normally be used. Under steady-state conditions:
                             Loss of inert in the purge D Rate of feed of inerts into the system
                     The concentration of any component in the purge stream will be the same as that in
                   the recycle stream at the point where the purge is taken off. So the required purge rate
                   can be determined from the following relationship:
                              [Feed stream flow-rate] ð [Feed stream inert concentration] D
                         [Purge stream flow-rate] ð [Specified (desired) recycle inert concentration]


                   Example 2.14
                   In the production of ammonia from hydrogen and nitrogen the conversion, based on either
                   raw material, is limited to 15 per cent. The ammonia produced is condensed from the
                   reactor (converter) product stream and the unreacted material recycled. If the feed contains
                   0.2 per cent argon (from the nitrogen separation process), calculate the purge rate required
                   to hold the argon in the recycle stream below 5.0 per cent. Percentages are by volume.


                   Solution
                   Basis: 100 mols feed (purge rate will be expressed as mols per 100 mol feed, as the
                   production rate is not given).
                     Process diagram

                                                                     Purge 5% argon
                                                 Recycle
                                 Feed                                   Liquid
                                 0.2%            Reactor
                                                                         NH 3
                                 argon                           Condenser
                   Volume percentages are taken as equivalent to mol per cent.
                     Argon entering system with feed D 100 ð 0.2/100 D 0.2mol.
                     Let purge rate per 100 mol feed be F.
                     Argon leaving system in purge D F ð 5/100 D 0.05F.
                     At the steady state, argon leaving D argon entering

                                                0.05F D 0.2
                                                         0.2
                                                    F D      D 4
                                                         0.05
                   Purge required: 4 mol per 100 mol feed.


                                                2.16. BY-PASS
                   A flow stream may be divided and some part diverted (by-passed) around some units.
                   This procedure is often used to control stream composition or temperature.
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