Page 180 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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178    Chapter 6 Evaporators





               Table 6.1 Comparison of multiple effect evaporator arrangements.
                Arrangement     Forward feed    Backward feed     Parallel feed    Mixed feed
               Entry of       First effect     Last effect      Each effect     Intermediate effect
               · Feed         First effect     First effect     First effect    First effect
               · Steam
               Liquor flow     Parallel to steam  Opposite to steam  Independently in  Forward feed for
                              flow              flow              each effect     some effects and
                                                                                backward feed for
                                                                                rest
               Product        Last effect      First effect     Each effect     First effect
               withdrawal from
               Advantages     Needs no inter-  -  Higher steam  -  Simplest in  -  Eliminates
                              effect transfer    economy          construction     some
                              pump             -  Suitable for  -  Feed washes     intermediate
                                                 viscous          deposit/scales   liquor pumps
                                                 products       -  More than one  -  Allows product
                                                                  product          draw from the
                                                                  concentration    highest
                                                                  obtained         temperature
                                                                                   stage
               Limitations    Low steam        -  Needs inter   Low steam       Low steam
                              economy for cold   effect transfer  economy       economy
                              feed               pump
               Applications   -  Hot feed      -  Cold feed     -  Used as      -  Used when
                              -  Product with  -  High product    crystallizing    liquor at
                                 scaling         viscosity        evaporator       intermediate
                                 tendency at a                    (e.g., Brine     concentration
                                 higher                           evaporation to   is also a
                                 temperature                      make common      product
                              -  Product                          salt)
                                 sensitive to a
                                 higher
                                 temperature
               General        Greater economy  Greater economy
               observation    for hot feed     for cold feed




                Thermocompression (TC) is attractive when steam is available at pressures much higher than can
                                                                2
                                                                                          2
                                    be used in evaporators, (>3 kg/cm (g)) and preferably over 7 kg/cm (g)).
                                    Usually, a portion of the steam evaporated from the product is compressed
                                    by a steam ejector and returned to the steam chest. The ejector also serves
                 Thermocompression
                                    as a reducing valve. Due to its low first cost and ability to handle large
                                    volumes of vapor, this method is an attractive option to improve the
                                    economy of evaporators that must operate at low temperatures, and hence,
             cannot be operated in the multiple-effect configuration. TC units do not operate well outside the design
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