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8-14   WATER AND WASTEWATER ENGINEERING

                             TABLE 8-2
                              Typical ranges for design data and criteria for strong acid cation and strong base anion resins
                                                      Strong acid     Strong base
                            Parameter                 cation resin    anion resin        Unit
                            Exchange capacity         3.6–5.5         1.8–2.0            meq/g as CaCO 3
                                                      1.6–2.2         0.8–1.4            meq/mL as CaCO 3
                                          a
                            Operating capacity        50–70           40–60              % of exchange capacity
                            Moisture content          40–80           35–80              %
                                                                                             3
                            Shipping weight (moist)   640–930         670–720            kg/m
                            Screen size               16   50         16   50
                                                                                           3    3
                            Service flow rate         200–2000        200–2000           m /d · m  of resin
                                                      8–40            8–40               BV/h
                                                                                           3    2
                            Surface loading rate      400–800         400–800            m /d · m  or m/d
                                                                                           3    2
                            Backwash rate             12–20           5–7.5              m /h · m  or m/h
                            Backwash duration         5–15            5–20               min
                            Bed expansion             50              50–75              %
                            Regenerant                NaCl            NaCl
                            Regenerant concentration  5–10            2–15               %
                                                                                                  3
                            Regenerant dose           80–320          80–320             kg NaCl/m  of resin
                                                                                                2
                                                                                           3
                            Regeneration flow rate    60–120          60–120             m /d · m  or m/d
                                                      2–5             2–5                BV/h
                            Rinse volume              2–5             2–10               BV
                            pH range                  0–14            0–14               units

                            Max. operating temp.      140             OH  form   60;     	C

                                                                      C  form   100
                            Turbidity limit           5               5                  NTU
                            Iron limit                5               0.1                mg/L as Fe
                            Total Fe   Mn             0.3             0.3                mg/L
                            Chlorine limit            1.0             0.1                mg/L of Cl 2
                              a
                                Operating capacity depends on the method of regeneration and amount of regenerant applied.
                               Sources:  Clifford, 1999; GLUMRB, 2003; MWH, 2005.


                            from the exchange capacity in that it is a measure of the actual performance of the resin under
                            a defined set of conditions such as the raw water composition,  empty-bed contact time  (EBCT)
                            or  service flow rate  (SFR), and degree of regeneration. The operating capacity is always less
                            than the advertised exchange capacity because of incomplete regeneration, early leakage (break-
                            through) that causes termination of the operational cycle to meet design limits, and efficiency of
                            regeneration (measured as eq NaCl/eq CaCO  3  ).
                                 Small laboratory columns (1.0 to 5.0 cm inside diameter) have been effective in analyzing
                            alternative resins. These columns can be scaled directly to full scale design if the loading rate
                            and EBCT are the same. Because the resin beads are small compared to the column diameter,
                            the error due to channeling of the water down the walls is small. The hydraulics of full scale
                            operation cannot be modeled by these small scale columns (MWH, 2005).
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