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842                                                               Appendix F:  Alum Data and Conversions



            Equation F.7 was the basis for obtaining the values in Figure  set of experimental data such as given in Table CDF.3
            F.4b. The terms in the denominator for the conversions were,  (adapted from Table 1, General Chemical, 1995) one can
            SG(alum solution) ¼ 1.335, r(water) ¼ 998.2 g=L (208C).  use SG as a surrogate for concentration. Table CDF.3 has
                                                               several sub-tables as follows:
                                                                  Tables CDF.3(a) through CDF.3(d) are encapsulated in
            F.4.6 SPECIFIC GRAVITY–CONCENTRATION RELATION
                                                               Figures F.5 and F.6. Table CDF.3(e) expands on Section F.4.7.
            The specific gravity (SG) of an alum solution depends on its  Figure F.5 shows a plot of the data from Table CDF.3(d).
            concentration, i.e., mg Al 2 (SO 4 ) 3   14H 2 O=L solution. From a  The polynomial coefficients, also shown in Figure F.5, are a


                              TABLE CDF.3
                              Alum Conversions
                              Table CDF.3(a) Molecular weight of alum forms
                              Table CDF.3(b) Polynomial coefficients for estimating alum concentrations from SG
                              Table CDF.3(c) Polynomial coefficients for estimating alum mass percent solids from SG
                              Table CDF.3(d) Alum concentration as function of ‘‘dry alum’’ added
                              Table CDF.3(e) Cost calculation for alum as Al 3þ  and sensitivity to SG of liquid alum and C(Al )
                                                                                            3þ
                              [Double click on ‘‘Table CDF.’’ below to bring up Table CDF.3]




                         TABLE CDF.3
                         Alum Conversions (Excerpt Showing only Tables CDF.3(a) and (b))

                         Table CDF.3(a) Molecular Weights of Alum Forms  Table CDF.3(b) Polynomial Coefficients a
                         Element  at. wt.  Compound     MW       Compound      M0       M1      M2
                         Al      26.982  Al 2 (SO 4 ) 3   14H 2 O  594.136  Al 2 (SO 4 ) 3   14H 2 O   1011.9  312.25  699.2
                         S       32.066  Al 2 (SO 4 ) 3   18H 2 O  666.132  Al 2 (SO 4 ) 3   18H 2 O   1134.3  350.01  783.01
                         O       15.999  Al 2 (SO 4 ) 3  342.15  Al 2 (SO 4 ) 3   577.37  178  399.11
                         H        1.000  Al 2 O 3      101.961  Al 2 O 3       172.09  53.103  118.91
                         O       15.999  Al 2           53.964  Al 2           91.909  28.361  63.506

                                           3
                         Note: r(water) ¼ 998 kg=m .
                                                               a
                                                                For alum concentrations from SG alum, i.e.,
                                                                        y ¼ M0 þ M1   x þ M2   x 2



                            TABLE F.3
                            Cost of Liquid Alum a
                            (1) The cost of liquid alum in metric units is
                                              dollars       $181     ton  2:205 lb

                                          kg alum solution  ¼  ton alum solution 2000 lb     kg
                                                           $0:20
                                                      ¼
                                                       kg alum solution
                            (2) In terms of Al, the cost is (using mass percent Al from Table F.3 for SG ¼ 1.34)
                                              dollars   $0:20   kg alum solution
                                              kg Al  ¼  kg alum solution     0:0445 kg Al
                                                    $4:48
                                                   ¼
                                                    kg Al
                            Sources: Adapted from Letterman, R. D., Overview of Operational Control of Coagulation and Filtration
                                   Processes, Department of Civil Engineering, Syracuse University, Syracuse, NY, 2000, paper
                                   presented at Seminar on Water Treatment, New York Section, American Water Works
                                   Association Seminar, Rochester, NY, November 1985.
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