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834                                                               Appendix F:  Alum Data and Conversions






                                                                               Ore


                             Sulfuric acid
                         Treating agents        Reactor
                                  Aluminum sulfate




                              Reactor
                                                       Water


                                                  Storage
                                                (liquid alum)
                                                                   Steam
                         Shipment:
                                     3
                         1. Rail 30.3–68.1 m  (8,000–18,000 gal)         Evaporator
                                          3
                         2. Tank truck: 12.5–20.8 m  (33,000–5,500 gal)


                                                          Crushing
                                                                              Cooling
                                      Grinding




                                                             Screening






                                                  Powder  Ground Granular  Lump  Shipment:
                                                                              1. Bulk by hopper rail car or truck
                                                                              2. 50–100 lb bags
                                                  Bags only
            FIGURE F.1 Alum manufacture—schematic. (Adapted from Harringer, R.D., Aluminum sulfate coagulation low temperature water,
            unpublished paper presented at CH2M-Hill Cold Water Coagulation Seminar, Denver, CO, July 13, 1984; General Chemical, Aluminum
            Sulfate (Alum)—Technical Data, Brochure CHEM-M5-23, General Chemical Corporation, 1995.)



            plant flow. These three flows are represented as one equation,  As stated, Equation F.1 encompasses the mass flow of
                                                                                                      _
            having three parts, i.e.,                          solid alum through the alum feeder, i.e., M(alum), the
                                                               mass flow of alum from the dissolution reactor (to the
                   _
                  M(alum) ¼ Q(alum feed)   C(alum feed)        rapid mix), and the mass flow of alum in the feed flow
                          ¼ Q(plant)   C(alum-in-plant-flow)  (F:2)  through the rapid mix. The concentration of alum in the
                                                               plant flow, i.e., C(alum in plant flow), is the ‘‘driver’’
            in which                                           variable and is determined by jar tests and=or by pilot
               _
              M(alum) is the mass flow of alum                  plant tests and may vary with changing raw-water quality.
                                                        3
              Q(alum feed) is the alum feed flow to rapid mix (m =s)  Example F.1 illustrates calculations to determine the mass
                                                                             _
              C(alum feed) is the concentration of alum in alum feed  flow of alum, M,and flow of alum concentrate feed,
                                    3
                flow to rapid mix (kg=m )                       Q(alum feed). As a criterion, the alum concentration,
                                                    3
              Q(plant) is the raw water flow through plant (m =s)  C(alum feed) should be >1%,i.e.,10gAl 2 (SO 4 ) 3
              C(alum in plant flow) is the concentration of alum as found  14H 2 O=L solution, since weaker solutions will hydrolyze
                                   3
                in the rapid mix (kg=m )                       and eventually plug lines.
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