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Flocculation                                                                                     293



            coagulant and the passage of water through the sand.’’ Sedi-  The research and the ensuing design for the Sacramento plant
            mentation of the ‘‘coagulum’’ prior to filtration was a recog-  (Langelier, 1921), established the guidelines for flocculation
            nized part of the treatment train. Initially, the Sacramento  practice. The outcomes of this work were as follows:
            plant had ample sedimentation detention time but did not
            have provision for thorough mixing of the alum after its  1. The jar test was invented as a means to explore the
            addition. This led to dramatic breakthroughs in water treat-  role of coagulation variables.
            ment, described in Langelier’s words in an oral history inter-  2. The concept of flocculation was discovered.
            view by Chall (1982, pp. 24–26):                      3. The role of gentle mixing to promote floc growth
                                                                    was established.
                                                                  4. Paddle-wheel flocculators were developed.
              It immediately occurred to me that I could demonstrate in our
                                                                  5. An on-site pilot plant study complemented the
              laboratory the advantages of thorough mixing in effecting good
                                                                    laboratory work.
              coagulation. I proposed this to Professor Hyde who readily
              agreed with my suggestion. I devised an apparatus for the  6. The studies led to the first full-scale plant to imple-
              demonstration. It consisted of six in-line, one liter, clear glass  ment paddle-wheel flocculators, i.e., at the new water
              jars, each provided with a slowly revolving paddle. The paddles  filtration plant at Sacramento, California, put on line
              were driven by a motorized shaft equipped with mitre gears.  in January, 1924.
                                                                  7. The importance of pH and alkalinity was discovered
              The first test runs were made with muddy water from the
                                                                    and principles were established that pH control was
              Sacramento River, and from the beginning our results were
                                                                    an important part of the coagulation process.
              strikingly successful and far beyond our expectations. The
                                                                  8. Langelier  recognized  the  complexity  of  the
              multi-jar feature made it possible to observe the effect of any
                                                                    coagulation–flocculation process and that the jar
              one variable; for example, the coagulant dosage, mixing time
                                                                    test apparatus and a pilot plant were the means to
              period, or rotational speed on the effectiveness of floc forma-
              tion and subsequent clarification through sedimentation.  isolate the variables.
              In these early tests, the outstanding observation was that in the  Figure 11.1 shows the design of the Sacramento WTP as
              absence of prolonged agitation or stirring beyond that required  modified by Langelier in 1919 to include paddle-wheel floc-
              to instantly diffuse the added coagulant chemical solution,  culators (but, as seen, did not include rapid mix). Langelier
              visible coagulation did not occur for several hours and clarifi-  also delineated the details of design, specifying that the
              cation often required an overnight settling period. With pro-
                                                               velocities of the water should be up to about 2.0 ft=s (as
              longed stirring, tiny flocs began to form within a few minutes
                                                               induced by the paddle wheels) and flocculation detention
              and as time progressed up to about 10 min, the individual floc
                                                               times should be about 30 min. Langelier also compared end-
              particles continued to grow in size and ultimately became
                                                               around baffling with the paddle-wheel design, in a separate
              widely separated. When the stirring was stopped, the flocs
              settled within a few minutes leaving a clear water above.  pilot plant constructed for such purpose, and concluded that
              After many repeated tests, it was concluded that adequate  the paddle-wheel method was the most desirable because of
              clarification with least chemical for a given water normally  greater flexibility in operation.
              required a mixing period of about 10 to 20 min.
                                                               11.3.1.3  Design Guidelines
              Using synthetic waters, we noted a moderate increase in the  To illustrate the evolution of practice, Leopold (1934,
              required coagulant with increased turbidity, but more signifi-
                                                               p. 1070) described the ‘‘mechanical agitation’’ used for alum
              cantly, and much to our surprise, we noted that the alum
                                                               floc formation in a 11.4 ML=day (3 mgd) plant at Winnetka,
              demand increased more directly with the bicarbonate alkalin-
                                                               Illinois treating water from Lake Michigan. The plant was
              ity of the water. This intrigued us very much and we tried
                                                               expanded to 22.8 ML=day (6 mgd) in 1932 with six floccula-
              increasing the bicarbonate content of the water by adding
                                                               tion basins with combined detention period of 30 min. The
              small increments of bicarbonate of soda.
                                                               mixer assembly was a 1.5 kW (2 hp), 5 speed motor, a speed
              In all these tests, we noted that optimum flocculation occurred  reducer, one set of bevel gears, and a vertical drive paddle
              when a definite fraction of the total alkalinity had been neu-  shaft. Each agitator had one paddle with a total surface area of
                                                                            2
                                                                     2
                                                                                          3
                                                                                                         2
              tralized. Without going into the chemical theory too deeply,  0.61 m (6.6 ft ) each or 125 m basin volume=m paddle
              this indicated that optimum flocculation was occurring at a  surface area (409 ft =ft ). The tip velocity of the paddle wheel
                                                                                 2
                                                                              3
              constant hydrogen ion concentration or pH, slightly above true  was variable, e.g., 0.24   v(tip)   0.74 m=s (0.78   v(tip)
              neutrality. We had arrived at an important conclusion in a
                                                                 2.41 ft=s) and u (all floc basins) ¼ 30 min. Camp (1955)
              roundabout way.
                                                               adopted the first two criteria in his recommendations for
                                                               design of flocculation basins; paddle-wheel area, however,
              The first few series of the jar tests proved very convincing
                                                               was a fraction of the cross-sectional area of the basin, i.e.,
              and he (Professor Hyde) immediately arranged for a small,
              continuous flow pilot installation in Sacramento for the  0.15–0.20 to avoid rotation of the water mass (p. 11) instead
              following summer. My recollection is that the Sacramento city  of as a ratio with respect to the basin volume. In other words,
              filtration plant, the first to use prolonged mechanical agitation to  in advancing the concept of flocculation to practice-specific
              induce flocculation, was placed in service in January, 1924.  guidelines were the key, and evolved with experience.
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