Page 644 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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Gas Transfer                                                                                     599



            18.4.2.3  Wurtsmith AFB: Oscoda, Miami                     dioxide concentration (by titration). From what
            The contamination at the site was trichloroethylene (TCE),  you know of Henry’s law, estimate the concen-
            caused by a leaking underground storage tank near a main-  tration that you would measure assuming no
            tenance facility. Two packed-tower air strippers in series were  experimental error of analysis.
            installed, each 1.52 m (5 ft) diameter, 9.14 m (30 ft) high, with  (c) Assume that you obtain a measurement of carbon
            5.49 m (18 ft) 16 mm pall-ring packing, with air=water     dioxide in (b) by titration. Describe the major
                                            3
            ratio ¼ 25:1 and Q(water) ¼ 0.0378 m =s (600 gpm). The     experimental error.
            TCE removal was 0.86–0.98 fraction for a single tower and  18.4 Gas Transfer Coefficient—Is Determination for Oxygen
            0.999 fraction overall. Biological growths were a maintenance  Applicable to Different Gases Using the Same System?
            problem and required repeated removal and cleaning.     Given=Required
                                                                    For a lab experiment, K L a was determined to be 0.029
                                                                    min  1  for stripping or adding oxygen. Assume the
            18.4.2.4  Hyde Park Superfund Site, New York
                                                                    reactor was ‘‘complete mix.’’
            The site treated Q ¼ 3.50 L=s (80,000 gpd) landfill leachate.
                                                                    (a) Estimate K L a(benzene)
            Total organic carbon (TOC) (influent) ¼ 4000 mg=L; the air
                                                                    (b) Suppose, using the same reactor in the batch mode,
            stripper removed about 0.90 fraction TOC.
                                                                       you had to strip benzene at a concentration of
                                                                       20 mg=L to a concentration of 0.5 mg=L. Estimate
                                                                       the time required.
            PROBLEMS
                                                                    (c) Suppose the same reactor is used as a continuous-
            18.1 Applications of Henry’s Law                           flow reactor, with flow coming in at the top and out
                Given=Required                                         at the bottom. Does this affect K L a? What should be
                Determine the concentration of atmospheric gases       the detention time?
                (O 2 ,N 2 ,CO 2 ) using Henry’s law, Table H.5.  18.5 Application of W(O 2 ) versus rpm(Impeller) Character-
                (a) At sea level at 258C.                           istic Curve for a System
                (b) At the Engineering Research Center (ERC) at     Given
                                                                                               3
                                                                                      3
                    Colorado State University (CSU) elevation, eleva-  . Assume Q ¼ 9000 m =d (375 m =h) (or 2.4 mgd).
                                                                                                          3
                    tion is 1615 m (5300 ft) at 258C based upon tabular  . [BOD in   BOD out ] ¼ 200 mg=L (0.200 kg=m ).
                    data or formula for the effect of elevation on atmos-  .  Assume also that the detention time for the reactor is
                    pheric pressure.                                  u ¼ 6h.
                                                                                      3              3
                (c) Read the barometric pressure from the mercury   . V(reactor) ¼ (375 m =h)   6h ¼ 2350 m .
                    barometer. Compare the reading with the estimate  . A single 2.13 m (7.0 ft) impeller is used.
                    in (b).                                         . A characteristic curve is given by Figure 18.15.
                (d) Determine the concentration of the three atmos-  . Elevation ¼ 1610 m
                    pheric gases in equilibrium with the atmosphere in  . T ¼ 158C.
                    distilled water based upon observed barometric  . A direct current motor is used.
                    pressure (or elevation of site).                .  Power expended is proportional to the rotational
            18.2 Application of Henry’s Law to Oxygen                 velocity with 60 kW expended at 60 rpm.
                Given=Required                                      Required
                Determine the concentration of oxygen using Henry’s  (a) Determine the K L a required.
                law:                                                (b) Calculate rpm(impeller) for the system to provide
                (a) At sea level at 258C.                              the required K L a.
                (b) At the ERC elevation, elevation is 1615 m (5300 ft)  Hint: Example 18.4 provides a pattern for solution. Note
                    at 258C based upon tabular data for the effect of  that C s will reflect the elevation and temperature, which
                    elevation on atmospheric pressure, Table B.6, and  in turn will affect K L a.
                    using Henry’s law coefficients, Table H.5.  18.6 Explanations of Test Results and Gas Transfer
            18.3 Application of Henry’s Law to Carbon Dioxide       Variables
                Given=Required                                      Given=Required
                (a) Determine the concentration of carbon dioxide in  (a) Measurements of dissolved oxygen levels in full-
                    equilibrium with the atmosphere in distilled water  scale aeration tests, at various sampling points, often
                    at your location.                                  show dissolved oxygen concentrations greater than
                (b) Bubbles are seen emerging from a primary clari-    saturation with respect to the atmosphere. Explain.
                    fier. The bubbles are determined to be about     (b) Delineate in a mathematical format, the system
                    two-thirds carbon dioxide and one-third methane.   variables which may influence K L a.
                    Assume that you have a Kemmerer water bottle    (c) What important principles must be operative in
                    (device to take a water sample at some depth) and  surface aerator performance with respect to turbu-
                    you bring up the sample to measure the carbon      lence (i.e., scale of eddies, intensity of turbulence).
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