Page 133 - Materials Chemistry, Second Edition
P. 133

116       Practical Design Calculations for Groundwater and Soil Remediation



             Assumption of steady-state is frequently used in the analysis of flow reac-
           tors. It should be noted that a batch reactor is operated under unsteady state
           because the concentration in the reactor is changing, and it is not a flow reac-
           tor because there is no flow in and out of the reactor when it is in operation.
             The general mass-balance equation (i.e., Equation 4.1) can also be expressed as:

                              dC
                            V    = ∑ QC in − ∑  QC out ±  ( V × γ )        (4.5)
                                       in
                                                 out
                              dt
           where V is the volume of the system (reactor), C is the concentration, Q is the
           flow rate, and γ is the reaction rate. The following sections will demonstrate
           the role of the reaction in the mass-balance equation and how it affects the
           reactor design.

           Example 4.1:   Mass-Balance Equation: Air Dilution (No
                        Chemical Reaction Occurring)
           A glass bottle containing 900 mL of methylene chloride (CH Cl , specific grav-
                                                               2
                                                                  2
           ity = 1.335) was accidentally left uncapped in a poorly ventilated room (5 m ×
           6 m × 3.6 m) over a weekend. On the following Monday it was found that two-
           thirds of methylene chloride had volatilized. An exhaust fan (Q = 200 ft /min)
                                                                         3
           was turned on to vent the fouled air out of the laboratory. How long will it take
           to reduce the concentration down below the Occupational Safety and Health
           Administration (OSHA’s) short-term exposure limit (STEL) of 125 ppmV?

              Strategy:
              This is a special case (no reactions occurring) of the general mass-
                balance equation. For this case Equation 4.5 can be simplified into:
                                  dC
                                V    = ∑  QC in − ∑  QC out                (4.6)
                                           in
                                                     out
                                  dt
              The equation can be further simplified with the following assumptions:
                1.  The air leaving the laboratory is only through the exhaust fan,
                   and the air ventilation rate is equal to the rate of air entering the
                   laboratory (Q  = Q  = Q).
                                    out
                               in
                2.  The air entering the laboratory does not contain methylene chlo-
                   ride (C  = 0).
                         in
                3.  The air in the laboratory is fully mixed; thus the concentration of
                   methylene chloride in the laboratory is uniform and is the same
                   as that of the air vented by the fan (C = C ).
                                                        out
                                          dC
                                        V    =− QC                         (4.7)
                                          dt
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