Page 143 - Materials Chemistry, Second Edition
P. 143

126       Practical Design Calculations for Groundwater and Soil Remediation



              Strategy:
              It requires a two-step approach to solve this problem. The first is to
                determine the rate constant using the given information. Then, use
                this obtained k value to estimate the residence time for other conver-
                sions. The given information did not tell us the order of the reaction.
                We assume it is a first-order reaction, but this should be confirmed
                with additional test data.
              Solution:
               (a)  Insert the known values into Equation (4.16) to find the value of
                   k:

                                      50  =  0.20 =  e − k(10)
                                      250
                                        k = 0.161 h −1


               (b)  The time required to achieve a concentration of 10 mg/kg:

                                      10  =  0.04 =  e − 0.161τ
                                     250
           	                           τ = 20.0 h


              Discussion:
              It is assumed that the reaction is first-order. One should check the valid-
                ity of this assumption, for example, by running the pilot run longer.
                For example, if the run is extended to 20 hours and the final concen-
                tration is close to 10 mg/kg, the assumption of first-order kinetics
                should be valid.


           Example 4.9:   Determine the Rate Constant from Batch Experiments
           An in-vessel bioreactor is designed to remediate soil impacted by cresol. A
           bench-scale batch reactor was set up to determine the order and rate constant
           of the reaction. The following concentrations of cresol in the batch reactor at
           various times were observed and recorded as:

                            Time (hours)  Cresol concentration (mg/kg)
                                0                350
                                0.5              260
                                1                200
                                2                100
                                5                 17
   138   139   140   141   142   143   144   145   146   147   148