Page 99 - Packed bed columns for absorption, desorption, rectification and direct heat transfer
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                           fi L is the liquid viscosity at 20°C;
                                                      3
                           p L is the liquid density in kg/m .
                                  The diffiisivity of some gases dissolved in water is given in Table 3 A.
                                  For determination of the diffiisivity at temperature t (in °C), the
                           following equation can be used


                           A. = D LX[l + 0.02(t-20)J.                                      (5A)


                                  For calculation of the diffiisivity of dilute solution, the following
                           equation is proposed:



                                               M T
                           D =7.4x ltr" & )                          rf .                   (6A)
                                                                       /g
                             L
                             1                      06
                                            iooojiy
                           Here Mis the mol mass of the solvent;
                           V- mol volume of the diffusing substance;
                           fi L - liquid viscosity, Pa.s;
                           /?- parameter which takes into account the association of the solvent molecule.
                           Its value for different solvents is given below.

                           The value of /?:
                           For water            2.6
                           For methanol         1.9
                           Forethanol           1.5
                           For non-associated such as benzene, ether, heptane and so on, 0 = 1.



                                           Table 3 A. Diffiisivily of some gases in water at 20°C
                                                         9
                                                           2
                                                                          9
                                                                            2
                                              Gas  D,2o.l0 m /s Gas D/ 3n.l0 m /s
                                              co 2  1.8        H 2  5.3
                                              N 20  1.8        N 2  1.9
                                                   1.6              2.1
                                              Ci 2             Oj
                                              H 2 S  1.6       NH 3  1.8
                                              HC1 2.3
   94   95   96   97   98   99   100   101   102   103   104