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430   Fi b er   L a s er s            Intr oduction to Optical Fiber Lasers    431


                    1.0                            1.0
                                  4.5                                 P /P CR  = 0.1
                                                                       0
                    0.8                            0.8
                                                                           0.5
                                        2.5
                    0.6                 2          0.6
                   ω/ω 0         V = 1.5          ω/ω 0
                    0.4                            0.4
                    0.2                            0.2
                                                         5   2           1
                    0.0                            0.0
                     0.0  0.2  0.4  0.6  0.8  1.0    0      1     2     3     4
                                 P /P CR                         z/z R
                                  0
                                  (a)                            (b)
                 Figure 15.15  Effect of self-focusing in optical fibers—normalized mode spot size
                 versus (a) normalized power at various V values and (b) z/z  at various normalized
                                                              R
                                                              2
                 powers, where z  is Rayleigh range z  = πω /λ and ω  is 1/e  beam radius.
                                                  2
                             R              R    0       0

                      Thermal Effects
                      Assuming only convection heat removal from the fiber surface  for a
                                                                          23
                      bare fiber with core radius ρ, outer radius R, homogenous thermal
                      conductivity K , surface heat transfer coefficient h, heat density Q
                                                                               0
                                   c
                      generated only in the core, and ambient temperature T , the steady-
                                                                     s
                      state temperature distribution is given by
                                    Q ρ 2       R  2 K  r    2 2 
                                          +
                           Tr () =  T +  0   12  ln  +  c  −    0 ≤≤r  ρ
                                                           ρ
                                                ρ
                                                
                                 s  4 K c       Rh       
                                    Q ρ  K      r 
                                       2
                               = Tr ()  s  + T  0    c  − ln    ρ  ≤≤ R    (15.24)
                                                         r
                                    2K c  Rh   R  
                      The temperature rise in the core is given by
                                              Q ρ 2        2 K  
                                                          D
                                                    + ln
                                ∆= T()0  −  s  = T  4 0   12     +  c      (15.25)
                                 T
                                                          ρ
                                               K c          Rh  
                         For silica fibers, K  is 1.38 W/(m · K), and the heat transfer coeffi-
                                        c
                      cient h is both a function of fiber radius R and temperature difference
                      between fiber surface and air ∆T = T(R) – T . The heat transfer coeffi-
                                                          s
                      cient h increases with the temperature difference between fiber sur-
                      face and air ∆T and can be estimated as h = 0.2K /R, where K = 2.54 ×
                                                                        a
                                                              a
                               2
                      10  W/m /KW/(m · K), at very small temperature difference ∆T.
                        –2
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