Page 161 - Design of Solar Thermal Power Plants
P. 161

146         3. GENERAL DESIGN OF A SOLAR THERMAL POWER PLANT

               convection thermal radiation. The mean Nusselt number of receiver
               exterior wall surface is calculated through Eq. (3.27) [52]
                                                2
                        8                     9
                        >                     >
                                         1
                        >                     >
                                  0:387Ra
                        >                6    >
                        <                     =
                 Nu wb ¼  0:6 þ          wb      ; 10  5  < Ra wb < 10 12  (3.27)
                                           9
                               h
                        >            0:559  10  i 8 >
                        >                    27>
                                1 þ
                        >                     >
                        :                     ;
                                      PR
                                                         3
                                      gbðT wb    T a Þðr AP þ dÞ
                               Ra wb ¼
                                               va
                                                                       (3.27a)
                                                        3
                                      gðT wb   T a Þðr AP þ dÞ
                                    ¼
                                              vaT a
                                                              92
                                        8
                                        >                     >
                                        >                     >
                                        >                     >
                                        >                     >
                                        >                1    >
                                        >                6    >
                              lNu wb   l  <       0:387Ra wb  =
                         h wb ¼     ¼     0:6 þ             # 8         (3.28)
                                H     H >      "           9  27>
                                                     0:559
                                        >                  16  >
                                        >                     >
                                        >                     >
                                                1 þ
                                        >                     >
                                        >                     >
                                        :             P r     ;
               in which b is the volumetric expansion coefficient of the air, 1/ C, as

                                                         2
               b ¼ 1/T a ; v is the kinematic viscosity of the air, m /s; a is temperature
                                   2
               diffusion coefficient, m /s; P r is the Prandtl number of the air; T wb
               is the mean temperature of absorber exterior wall surface, C.

                  We substitute Eqs. (3.26e3.28) into (3.25)
                        2                           3
                            2pkH
               P COND ¼  4           þ pðr AP þ dÞHh wb ðT w   T a Þ
                                                    5
                            r AP þ d
                         ln
                              r AP
                        2                                      92        3
                                        8
                                        >                      >
                                        >                      >
                        6               >                      >         7
                                        >                      >
                        6               >                1     >         7
                            2pkH                   0:387Ra
                                        >
                                                               >
                        6               <                6     =         7
                        6                                wb              7
                                     þ dl 0:6 þ
                            r AP þ d           "            9
                      ¼ 6                                   # 8  ðr AP þ dÞ7
                        6ln             >            0:559  16  27>      7
                        6
                                                               >
                                        >
                                        >
                                                                         7
                                                               >
                                        >                      >
                        4     r AP      >       1 þ            >         5
                                                               >
                                        >
                                                      P r
                                        :                      ;
                        ðT w   T a Þ
                                                                        (3.29)
                  In the case that the reference temperature is the ambient air
               temperature, P r ¼ 0.71, we substitute it into Eq. (3.29)
                        2                                       3
                            2pkH                     1    2
               P COND ¼  4           þ pl 0:6 þ 0:32Ra 6 wb  ðr AP þ dÞ ðT w   T a Þ
                                                                5
                            r AP þ d
                         ln
                              r AP
                                                                        (3.30)
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