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= 2040.81 collector

               So, we need 2041 LS-2 PTC

               thermal efficiency for solar collectors (η col) with three approximation formulas is
               given below :

                                          3
                           =     +     .                                                                                  (3.8)
                          0
                                  3
                                           
                                        3
                          =    +    .    +     .                                                                       (3.9)
                                 3
                          0
                                         
                                                   2            3           4
                          =    +    .  +    .       +    .      +    .        +     .          (3.10)
                                1
                          0
                                                        3
                                                                     4
                                            2
                                                                             
               Note that the thermal efficiency was found η col ≈ 0.72 according to the dataset for
               the approximation studies in Appendix A-1.
               The total required area for the PTSC is given by :

                   =      ∗                                                                                                 (3.11)
                                   
                   
                             
                    = 2041 *39.2
                    = 80007.2 m  2

                    =8 Hectare

               Now we will enter the hot brine water in flash vessels .

                Flash vessels calculation:
                                                                                 m steam= 883kg/hr
                 st
               1  stage  ( 0.4 bar ) :


                  T =110°c                                                  T =109.55°c
                                                    st
                                                  1  stage
                  P =1.5 bar                       0.4 bar                  P =0.4 bar
                  m= 1 Mkg/hr                                               m= 0.999 Mkg/hr



               For the given data T=110  c, P=1.5 bar  , from appendix A
                                             o

               Specific enthalpy (h inlet) = 461.47 KJ/Kg





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