Page 331 - Fluid mechanics, heat transfer, and mass transfer
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SHELL AND TUBE HEAT EXCHANGERS
            312
            TABLE 10.10 Specification Sheet for a Shell and Tube Heat Exchanger

               1   Company/Customer.
                  Reference No.                                          Proposal No.                                                                                              Date:

               2   Plant Location:
               3   Service: To remove heat from water in closed circuit with  pond water
               5   Size:                   Type: TEMA NEN        Connected In              Parallel            Series
                                                   2
               6   Surface/Unit (Gross/Effective)                            m     No. of Shells/Unit           Surface/Shell (Gross/Effective)                       m 2
               7  Performance of One Unit
               8   Fluid Allocation                                        (In) Shell (Out)   (In) Tube (Out)

               9   Fluid Name                                                 Water             Pond Water
              10   Fluid Quantity, kg/h

              11  Temperature, C
              12   Density, kg/m  3

              13   Viscosity, cP
              14  Specific Heat, J/(kg ºC)

              15  Thermal Conductivity, W/(m ºC)
              16   Inlet Pressure, kPa (abs)

              17   Fluid Velocity, m/s

              18   Pressure Drop (Allowable/Calculated),  kPa                   /                  /
                                    2
              19  Fouling Resistance (min) (m  ºC/W)
              20   Heat Exchanged, J/h

                                              2
              21  Heat Transfer Rate for Clean Service, W/(m  ºC)
              22  Construction of One Shell





                  the highest cold fluid temperature is always less than  (two-phase flow). An example is a condenser, in
                  the lowest hot fluid temperature.                     which vapor enters the shell side and cooling water
                                                                       flows through the tubes condensing the vapor.
                LMTD ¼½ðT 1   t 1 Þ ðT 2   t 2 ފ=ln½ðT 1   t 1 Þ=ðT 2   t 2 ފ:  & Large volumes of vapor may be condensed using
                                                                       cross flow.
                                                      ð10:24Þ
                                                                     & In actuality, most large heat exchangers are not
                 & Cross Flow: Exists when one fluid flows perpendic-    purely parallel flow, counterflow, or cross flow. They
                  ular to the second fluid, that is, one fluid flows      are usually a combination of the two or all three types
                  through tubes and the second fluid passes around      of heat exchangers.
                  the tubes at 90 angle.                             & The rate of heat transfer in any of the types of flow

                 & Cross-flow heat exchangers are usually found in      varies along the length of the exchanger tubes
                  applications where one of the fluids changes state    because its value depends upon the temperature
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