Page 401 - Handbook of Energy Engineering Calculations
P. 401

External Steam Tracing Heat-Transfer Design for Pipelines


                     Selecting Air-Cooled Heat Exchangers


                     Quick Design and Evaluation of Heat Exchangers


               HEAT-TRANSFER CALCULATION PARAMETERS




               In  the  world  of  energy,  heat  transfer  is  of  critical  importance  because  the
               greater the efficiency of heat transfer, the more heat can be recovered from
               the process being considered. And, in general, the more heat recovered, the
               more attractive the project is, provided the cost of recovering the heat is not

               excessive.  Greater  efficiency  in  heat  recovery  is  producing  more  energy
               savings while reducing carbon-dioxide emissions worldwide. As a result, the
               overall energy field is benefiting, as is the atmosphere.
                  To save energy in the heat-transfer process, several requirements must be

               met:  (a)  a  sufficient  temperature  difference  must  exist  to  provide  a  “heat
               head” to make heat transfer economical; (b) there must be a need and use for
               the recovered heat; (c) the heat transfer must result in a fuel saving that is
               enough  to  pay  for  the  needed  equipment  in  an  acceptable  time  frame—

               usually 3 years, or less.
                  Factors important in providing effective heat transfer at an economical cost
               include: (a) type of heat exchanger selected for the application, with the type
               ranging  from  shell-and-tube,  direct-contact  with  mixing,  regenerative-plate

               type, to double-tube exchanger; (b) type of heat transfer occurring—heating,
               cooling, boiling, or condensing; (c) overall heat-transfer coefficient, U, which
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               can vary from 1 to 1000 Btu/(h · °F · ft )[W/m  · °C], depending on the fluid,
               type of heat exchanger, relative flow direction, and other factors; (d) size of
               exchanger chosen relative to the amount of heat being transferred—whether
               the exchanger is over-, under-, or right-sized; (e) type of fluid flow selected
               for the heat exchanger—parallel or counterflow; and (f) obtaining, and using,
               the  actual  logarithmic  mean  temperature  difference  (LMTD)  in  the  heat–

               transfer  calculations.  This  section  of  the  handbook  focuses  on  energy
               conservation  using  heat  exchangers  of  various  types  to  reduce  heat  losses
               while recovering the maximum amount of usable heat possible.
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