Page 34 - Chemical Process Equipment - Selection and Design
P. 34

1.10. STEAM  AND  POWER  SUPPLY  11



               EXAMPLE 1.3                                      key  points  are  indicated  on  the  enthalpy-entropy  diagram.  The
               Steam Plaint cycle for Generation of Power and LOW Pressure   process  steam  is  extracted  from  the  turbine  at  an  intermediate
               Process Steam                                    point,  while  the  rest  of  the  stream  expands  to  1 in.  Hg  and  is
            The  flow  diagram  is  for  the  production  of  5OOOkW  gross  and   condensed  (example  is  corrected  from  Chemical  Engineers
            20,000 lb/hr of  saturated process steam at 20 psia. The feed and hot   Handbook, 5th ed., 9.48, McGraw-Hill, New York, 1973).
            well pumps make the net power production 4700 kW. Conditions at
                                                                                                   op”’
                                                                                                 ‘6





















                                                                                           1.618   1.838
                              Feed pump                                              s =entropy, B.1 u. /(lb.)(DR 1







               EXAMPLE 1.4                                     whose main function is to supply heat to crude topping and vacuum
               Pickup of  Waste Heat by  Generating and Superheating Steam   service  in  a  20,00OBbl/day plant.  (a)  Recovery  of  heat  from  a
               h a Petroleum Refinery                          sidestream of  a fractionator in a 9000 Bbl/day fluid catalytic cracker
            The  two  examples  are  generation  of  steam  with  heat  from  a   by  generating steam,  Q = 15,950,000 Btu/hr. (b) Heat recovery by
            sidestream of  a fractionator in a 9000 Bbl/day  fluid cracking plant,   superheating  steam  with  flue  gases  of  a  ZO,OOOBbl/day  crude
            and  superheating  steam  with  heat  from  flue  gases  of  a  furnace   topping and vacuum furnace.


                                                                                      A
                                                FRACTIONATOR
                                                SIDESTREAM
                (4                              17,300 pph        (b)      STEAM                   Q = 1.2  MBtulhr
                                                580 F

                                                                                                   Q = 53.2  MBtulhr
                                                 RETURN
                                                 425 F                                             Q = 9.2  MBtulhr
            WATER                                                     VACUUM COIL
            17,300 pph






            are  of  steam  generation  in  a  kettle  reboiler  with  heat  from  a   with an expansion turbine. Recovery of power from a high pressure
            fractionator sidestream and of steam superheating in the convection   gas  is  a  fairly  common  operation.  A  classic example  of  power
            tubes of  a furnace that provides heat to fractionators.   recovery from a high pressure liquid is in a plant for the absorption
               Recovery  of  power  from  the  thermal  energy  of  a  high   of  CO,  by  water  at  a  pressure  of  about  4000psig.  After  the
            temperature stream is the subject of  Example 1.5. A closed circuit   absorption, the CO,  is released and power is recovered by releasing
            of propane  is  the  indirect means whereby the power is recovered   the rich liquor through a turbine.
   29   30   31   32   33   34   35   36   37   38   39