Page 374 - Handbook of Energy Engineering Calculations
P. 374

Figures 2 and 3 show a schematic and T-S diagram of a vapor-dominated
               power system. Dry steam from the well (1) at perhaps 400°F (200°C) is used.
               It  is  nearly  saturated  at  the  bottom  of  the  well  and  may  have  a  shut-off
               pressure up to 500 psia (∼35 bar). Pressure drops through the well causing it
               to slightly superheat at the well head (2). The pressure there rarely exceeds

               100  psia  (∼7  bar).  It  then  goes  through  a  centrifugal  separation  to  remove
               particulate matter and enters the turbine after an additional pressure drop (3).
               Processes  1-2  and  2-3  are  essentially  throttling  processes  with  constant

               enthalpy. The steam expands through the turbine and enters the condenser at
               (4):
                  Because turbine flow is not returned to the cycle but reinjected back into
               the  earth  (Mother  Nature  is  our  boiler),  a  direct-contact  condenser  of  the
               barometric  or  low-level  type  may  be  used.  Direct-contact  condensers  are

               more effective and less expensive than surface-type condensers. (The latter,
               however, are used in some new units with H S removal systems, below.) The
                                                                     2
               turbine exhaust steam at (4) mixes with the cooling water (7) that comes from
               a cooling tower. The mixture of 7 and 4 is saturated water (5) that is pumped
               to  the  cooling  tower  (6).  The  greater  part  of  the  cooled  water  at  7  is
               recirculated to the condenser. The balance, which would normally be returned

               to the cycle in a conventional plant, is reinjected into the ground either before
               or after the cooling tower. The mass-flow rate of the reinjected water is less
               than  that  originating  from  the  well  because  of  losses  in  the  centrifugal
               separator,  steam-jet  ejector  (SJE),  evaporation,  drift  and  blow-down  in  the

               cooling tower, and other losses. No makeup water is necessary.
                  A relatively large SJE is used to rid the condenser of the relatively large
               content of noncondensable gases and to minimize their corrosive effect on the
               condensate system.

                  This  procedure  and  the  data  and  illustrations  presented  in  Related
               Calculations  are  the  work  of  M.  M.  El-Wakil,  as  presented  in  his  book
               Powerplant Technology, McGraw-Hill, 1984. At the time of publication he
               was Professor of Mechanical and Nuclear Engineering at the University of

               Wisconsin.


               GEOTHERMAL  AND  BIOMASS  POWER-GENERATION

               ANALYSES
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