Page 338 - Introduction to Marine Engineering
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312   Instrumentation  and  control

                    The  problems  associated with swell and shrinkage  are removed by the
                  use of a second  measuring element, 'steam flow'. A third  element,  'feed
                  water  flow',  is added  to  avoid  problems  that  would  occur  if  the  feed
                  water  pressure  were to vary.
                    A  three  element  control  system  is  shown  in  Figure  15.$6.  The
                  measured  variables or  elements are  'steam flow', 'drum  level* and  'feed
                  water flow*. Since  in a  balanced  situation  steam  flow  must  equal  feed
                  flow, these  two signals  are  compared  in a differential  relay. The  relay
                  output  is fed  to a  two-term controller  and  comparator  into  which the
                  measured  drum  level  signal  is  also  fed.  Any  deviation  between  the
                  desired  and actual drum level and any deviation between feed and steam
                  flow will result in controller  action  to adjust the feed water control valve.
                  The  drum  level will then be returned  to its correct  position.
                    A sudden  increase in steam demand would result in a deviation signal
                  from  the differential relay and an output  signal to open the  feed water
                  control valve. The  swell effect  would therefore  not influence the correct
                  operation  of  the  control  system. For a  reduction  in  steam demand,  an
                  output  signal  to  close  the  feedwater  control  valve  would  result,  thus
                 avoiding  shrinkage  effects.  Any change  in  feed  water  pressure  would
                 result in feed water control valve movement to correct the change before
                 the drum level was  affected.


                 Exhaust steam pressure  control
                 Exhaust  steam  for  various  auxiliary  services  may  be  controlled  at
                 constant  pressure by appropriate  operation  of a surplus steam (dump)
                 valve  or  a  make-up  steam  valve,  A  single  controller  can  be  used  to
                 operate one  valve or  the  other  in what is known as 'split range control*.
                   The  control  arrangement  is  shown  in  Figure  15.37.  The  steam
                 pressure  in  the  auxiliary  range  is measured  by a  pressure  transmitter.

                             Exhaust steam for  auxiliary services
                                     JL                           "
                              Pressure  I                      n   Make up
                             transmitter |  |           Controller  valve open
                                      J   desired       pressure   Dead band {both valves cloj
                                         value          range
                                                                   Dump
                                                               ii * valve open
                                          P  +  1
                                          controller
                 Surplus  •  i                  *   >
                 steam  \Lrt-U                  LurHA ' Make up
                 (dump) A Y  "^       i         '* Y  21 steam
                 valve
                                                       Steam
                                                       supply
                     Steam
                     exhaust
                 Figure  15.37 Exhaust  steam  pressure control
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