Page 108 - Improving Machinery Reliability
P. 108

80    Improving Machinery Reliability



                                __________________
                                CONSlDEKATlONS  FUR  EVALUATING CENTKIFUGAL  COMPRESSOR  BIDS
                          Item r
                         --         questions,  Considerations  and/or  Action  Plans
                          1   Have  all  compressor  niodels  been  successfully  operated  elsewhere?
                          2   lire  tllefe  ally  ddVdntageSldiSadVd0tngFs  to  barrel  COnStrUCtlOn  for  this  Sel-vlCe?
                          31   Does  tlie  [machine  with  fewer  impellers  produce  too  much  head  in the  second  section?
                          4)
                          5   Compare  quoted  diameters  with  tip  speeds.  Suitable  for  impeller  fabrication  method?
                          6)   Consistent  with  tip  speeds?  Maximuin  allowed  continuous  speed?
                          7)
                          8)   Are  these  vdlUeS  coiisistent  With  th?  related ddtd,  above?  UOfS
                          91   tlie  vendor  have  experience with  inipellers  at  these  tip speeds?
                          1u   How  calculated?  Sufficiently  far  froni  anticipated operating  Speed  range?
                          111   Are  apparent  efficiencies  and  losses  realistic?  How  determined?
                          12 I
                          13   Are  higher  dnticipdled discharge  teinperatures  (Vendor  8)  detriinental  to  process!   Costly?
                          14   Explain  significant  difference  in  gas  data  for  VPndor  B.   Reconcile  witn  othrr5.
                          15   ure  capacity uiffewnces  significant  in  liqlit  of  future  uprate  requirefiierits?
                          161   Nozzle  ratings limy  reflect  desigi  consei'vatism  and  uprat.e  capablllt1c.s.   llave  you
                          171   llldde  d  CUlllpdfiSOll?   DO  VCiIdUT  PtUpUSed  VrlOCltieS  dCCUrdteIy  ref leCt  Sldled  gas
                          181   volulnes  divided  by nozzle  et'ea?   Rfcvncile  discrepencies.
                          19)
                          20)   Are  quoted  llidterldlS COllSlSterlL  With  specified  liidterldlS?  IndUSlry prdCtlteS?
                          21)   Vendor  rxperieiice  with  quoted  nidteridls?
                          22 )
                          23   Sliould  credit  be  given  tu  cast  rteel  construction?
                          24   Why  is Vendor  (I offeriny PTFE-Coated  labyrinth  Ilidteridl?
                          25 )   Does  luwer  Iiiaiiitendnce weight  allow  installation  of  less wpensive  overliead
                          26 )   crane?  Is credit due?
                          27   Investigate possible eifects  of  Veiidor  C  not  offerinu coniiion  baseplate.
                          78   Who  is responsible  for  tlie  design  of  the  SUbCvntrdCtcd  baseplate  proposed  by
                              Vendor  C?
                          29   WOUlO  Sepdl'dte  lube  dnd  Sed1  011  SySlWlS  lldVe  been  ddVdlltdgC'OUS?
                          30   Why  docs  Vendor  U  propose  iiieclianical  contact  seals?  Are  there  any  ddvdntages?
                          31)   Shat  is  this overhead  vessel  acconlplisliing?   Vendor  A  lists tlie  runduwii  capacity
                          32)   to  be  in excess  of  the  vessel  capacity.   Is  this  logical?
                          33   hhdt  i5  the  CdlCuldtlUn  DdSiS  Used  to  arrive at  1000  qallOllS  VS.  2000  qdllOnS
                              rundown  capacity?
                          34   Any  adverse  experience  with  riveted  impellers  in this  service?
                          35   ilhy  does  Veiidor  C  propose  to  indnufacture  his own  thrust  bearinqs?
                          36   Could  d  IIIO~L!  Suitable  balance  pistun design  be  used  by Vendor  C  for  tllrust  reductlorl?
                          37   Lhy  does  Vendor  ti  propuse  to  iiianufacture  his ohn  journal  bearings!
                          3M   Investigate rating basis  used  OY  rdcli  vendor.   h'hy  thf  difference?
                          3Y   Is  the  clarifier  intended  to  reiiiove  only  water?  Water  and  Iiglit  tiyarocarbons?
                          4u   Coupling offer  n  allows  for  Iiiuher  torque,  but  less  iiiisaliyrrent  than  offer  B.
                              Have  you  evaluated  the  pros  and  cons?
                          41   Is  each  control  panel  fully equipped  with  all  specified  instruments?  Any  extra  ones?
                          42   What  do  we  know  about  offers  8  and  C?  Long-term  experience?
                          43   Any  service problenis  anticipated  for  the  installation  destination?
                          44   lhiportdnt  orily  if  geared  train coilfiguration.
                                                  .
                          45   Is  Vendor  C  offerinu  an  uiitested  orototvoe?  Whv  no  urrforinarice  curves?
                                                          ~r
                                                      I.
                                              ~
                          4b   Low  pressure  rise  to  surge  would  illandate  implementation  of  flow  control  scheme.
                              Is  this  possible?  lnvestiqate  process considerations.
                          47   Insist  on  early  submittal  of  spare  parts  data  frulii  Vendors  8  drid  C.
                          4n   Clarify status  of  rotor  via discussion  with  Vendor  U.
                          49   Clarify  status  of  mechanical  run  tests  via  discussion  with  Vendor  C.
                          50   Verlfy  no  closed  loop  perforrliance  test  was  Spccified.   Is  it desirable?
                          51   Why  did  Vendor  A  include  winterization?  What  does  it consist  of?
                          52   Shipping costs,  yotcntial  delays.  extra  expediting costs,  service  arranqeinents
                              niust  be  understood  -  especially  fat-  overseas  point  of  origin.
                          53   Discuss  experience  qualifications  with  Vendors  B  and  C  as  soon  as  possible.
                          54   Vendor  C  nust  SUbniIt  full  API  data  before  further  consideration  Can  be  glwn.
                              Uoes  he  have  soniethiny  to  Iiide?
                          55   YoSitiOn  taken  by Vendor  A  is not  acceptable.  Expedite  Vendor  E.
                          56   Verify  that  bearing spans  are  covered  by vendors'  previous  experience.
                          57 I   Are  vendors  familiar  with  data  subiuission  requirements  imposed  by purchaser?
                          58 1   kill  they  contractually  agree  to  submit  such  data  as  rotor design  dimensions
                          59)   and  as-built  dimensions?
                          60   Is  each  impeller  of  proven  design?  Will  impeller  perforindnce  curves be  provided?
                          61   Are  these  Mach  numbers  sufficiently  low for  the  gas  being compressed?
                          67 )   Are  imyeller  and  diffuser  diinensioris  large enough  for  potentially foulinq
                          63)   services?
                          b4   Verify  experience  to  ensure  against  rotor  dynamics  problems.
                          65   00 stress  calculations  make  use  of  stress  concentration  factors  or  orily sTmpliftcd
                              calculations?  Reconcile  high  stress  quoted  by  Vendor  C.
                          66   Are  quoted  coupling bores  near  niaximuni  permissible  diameters?  How  are  hubs
                              engaged  to  shafts?  Hydraulic  fit?  Who  will  supply  special  mounting  tools?
                          67   Are  couplings  suitable  for  future  uprate  requirements?
                       ~
                            Figure 2-17. Considerations for evaluating centrifugal compressor bids.
   103   104   105   106   107   108   109   110   111   112   113