Page 145 - Pipeline Risk Management Manual Ideas, Techniques, and Resources
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6/122 Incorrect Operations Index
           the other party. In such cases, allowances must be made for   remote  observation  provides  some  additional  backupthe
           the  other  party’s  procedures  and  operating  discipline.   monitoring personnel can at least notify field personnel to take
           Uncertainty may be reduced when there is direct inspection   action.
           or witnessing of the calibration and maintenance of the other   Points can be given for such systems when such observation
           party’s  safety  equipment,  but  this  does  not  replace  direct   is reliable 95 to 100% of the time. An example would be a pres-
           control ofthe equipment.                   sure that is monitored and alarmed (visible andor audible sig-
            There is some redundancy between this variable and the pre-   nal to observer) in a control room that is manned 24 hours a day
           viously assessed MOPpotential since safety systems are noted   and that has a communication reliability rate of more than 95%.
           there also. A point schedule should be designed to accommo-   On notification of an abnormal condition, the observer can dis-
           date all situations on the pipeline system. [Note: The evaluator   patch personnel to correct the situation.
           must decide if she will be considering the pipeline system as a
           whole (ignoring section breaks) for this item. A safety system   E.  Remote, observation and control  This is the same situa-
           will often be physically  located  outside of the pipeline  seg-   tion as the previous one with the added feature of remote con-
           ments it is protecting  (see Example  6.3 later).] An  example   trol capabilities. On notification of rising pressure levels, the
           schedule follows:                          observer is able to remotely take action to prevent overpressure.
                                                      This may mean stopping a pump or compressor and opening or
           A.  No safety devices present   0 pts      closing  valves.  Remote  control  capability  can  significantly
           B.  On site, one level only   3 pts        impact the risk picture only if communications are reliable-
           C. On site, two or more levels   6 pts     95% or better  for both receiving  of the pressure  signal and
           D.  Remote, observation only   1 Pt        transmission of the control signal. Remote control generally
           E.  Remote, observation and control   3 pts   takes the form of opening or closing valves and stopping pumps
           F.  Non-owned active witnessing   -2  pts   or compressors. This condition receives more points because
           G. Non-owned no involvement   -3  pts      more immediate corrective action is made possible by the addi-
           H.  Safety systems not needed   IO pts     tion of the remote control capabilities.
            In this example schedule, more than one safety system “con-   R  Non-owned,  active  witnessing  Here,  overpressure pre-
           dition” may exist at the same time. The evaluator defines the   vention devices exist, but are not owned, maintained or con-
           safety system and the overpressure scenarios. He then assigns   trolled by the owner of the equipment that is being protected.
           points for every condition that exists. Safety systems that are   The  pipeline  owner  takes  steps  to  ensure  that  the  safety
           not thought to adequately address the overpressure scenarios   device(s) is properly calibrated and maintained by witnessing
           should not be included in the evaluation. Note that some condi-   such activities.  Review  of  calibration or inspection reports
           tions cause points to be subtracted.       without actually witnessing the activities may, in the evalua-
                                                      tor’s judgment, also earn points. Points awarded here should
           A. No safety devices present  In this case, reaching MOP is   reflect the uncertainties arising from not having direct control
           possible, and no safety devices are present to prevent overpres-   of the devices. By assigning negative points here, identical
           sure.  Inadequate  or  improperly  designed  devices  would   safety systems under different ownerships would have differ-
           also fall into this category. A relief valve that cannot relieve   ent point values. This reflects a difference in the risk picture
           enough to offset the pressure source is an example of an inef-   caused by the different levels of operator control and involve-
           fective device. Lack of thermal overpressure protection where   ment.
           the need exists is another example of a situation that should
           receive 0 pts.                             G.  Non-owned. no involvement  Here again, the overpressure
                                                      devices are not owned operated, or maintained by the owner of
           B.  On  site,  one  level  For  this  condition  a  single  device,   the equipment that is being protected. The equipment owner is
           located at the site, offers protection from overpressure. The site   relying on another party for her overpressure protection. Unlike
           can be the pipeline or the pressure source. A pressure switch   the previous  category, here  the pipeline  owner is taking  no
           that closes a valve to isolate the pipeline segment is an example.   active role in ensuring that the safety devices are indeed kept in
           A properly sized relief valve on the pipeline  itself is another   a state of readiness. As such, points are subtracted-the  safety
           example.                                   system effectiveness has  been  reduced  by  the added  uncer-
                                                      tainty.
           C.  On site,  two or more  levels  Here, more than one safety
           device is installed at the site. Each device must be independent   H.  Safety  systems  not  needed  In the previous  item,  MOP
           of all others and be powered by a power source different from   potential,  the most points  were awarded for the  situation in
           the others. This means that each device provides an independ-   which it is impossible for the pipeline to reach MOP. Under this
           ent level of safety. More points should be awarded for this situa-   scenario, the highest level ofpoints is also awarded for this vari-
           tion because redundancy of safety devices obviously reduces   able because no safety systems are needed.
           risk.
                                                       For all safety systems, the evaluator should examine the sta-
           D.  Remote,  observation  on!v  In  this  case,  the  pressure  is   tus of the devices under a loss of power scenario. Some valves
           monitored  from  a  remote  location.  Remote  control  is  not   and switches are designed to “fail c1osed”on loss oftheir power
           possible and automatic overpressure protection is not present.   supplies (electric or pneumatic, usually). Others are designed
           While not a replacement for an automatic safety system, such   to “fail open,” and a third class remains in its last position: “fail
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