Page 186 - Pipeline Risk Management Manual Ideas, Techniques, and Resources
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Adjustments to scores 71163
               Table 7.14  Matrix for evaluating ability of leak detection systems to   nance)  of additional valves would far outweigh the possible
               detect various leak rates                  benefits,  and also imply that such valves may actually intro-
                                   *,                     duce new hazards.
               Leak detection system   TI"   T,oo   TI000
                                                          C. Sensing devices. Part of the equation in response time is the
               Mass balance for facility                    first opportunity to take action. This opportunity depends on
                (SCADA and manual)                          the sensitivity of the leak detection. All leak detection will
               Patrol                                       have an element ofuncertainty, from the possibility of crank
               Overline surveys
               Acoustic monitoring                          phone calls to the false alarms generated by instrumentation
               SCADA alarms                                 failures or instrument reactions to pipeline transients. This
               SCADA-based computational                    uncertainty must also be included in the following item.
                methods                                   D. Reaction times. If an operator intervention is required to ini-
               SCADA-based mass balance                     tiate the proper response, this intervention must be assessed
               Staffing of surface facilities               in terms of timeliness and appropriateness. A control room
               Passerby reporting                           operator must often diagnose the leak based on instrument
               Other
                                                            readings transmitted to him. How quickly he can make this
                                                            diagnosis depends on his training, his experience, and the
               check valves may reduce the draining or siphoning to a spill at a   level of  instrumentation  that  is  supporting  his  diagnosis.
               lower elevation. Included in this section should be automatic   Probable reaction  times  can be judged from mock  emer-
               shutoffs ofpumps, wells, and other pressure sources. Redundancy   gency drill records when available. The evaluator can incor-
               should be  included  in all such systems before  risk-reducing   porate  his  incorrect  operations  index  ratings  (training,
               credit is awarded (see Chapter 6, Incorrect Operations Index).   SCADA, etc.) into this section also. If the control room can
                                                            remotely operate equipment to reduce the leak, the reaction
               B.  Valve spacing. Close valve spacing may provide a benefit in   time is obviously improved. Travel time by first responders
                 reducing the spill amount. This must be coupled with the   must otherwise be factored in. If the pipeline operator has
                 most probable reaction time in closing those valves.   provided  enough  training  and  communications  to  public
                                                            emergency  response  personnel  so that  they  may  operate
                 Discounting failure opening size and pressure, the two com-   pipeline  equipment, response time may  be  improved,  but
               ponents of a release volume from a liquid line are (1)  the con-   possibly at the expense of increased human error potential.
               tinued pumping that occurs before the line can be shut down   Public emergency response personnel are probably not able
               and (2) the liquid that drains from the pipe after the line has   to  devote  much  training  time  to  a  rare  event  such  as  a
               been  shut down. The  former is only minimally impacted  by   pipeline failure. If the reaction is automatic (computer-gen-
               additional  valves-perhaps   only helping  to  stop momentum   erated valve closure, for instance) a sensitivity is necessarily
               effects from pumping  if a valve is rapidly closed (but poten-   built in to eliminate false alarms. The time it takes before the
               tially generating threatening pressure waves ). The main role of   shut down device is certain of a leak must be considered.
               additional valving, therefore, seems to be in reducing drain vol-
               umes.  Because a pipeline is a closed  system, hydraulic head
               andor a  displacement  gas is needed to affect  line drainage.   '%ea  of  Opportunity " Limitinghctions
               Hilly terrain can create natural check valves that limit hydraulic   As noted previously, the area of opportunity can sometimes
               head and gas displacement of pipeline liquids.   be limited by protecting or removing vulnerable receptors, by
                 Concerns with the use of additional block valves include costs   removing possible ignition sources, or by limiting the extent of
               and increased system vulnerabilities from malfunctioning com-   the spilled product.
               ponents andor accidental closures, especially where automatic
               or remote capabilities are included. For unidirectional pipelines,   A. Evacuation. Under the right conditions, emergency response
               check valves (preventing backflow) can provide some conse-   personnel may be able to safely evacuate people from the
               quence  minimization benefits.  Check  valves  respond  almost   spill area. To do this, they must be trained in pipeline emer-
               immediately to reverse flow and are not subject to most of the   gencies. This includes having pipeline maps, knowledge of
               incremental risks associated with block valves since they have   the product characteristics, communications equipment, and
               less chance of accidental closure due to human error or, in the   the proper equipment for entering to the danger area (breath-
               case of automatidremote valves, failure due to system malhc-   ing  apparatus,  fire-retardant  clothing, hazardous  material
               tions. Their failure rate (failure in a closed position) is uncertain.   clothing, etc.). Obviously, entering a dangerous area in an
                 Studies  of possible  benefits of shorter distances  between   attempt to evacuate people is a situation-specific action. The
               valves of any type produce mixed conclusions. Evaluations of   evaluator should look for evidence that emergency respon-
               previous accidents can provide insight into possible benefits   ders are properly trained and equipped to exercise any rea-
               of closer valve spacing in reducing consequences of specific   sonable options after the situation has been assessed. Again,
               scenarios, By one study of 336 liquid pipeline accidents, such   the criteriamust include the time factor. Credit is given when
               valves could, at best, have provided a 37% reduction in damage   the risk can be reliably reduced by 50% due to appropriate
               [76]. Offsetting potential benefits is the often substantial costs   emergency response actions.
               of additional valves and the increased potential for equipment   B. Blockades. Another  limiting  action  in  this  category  is to
               malfunction, which may increase certain risks (surge potential,   limit the possible ignition sources. Preventing vehicles from
               customer  interruption,  etc.).  Rusin  and  Savvides-Gellerson   entering the danger zone has the double benefit of reducing
               [76] calculate that the costs (installation and ongoing mainte-   human exposure and reducing ignition potential.
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