Page 173 - Pipeline Risk Management Manual Ideas, Techniques, and Resources
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7/150 Leak Impact Factor
           a jet fire to a massive fireball and detonation. On ignition, a   with minimum lateral spreading.  An HVL cloud will normally
           flame propagates through the cloud, entraining surrounding air   be negatively buoyant (heavier than air) due mostly to the evapo-
           and  fuel  from  the  cloud.  If  the  flame  propagation  speed   rative cooling of the material. These dense vapors tend to slump
           becomes high enough, a fireball and possibly a detonation can   and flow to low points in the immediate topography. Typical
           occur. The fireball can radiate damaging heat far beyond the   cloud configurations are roughly cigar or pancake shaped.
           actual flame boundaries, causing skin and eye damage and sec-   A stable atmospheric condition is usually chosen for release
           ondary fires. If the cloud is large enough, a “fire storm” can be   modeling, in order to generate scenarios closer to worst case
           created, generating its  own  winds  and  causing far-reaching   scenarios.  Atmospheric  stability  classes  are  discussed  in
           secondary fires and radiant heat damage.   Chapter 14 and shown in Table 14.3 1. This stability class repre-
             Ignition probabilities are discussed in Chapter 14.   sents some fraction of possible weather type days in any year.
                                                      Under very favorable conditions, unignited cloud drift may lead
           Overpressure wave                          to extended hazard zone distances, but such events are seen to be
                                                      rare, difficult to estimate, and generally considered within the
           In rare cases, a vapor cloud ignition can lead to an explosion.   conservative assumptions already included  in these estimates.
           An explosion involves a detonation and the generation of blast   Many  variables  affect the  dispersion of  vapor  clouds. In
           waves, commonly measured as  overpressure in psig. Anuncon-   general, these include
           fined vapor cloud explosion, in which a cloud is ignited and the
           flame front travels through the cloud quickly enough to gener-   Release rate and duration
           ate a shock wave, is a rare phenomenon. Such a phenomenon is   0  Prevailing atmospheric conditions
           called an overpressure wave. A confined cloud is more likely to   Limiting concentration
           explode, but confinement is difficult to accurately model for an   Elevation of source
           open-terrain release. The intensity of the overpressure event is   0  Surrounding terrain
           inversely  proportional  to  the  distance  from  the  explosion   Source geometry
           point-the  intensity is less at greater distances. Various over-   0  Initial density ofrelease [5].
           pressure levels can be related to various damages.  An overpres-
           sure  level  of  10 psi  generally  results  in  injuries  (eardrum   Release duration is not as critical in estimating maximum
           damage) among an exposed population. Higher overpressure   cloud size since the release rate will diminish almost instantly
           levels cause more damages but would only occur closer to the   as the pipeline rapidly depressures under the pipeline rupture
           explosion point. It is conservatively assumed that an uncon-   scenario. Smaller size leaks could  create vapor  clouds that
           fined vapor cloud explosion can originate in any part of the   would be more dependent on release duration, especially under
           cloud. Therefore, the  overpressure distance is conservatively   weather conditions that support cloud cohesiveness, but these
           added to the LFL distance (the ignition distance) for purposes   scenarios are not thought to produce maximum cloud sizes.
           of hazard zone estimation.                   The extreme complexities surrounding a vapor release sce-
             The manner  in  which  an  ignited vapor  cloud potentially   nario make the problem only approximately solvable for even a
           transforms from a burning event to an exploding event is not   relatively  closed system. An  example of a  somewhat closed
           well understood. It rarely occurs when the weight of airborne   system is a well-defined leak from a fixed location where the
           vaporis less than 1OOOpounds [83].         terrain is known and constant and where weather conditions
             Should a detonation occur, widespread damage is possible. A   can  be  reasonably estimated from  real-time  data. A  cross-
           detonation  can  generate powerful  blast  waves  reaching  far   country pipeline, on the other hand, complicates the problem by
           beyond  the  actual  cloud  boundaries.  Most  hydrocarbodair   adding variables such as soil conditions (moisture content, tem-
           mixtures have  heats of  combustion greater than the  heat of   perature, heat transfer rates, etc.), topography (elevation pro-
           explosion of TNT  [8], making them very high energy sub-   file, drainage pathways, waterways, etc.), and often constantly
           stances. The possibility of vapor cloud explosions is enhanced   changing terrain  and weather patterns  (amount of  sunshine,
           by closed areas, including partial enclosures created by trees or   wind speed and direction, humidity, elevation, etc.).
           buildings.  Unconfined vapor  cloud explosions are  rare  but   Even though it vaporizes quickly, a highly volatile pipeline
           nonetheless a real danger. Certain experimental military bombs   product can form a liquid pool immediately after release. This
           are designed to take advantage of the increased blast potential   could be the case with products such as butane or ethylene. The
           created by  the ignition of an unconfined cloud of hydrocar-   pool  would  then  become  a  secondary source of the vapors.
           bodair vapor.                              Vapor generation would be dictated by the temperature of the
             Damages that could result from overpressure (blast) events   pool surface, which in turn is controlled by the air temperature,
           are discussed in Chapter 14.               the wind speed over the pool, the amount of sunshine to reach
                                                      the pool, and the heat transfer from the soil (Figure 7.6). The
            Vapor cloud size                          soil heat transfer is in turn governed by soil moisture content,
                                                      soil type, and both recent and current weather. Even if all of
           The predicted vapor cloud size is a function of variables such as   these factors could be accurately measured, the system is still a
           the  release  rate,  release  duration,  product  characteristics,   nonlinear relationship that cannot be exactly solved.
           threshold concentrations of interest, and surrounding environ-
           ment (e.g., weather, containment barriers, ignition source prox-   Cloud modeling
           imity) at the release site.
             A  cloud of  lighter-than-air  vapors  such as natural gas or   A vapor cloud that covers more ground surface area, either due
           hydrogen will normally be buoyant-it  will tend to rise quickly   to its size or its cohesiveness, has a greater area of opportunity
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