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B.Worst Case Discharge Analysis and Scenarios Version:27.10.4 <br /> B.3 RESPONSE CAPABILITY SCENARIOS <br /> The occurrence of a Small, Medium, or Worst Case Discharge could be the result of any <br /> number of scenarios at the Facility including: <br /> • Failure of manifold, mechanical loading arm, other transfer equipment, or hoses, as <br /> appropriate. <br /> . Tank overfill and/or failure. <br /> • Piping line, valve, or flange leak and/or rupture. <br /> . Tank truck and/or tank car loading overfill and/or failure. <br /> • Explosion or fire. <br /> • Equipment failure (e.g. pumping system failure, relief valve failure, or other general <br /> equipment relevant to operational activities associated with internal or external facility <br /> transfers). <br /> Events and conditions that pose a substantial threat of a Worst Case Discharge might <br /> include: <br /> . Tank and associated piping fire. <br /> • Catastrophic tank shell failure. <br /> . Natural disaster induced tank shell or major piping failure. <br /> A sudden release of tank contents due to the above potential threats could result in a breach <br /> of the tank basin secondary containment. <br /> Actions to prevent or mitigate a Worst Case Discharge due to the above potential threats <br /> include: <br /> . Periodic inspection of the tank to confirm integrity. <br /> • Periodic inspection of the tank basin secondary containment to confirm integrity. <br /> • Preventive maintenance as appropriate of the tank and associated piping. <br /> . Training of facility personnel on the proper procedures in event of a natural disaster to <br /> minimize the potential impact. <br /> Abnormal operations, which could result in a substantial threat of a worst case discharge, <br /> may include: <br /> . Unintended closure of valves. <br /> • Pressure differential exceeds or drops below the normal operating limits. <br /> • Loss of communications. <br /> . Operations of any safety device (i.e., relief valve or rupture disc). <br /> If any of these events occur, the affected system will be investigated, corrective action <br /> initiated, and the situation monitored by pipeline personnel. All corrective actions will be <br /> performed by qualified personnel appropriate to the task. <br /> The response actions to each of these scenarios are outlined in Section 3.0. The response <br /> resources, including details on equipment and manpower, are identified in Appendix A. <br /> Facility response personnel list/telephone numbers and other internal/external resources <br /> telephone numbers are detailed in Figures 2.1, 2.2 and 2.5. <br /> Shell Supply and Distribution B-6 Stockton Terminal FRP <br /> ©2019 Witt O' Brien's Revision Date:October, 2019 <br />