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Guo, Boyun / Computer Assited Petroleum Production Engg 0750682701_chap01 Final Proof page 12 4.1.2007 6:12pm Compositor Name: SJoearun




               1/12   PETROLEUM PRODUCTION ENGINEERING FUNDAMENTALS
               from the process and to minimize the adverse effects of  3. Mechanical failure due to temperature change,
               such releases if they occur. This can be achieved by the  overpressure and underpressure, and external im-
               following:                                    pact force
                                                         C. Liquid overflow caused by
               1. Preventing undesirable events            1. Increased input flow due to upstream flow-control
               2. Shutting-in the process                    device failure
               3. Recovering released fluids               2. Decreased output flow due to blockage in the liquid
               4. Preventing ignition                        discharge
               The modes of safety system operation include  D. Gas blow-by caused by
                                                           1. Increased input flow due to upstream flow-control
               1. Automatic monitoring by sensors            device failure
               2. Automatic protective action              2. Decreased output flow due to blockage in the gas
               3. Emergency shutdown                         discharge
               Protection concepts and safety analysis are based on un-  E. Underpressure caused by
               desirable events, which include             1. Outlet flow-control device (e.g., choke) failure
                                                           2. Inlet blockage
               A. Overpressure caused by                   3. Cooling of closed system
                 1. Increased input flow due to upstream flow-control  F. Excess temperature caused by
                    device failure                         1. Overfueling of burner
                 2. Decreased output flow due to blockage  2. External fire
                 3. Heating of closed system               3. Spark emission
               B. Leak caused by
                 1. Corrosion                            Figure 1.17 presents some symbols used in safety system
                 2. Erosion                              design. Some API-recommended safety devices are shown
                                                         in Figs. 1.18 through 1.22.


                           Flow Safety    Burner Safety   Pressure Safety  Pressure Safety
                             Valve           Low            High & Low       Element


                              FSV
                                              BSL             PSHL                PSE




                        Flow Safety       Flow Safety
                          High
                                             Low                   Pressure Safety Valve


                           FSH               FSL
                                                                   PSV
                                                                                   PSV




                          Level Safety     Level Safety
                            High             Low           Temperature      Temperature
                                                           Safety High      Safety Low

                             LSH              LSL            TSH               TSL




                          Flow Safety     Level Safety
                          High & Low      High & Low       Temperature    Temperature
                                                             Safety      Safety Element
                                                           High & Low
                            FSHL            LSHL                             TSE
                                                              TSHL




                                          Figure 1.17 Safety device symbols.
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