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1 Twelve Steps to Engineering Safe Oil and Gas Facilities Based on SPE 141974 By: Jim Johnstone and Jim Curfew – Contek Solutions LLC Presenter: Mike Leonard – VP of Special Projects – Contek Solutions LLC Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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2 Twelve Steps to Engineering Safe Oil and Gas Facilities 1.Set a Design Standards Policy 2.Lay Out the Site for Safety 3.Personnel Safety 4.Design Piping Properly 5.Select the Proper Pressure Vessel 6.Picking the Right Tank 7.Specifying Rotating Equipment for Safety 8.Relief-System Design is Critical 9.Determining the Right Electrical-Area Classification 10.Design the Instrumentation and Control System for Safety 11.Conduct a Process Hazard Analysis 12.Design Verification and Commissioning Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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3 Get Management On Board Are you following the “High Road”? Does the company have personnel with facility safety engineering experience? Is cost a barrier to safety? Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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4 1. Set a Design Standards Policy What Standards to Follow? Communicate to ALL Example Statement: “All facilities will be designed in accordance with good industry design practices and codes, and to also meet all regulatory requirements.” Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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5 2. Lay out the Site for Safety Vents, Flares, Fired Equipment, Engines, Vessels, Tanks, Offices and Control Equipment Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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6 Spacing Guidelines Reference: PIP PNE 00003 “Process Units and Offsite Layout Guide Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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7 Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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8 3. Personnel Safety Exit Routes Stairs Platforms Guarding Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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9 4. Design Piping Properly B31.3 – Process Piping B31.4 – Liquid Pipelines B31.8 – Gas Pipelines Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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10 5. Select the Proper Pressure Vessel ASME Section VIII Division 1 Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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11 6. Picking the Right Tank Fiberglass or Steel? Atmospheric or Low Pressure? Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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12 7. Specifying Rotating Equipment for Safety Pumps IC Engines Compressors Electric Motors Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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13 8. Relief System Design is Critical Capacity Types Sizing System Design Vent or Flared Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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14 9. Determining the Right Electrical Area Classification API RP 500 NFPA 497 Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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15 Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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16 10. Design the Instrumentation and Control System for Safety Levels of Protection Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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17 Safe Alarm and Control Systems ConditionCauseEffectPrimary ProtectionSecondary ProtectionLocation of Safety Devices OverpressureHigh inflow pressure; thermal expansion Sudden rupture or leakPSHPSVGas vapor section LeakCorrosion, erosion, mechanical failure, rupture, external damage Release of hydrocarbons to the atmosphere PSL to shut off inflow; Check Valve to prevent backflow; LSL on an atmospheric tank or vessel Sump/drain system; LSH on sump system PSL in vapor section; LSL at lowest point in atmospheric tank Liquid OverflowHigh liquid inflow; Upstream failure of a device; Blockage of liquid outflow Overpressure or excess liquids in downstream devices; Release of hydrocarbons to atmosphere LSHSump/drain system; LSH on sump system LSH at high point in vessel or tank Gas BlowbyFailure of liquid level system; opening of bypass Overpressure of downstream components LSLSafety devices on downstream component LSL at lowest point in vessel or tank UnderpressureWithdrawal in excess of inflow; thermal contraction when blocked in Collapse of the component; leak Atmospheric vessels: vent; Pressurized vessels: gas makeup system Atmospheric vessels: second vent or PSV; Pressurized vessels: PSL to shut off inflow and outflow PSL at highest practical point; PSVs and Vents in accordance with good Eng. Practices Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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18 11. Conducting a Process Hazard Analysis Obtain Drawings Select type of PHA Incorporate results into final design Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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19 Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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20 12. Design Verification and Commissioning Pre-Startup Safety Review (PSSR) Site Punch List Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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21 Conclusions and Recommendations Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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22 Questions? Contek Solutions LLC ENGINEERING ENVIRONMENT SAFETY MANAGEMENT SYSTEMS
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