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2015 Intern Presentation Jakeway

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Maryrose Jakeway

Maryrose Jakeway interned as a mechanical engineer at ArcelorMittal Burns Harbor. During her summer internship, she completed safety tours of the facility and received training in CPR and arc flash safety. For her projects, she created a report on a recent fire and analyzed the operational envelope of a steam pressure reducing valve after a failure in March. By modeling the steam system and comparing ideal conditions to actual conditions, she aimed to understand why and how the failure occurred and develop lessons learned.

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Maryrose Jakeway-Maryrose Jakeway- Mechanical Engineer InternMechanical Engineer Intern ArcelorMittal Burns Harbor: MEU-PSUSArcelorMittal Burns Harbor: MEU-PSUS August 2015
08/04/15 Jakeway, Maryrose 2 IntroductionIntroduction Maryrose Jakeway Michigan State University Mechanical Engineering Exp Grad: December 2016 MEU Op Tech Manager: Derek Rinaldo Mentor: Kaethe Pfeiffer
08/04/15 Jakeway, Maryrose 3 What I Did This SummerWhat I Did This Summer For Fun Reading/Cooking/Painting/Exploring the Area/Binge Watching TV Boat Cruise RailCats Game White Sox Game For Work Safety Tours & Training Eagle Incident Report Power Station SPRV
08/04/15 Jakeway, Maryrose 4 Tours & Training (1-2)Tours & Training (1-2) Safety Tours Sewage Pumping Station Shops Complex Docks Locomotive Repair Fabrication Shop Machine Shop Crane Repair Central Spares Main Shop & Annex Building Blast Furnace Closed Water Pumping Station Lakewater Pumping Station No. 1
08/04/15 Jakeway, Maryrose 5 Tours & Training (2-2)Tours & Training (2-2) Additional Tours Power Station Steel Producing Iron Producing Sinter Plant Hot Mill I/N Tek & I/N Kote Research & Development Training CPR / First Aid Arc Flash
08/04/15 Jakeway, Maryrose 6 ProjectsProjects Eagle Incident Report Created follow-up document for June 6th fire under waste treatment bridge. Power Sta South 900/265 psi Steam Pressure Reducing Valve (PRV) Modeled S. PRV steam system. Analyzed current design to determine nominal operational envelope. Compared ideal conditions to 3/20/15 failure. In progress: Operational Procedure Report.
Safety Valves on 265 # pipe Damage resulting from 3/20/15 Learned how to perform an engineering and failure analysis. First learn how and why things work. Then look at a failure. What fails? When? Why? How? Knowing max steam flow rates at different pressures/ temperatures changes the operating envelope of the system and how the equipment will respond. Develop a model of the system. South PRV: LearningSouth PRV: Learning LessonsLessons
500 600 700 800 900 1000 1200 200 2.725 3.059 3.38 3.693 4.003 4.31 4.917 250 2.151 2.426 2.688 2.943 3.193 3.44 3.929 300 1.767 2.005 2.227 2.442 2.653 2.861 3.27 400 1.258 1.477 1.651 1.817 1.978 2.136 2.446 500 0.993 1.159 1.304 1.441 1.573 1.701 1.95 600 0.795 0.946 1.073 1.19 1.302 1.411 1.621 700 0.793 0.908 1.011 1.109 1.204 1.385 800 0.678 0.7383 0.877 0.964 1.048 1.209 900 0.588 0.686 0.772 0.852 0.928 1.071 1000 0.514 0.608 0.688 0.761 0.831 0.962 1100 0.453 0.545 0.619 0.687 0.75 0.872 Input Temperature (属F) 900 Pressure (PSIA) 900 Sp. Volume (ft 3 /lb) 0.852 Diameter (inches) 20 Min Velocity (ft/s) 100 Max Velocity (ft/s) 300 1250 Output Min Capacity (klb/h) 921.83 Max Capacity (klb/h) 2,765.49 135.6 Pressure(PSIA) Temperature (属F) Properties of Superheated Steam Velocity (ft/s) For known capacity and unknown velocity, use alternative input/output. Alternative Input Capacity (klb/h) Alternative Output This model uses the continuity equation to determine capacity at a given temperature, pressure, pipe dimension, and an assumed range of operational velocity. *specific volume is automatically found using steam table
Questions? 08/04/15 Jakeway, Maryrose 9
Questions? 08/04/15 Jakeway, Maryrose 9

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2015 Intern Presentation Jakeway

  • 1. Maryrose Jakeway-Maryrose Jakeway- Mechanical Engineer InternMechanical Engineer Intern ArcelorMittal Burns Harbor: MEU-PSUSArcelorMittal Burns Harbor: MEU-PSUS August 2015
  • 2. 08/04/15 Jakeway, Maryrose 2 IntroductionIntroduction Maryrose Jakeway Michigan State University Mechanical Engineering Exp Grad: December 2016 MEU Op Tech Manager: Derek Rinaldo Mentor: Kaethe Pfeiffer
  • 3. 08/04/15 Jakeway, Maryrose 3 What I Did This SummerWhat I Did This Summer For Fun Reading/Cooking/Painting/Exploring the Area/Binge Watching TV Boat Cruise RailCats Game White Sox Game For Work Safety Tours & Training Eagle Incident Report Power Station SPRV
  • 4. 08/04/15 Jakeway, Maryrose 4 Tours & Training (1-2)Tours & Training (1-2) Safety Tours Sewage Pumping Station Shops Complex Docks Locomotive Repair Fabrication Shop Machine Shop Crane Repair Central Spares Main Shop & Annex Building Blast Furnace Closed Water Pumping Station Lakewater Pumping Station No. 1
  • 5. 08/04/15 Jakeway, Maryrose 5 Tours & Training (2-2)Tours & Training (2-2) Additional Tours Power Station Steel Producing Iron Producing Sinter Plant Hot Mill I/N Tek & I/N Kote Research & Development Training CPR / First Aid Arc Flash
  • 6. 08/04/15 Jakeway, Maryrose 6 ProjectsProjects Eagle Incident Report Created follow-up document for June 6th fire under waste treatment bridge. Power Sta South 900/265 psi Steam Pressure Reducing Valve (PRV) Modeled S. PRV steam system. Analyzed current design to determine nominal operational envelope. Compared ideal conditions to 3/20/15 failure. In progress: Operational Procedure Report.
  • 7. Safety Valves on 265 # pipe Damage resulting from 3/20/15 Learned how to perform an engineering and failure analysis. First learn how and why things work. Then look at a failure. What fails? When? Why? How? Knowing max steam flow rates at different pressures/ temperatures changes the operating envelope of the system and how the equipment will respond. Develop a model of the system. South PRV: LearningSouth PRV: Learning LessonsLessons
  • 8. 500 600 700 800 900 1000 1200 200 2.725 3.059 3.38 3.693 4.003 4.31 4.917 250 2.151 2.426 2.688 2.943 3.193 3.44 3.929 300 1.767 2.005 2.227 2.442 2.653 2.861 3.27 400 1.258 1.477 1.651 1.817 1.978 2.136 2.446 500 0.993 1.159 1.304 1.441 1.573 1.701 1.95 600 0.795 0.946 1.073 1.19 1.302 1.411 1.621 700 0.793 0.908 1.011 1.109 1.204 1.385 800 0.678 0.7383 0.877 0.964 1.048 1.209 900 0.588 0.686 0.772 0.852 0.928 1.071 1000 0.514 0.608 0.688 0.761 0.831 0.962 1100 0.453 0.545 0.619 0.687 0.75 0.872 Input Temperature (属F) 900 Pressure (PSIA) 900 Sp. Volume (ft 3 /lb) 0.852 Diameter (inches) 20 Min Velocity (ft/s) 100 Max Velocity (ft/s) 300 1250 Output Min Capacity (klb/h) 921.83 Max Capacity (klb/h) 2,765.49 135.6 Pressure(PSIA) Temperature (属F) Properties of Superheated Steam Velocity (ft/s) For known capacity and unknown velocity, use alternative input/output. Alternative Input Capacity (klb/h) Alternative Output This model uses the continuity equation to determine capacity at a given temperature, pressure, pipe dimension, and an assumed range of operational velocity. *specific volume is automatically found using steam table