Please answer these questions. Find out your score at the end.
A. Construction and design information, operating and inspection history
B. A complete weld map from the original construction plans
C. The exact location on a facility plan
D. The schedule and piping sizes for the vessel
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A. The authorized pressure vessel inspector
B. The maintenance manager
C. The production manager
D. The insurance company
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A. Cracks open to the surface
B. Laminations on the surfaces of plate
C. Internal cracking of welds
D. Subsurface porosity
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A. Hydro blasted
B. Grit blasted to SA 2
C. Wire brushed
D. The type of surface preparation depends on individual circumstances and could be any of the above
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A. ASME Section VIII
B. ASME Section V
C. API 572
D. API 510
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A. A container designed to withstand internal or external pressure
B. A vessel for the containment of process fluids with or without internal pressure
C. A container designed to operate below atmospheric pressure
D. A container no greater than 8” in cross section
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A. Any standard used to build a vessel
B. Any technique of construction
C. Any standard used to repair vessel
D. The Code or standard to which a vessel was originally built
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A. From data collected on vessels providing the same or similar service or from published data on vessels providing comparable service
B. Employing highly experienced inspectors or engineers
C. Corrosion tabs and UT readings
D. Assuming a standard corrosion rate
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A. Vessels constructed to API-572
B. Vessels after they have been placed in service
C. Pressure vessel being fabricated to ASME Section VIII, Division 1 or 2
D. Only pressure vessels being fabricated for refinery/petro-chemical service
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A. The full remaining safe operating life up to a maximum of 4 years
B. The full remaining safe operating life up to a maximum of 2 years
C. The full remaining safe operating life up to a maximum of 1 year
D. The full remaining life of the vessel
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A. AI
B. Jurisdiction
C. Owner/user
D. Pressure vessel engineer
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A. Close monitoring of the welding operation
B. A metallurgical review conducted by an engineer shall be performed to assure the proposed alternative is suitable for the application
C. Time required to do the repair, and personnel safety
D. Consultation with the jurisdictional requirements
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A. The owner-user
B. The pressure vessel engineer
C. The National Board inspector
D. The vessel manufacturer
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A. Approval of the ASME
B. Report from an external professional engineer
C. Approval of the operation’s engineering department
D. Calculations from the manufacturer or the owner-user’s engineer
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A. The corners shall be squared
B. The corners shall be rounded 1 inch minimum radius
C. The corners shall be provided with a 3 inch radius
D. The corners shall be provided with a 6 inch radius
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A. You may not use any plug locations used for UT thickness reading to inspect the vessel
B. Select portions must be removed for inspections
C. It shall always be removed to inspect underneath
D. If insulation is in good condition and the vessel operates within the high and low temperatures stated in API 510, removal of insulation is not necessary for inspection of the vessel
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A. Precipitation at the grain boundaries may occur.
B. The rupture disk may implode
C. The relief device may fail
D. Creep of the vessel’s material may occur
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A. The vessel must be inspected and certified by the original vessel manufacturer
B. The vessel must be externally and internally inspected prior to re-use
C. The vessel must be inspected externally and certified by the owner/user
D. A new nameplate shall be attached to the vessel
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A. likelihood of poor inspection and the consequence of failure
B. likelihood of failure and the effects on plant operation of failure
C. chances of failure and the cost of failure
D. likelihood of failure and the consequence of failure
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A. One half the estimated remaining life or 15 years whichever is less
B. One half the estimated remaining life or 10 years whichever is greater
C. One half the estimated remaining life or 10 years whichever is less
D. One half the estimated remaining life or 15 years whichever is greater
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A. 5 years
B. 6 years
C. 10 years
D. 12 years
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A. at installation of vessel
B. whenever there is a change in fluid service
C. whenever the vessel's ownership changes
D. whenever the vessel's ownership and location changes
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A. An engineer experienced in pressure vessel design and the API inspector must be consulted
B. The API inspector must be consulted
C. The API inspector and NBIC inspector must be consulted
D. An experienced engineer must be consulted
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A. 1000 hours
B. 100 months
C. 1000 days
D. 1000 weeks
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A. Inspect the vessel for proper electrical grounding
B. The area should be roped off and no one else is to be working in the area
C. No hot work permits in the immediate area must be issued until the inspection is complete
D. OSHA rules should be reviewed and followed where applicable
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A. Base line thickness reading must be taken per NBIC regulation 6
B. Base line thickness readings must be taken per API 572
C. A first internal inspection.
D. A first internal inspection, however if a manufactures’ data report (U1) assuring that the vessel is satisfactory for its intended service is available the first internal may be waived
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A. 300˚F
B. 700˚F
C. 500˚F
D. 900˚F
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A. Calculations from either the manufacturer or an owner-user engineer experienced in pressure vessels
B. Review Inspection records verify the pressure vessel has been in the proposed service previously
C. Use of Non-Code requirements as established in accordance with the alternative rules of API 572
D. Calculations from only a manufacturer experienced in pressure vessels
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A. Authorized repair organization
B. Owner-user
C. Authorized inspection agency
D. Authorized engineering company
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A. 0.005” per year
B. 0.001” between inspections not to exceed 5 years between inspections
C. 0.001”per year
D. 0.005” between inspections not to exceed 3 years between inspections
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A. Call in a pressure vessel engineer
B. Design an overlay patch to completely cover the affected area that has rounded corners
C. Using an insert patch, to completely remove the affected area
D. Removing the crack using by grinding and inspect using an NDE procedure before repair by welding
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A. The API authorized inspector
B. An engineer competent in pressure vessel design and the API authorized inspector
C. A repair organization which holds a valid NBIC R stamp
D. Any of the above
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A. Surface corrosion on the body of the relief device
B. If a pressure test is being conducted in which the test pressure will exceed the set pressure of the safety relief valve with the lowest setting
C. The safety relief device was opening on a irregular, unexplainable basis
D. Blowback had been detected and the manufacturers recommend removal
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A. The condition of the vessel and the recommendations described by NBIC
B. The condition of the vessel and the recommendations of the repair organization
C. The recommendation of the repair organization and the environment in which the vessel operates
D. The condition of the vessel and the environment in which the vessel operates
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A. Minimum temperature shall be at least 20˚F above the minimum design metal temperature
B. Minimum temperature shall be at least 30˚F above the minimum design metal temperature
C. Minimum temperature shall be ambient temperature but not less than 55°F
D. Minimum temperature shall be 60°F
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A. 10 ° F above MDMT
B. 65 ° F above ambient
C. 30 ° F above ambient
D. 30 ° F above testing liquids temperature
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A. The NBIC
B. The current ASME Code edition
C. The API 510 Code
D. The Code the vessel was constructed to including non-standard and jurisdictional special vessels
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A. Cracking due to operating at high temperatures above 650°F – 1100°F
B. Cracking due to low temperature service
C. Loss of ductility and notch toughness due to exposure above 650°F – 1100°F
D. Flaking of the metal surfaces, causing dip pits due to exposure above 650ºF – 1100°F
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A. The chief inspector and the unit engineer
B. The API authorized inspector
C. A professional engineer only, is allowed to perform these calculations
D. The manufacturer or an owner-user engineer (or his designated representative)
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A. operating temperature increases
B. operating pressure decreases
C. operating pressure increases
D. fluid composition changes
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A. authorized inspector
B. repair organization owner/user
C. pressure vessel engineer
D. welding inspector
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A. The attachment of an additional nameplate of stamping
B. The pressure test required by the code
C. The final painting of the vessel
D. The stamping of welds by each welder
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A. only ASME B&PV Section VIII
B. only ASME B&PV Section VIII and the API/ASME Code for Unfired Pressure Vessels
C. ASME B&PV Section VIII and other current codes (except French vessel code)
D. any fabrication code
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A. Longitudinal stress acting along the longitudinal axis
B. Circumferential stress acting along the longitudinal axis
C. Circumferential stress acting along the circumferential axis
D. Longitudinal stress acting along the circumferential axis
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A. 15 years
B. 10 years
C. 5 years
D. 20 years
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A. 175°F and 350°F for austenitic stainless steels
B. 20°F and 350°F for carbon and low alloy steels
C. 10°F and 350°F for carbon and low alloy steels
D. 275°F and 450°F for austenitic stainless steels
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A. Review all NDE procedures prior to commencement of the NDE used to waive the hydrostatic test requirement
B. Consult with the chief inspector of the jurisdiction
C. Make certain it is permitted by any jurisdictional rules that may exist and consult with an engineer experienced in pressure vessel design and the Authorized Pressure Vessel Inspector
D. Check with the NBIC Authorized inspector
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A. A pressure vessel repair organization
B. A registered professional engineer
C. A corrosion specialist
D. An authorized Inspector
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