NCCER Pipeline Mech study materials
NCCER Pipeline Mech study resources

NCCER Pipeline Mech cheat sheet

NCCER Pipeline Mech · Keep the key ideas within reach.

Quick reference

Pipeline Mechanic

  • Pipe size is stated as nominal pipe size (NPS) with wall thickness by schedule number; for a given NPS, higher schedule numbers mean thicker walls and smaller inside diameter.

  • Line pipe dimensions follow API 5L; grade designations such as X42, X52, X65, and X70 give minimum yield strength in ksi (X65 = 65,000 psi minimum yield).

  • Barlow's formula: internal pressure P = 2St/D, where S is allowable stress, t is nominal wall thickness, and D is outside diameter; design codes apply a design factor F to S.

  • Hydrostatic test pressure is typically 1.25 to 1.5 times the maximum allowable operating pressure, held long enough to inspect for leaks and pressure loss.

  • Buttweld fit-up: root gap, bevel angle (commonly 30 degrees per land), and line-up clamp alignment must meet the welding procedure specification before the root pass.

  • Flange bolt tightening uses a star or crisscross pattern in stages (typically 30, 60, 100 percent of target torque) to seat the gasket evenly and avoid uneven loading.

  • Cold field bends on line pipe are limited by code to a minimum radius (commonly 18 to 24 times pipe diameter) and must be checked for ovality and wall thinning.

  • Coating holiday detection uses a high-voltage holiday detector set to the coating thickness; excessive voltage can damage sound coating and give false indications.

Quick reference

Pipeline Mechanic

  • Pipe lowering-in requires enough sideboom spread so that combined stresses from span and curvature stay within allowable limits; long unsupported spans cause overstress and buckling.

  • Trench safety: spoil piles and equipment are kept back from the excavation edge, and protective systems (sloping, shoring, shielding) are required in unstable or deep excavations.

  • Pipeline pigging: a gauging pig verifies bore roundness, a cleaning pig removes debris, and a smart or instrumented pig records metal loss and geometry for integrity assessment.

  • Cathodic protection criterion commonly used is a pipe-to-soil potential of -0.85 V (copper/copper sulfate reference) or more negative for coated steel pipe.

  • Hot work near a live pipeline requires gas testing for flammables and oxygen, plus isolation or purging of the section before welding or cutting.

  • Torque values for bolted connections come from the project specification or manufacturer data; lubricant condition changes the achieved clamp load for the same torque.

  • A pipeline pressure test must be held with the section isolated, gauges calibrated, and air and water vented so trapped gas does not cause a violent release on failure.