7.1 Piping Components and Valves (API RP 574)

API 570 Piping Inspector Exam

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1 Chapter 1: Piping Inspection Planning & Circuits

1.1 Inspection Planning, History, and Safety 1.2 Piping Circuitization and Circuit Design 1.3 Condition Monitoring Locations (CMLs) & Coverage

2 Chapter 2: Inspection Intervals & Extent of Inspection

2.1 Piping Classifications (Classes 1, 2, 3, and 4) 2.2 Thickness Inspection Intervals (Half-Life & Visual Rules) 2.3 Owner-User QA and Roles (Inspector, Engineer, Examiner)

3 Chapter 3: Calculations & Remaining Life

3.1 Corrosion Rates (Short-Term, Long-Term, and Initial Estimates) 3.2 Remaining Life and Retirement Thickness Calculations 3.3 MAWP Calculations for In-Service Piping

4 Chapter 4: ASME Codes for Piping Design

4.1 Wall Thickness Calculations for Pipe under Pressure (ASME B31.3) 4.2 Flange Ratings & P-T Limits (ASME B16.5) 4.3 Pressure & Leak Testing Rules (Hydrostatic vs. Pneumatic) 4.4 Weld Joint Quality Factors (Ej) and Casting Quality Factors (Ec) 4.5 Impact Testing, MDMT Exemption, and Charpy Requirements 4.6 Thermal Expansion Calculations (ASME B31.3 Appendix C) 4.7 Minimum Required Thickness of Permanent Blanks

5 Chapter 5: Nondestructive Examination (NDE)

5.1 Visual, Penetrant, and Magnetic Testing (VT, PT, MT) per ASME Sec V 5.2 Radiographic and Ultrasonic Testing (RT, UT) per ASME Sec V 5.3 Examiner Selection, Calibrations, and Acceptance Standards 5.4 Leak Testing per ASME Section V Article 10

6 Chapter 6: Welding Procedures & Qualifications

6.1 Reviewing WPS and PQR per ASME Section IX 6.2 Welder Performance Qualification (WPQ) and Limits 6.3 Preheating & PWHT Rules and Controls 6.4 Welding Processes, Inspection, and Metallurgy (API RP 577)

7 Chapter 7: Valves, Components, Materials & PRDs

7.1 Piping Components and Valves (API RP 574) 7.2 Positive Material Identification (PMI) (API RP 578) 7.3 Pressure Relieving Devices (PRDs) (API RP 576)

8 Chapter 8: Damage Mechanisms & Repairs

8.1 Corrosion Under Insulation (CUI) and Ambient Mechanisms 8.2 Process-Driven Damage Mechanisms (API RP 571) 8.3 Temporary and Permanent Repair Methods (ASME PCC-2 & API 570) 8.4 Soil Corrosion, Galvanic Corrosion, and Boiler Water Condensate Corrosion 8.5 Piping Rerating and Alterations (API 570) 8.6 Inspection Records, Reports, and Documentation 8.7 Amine/Caustic SCC, HCl, Sour Water, and MIC (API RP 571)

7.1 Piping Components and Valves (API RP 574)

Key Takeaways Explain This Topic AI

API RP 574 provides detailed inspection guidelines for piping system components, including pipe, fittings, and valves.

The extrados (outer radius) of elbows and the opposite wall of branch connections on tees are highly prone to localized erosion-corrosion.

Selective seam weld corrosion (SSWC) is a severe vulnerability in older ERW piping weld joints, producing V-shaped grooving.

Check valve swing disc detachment due to hinge pin wear poses a critical downstream piping and equipment obstruction hazard.

Throttling service in gate valves accelerates seat erosion and gate binding; globe valves have high pressure drop and downstream turbulence.

Last updated: July 2026

• 7.1 Piping Components and Valves (API RP 574)
• 1. Introduction to API RP 574

Piping systems are composed of a vast array of components, each presenting distinct metallurgical, mechanical, and geometric vulnerabilities. API RP 574 serves as the primary guidance document for the inspection of these components. Inspectors must understand the manufacturing variations of pipe, the wear characteristics of elbows, tees, and reducers, and the internal degradation modes of gate, globe, check, and ball valves. Proper inspection planning requires focusing non-destructive examination (NDE) on localized areas where velocity changes, flow impingement, or chemical concentration gradients accelerate wall thinning.

2. Pipe Manufacture and Inspection Concerns

Pipes are manufactured either as seamless or welded products. Seamless pipe is produced by piercing a solid billet and is generally preferred for severe, high-temperature, or high-pressure services. Welded pipe (such as Electric Resistance Welded - ERW, or Electric Fusion Welded - EFW) contains a longitudinal weld seam. Historically, older ERW pipe (manufactured before the mid-1980s) is susceptible to selective seam weld corrosion (SSWC), where the weld seam and its heat-affected zone (HAZ) corrode at a much faster rate than the base metal. This results in narrow, V-shaped grooving along the seam. Inspectors must utilize ultrasonic thickness testing (UT) or radiographic testing (RT) specifically targeted at the weld seam when inspecting older ERW systems.

3. Fittings: Elbows, Tees, and Reducers

Fittings are the primary sources of direction and size changes in piping systems, making them highly susceptible to localized wear:

Elbows : Flow velocity and centrifugal force cause fluid and entrained particles to impinge directly on the outer radius of the bend (the extrados). In erosive or corrosive services, this leads to rapid erosion-corrosion. Conversely, in low-flow or stagnant services, the inner radius (the intrados) may experience pitting due to sediment deposition. Long-radius (LR) elbows distribute flow change more gradually than short-radius (SR) elbows, but both require thick-map UT grids on the extrados.

Tees : Tees experience severe turbulence as flow splits or merges. The most critical wear point is the wall of the run pipe directly opposite the branch connection in a merging or tee-splitting flow. This area absorbs the direct impact of the fluid stream.

Reducers : Concentric and eccentric reducers are used to transition piping diameters. The change in cross-sectional area increases velocity (in reducing flow) or creates turbulence (in expanding flow). The transition angle of the reducer creates localized eddies that thin the wall immediately downstream of the weld joint.

Fitting Wear Summary Table

• Fitting Type Critical Wear Zone Primary Mechanism Recommended NDE
• Long/Short Radius Elbow Extrados (outer curve) Erosion-Corrosion / Impingement UT grid scanning / Profile RT
• Standard Tee Wall opposite branch inlet Flow Impingement / Turbulence UT grid / Radiography

Concentric/Eccentric Reducer Transition slope & downstream weld Localized Turbulence / Cavitation UT grid scanning

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4. Valve Inspection and Weak Spots

Valves are mechanical devices that control flow, isolate circuits, or prevent backflow. Each design has unique internal wear mechanisms:

Gate Valves : Designed primarily for isolation (fully open or fully closed). Operating a gate valve in a partially open (throttling) position causes severe erosion-corrosion of the gate (wedge) and the body seats. The gate guide slots can also wear, leading to gate binding. Stems are prone to corrosion and thread wear, and packing glands are common sites for external leaks.

Globe Valves : Designed specifically for throttling, globe valves force the process fluid to change direction twice in an S-shaped path. This creates a high pressure drop and extreme turbulence downstream of the seat. The seat and plug (disc) are prone to "wire-drawing" (erosion from high-velocity fluid leakage across a partially closed seat) and cavitation.

Check Valves : Swing check, piston check, and lift check valves prevent backflow. The single most critical safety hazard is hinge pin wear. Over time, constant turbulence causes the hinge pin to wear, leading to disc misalignment, seat leakage, or complete disc detachment. A detached disc can travel downstream, plugging critical piping or destroying downstream pumps. Lift check valves can suffer from guide rib wear, causing the piston to stick in the open or closed position.

Ball Valves : Excellent for quick, quarter-turn isolation. The primary wear mechanism is deterioration of the elastomer or metal seats due to particle entrapment. The ball surface can become scored by process debris, leading to bypass leakage. Stem packing leakage is also a concern.

5. Worked Example: Elbow Thickness Assessment

Consider an NPS 8 (8.625" OD), Schedule 40 carbon steel piping circuit (nominal thickness = 0.322 inches) operating in a corrosive hydrocarbon service. The minimum required thickness ( t m i n t_{min} t min ​ ) for pressure containment is calculated as 0.180 inches. During a turnaround, the inspector performs a grid UT scan on a 90-degree long-radius elbow.

Nominal Thickness: 0.322 in 0.322\text{ in} 0.322 in

Measured Minimum Thickness on Extrados ( t a c t u a l t_{actual} t a c t u a l ​ ): 0.210 in 0.210\text{ in} 0.210 in

Previous Measured Thickness (5 years ago): 0.245 in 0.245\text{ in} 0.245 in

Step 1: Calculate the Corrosion Rate (CR) CR = t p r e v − t a c t u a l years = 0.245 in − 0.210 in 5 years = 0.007 in/year \text{CR} = \frac{t_{prev} - t_{actual}}{\text{years}} = \frac{0.245\text{ in} - 0.210\text{ in}}{5\text{ years}} = 0.007\text{ in/year} CR = years t p re v ​ − t a c t u a l ​ ​ = 5 years 0.245 in − 0.210 in ​ = 0.007 in/year

Step 2: Calculate the Remaining Life (RL) RL = t a c t u a l − t m i n CR = 0.210 in − 0.180 in 0.007 in/year = 4.28 years \text{RL} = \frac{t_{actual} - t_{min}}{\text{CR}} = \frac{0.210\text{ in} - 0.180\text{ in}}{0.007\text{ in/year}} = 4.28\text{ years} RL = CR t a c t u a l ​ − t min ​ ​ = 0.007 in/year 0.210 in − 0.180 in ​ = 4.28 years

Step 3: Inspection Interval Determination

Under API 570, the thickness inspection interval must not exceed half the remaining life ( R L / 2 = 2.14 years RL/2 = 2.14\text{ years} R L /2 = 2.14 years ) or the maximum class-based interval (e.g., 5 years for Class 2 piping). Therefore, the next thickness measurement must be scheduled within 2.14 years.

6. High-Risk Localized Wear Areas

Beyond basic fittings, several system-level configurations are prone to accelerated localized wear:

Deadlegs : Stagnant sections where there is no flow. These collect corrodents (like water, acids, or salts) and are prone to severe pitting and Microbiologically Influenced Corrosion (MIC).

Injection Points : Mixing zones where a chemical or process fluid is introduced into a process stream. High shear forces and thermal gradients cause rapid localized thinning, requiring a specified inspection zone extending 12 inches or 3 times the pipe diameter upstream and downstream.

Soil-to-Air Interfaces : The interface where piping enters the ground, subject to atmospheric moisture and soil-based corrosive agents; visual inspection and excavation are required.