Inflection Point Engineering Materials and Corrosion Curriculum

Mod 8 - Material Selection

Module from the Materials and Corrosion Curriculum curriculum.

MATERIAL SELECTION GUIDELINES · Learning Objectives · 1. Apply corrosion allowance, design temperature, and hardness criteria 2. Specify PWHT and hardness limits for sour service 3. Balance initial cost vs life-cycle cost in material selection 4. Reference API 571 for damage mechanism-driven selection · Material Selection by Service — Typical Refinery Applications

Service Temperature Pressure Typical Material Alternative (Upgrade) Corrosion Allowance Notes
Crude Overhead (desalted) <250°F 100 psig CS + inhibitor injection Mo2 SS if TAN >0.5 1/8" (3 mm) Cl⁻ control critical, no upper cutline moisture
Crude Unit HVGO / Fractionator 600-750°F 50 psig 5Cr-0.5Mo (9Cr) 317L SS for TAN >2.0 1/16" Sulfur + naphthenic acid corrosion
Hydroprocessing Reactor 650-800°F 1500-2500 psig 2.25Cr-1Mo V-mod (SA 336) 2.25Cr-1Mo + 347 SS weld overlay 1/8" H2 attack resistance, temper embrittlement
Amine Absorber (lean/rich) 100-150°F 150 psig CS PWHT + HIC plate 316 SS if corrosion severe 1/4" (6 mm) Wet H2S + amine degradation products
Sour Water Stripper 250-350°F 50 psig CS PWHT + 410SS weld overlay Duplex 2205 for severe 1/4" High CO2 + H2S + NH3, SSC + corrosion
Alkylation (sulfuric acid) 40-120°F 150 psig Monel 400 (piping), CS PWHT (vessels) Alloy 625 for severe 1/16" Acid type-dependent material
FCC Regenerator 1250-1350°F 30 psig CS with refractory lining None upgraded Refractory dependent High temp + oxidation — refractory protects
Cooling Water 85-125°F 150 psig CS + inhibitor + biocide Cu-Ni (90/10) for seawater 1/16" Microbiological + corrosion + erosion
Source: API 571 Damage Mechanisms, Materials_Selection_Guide_v1.xlsx, IPE-EP-10 series (20 documents)

Source: Materials_and_Corrosion_Curriculum_v1.xlsx · Sheet: Mod 8 - Material Selection