General Education
 
 

Corrosion Control In The Refining Industry
4-Day Classroom Course

Description
The Corrosion Control in the Refining Industry Course provides an overview of refinery process units and specific process descriptions, and focuses on the examination and identification of metallurgical problems that occur in process units. Students receive REFIN - COR 6.0 software which is a database of experiences, problems, and solutions encountered by refining industry corrosion engineers and includes minutes of meetings of NACE Committee TEG 205X (formerly T-8) on Refining Industry Corrosion from 1957 through 2002. This is information which can be used on-the-job and cannot be found anywhere else.

Who Should Attend

This course is geared toward those with a minimum of 1-2 years experience in refineries including: design engineers, process engineers, procurement agents, maintenance planners, service company representatives who support refineries, corrosion and equipment engineers, metallurgists, inspectors, and inspection supervisors.

Prerequisites
No prior training is required.

Course Highlights (include but are not limited to)

  • Refinery Corrosion
  • Failure Analysis-Techniques and Test Methods
  • Materials of Construction for Refinery Applications
  • Refinery Operations and Its Interactions with Corrosion
  • Refinery Units/Processes-Crude Distillation/Desalting, Fluid Catalytic Cracking Unit, CLER Unit, Hydroprocessing Unit, Catalytic Reforming, Decoking Units
Corrosion Monitoring Methods in Refineries

Course Outline

I. Corrosion and Other Failures

 

Introduction to Corrosion

Low-Temperature Refinery Corrosion

Low-Temperature Corrosion Principles

 

High-Temperature Refinery Corrosion

High-Temperature Corrosion Principles

High-Temperature Conditions

 

Corrosion/Failure Mechanisms

Metal Loss-General and/or Localized

 

Stress Corrosion Cracking

 

Hydrogen Blistering

 

Sulfide Stress Corrosion Cracking

 

Hydrogen Induced Cracking

 

Stress Oriented Hydrogen Induced Cracking

 

Hydrogen Cyanide

 

High-Temperature Hydrogen Attack

Metallurgical Failures

Grain Growth

Graphitization

Hardening

Sensitization

Sigma Phase

885 ° F (475 ° C) Embrittlement

Temper Embrittlement

Liquid Metal Embrittlement (LME)

Carburization

Metal Dusting

Decarburization

Selective Leaching

Mechanical Failures

Incorrect or Defective Materials

Mechanical Fatigue

Corrosion Fatigue

Cavitation Damage

Mechanical Damage

Overloading

Overpressuring

Brittle Fracture

Creep and Stress Rupture

Thermal Shock

Thermal Fatigue

 

Other Forms of Corrosion

Boiler Feedwater

Steam Condensate

Cooling Water Corrosion

Fuel Ash Corrosion

 

II. Failure Analysis in Refineries

 

Procedural Approach and Test Methods

Background Information

Initial Examination

Nondestructive Testing

Sectioning

Macroscopic Examination of Fracture Surfaces

Microscopic Examination

Fracture Appearance

Additional Testing and Analysis

Root Cause Analysis

Recommendations

 

III. Materials of Construction for Refinery Applications

 

The Role of the Corrosion Engineer

 

Corrosion Failures

Corrosion Testing Methods

Materials Selection Approach

Using Professional Consultants

Specifying Materials

National Standards

Company Standards

What the Designer Should Remember When Writing Specifications

Questions the Designer Should Ask to Control Quality

Fitness for Service

Refinery Materials of Construction

Introduction

Killed Steel

Steels

Carbon Steel

C-Mo Steels

Low-Alloy Steels

Cr-Mo Steels

Nickel Steels

Stainless Steels

Other Metals and Alloys

Non-Metallic Materials

 

Heat Treatment

Welding

 

IV. Refinery Operations and Overview

 

Refinery Operating Objectives

Refinery Process Overview

 

Process Interactions with Corrosion

 

V. Crude Distillation and Desalting

Introduction

Sources of Crude Oil

Composition of Crude Oil

Remaining Constraints

More About Crude Oil Composition

 

Crude Oil Pretreatment

Desalting

Preflash

 

Crude Distillation Unit

Operation of a Crude Distillation Unit

 

Corrosion in Crude Distillation Units

Columns

Exchangers and Piping

Fired Heaters

 

Other Corrosion Combating Measures

Blending

Desalting

Caustic Addition

Overhead pH Control

Corrosion Inhibitor

Water Washing


Corrosion Monitoring in Crude Units

Water Analysis (Overhead Corrosion Control)

Hydrocarbon Analysis

Corrosion Rate Measurement

On-Stream, Nondestructive Examination

 

VI. Fluid Catalytic Unit Corrosion and Metallurgical Damage

 

Process Description

Introduction

Hardware

Riser/Reactor

Regenerator

Flue Gas System

Fractionator

 

Corrosion Control in FCC Units

Materials of Construction

Damage Mechanisms and Suitable Materials

Reactors

Regenerators

Catalyst Transfer Piping System

 

Regenerator Reaction Mix Line, Main Fractionator, and Bottoms Piping

Flue Gas Systems

Inspection and Control Considerations

High-Temperature Oxidation

High-Temperature Sulfidation (H 2 S Attack)

High-Temperature Carburization

Polythionic Acid Stress Corrosion Cracking

Catalyst Erosion

Feed Nozzle Erosion

Refractory Damage

High-Temperature Graphitization

Sigma-Phase Embrittlement

885 ° F (475 ° C) Embrittlement

Creep Embrittlement

High-Temperature Creep

Thermal Fatigue

 

VII. Corrosion Control in Catalytic Light Ends Recovery (CLER) Units

CLER Process Description

Materials of Construction

Columns

Exchangers


Corrosion Problems:

Corrosion

Hydrogen Induced Damage

Inspection Techniques for Hydrogen Induced Damage

Prevention and Repair Techniques

Ammonia Stress Corrosion Cracking

Carbonate Stress Corrosion Cracking

Fouling/Corrosion of Reboiler Circuits

 

Corrosion Control Measures

Water Washing

Polysulfide Injection

Corrosion Inhibitors

Corrosion Monitoring

Hydrogen-Activity Probes

Chemical Tests

Corrosion Probes

 

VII. Sulfuric Acid Alkylation

Process Description

Reaction Section

Treating Section

Fractionation Section

Refrigeration Section

 

Materials of Construction

 

Materials and Corrosion Problems

Sulfuric Acid Corrosion

Acid Concentration

Acid Temperature and Velocity

Acid Dilution

Hydrogen Grooving

Feed Contaminants

Acid and Neutral Esters

Acid Carryover

Corrosion Under Insulation

Fouling Problems

Corrosion Control Measures

Reactor Section Corrosion

Tower Overhead Corrosion

Reboiler Corrosion and Fouling Control

Acid Tanks

Corrosion Control During Unit Shutdowns

Corrosion Under Insulation

Corrosion Monitoring

Inspection

Reaction Section

Treating Section

Fractionation Section

Refrigeration Equipment

Acid Tank

 

IX. Corrosion in Hydroprocessing Units

Hydroprocessing

Hydrotreating

Hydrocracking

Variations on Hydroprocessing

 

Common Corrosion Types in Hydroprocessing Units

High-Temperature Hydrogen Attack

High-Temperature H 2 S Corrosion-With Hydrogen Present

High-Temperature H 2 S Corrosion-With Little or No Hydrogen Present

Naphthenic Acid Corrosion

Ammonium Bisulfide Corrosion

Chloride Stress Corrosion Cracking

Failures Often Happen After Startup

Failures Happen at Predictable Points

Reactions with Stainless Steel

Polythionic Acid (PTA) Stress Corrosion Cracking

Stainless Steels Used to Prevent PTA

Other Methods Used to Prevent PTA SCC

Wet H 2 S Cracking

Sulfide Stress Cracking

 

Cracking: Hydrogen Induced and Stress-Oriented Hydrogen Induced

 

Material Property Degradation Mechanisms

Temper Embrittlement

Hydrogen Embrittlement

 

Selection of Materials

Reactor Loop -General

Reactor Feed System

Reactor Feed Furnaces

Reactors

Reactor Effluent System

Reactor Effluent-Distillation Feed Exchangers

 

Effluent Air Coolers

Effluent Air Cooler Inlet and Outlet Piping

Separator Vessels

Recycle Hydrogen System

Distillation Section

 

X. Catalytic Reforming

Introduction

Octane Number (RON)

Catalyst

Catalytic Reforming Process

Platformer (UOP)

Catalytic Reformer, Semi-Regenerative

Reactor Design

Corrosion Phenomena in Catalytic Reformers

HTHA

Stress Corrosion Cracking

Materials of Construction

Reactors

Exchangers and Piping

Fired Heaters and Other Equipment

Corrosion Control

Corrosion Monitoring

Inspection in Catalytic Reformers

 

XI. Delayed Coking Units-Corrosion, Materials, and Inspection

Considerations

Equipment and Operation of the Delayed Coking Unit

Corrosion and Other Problems in Delayed Coking Units

High-Temperature Sulfur Corrosion

Naphthenic Acid Corrosion

High-Temperature Oxidation/Carburization/Sulfidation

Erosion-Corrosion

Aqueous Corrosion

Corrosion Under Insulation

 

Thermal Fatigue, Temper Embrittlement of Cr-Mo Steels Used in Delayed Coking

Units

Inspection of Coking Units

General Inspection

Coke Drum Inspection

 

XII. Process Additives and Corrosion Control

Factors Affecting Corrosion

Acids

Temperature

Pressure

Flow

Turbulence

Material Selection

 

Methods to Mitigate Corrosion

Desalting and Caustic Injection

Water Washing

Acid Neutralization

Barrier Between Metal and Environment

 

Chemicals Used to Combat Corrosion

Filming Amines

Filming Formulation

Filmer Application

Treat Rates

Monitoring Filmer Performance

Neutralizing Amines

Polysulfides

Napthhenic Acid Corrosion Inhibitors

 

Application of Corrosion Inhibitors

XIII. Corrosion Monitoring Methods in Refineries

Introduction

Uses of Corrosion Monitoring

Corrosion Monitoring Techniques

Corrosion Coupons

Electrical Resistance Monitoring

Electrochemical Corrosion Monitoring

Linear Polarization Resistance

Potential Monitoring

Zero Resistance Ammetry (ZRA)

Electrical Impedence Spectroscopy (EIS)

Electrochemical Noise (EN)

Hydrogen Flux Monitoring

A Comprehensive Corrosion Monitoring Program

Corrosion Monitoring Sites

Corrosion Monitoring in Specific Process Units

Atmospheric Distillation Unit

Vacuum Distillation Unit

Fluid Catalytic Cracking Unit

Amine Treating Unit

Sour Water Stripper Units

Sulfuric Acid Alkylation Unit

Automated On-Line Monitoring

 

XIV. Refinery Injection Systems

Injection System Design Parameters

Engineering Practices

Process Design

Materials Selection Considerations

Inspection of Injection Point Locations

Location of Injection Point

 

Injection System Hardware

Chemical Storage Tanks

Chemical Injection Pumps

Additive Control Systems

Piping Systems

Injector

 

XV. Amine Treating

Refinery Amine Process Description

Tail Gas Units

Corrosion Phenomena

Corrosive Species

Amine Degradation

Cracking Phenomena

Corrosion Inhibitors

Materials of Construction

Corrosion Monitoring

Corrosion Control Measures

XVI. Sulfur Recovery Units

Sulfur Recovery Units

Sulfur Chemical Processes

Sulfur Recovery Process

Tail Gas Treating Unit

Incinerator

Cold Bed Adsorption (CBA) Unit

 

Corrosion Mechanisms

Sulfidation of Carbon Steels

Sour Environment Corrosion

Weak Acid Corrosion

 

Corrosion of Claus Units, by System

Feed Gas System

Corrosion Concerns

Mitigation of Corrosion

Inspections of the Feed Gas System

Reaction Furnace and Waste Heat Exchanger Systems

Corrosion Concerns

Mitigation of Corrosion

Inspections in the Reaction Furnace and Waste Heat Exchanger System

Claus Reactors, Condensers, and Reheat System

Corrosion Concerns

Mitigation of Corrosion

Inspections in the Claus Reactors, Condensers, and Reheat System

Liquid Sulfur Rundown Lines and Storage System

Corrosion Concerns

Mitigation of Corrosion

Inspections in Liquid Sulfur Rundown Lines and Storage System

 

Corrosion of CBA Units

Corrosion Concerns

Mitigation of Corrosion

Inspection of CBA Reactors, Condensers, and Piping

 

Corrosion of Tail Gas Treating Units

Burner and Mixing Chamber

Tail Gas Reactor and Waste Heat Exchanger

Water Quench and Re-Circulation Blower System

H 2 S Adsorption System

 

Corrosion in the Incinerator System

 
       
Designed & Maintained by Anis Chief