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Acoustic Emission Examination of Metal Pressure Vessels
Anatomy of a Catastrophic Boiler Accident
Austenitic Stainless Steel
Basic Weld Inspection - Part 1
Basic Weld Inspection - Part 2
Black Liquor Recovery Boilers - An Introduction
Boiler Efficiency and Steam Quality: The Challenge of Creating Quality Steam Using Existing Boiler Efficiencies
Boiler Logs Can Reduce Accidents
Boiler/Burner Combustion Air Supply Requirements and Maintenance
Carbon Monoxide Poisoning Preventable With Complete Inspection
Combustion Air Requirements:The Forgotten Element In Boiler Rooms
Creep and Creep Failures
Description of Construction and Inspection Procedure for Steam Locomotive and Fire Tube Boilers
Ensuring Safe Operation Of Vessels With Quick-Opening Closures
Environmental Heat Exchangers
Factors Affecting Inservice Cracking of Weld Zone in Corrosive Service
Failure Avoidance in Welded Fabrication
Finite Element Analysis of Pressure Vessels
Fuel Ash Corrosion
Fuel Firing Apparatus - Natural Gas
Grain Boundaries
Heat Treatment - What Is It?
How to Destroy a Boiler -- Part 1
How to Destroy a Boiler -- Part 2
How to Destroy a Boiler -- Part 3
Identifying Pressure Vessel Nozzle Problems
Inspection, Repair, and Alteration of Yankee Dryers
Inspection, What Better Place to Begin
Laminations Led to Incident
Lay-up of Heating Boilers
Liquid Penetrant Examination
Low Voltage Short Circuiting-GMAW
Low Water Cut-Off Technology
Low-Water Cutoff: A Maintenance Must
Magnetic Particle Examination
Maintaining Proper Boiler Inspections Through Proper Relationships
Microstructural Degradation
Miracle Fluid?
Organizing A Vessel, Tank, and Piping Inspection Program
Paper Machine Failure Investigation: Inspection Requirements Should Be Changed For Dryer Can
Pipe Support Performance as It Applies to Power Plant Safety and Reliability
Polymer Use for Boilers and Pressure Vessels
Pressure Vessel Fatigue
Pressure Vessels: Analyzing Change
Preventing Corrosion Under Insulation
Preventing Steam/Condensate System Accidents
Proper Boiler Care Makes Good Business Sense:Safety Precautions for Drycleaning Businesses
Putting a Stop to Steam Kettle Failure
Quick Actuating Closures
Quick-Actuating Door Failures
Real-Time Radioscopic Examination
Recommendations For A Safe Boiler Room
Recovering Boiler Systems After A Flood
Rendering Plants Require Safety
Repair or Alteration of Pressure Vessels
Residential Water Heater Safety
School Boiler Maintenance Programs: How Safe Are The Children?
Secondary Low-Water Fuel Cutoff Probe: Is It as Safe as You Think?
Short-Term High Temperature Failures
Specification of Rupture Disk Burst Pressure
Steam Traps Affect Boiler Plant Efficiency
Steps to Safety: Guide for Restarting Boilers After Summer Lay-Up
Stress Corrosion Cracking of Steel in Liquefied Ammonia Service - A Recapitulation
Suggested Daily Boiler Log Program
Suggested Maintenance Log Program
System Design, Specifications, Operation, and Inspection of Deaerators
Tack Welding
Temperature And Pressure Relief Valves Often Overlooked
Temperature Considerations for Pressure Relief Valve Application
The Authorized Inspector's Responsibility for Dimensional Inspection
The Effects of Erosion-Corrosion on Power Plant Piping
The Forgotten Boiler That Suddenly Isn't
The Trend of Boiler/Pressure Vessel Incidents: On the Decline?
The Use of Pressure Vessels for Human Occupancy in Clinical Hyberbaric Medicine
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Top Ten Boiler and Combustion Safety Issues to Avoid
Typical Improper Repairs of Safety Valves
Wasted Superheat Converted to Hot, Sanitary Water
Water Maintenance Essential to Prevent Boiler Scaling
Water Still Flashes to Steam at 212
Welding Consideration for Pressure Relief Valves
Welding Symbols: A Useful System or Undecipherable Hieroglyphics?
What is the Best Welding Process?
What Should You Do Before Starting Boilers After Summer Lay-Up?
Why? A Question for All Inspectors

Factors Affecting Inservice Cracking of Weld Zone in Corrosive Service

Harold L. Schmeilski
Illinois Division of Boiler and Pressure Vessel Safety, D. R. Gallup, Superintendent.

January 1986  

Category: Incidents 


Summary: The following article is a part of National Board Classic Series and was reprinted in the January 1986 National Board BULLETIN. Permission to reprint was granted by the Illinois Division of Boiler and Pressure Vessel Safety, D. R. Gallup, Superintendent. (6 printed pages)




This article describes the cause of failure of a monoethandamine (MEA) absorber vessel that ruptured in the state of Illinois in 1984, resulting in 17 fatalities and property damage in excess of $100 million.


The ruptured vessel was designed in accordance with The American Society of Mechanical Engineers (ASME) Boiler and Pressure Vessel Code, Section VIII rules. The vessel was constructed of 1 inch thick SA516 Gr 70 steel plates rolled and welded with full penetration submerged arc joints, without postweld heat treatment. The cylindrical vessel measures 81/2 feet in diameter with hemispherical ends comprising an overall height of 55 feet. Operating conditions were 200 psig internal pressure containing largely propane and hydrogen sulfide at 100¡F. An internal system distributed monoethanolamine (MEA) through the vessel for the purpose of removing hydrogen sulfide from the gas.



The vessel went into operation in 1969. Soon after start-up, hydrogen blisters were observed to be forming in the bottom two courses of the cylindrical vessel wall. Metallurgical analysis showed laminations to be present in the steel.

In 1974, due to the large blister area found in the second course, a full circumferential ring 8 feet high was replaced in field by inserting a preformed ring in three equal circumferential segments. The welding was accomplished by the shielded metal arc process ("stick welding") without preheating or postweld heat treating.

The ASME Code does not require preheating or postweld heat treatment for SA516 Gr 70 steel 1 inch thick or less. However, this steel is slightly air hardenable during welding, depending on the welding process, position and procedure employed. This material is classified as a P1, Group 2 material according to ASME Code Section IX.

The vessel was operated under the owner/user option of the Illinois Boiler and Pressure Vessel Safety Act and received a certification inspection approximately every two years. Continuing corrosion problems in the lower end of the vessel resulted in the installation of an internal Monel liner in 1976 covering the bottom head and most of the first ring, stopping short of the replaced ring. Periodic internal inspections were mainly visual with wall thickness determinations made by an ultrasonic thickness gauge.

Just prior to the rupture, an operator noted a horizontal crack about 6 inches long spewing a plume of gas. While attempting to close off the main inlet valve, the operator noted the crack had increased in length to about 2 feet. As the operator was evacuating the area and as the firemen were arriving, the vessel ruptured releasing a large quantity of flammable gas which ignited shortly thereafter creating a large fireball and the ensuing of deaths and damage. The separation occurred along the lower girth weld joint made during the 1974 repair. The upper portion of the vessel was propelled 3500 feet by the thrust of the escaping gas.



The fracture surfaces exhibited the presence of four major prerupture cracks in the heat affected zone (HAZ) of the lower girth field repair weld. The cracks originated on the inside surface and had progressed nearly through the wall over a period of time. The largest precrack was located in the same area as the prerupture leak reported by the operator. In total, the four cracks encompassed a circumferential length of about 9 feet (33.7% of circumference). The remainder of the fracture exhibited a fast running brittle separation.

 Microscopic examination of various cross sections through the failed weld joint area showed the cracking originated in a hard microstructure in the HAZ and progressed in a manner characteristic of hydrogen related damage in hard steels (see figures above). The HAZ exhibited hardness of up to 45 HRC (Hardness Rockwell "C") (450 Brinell), equivalent to a tensile strength of over 200,000 psi in the region of weld cracking. By comparison, the base metal had a hardness value of less than 20 HRC (229 BHN [Brinell Hardness Number], 110,000 psi tensile strength). The following sections discuss technical factors contributing to in-service cracking of weld joints under such conditions.


Welding procedures adopted must take into account not only the minimum requirements of ASME Code Section IX and the appropriate design section, but must also be suitable for the specific service conditions likely to be encountered. Stress corrosion cracking, hydrogen embrittlement and corrosion fatigue are typical of material/environment interactions that are not fully accounted for in the ASME Code design rules. Appreciation of such potential problems is left to the process designer, vessel designer, owner, contractor or inspector. Reliance on only the ASME Code rules is not enough to assure safety of vessels operating in many corrosive environments.

The weld HAZ contains potentially crack susceptible metallurgical structure, hardness variations and residual stresses that can promote various types of unexpected service induced cracking depending on the chemical environment and operating temperature. Industry experience has shown that steel having a hardness of 22 HRC maximum is resistant to cracking even under severe exposure conditions where hydrogen can be absorbed by the steel. At hardness levels above 22 HRC, steel becomes less resistant to hydrogen induced cracking and other environmental effects. At high hardness (above about 40 HRC), steel becomes quite susceptible to cracking in the presence of hydrogen.

In potentially critical environments, the weld joint properties must be carefully controlled. Weld HAZ hardness is a function of the cooling rate after welding. Preheating to at least several hundred degrees and maintaining an interpass temperature during welding can warm the joint area sufficiently to prevent rapid cooling after welding. Carbon content and alloy composition will dictate the appropriate temperature. Rapid cooling of even mild steel can result in unacceptably high HAZ hardness for service in aggressive chemical environments.

Postweld heat treating (PWHT) is often necessary in critical weld joints to temper (soften) or stress relieve weld joints in rugged duty or aggressive chemical environments. Higher carbon steels and more alloyed steels are nearly always given PWHT. Even when not specifically called for in ASME Code Section IX, preheating or PWHT may be necessary. In hydrogen environments, avoiding formation of a hard HAZ is crucial. Other corrosive environments present similar concerns.

The specific weld procedure employed must be developed by individuals with pertinent knowledge of the ASME Code (which should be viewed as the minimum guideline) as well as material behavior expertise in aggressive environments.


There are many specific ways that corrosion may contribute to unexpected failures. Often, corrosion problems are handled simply by making the component thicker (a corrosion allowance). This is appropriate so long as the corrosive conditions are known, the vessel is periodically inspected and if the corrosion is not highly localized. Corrosion fatigue, pitting, stress corrosion and hydrogen attack are examples of metal/environment problems that cannot be adequately handled by a corrosion allowance and superficial inspection methods alone.

Hydrogen-assisted cracking and stress corrosion cracking will not always be readily apparent. Carefully preparing the surface for visual examination, along with other techniques such as dye penetrant, magnetic particle, or shear wave ultrasonic inspection methods, may be required to detect such defects. Corrosion-enhanced damage is often associated with welds, nozzles, or areas of unstable environmental conditions; places where either the environment, stress, or metallurgical condition may abruptly change.


High pressure hydrogen or acidic environments can introduce damaging levels of hydrogen into steel, particularly hard steels or hard HAZs. The mechanism of hydrogen evolution and penetration is illustrated above. The absorbed hydrogen atoms are attracted to high stress regions in the structure, such as crack-like defects. The combination of hard steel and absorbed hydrogen leads to the development of cracks. Once inside the steel, these hydrogen atoms also migrate to inclusions or laminations and create hydrogen fissures and blisters.

Hydrogen sulfide, cyanide and arsenic, even in trace deposits, are examples of materials that greatly increase the amount of hydrogen that becomes absorbed by steel. Therefore, under acidic corrosive conditions, particularly those environments that also contain hydrogen sulfide, cyanide or arsenic, hydrogen damage can be severe. Weld HAZ hardness must be carefully controlled under these circumstances, regardless of whether or not the ASME Code or the National Board Inspection Code specifically address the subject.

Welding procedures, repair methods, and inspection procedures must include careful consideration of potential failure modes in corrosive environments. If pressure vessels or allied components are operating in an aggressive environment, special steps should be taken to assure that individuals with pertinent expertise are involved in the planning and review stages of design, inspections and repairs. When distress signals are present, take the time to evaluate the cause and determine what special precautions are necessary.


The problems of in-service cracking of weld zones can be minimized by attention to the important factors summarized below.

  • Preheat or postweld heat treat weld joints that may develop a hard HAZ when corrosive conditions are met.
  • Inspect weld HAZs for cracks by a suitable NDE method if hard HAZs are suspected.
  • Field repair welds are likely to have hard HAZs unless proper preheat or PWHT is applied.
  • Small welds on thick members and arc strikes are examples of conditions resulting in rapid heating and cooling and are likely areas for trouble.
  • Shop welds made according to the ASME Code may also crack in service under severely corrosive conditions.
  • Preheating field weld joints will help drive off the dissolved hydrogen that has been picked up by the steel in service.
  • Be particularly cautious when inspecting critical components in unfamiliar corrosive service, especially when prior history reveals problems and when field repairs have been made.



Editor's note: Some ASME Boiler and Pressure Vessel Code requirements may have changed because of advances in material technology and/or actual experience. The reader is cautioned to refer to the latest edition of the ASME Boiler and Pressure Vessel Code for current requirements.


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