==================================================================

Storage tanks similar to the ones that exploded are often not considered to be covered by the OSHA PSM standard. The exclusion of many storage tanks from PSM coverage is inappropriate. Insurers of the petrochemical industry report that nearly 50 percent of all mechanical failures resulting in disasters involve storage tank or pipe failures.
Causes of the disaster included unsafe construction design and lack of inspection and maintenance of the tanks. Reliance on American Petroleum Institute and other industry published recommendations is inadequate because many of these guidelines primarily address newly installed equipment. For existing equipment, companies are usually only expected to consider whether or not they should comply with safety guidelines.
The Pennzoil tanks that exploded were nearly 60 years old and did not meet modern design safety requirements. The general practice of applying design safety guidelines only to newly constructed equipment while using inferior guidelines for existing equipment should be stopped. Workers operating and maintaining older process or storage equipment deserve the same degree of safety protection as workers involved with new equipment.
Failure by Pennzoil to individually dike tanks allowed burning liquid to quickly spread over a wide area of the plant, causing extensive damage. OSHAs diking standards need to be strengthened.
The placement of four contractor trailers in close proximity to the tanks allowed the fire to quickly engulf the trailers, resulting in the deaths of three workers.
The lack of these basic safety features allowed the tanks to fail at their bottom seams and take off like rockets, releasing all of the flammable contents.
The tanks that exploded were located only 4 feet apart. This allowed the explosion of the first tank to immediately spread to the second tank. This siting analysis should insure that a fire in one tank will not spread to other tanks.
The tank that first exploded was not properly isolated prior to welding being conducted. Numerous openings in the tank allowed flammable vapors to be released. The hazard of increases in ambient air temperature generating increasing amounts of flammable vapor was not recognized in the facility training program or in its welding procedures.
Air tests at Pennzoil showed that it was safe to weld in the early morning hours. However, conditions are often changing in facilities such as oil refineries. In this case, a change of only 9 degrees in the outside temperature over about 2 1/2 hours generated flammable vapors that ignited. Monitoring the air for flammable vapors once in the morning or periodically is not sufficient. Continuous monitoring for flammables can be easily accomplished using existing testing equipment found in most facilities.
The material that exploded at Pennzoil was methyl ethyl ketone (MEK). The EPA report ignored the toxic hazard of this material. Many flammable materials exceed their permissible exposure level (PEL) for health protection at concentrations far lower than their lower explosive limit (LEL). The PEL for MEK is 90 times lower than the LEL. The Immediately Dangerous to Life and Health (IDLH) level for MEK is 6 times lower than the LEL. Monitoring for toxic exposure to MEK or other toxic flammables provides advanced warning of danger.
Many companies believe that workers are protected from toxic exposures because their safety programs do not allow hot work, such as welding, when flammable vapors exceed 10 percent of the LEL. This is a mistake. In the case of MEK, 10 percent of the LEL is still 9 times the PEL. The safe health exposure levels for common flammable materials such as benzene, toluene, xylene, and styrene are even lower than the level set for MEK.
The tank that exploded contained a considerable amount of MEK. The tank was not designed to safely store this flammable material. Company procedures did not cover essential elements of the safe operation of vacuum truck loading and unloading.
The build-up of gravel and dirt around the bottom of the tanks that exploded allowed severe corrosion to take place around the bottom seams. These seams failed catastrophically.