MONACA, PA —
OSHA Inspection: HORSEHEAD CORPORATION
Accident-driven inspection · Safety discipline
At a glance
On , OSHA opened an accident-driven safety inspection of HORSEHEAD CORPORATION in 300 FRANKFORT ROAD, MONACA, PA 15061 (NAICS 331419). OSHA activity number 314109356.
Where did this inspection happen?
- Establishment
- HORSEHEAD CORPORATION
- Site address
- 300 FRANKFORT ROAD
- City
- MONACA
- State
- PA
- ZIP
- 15061
What kind of inspection was it?
- Inspection type
- Accident-driven (A)
- Scope
- Partial (B)
- Discipline
- Safety
- Advance notice
- Yes
- Union status
- Y
When did the case open and close?
- Opened
- Closing conference
- Case closed
- Last modified
- Data loaded
Establishment context
- NAICS code
- 331419
- SIC code (legacy)
- 3339
- Employees
- 550
- Ownership type
- A
Citations
3 citations on file for this inspection.
5(a)(1)
- Issued
- Abate by
- Penalty
- Initial $7000.00 · Current $7000.00
General-duty citation text
Section 5(a)(1) of the Occupational Safety and Health Act of 1970: The employer did not furnish employment and a place of employment which were free from recognized hazards that were causing or likely to cause death or serious physical harm to employees in that employees were required to work in close proximity to, and within the vent relief area and fireball hazard zone of, explosion-relief vents (or deflagration vents) on a zinc distillation column, creating the potential, in the event of an explosion, for the bricks comprising the vents to burst outward and contact employees, and flames and/or fireballs to exit the vents and engulf employees. (a) Facility, Zinc Refinery Building: Two explosion-relief vents on the third floor, and two explosion-relief vents on the second floor of a zinc distillation column ("B column"), each made of brick, were located such that bursting bricks, vented flames and fireballs, and vented gasses resulting from an explosion in the column would be discharged directly into an area in which employees were required to work. Among other methods, one feasible and acceptable means of abatement is to comply with NFPA 68 ("Standard on Explosion Protection by Deflagration Venting") and NFPA 86 ("Standard for Ovens and Furnaces") with regard to the location of explosion-relief vents (or deflagration vents) relative to the location of personnel. Examples of relevant provisions of NFPA 68 and NFPA 86 include but are not limited to: NFPA 86 Section 5.2.8.1 provides: "Bursting discs or panels, mixer openings, or other parts of the furnace from which flame or hot gases could be discharged shall be located or guarded to prevent injury to personnel." NFPA 86 Section 5.3.5 provides: "Explosion-relief vents shall be located or retained so that personnel are not exposed to injury by operation of the vents." NFPA 68 Section 4.2.1.3 provides: "Deflagration venting shall be arranged to avoid injury to personnel by the vent discharge." NFPA 68 Section 6.6.2 provides: "Property damage and injury to personnel due to material ejection during venting shall be minimized or avoided by locating venting equipment outside of buildings and away from normally occupied areas." Section 6.6.2 also references Section 7.6.4 which explains how to calculate the dimensions of a "fireball hazard zone."
Recent events (2)
- — F (S) $7000.00
- — Z (S) $7000.00
5(a)(1)
- Issued
- Abate by
- Penalty
- Initial $7000.00 · Current $7000.00
General-duty citation text
Section 5(a)(1) of the Occupational Safety and Health Act of 1970: The employer did not furnish employment and a place of employment which were free from recognized hazards that were causing or likely to cause death or serious physical harm to employees in that the explosion-relief vents (or deflagration vents) on a zinc distillation column ("B Column") were not safely designed according to industry standards, creating the potential for a partial or complete failure of the column. (a) Facility, Zinc Refinery Building: Two explosion-relief vents on the third floor, and two explosion-relief vents on the second floor of a zinc distillation column ("B Column"), were not safely designed according to industry standards, creating the potential for a partial or complete failure of the column The design deficiencies included: the design of the vents was not based on calculated value of the vented deflagration pressure no greater than two-thirds of the ultimate strength of the combustion chamber; the brick explosion-relief vents were not sized based on the burning velocity of the gaseous fuel inside the vented enclosure; the opening pressure of the explosion-relief vents was not tested or documented or maintained at the worksite; the explosion vented into an enclosed area rather than an outdoor area that is free and clear of any obstruction; and the design calculation data sheets for the explosion-relief vents, including descriptions of personnel proximity to the vent relief path, were not developed and maintained suitable for review by an authority having jurisdiction. Among other methods, one feasible and acceptable means of abatement is to comply with NFPA 68 ("Standard on Explosion Protection by Deflagration Venting") and NFPA 86 ("Standard for Ovens and Furnaces") with regard tot he safe design and structure of explosion-relief vents (or deflagration vents). Examples of relevant provisions of NFPA 68 and NFPA 86 include but are not limited to: NFPA 68 Section 6.3.1.1 provides "Pstat shall not exceed two-thirds of the ultimate strength for the vented enclosure, provided deformation of the equipment can be tolerated." NFPA 68 Section 6.7.2 provides: "A vent closure shall have low mass to minimize inertia, thereby reducing opening time," and Section 7.3.3.6 provides the particular equation that should have been used to calculate the mass of the vent closure. NFPA 68 Section 7.2.2 provides the equation that should have been used to determine the size of the vents based upon the type of gaseous fuel. NFPA 68 Sections 10.2.1, 10.2.2.2, 10.2.2.2.1, and 10.2.2.2.2 require the designer and/or manufacturer to test and document the value and tolerance of the Pstat of a vent enclosure, and to maintain such documentation. NFPA 68 Section 6.6.1 provides: "The material discharged from an enclosure during the venting of a deflagration shall be directed outside to a safe location." NFPA 68 Section 11.2 provides: "Data sheets, installation details, and design calculations shall be developed and maintained for each vent closure application, suitable for review by an authority having jurisdiction that verifies the vent area is sufficient to prevent deflagration pressure from exceeding the enclosure strength and identifies areas exposed to potential overpressure, event propagation, and fireball effects during venting. Documentation shall include all of the following:... (13) Proximity of personnel to vent relief path...(19) Employee training requirements."
Recent events (2)
- — F (S) $7000.00
- — Z (S) $7000.00
5(a)(1)
- Issued
- Abate by
- Penalty
- Initial $7000.00 · Current $7000.00
General-duty citation text
Section 5(a)(1) of the Occupational Safety and Health Act of 1970: The employer did not furnish employment and a place of employment which were free from recognized hazards that were causing or likely to cause death or serious physical harm to employees in that a consistent heat-up rate was not maintained during a 10-day heat-up of a zinc distillation column which potentially allowed for greater variation in the temperature of the column. (a) Facility, Zinc Refinery Building: A consistent heat-up rate was not consistently maintained during the 10-day heat-up of B Column beginning on June 30, 2010. On multiple occasions temperatures in the column were increased at a higher rate that the company's own target rate of 4 degrees C/hour as set fourth in the company's written heat-up schedule. The results of this inconsistent heat-up rate include, but are not limited to: multiple instances when column temperatures were as much as 60 degrees to 100 degrees C higher than targeted temperatures as set forth in the company's written heat-up schedule; and multiple instances when temperatures in the sump area of the column were more than 100 degrees C lower than targeted temperatures as set forth in the company's written heat-up schedule. Among other methods, one feasible and acceptable means of abatement is: to implement flow gauges or regulators on the currently-used flame-safe heaters, to more accurately determine the amount of gas flow (and, thereby determining the temperature of the heat being produced); to monitor the average temperatures of the six thermocouples currently available on the column during heat up; to install additional thermocouples throughout the column to better monitor temperature distribution; to set standards among operators regarding how much deviation from the target temperature during heat-up is allowable; and to improve burner placement to eliminate direct heating or overheating of refractory trays.
Recent events (2)
- — F (S) $7000.00
- — Z (S) $7000.00
More inspections at HORSEHEAD CORPORATION
PALMERTON, PA—2017-04-04 00:00:00
HORSEHEAD CORPORATION
PALMERTON, PA—2016-06-23 00:00:00
HORSEHEAD CORPORATION
PALMERTON, PA—2016-03-29 00:00:00
HORSEHEAD CORPORATION
CHICAGO, IL—2015-06-15 00:00:00
HORSEHEAD CORPORATION
PALMERTON, PA—2015-05-26 00:00:00
HORSEHEAD CORPORATION
View HORSEHEAD CORPORATION's full OSHA safety record →
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Source
This record is reproduced from the U.S. Department of Labor Open Data API (OSHA inspection dataset). The original IMIS detail view is available at OSHA's Establishment Search for activity number 314109356.