BOC Gases - Weirton - Executive Summary

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The BOC Gases Weirton facility, owned and operated by The BOC Group, Incorporated is located at 909 4th Street, Weirton, WV. The management and employees of the Weirton facility are committed to the prevention of any accidental releases of hydrogen.  If an accidental release should occur, the facility is prepared to work with the local fire department, or other authorities to mitigate any release and minimize the impact of the release to the community and the environment. 
 
The facilities primary operation is the storage of liquid hydrogen and transmission of  gaseous hydrogen to Weirton Steel for their use.  Liquid Hydrogen is received and stored in a 20,000 gallon tank at very cold temperatures (-420 F).  The hydrogen is then sent to a vaporizer where the liquid hydrogen is changed into a gas and then delivered to Weirton Steel for their use.  
 
The worst-case scenario, based on the EPA's definition for a flammable gas release, would be the rupture of the 20,000 gallon Liquid Hydrogen  
Tank. The results would be a maximum release of 11,800 lbs of  hydrogen over a 10 minute period. 
 
The endpoint of  1 psi overpressurization from a Vapor Cloud Explosion was determined to be 0.245 miles using the RMP*Comp. (1.06) software. The weather conditions used were a wind speed of 1.5 meters/sec., Stability Class F, an air temperature of 77 degrees F and urban topographical terrain. 
 
The impacted area would affect 175 residents and several special receptors; St Peters AME Church and a Day Care center, based on the 1990 US Census data obtained from "Land View III".  One industry ( Weirton  Steel) is also within the endpoint.  No passive/active mitigation or administrative controls were considered in this assessment. 
 
The alternative release, or more probable, scenario which was determined involved the rupturing of the  fill hose during filling of the tank from a road trailer. This release would result in the 10 second release of  55 lb. of liquid hydrogen prior to the activation o 
f the emergency shut-off valve. The Emergency Shut-off Valve would shut-off the liquid pump when activated by the driver, resulting in termination of the release. 
 
The release endpoint of  the Lower Flammable Limit was determined to be 0.03 miles using the RMP*Comp. (1.06) software. The Weather conditions used were a wind speed of 3.0 meters/sec., Stability Class D, and air temperature of 77 degrees F and urban topographical terrain. 
 
The affected area would include one resident with 4 individuals but no several public receptors. One business, Werirton Steel is also affected.  
 
Passive and Active Mitigation systems in place that would reduce the likelihood of a release or the release itself. These include check valves in the fill lines, and Emergency Shut-off Valves on the Delivery vehicle and tank,  a preventive maintenance schedule for the system, and safeties. 
 
The facility has developed a comprehensive prevention program designed to prevent accidental releases of hydrogen.  The pro 
gram utilizes state-of-the-art technology, sound engineering practices, administrative controls and active employee participation.  Employees serve on task groups and teams in developing and maintaining risk management program elements.  They are frequently consulted concerning the various aspects of the program and ways to continually improve the safety of the process.   
Written process safety information was developed for the hydrogen system to enable managers, supervisors, and employees to identify and understand the process hazards.  This information was utilized to develop a Process Hazard Analysis (PHA) which assists management and employees in making decisions for improving safety and reducing the consequences of releases of hydrogen. The PHA focuses attention on equipment, instrumentation, utilities, human actions, (routine and nonroutine), and external factors that might impact the process by identifying potential failure points or failure modes in the process. The PHA was rev 
iew and updated on August  1995 and will be updated at least every 5 years.  
 
Detailed 0perating procedures exist which describe tasks to be performed, dates to be recorded, operating conditions to be maintained, samples to be collected, and safety and health precautions to be taken.  The procedures were reviewed/approved to ensure they are technically accurate by employees, managers and personnel with the technical expertise/knowledge of the process.  The operating procedures were review on November 5, 1998 and are annually reviewed/revised as necessary to reflect current operations. 
 
Employees are thoroughly trained, including maintenance and contractor employees.  The training meets and exceeds the requirements as outlined in OSHA's hazard communication standard 29 CFR 1910.1200.  Training includes operating procedures, safe work practices, emergency procedures (including alarms), special assignments, evacuation and emergency response; safety rules and procedures; routine and nonrou 
tine work authorization; and other pertinent process safety information.  Each employee trained has a defined and documented program based on their job duties.  The training goals and objectives have been established and written in clear and measurable terms.  Hands-on training is provided to employees to enhance their senses beyond listening.  In addition, employees receive traditional classroom instruction including lectures, videos, programmed and on-the-job instruction.  Employees are encouraged to actively participate.  The employees  are periodically evaluated to ensure they posses the necessary skills and knowledge via written tests, observation and/or oral interviews. The training program was last reviewed on November 1998. 
 
A contractor screening process has been established and is designed to ensure that contractors hired or used can accomplish their assigned tasks without compromising the safety and health of employees and the public.   The screening program involves obtaini 
ng information on the contractor's safety performance, including injury and illness rates, and experience.  In addition, the contractor's safety performance, job skills, knowledge, and certifications (such as pressure vessel welders) are also verified. The contractors safety procedures were last review in November 1998.   
 
PreStart-up Safety Reviews (PSSR) are used for new or modified processes to improve the design and construction of the process from a reliability and quality stand point.  The PSSR recommendations are resolved before final installations are complete. Other items completed prior to initial process startup include piping and instrument diagrams, operating procedures, and ensuring operating personnel are fully trained.  The initial startup and normal operating procedures are fully evaluated as part of the PSSR to assure a safe transfer into the normal operating mode for meeting the process parameters. The last PreStart-up Safety Review was conducted on  . 
 
An on-going m 
echanical integrity program (maintenance) is used to ensure safe process operations. Equipment used to store, process, or handle hydrogen has been designed, constructed, installed, and maintained to minimize releases.  The mechanical integrity program includes the identification and categorization of equipment/instrumentation, inspection/tests and their frequencies, development of maintenance procedures and training of maintenance personnel, criteria for acceptable test results, documentation of test/inspection results, and documentation of manufacturer's recommendations to prevent failure of equipment and instrumentation. This program was review in November 1998. 
 
Hazardous work or nonroutine work is controlled in a consistent manner.  The hazards identified is communicated to those performing the work and to operating personnel whose work could affect the safety of the process.  The BOC Hazardous Work Program describes the steps that a supervisor, contractor representative or other a 
uthorized issuer needs to follow to manage hazardous work.   The program references and coordinates applicable lockout/tagout procedures, line breaking, hot work authorization, elevated work/fall protection, controlling access to covered process areas, and excavation procedures. BOC's Confined Space Entry Program is a separate permitting system designed to manage it's employees/contractors in performing this type of work. This Program was review in November 1998 for both employees and contractors. 
 
 
Management of Change (MOC) procedures have been developed for permanent changes to process chemicals, technology, equipment and facilities.  MOC procedures are designed to ensure that prior to any change occurring, that technically qualified personnel with knowledge and expertise of the chemical process, reviews and approves the proposed changes.  This would include both technical and mechanical changes.  Process changes include all modifications to equipment, procedures, raw materials and 
processing conditions other than "replacement in kind".  A Process Change Authorization is required for all changes.  Management of Change procedures were review in November 1998. 
 
Process incidents which result in or could reasonably have resulted in a release of hydrogen are investigated, including "near misses", within 48 hours of the incident.  The purpose of the incident investigation is to identify the underlying causes of the incident and to implement corrective action to prevent similar incidents and avoid past mistakes.  Process incidents are investigated by a Team which include both management and employees and is multidisciplinary. An incident report is prepared following the investigation which includes the findings, conclusions, and recommendations. The Facility Manager is responsible for ensuring that all report recommendations are completed or resolved by those individuals responsible for follow-up. All resolutions are communicated to all affected employees. 
 
The facili 
ty has an emergency preparedness/response plan.  The plan outlines what actions employees are to take when there is a release of hydrogen.  The plan complies with OSHA standard 29 CFR 1910.38 and has been coordinated with local emergency response agencies.  The facilities Emergency Response plan was review in November 1998 and tested at that time.  
 
The facility receives a compliance audit in accordance with EPA's Risk Management Standard Part 68 at least once every three years.  The audit includes an evaluation of the design and effectiveness of the risk management system and a field inspection of the safety and health conditions, and practices to ensure compliance.  The Team uses an audit tool to document each audit step and ensure an effective audit is conducted.  A Protocol Policy has been developed to ensure that proper follow-up is accomplished. 
 
BOC Gases will make available all information, including any Trade Secret information as it relates to compliance with this regulation. 
 
 
The facility has an Emergency Response Plan which has been integrated with the local community Emergency Response Plan. All employees and contractors are trained in the plan prior to commencement of work.  The Emergency Plan is tested and critiqued twice a year to insure that it is current. Changes are made and reviewed if deficiencies are found. The site does not have trained Emergency Responders at the technician level, however, BOC maintains trained technician level Emergency Responders on 24hr. call through out the US. 
 
Safety improvement is an on-going process at the facility.  Periodic evaluations are performed to assess the maintenance of safe conditions.  There are no additional specific hydrogen safety recommendations for implementation at this time.
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