Melton Hill WTP - Executive Summary

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Executive Summary for Hallsdale Powell Utility District 
Melton Hill Water Treatment Plant 
 
1.    Accidental Release Prevention and Emergency Response Policies 
We at Hallsdale Powell Utility District are strongly committed to employee, public and environmental safety.  Our accidental release prevention program that covers areas such as design, installation, operating procedures, maintenance demonstrates this commitment, and employee training associated with the processes at our Melton Hill Water Treatment Plant.  It is our policy to implement appropriate controls to prevent possible releases of regulated substances and to perform onsite response to repair damaged chlorine equipment.  Unforeseeably, if an offsite release does occur, we are coordinated with the Rural Metro Fire Department, which provides highly trained emergency response personnel to respond to a release of chlorine. 
 
 
2.    The Stationary Source and the Regulated Substances Handled 
Chlorine is the only regulated substance pres 
ent at our facility.  Chlorine is used for disinfection purposes in the treatment of potable water.  Chlorine is stored as a liquefied gas under pressure.  The vapor pressure of stored chlorine is 6.8 atmospheres (99.89 psi).  Chlorine gas is non-flammable, but it is a strong oxidizer that can support combustion of other materials.  Chlorine is a toxic gas that is considered by the National Institute of Occupational Safety and Health (NIOSH) to be immediately dangerous to life and health at concentrations exceeding 10 parts per million (ppm). 
 
The maximum inventory of chlorine at our facility is 10,000 lb.  The largest single vessels of chlorine at our facility are 2,000 lb. cylinders.  The chlorine cylinders are equipped with a fusible plug that is designed to fail if the temperature of the cylinder reaches 158 ( F.  The purpose of the fusible plug is to prevent cylinder failure in the event of an extended, hot fire by allowing a controlled release of the cylinder contents.  All of th 
e chlorine cylinders in our facility are located in the chlorine room, which is of fire-resistant construction in accordance with the Chlorine Institute specification for chlorine storage facilities. 
 
3.    The Worst Case Release Scenario and the Alternative Release Scenarios, including administrative controls and mitigation measures to limit the distances for each reported scenario 
The Risk Management Plan Rule requires Program Level 2 and 3 facilities to model the effects of a worst-case and one or more alternative release scenarios to predict the possible outcome of a chemical release from a facility.  These models evaluate the Distance to Toxic Endpoint based on the Emergency Response Planning Guideline 2 (ERPG-2).  These guidelines were developed by the American Industrial Hygiene Association to represent the maximum airborne concentration below which it is believed nearly all individuals could be exposed for up to one hour without experiencing or developing irreversible or other ser 
ious health effects or symptoms that could impair an individual's ability to take protective action.  The ERPG-2 toxic endpoint for chlorine is 0.0087 mg/L.  We performed the required offsite consequence analysis for our facility using the EPA's RMP-Comp Model, which is an electronic version of the look-up tables and equations provided by the EPA in the RMP Offsite Consequence Analysis Guidance. The release scenario modeling was performed using the EPA RMP-Comp computer program.  This program calculates the distance to the toxic endpoint for chlorine depending upon the effects of variable factors.  The wind speed and air stability class, presence of partial enclosures and general topographic types are all factors that affect the model calculations.  The type of release and release rates are also evaluated by the model. 
 
Because the chlorine storage area/chlorination process equipment is located in a semi-enclosed area the RMP-Comp model modified the release rate to 55 percent of the re 
lease rate entered into the model.  This takes into account the passive mitigation provided by the presence of the structure.  As an example, a 10-minute release of 2,000 lbs. of chlorine (i.e., a linear rate of 200 lbs. per minute) would be modeled as a 10-minute release at a rate of 110 lbs. per minute. 
 
The population estimate data is produced using 1990 United States Census Bureau data in conjunction with a geographic information system (GIS) computer program.  This data is designed to provide a general information about the population in a given area, but the data is provided by geographic block groups and the local accuracy of the data can be variable.  
 
The public and environmental receptor data represents a combination of United States Census Bureau data, information obtained from United States Geological Survey 7.5 minute topographic quadrangle maps and field observations. 
 
The following paragraphs provide details of the chosen scenarios. 
 
Worst-Case Release Scenario 
 
The wors 
t-case release scenario was estimated to involve the total release of one 2000 lb. cylinder of chlorine.  This is consistent with the regulation definition of a worst-case scenario as the release of the greatest quantity contained in the single largest vessel.  The use of check valves and other release prevention mitigative measures can not be considered for the worst case scenario.  The entire contents of the vessels were assumed to be released as a gas over a 10-minute period.  This type of catastrophe is extremely unlikely and would possibly require the complete failure of the cylinder to occur.  A simple puncture, valve failure or line failure would not be likely to result in a ten-minute release of the contents from the cylinder.  The EPA's RMP-Comp model was used assuming a "Rural" topography setting due to a flat, open topography on and near the plant site (note - the RMP-Comp model uses a "rural" setting for flat, open topography and an "urban" setting for areas with many build 
ings, trees or rough and broken topography.  In spite of the setting names, neither of these settings was designed to account for demographic variations).  The wind speed was assumed to be 3.4 miles/hour with a stability class of "F", according to EPA guidelines.  This stability class assumes the least amount of potential for air mixing due to turbulence or other factors.  The model determined the distance to the toxic endpoint to be 2.2 miles.  The population within this area is approximately 5,100 people, according to the 1990 census data.  The public receptors identified within the radial distance to the worst case endpoint included schools, residences, and churches.  No environmental receptors were identified within the 2.2 mile distance to toxic endpoint.   
 
Alternative-Case Release Scenarios 
 
Two alternative-case scenarios were modeled to represent circumstances that were estimated to be more likely to occur at the facility.  One alternative-case release scenario was estimated to 
involve the release of chlorine from a broken 3/4-inch valve-fitting over a ten-minute period (i.e., 787 pounds/minute).  This scenario assumed that the release detection system/automatic shutoffs malfunctioned and the cylinders had to be closed manually by facility personnel.  In this scenario 2,000 lbs. of chlorine was assumed to be released as a gas over a ten-minute period.  As with the worst-case scenario, the EPA's RMP-Comp model was used assuming a "Rural" topography setting.  The wind speed was assumed to be 6.7 miles/hour with a stability class of "D", according to EPA guidelines.  This stability class assumes a slight to moderate potential for air mixing due to turbulence or other factors. The model determined the distance to the toxic endpoint (i.e., 0.0087 mg/L based on ERPG-2) to be 0.8 mile.  The population within this area is approximately 550 people, according to the 1990 census data.  The public receptors identified within the 0.8 mile radial distance to the toxic end 
point included schools, residences, and churches.  No environmental receptors were identified. 
 
The second alternative-case release scenario was estimated to involve the total release of 120 lbs./minute of chlorine from a broken 1/4-inch feed line.  This scenario assumed that the release detection system/automatic shutoffs malfunctioned and the cylinders had to be closed manually by facility personnel.  In this scenario 1,200 lbs. of chlorine was assumed to be released as a gas over a ten-minute period.  As with the worst-case scenario, the EPA's RMP-Comp model was used assuming an "Rural" topography setting.  The wind speed was assumed to be 6.7 miles/hour with a stability class of "D".  The model determined the distance to the toxic endpoint (i.e., 0.0087 mg/L based on ERPG-2) to be 0.4 mile.  The population within this area is approximately 430 people, according to the 1990 census data.  The public receptors were identified within the radial distance to the worst case endpoint inclu 
ded schools, residences, and churches.  No environmental receptors were noted. 
 
 
4.    The General Accidental Release Prevention Program and the Chemical-Specific Prevention Steps 
Our facility has taken all the necessary steps to comply with the accidental release prevention requirement set out under 40 CFR part 68 (EPA) and the process safety management requirements under 29 CFR part 1910.119 (OSHA).    The following sections briefly describe the elements of the release prevention/process safety management programs relating to the Risk Management Plan Rule that are in place at our water treatment facility. 
 
Process Safety Information 
The staff of the water treatment facility maintains a detailed record of safety information that describes the chemical hazards, operating parameters and equipment designs associated with all processes. 
 
Process Hazard Analysis 
Our water treatment facility personnel conduct studies to ensure that hazards associated with our processes are identified and contr 
olled efficiently.  The methodology used to carry out these analyses is through the use of checklists.  The studies are undertaken by qualified personnel with expertise in engineering and process operations and will be revalidated at a regular intervals and whenever a major change is made to the covered process.  Any findings related to the hazard analysis will be addressed in a timely manner. 
 
Operating Procedures 
For the purposes of safely conducting activities within our covered processes, the water treatment facility maintains written operating procedures.  These procedures address various modes of operation such as initial startup, normal operations, temporary operations, emergency shutdown, emergency operations, normal shutdown and startup after a shutdown.  The information is regularly reviewed and is readily accessible to operators involved in the processes. 
 
Training 
The water treatment facility has a comprehensive training program in place to ensure that employees who are ope 
rating processes are competent in the operating procedures associated with these processes.  Refresher training is provided periodically. 
 
Mechanical Integrity 
The water treatment facility carries out documented maintenance checks on process equipment to ensure proper operations.  Process equipment examined by these checks includes among others; piping systems, ventilation systems, emergency shutdown systems, and controls.  Maintenance operations are carried out by qualified personnel with previous training in maintenance practices. Any equipment deficiencies identified by the maintenance checks are corrected in a safe and timely manner. 
 
Management of Change 
Written procedures are in place at the water treatment facility to manage changes in process chemicals, technology, equipment and procedures.  Process operators, maintenance personnel or any other employee whose job tasks are affected by a modification in process conditions are promptly made aware of and offered training to deal w 
ith the modification. 
 
Pre-startup Reviews 
Pre-start up safety reviews related to new processes and to modifications in established processes are conducted as a regular practice at the water treatment facility.  These reviews are conducted to confirm that construction, equipment, operating and maintenance procedures are suitable for safe startup prior to placing equipment into operation. 
 
Compliance Audits 
The water treatment facility personnel will undertake to conduct audits on a regular basis to determine whether the provisions set out under the RMP rule are being implemented.  These audits will be carried out at least every 3 years and any corrective actions required as a result of the audits will be undertaken in a safe and prompt manner. 
 
Incident Investigation 
The water treatment facility will promptly investigate any incident that results in, or could reasonably result in a catastrophic release of a regulated substance.  These investigations will be undertaken to identify the s 
ituation leading to the incident as well as any corrective actions to prevent the release from reoccurring.  All reports will be retained for a minimum of 5 years. 
 
Employee Participation 
Hallsdale Powell Utility District truly believes that process safety management and accident prevention is a team effort.  Water treatment facility employees are strongly encouraged to express their views concerning accident prevention issues and to recommend improvements.  In addition, our employees have access to all information created as part of the facility's implementation of the RMP rule, including information resulting from process hazard analyses in particular. 
 
Contractors 
On occasion, our company hires contractors to conduct specialized maintenance and construction activities.  Prior to selecting a contractor, an evaluation of safety performance of the contractor is carried out.  Hallsdale Powell Utility District has a policy of informing the contractors of known potential hazards related t 
he contractor's work and the processes.  Contractors are also informed of all the procedures for emergency response should an accidental release of a regulated substance occur. 
 
5.    Five-year Accident History 
The water treatment facility has had an excellent record of preventing accidental releases over the last 5 years. There have been no accidental releases during this period. 
 
6.    Emergency Response Plan 
The water treatment facility carries a written emergency response plan to deal with accidental releases of hazardous materials.  The plan includes all aspects of emergency response including adequate first aid and medical treatment, evacuations, notification of local emergency response agencies and the public, as well as post-incident decontamination of affected areas. 
 
To ensure proper functioning, our emergency response equipment is regularly inspected and serviced.  In addition, the plan is promptly updated to reflect any pertinent changes taking place within our processes that wou 
ld require a modified emergency response. 
 
7.    Planned Changes to Improve Safety 
Several developments and findings have resulted from the implementation of the various elements of our accidental release prevention program.  Future safety improvements include employee training, public education, and coordination with emergency responders. 
 
8.    Certification Statement 
The undersigned certifies that to the best of my knowledge, information, and belief, formed after reasonable inquiry, the information submitted is true, accurate and complete. 
 
Name: 
Signature: 
Title: 
Date signed: 
 
P:\2222-001\Hallsdale Powell WTP\Hallsdale Powell RMP execsum.doc
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