West Side Wastewater Treatment Plant - Executive Summary
Executive Summary |
Watts Engineers was subcontracted by Pratt and Huth Associates, LLP to provide the
City of Oswego a Level 3 Risk Management Program (RMP) and a Process Safety Management
(PSM) Program in accordance with 40 CFR 68 Risk Management Programs for Chemical
Accidental Release Prevention and 29 CFR 1910.119 Process Safety Management for it's West
Side Wastewater Treatment Plant (WWTP) located at First Avenue and West Schuyler Streets in
the City of Oswego, New York. This evaluation was performed to assure that the facilities
chlorine injection system complies with applicable regulations. Key elements of the Risk
Management Plan provided by Watts Engineers included: a review of the accidental release
prevention and emergency response policies; a review of the regulated substance handled; a
worst-case and an alternative release scenario; a review of the general accidental release
prevention program and chemical-specific prevention steps; a re
view of the five-year accident
history; a review the emergency response program; and participation in meetings and planning
changes to improve the Process Safety Program. Watts Engineers will electronically submit this
Risk Management Plan to the Environmental Protection Agency (EPA) by June 21, 1999.
The Oswego West Side WWTP is located on the West Side of the City of Oswego
between the Niagara Mohawk Power Station and the old oil refinery. It employs twenty (20)
full-time employees. Activities at the facility include the treatment of sewage, removal of solid
waste, and the treatment of the water portion with the addition of chlorine gas before returning
the water to Lake Ontario.
Chlorine is considered a regulated substance under the Risk Management and Process
Safety Programs. Characteristics of this gas or liquid include a pungent suffocating odor. It is
irritating to the mucous membranes. When chlorine reacts with water, it forms hydrochloric
oric acid gas is a toxic and corrosive fume. The odor threshold for chlorine is
about 0.5 ppm. Long term exposures to small concentrations or short term exposures to high
concentrations may result in adverse health effects. Since chlorine gas is heavier then air, It can
settle in low spots along the ground, therefore, care should be exercised while working in
confined spaces or low lying areas.
The City of Oswego and senior management at the West Side Wastewater Treatment
Plant have a strong commitment to the overall safety of it's employees, the public, and
the environment. It is the policy of the West Side WWTP to train each employee and contractor
about safety considerations and emergency procedures in the unlikely event of a discharge. A
maximum of four thousand (4,000) pounds of chlorine gas in two (2) tanks gas are either used or
stored at one time at the facility. Each tank contains two thousand (2,000) pounds of chlorine
gas. The chlorine is composed of 99.5 perc
ent chlorine and 0.5 percent inert ingredients. The
tanks are located on a storage pad behind the facility. The storage pad is covered by a canopy
constructed of sheets of corrugated steel used for a roof. The storage area is otherwise open to
air. Chlorine is being delivered by truck and unloaded using a two ton crane onto a set of steel
rails where the gas tank is stored until it is ready for use. Each end of the rails are chocked to
prevent the gas tanks from rolling. Each gas tank has it's own valve guard to prevent objects
from coming in contact with the valves.
When a chlorine tank is needed, a two ton crane lifts the cylinder and is moved along a
crane rail through a set of double steel doors and into the tank scale room. The tank scale room
is fully enclosed. The room is labeled "chlorine hazard" and emergency instructions are posted
at the door. Material Safety Data Sheets (MSDS) are located in a common hallway by the
Next to the ta
nk scale room is the chlorine injection room. PVC tubing leads
from the tanks, through the wall, and into the chlorine injection room. Here, the chlorine is
injected into the wastewater through a series of valves and PVC tubes.
The chlorine tanks are stored on to a calibrated scale, designed to hold the two, two
thousand pound tanks on roller trunnions. The chlorine containers have two valves in each head,
With the tank in a horizontal position and the valves in a vertical line, they deliver gas from the
upper valve and liquid from the lower valve. Five hundred (500) psig copper tubing fitted with a
special adapter is used to connect the tank to the tubing system. To connect the line to the
container, a valve protection hood and the valve outlet cap are removed. A wrench is used to
connect the valving to the yoke. A new gasket, which is supplied with the container is used each
time a connection is made. As part of the Process Safety Management Program leaks are then
ked using ammonia vapor. The appearance of white vapor indicates a chlorine leak. Gloves
and a self-contained breathing apparatus (SCBA) are worn by the operator while changing tanks.
In the past five years, this facility has had no accidental releases of chlorine.
The City of Oswego West Side Wastewater Treatment plant maintains a general
accidental release prevention program and chemical specific prevention steps. As a part of this
program, a chlorine alarm system is in place at the facility. The chlorine detector and alarm are
located on the wall outside of the chlorine injection room. The chlorine sensors are located in the
injection room and the tank scale room. In the event of a chlorine leak, a audio and visual alarm
will sound in the operator's control room which is staffed twenty four (24) hours a day, seven
days a week. The monitor is maintained and calibrated by an outside contractor. The calibration
frequency is yearly as recommended by the manufacturer. Lite
rature and information on the
alarm system is kept on file by the superintendent of the facility. All employees are trained
yearly on the chlorine alarm system. An operator receiving an alarm is to follow the Emergency
The chlorine injection system itself operates under a vacuum produced by the injector
mechanism. Gas leaves the tank through a vacuum regulating valve. A diaphragm senses
vacuum on one side and atmospheric pressure on the other. A spring loaded stem off the seat is
displaced by force on the diaphragm. Gas moves toward the flow control components and proper
vacuum is maintained. While under vacuum, gas enters the rotameter where it's flow is
measured. Gas flow rate is controlled by a v-notch orifice and either manual or automatic
positioning of the v-grooved plug in it's ring. A differential regulating valve is located after the
orifice which maintains the proper vacuum across the v-notch. A pressure-relief valve vents to
the atmosphere if a
malfunction occurs and pressure builds. Gas is then dissolved in the water
stream at the injector. Check valves are in place and designed to close on injector shutdown.
There are no lines carrying gas under pressure in this system. Loss of vacuum for any reason
causes the vacuum regulating valve to shut off the gas supply.
The facility also complies with the Occupational Safety and Health Process Safety
Management rule. Management believes that the training of it's employees and it's contractors is
crucial to maintaining a safe environment and continuing it's accident-free record for the chlorine
system. Training of all employees consists of a general orientation of the chlorine system first.
They are then instructed on the hazards and proper and safe handling of the chlorine system. The
following courses are administered to all employees and refreshed yearly:
General Safety Training
DEC Wastewater Operator Renewal Training
Hazard Communication Training
Confined Space Training
Respiratory Protection Program Training
Chlorine Tank Handling and Connections
Hearing Protection Program
Personal Protective Equipment Program
A record is kept of the training and placed in the training files. The record contains the
employee or contractor name, title of course, date the course was held, name of the trainer,
and results of any written, oral, or hands-on exam.
Accidents are also prevented by good administrative controls. Standard Operating
Procedures (SOPs) are kept on hand and are easily accessible to the workers. Each operator is
trained in the applicable aspects of their job functions. Those operators whose work is involved
with any aspect of the chlorine injection system are thoroughly trained in those specific SOPs.
Workers who need to be inside the chlorine tank scale room or the chlorine injection room are
provided chlorine specific training.
of Oswego West Side Wastewater Treatment Plant maintains an Emergency
Management Program. In the event of a chlorine leak, the operator will first notify the other
employees by sounding a general alarm and then determine the location and magnitude of the
leak. The magnitude is broken down to minor leaks; no yellowish gas is visibly present, and
major leak; yellowish gas is visibly present. For a minor leak, two trained operators will don
SCBAs and protective gear and using the ammonia and water vapor bottle, find where the leak is
and rectify the situation. In the event of a major leak, the operator will call the Oswego Fire
department immediately and then notify the other workers in the plant of the major chlorine leak.
The operator will designate one location that is upwind from the chlorine leak for all personnel to
assemble and remain until the fire department informs the operator otherwise. The
superintendent will then be called and informed of the situation. The Oswego F
will be in charge of the scene until they depart. The approximate response time is less than five
Each member of the fire department is trained to at least HazMat Level I. Two
members are trained to the Technician Level, and eleven members are trained to the Specialist
Level. The fire department has toured the plant to become familiar with what is on site, and
develop different leak scenarios and practice emergency response measures. In June of 1996, a
HazMat drill with the Fulton Fire Department Haz-Mat Team was conducted. The Haz-Mat
Team was activated. The scenario staged was that a tank while being changed, started leaking.
A full decon was set up. The entry personnel used the chlorine kit to stop the tank from leaking.
A full critique was conducted, and everyone at the scene reviewed the site. On March 18, 1997,
seven members of the Haz-Mat Team conducted a drill at the treatment plant. This scenario was
a leak in the feed line. The crew
followed SOPs to fix the problem. In August and September
1997, all four fire department shifts conducted a mock drill of a worker overcome by chlorine
while in a confined space. Monitoring equipment, rigging, and harnesses were used in the entry.
The fire department also has a chlorine tank simulator that they practice using an "A" and a "B"
chlorine tank repair kit on.
In the attached Risk Management Plan, toxic worst case and toxic alternative release
scenarios were examined. The scenarios were developed based on a two-thousand pound tank
filled with 99.5 percent chlorine. The quantity released was the full two thousand pounds at a
release rate of two hundred pounds per minute for ten minutes. The meteorological factors were
an atmospheric stability class of "F" and a wind speed of 1.5 meters per second. The topography
is urban. The release is assumed to be at ground level. The toxic endpoint is 0.0087mg/L
(3ppm). These airborne concentrations are the maximum airb
orne concentrations that most
people can be exposed to for up to one hour without experiencing serious or irreversible effects
or symptoms. The calculated distance to endpoint is 1.3 miles.
The alternate release scenario for the chlorine injection system is one that is more likely
to occur than the worst case scenario that reaches an end point off-site. A chlorine leak caused
by piping or valve failure is used in the alternative scenario. A hole diameter of 1/4 inch on the
piping or valve could theoretically occur. The release rate for this scenario is 9 pounds per
minute for 222.2 minutes. The meteorological conditions were atmospheric stability class of "D"
and a wind speed of 3.0 meters per second. The topography is urban. Again the toxic endpoint
is 0.0087 mg/L (3 ppm). The calculated distance to endpoint for the alternative scenario is 0.10
miles. Methodology for determining distance to endpoints was done by referencing Risk
Management Program Guidance for Wastewa
ter Treatment Plants (40 CFR Part 68).
The chemical of concern at the West Side Wastewater Treatment Plant is chlorine.
Chlorine can be toxic if not handled properly, however, the City of Oswego has a reasonable
program in place to minimize the potential risks to a chlorine gas release. A training program
combined with required recordkeeping, administrative controls, an effective emergency
management program, a local HazMat team, and an alarm system all address and meet the needs
of the applicable regulations as defined under 40 CFR 68 and 29 CFR 1910.119. The West Side
Wastewater Treatment Plant is currently evaluating improvements to their safety program. They
are investigating expanding the area that the chlorine sensors monitor along with visual, as well
as audio alarms. They are also taking this opportunity to improve and expand their training
programs, to make their employees further aware of the continued necessity for the safe use of