![]() |
|
PROJECT DESCRIPTION
The Soil Vapor Extraction System facility is designed to
extract soil vapor from the vent field through low and high vacuum systems.
Vapor will be transported by the manifold pipeline collection system to the
treatment plant. The extracted vapor will be drawn through a filter with a
blower, cooled, and treated/filtered through a granulated activated carbon bed.
Treated air will be discharged through the 50-foot stack or reinjected into the
well field. The project lifetime is expected to be 8.5 years. The Soil Vapor Extraction System consists of four primary
elements: The vent field consists of clusters of soil vents (vertically
installed perforated pipes) placed underground into the 10 acres of contaminated
soils. Each vent cluster includes three to six vents. Soil vents are connected
to a common set of collection pipelines (manifolds) which are also placed
underground. Collection pipelines carry the vapors to the soil vapor treatment
plant. The soil vapor treatment plant receiSoil Vapor Extraction
System the soil vapor collected by the soil vent system. The soil vapor then
passes through filters and extraction blowers, and through a common heat
exchanger to cool flows. It is then filtered through a granulated activated
carbon adsorption system to remove almost all of the VOCs. The treated air
(effluent) is measured for VOCs, if the concentration level exceeds 9.8 lbs per
day, it is recycled through the blower and granulated activated carbon
adsorption system; otherwise it is introduced back into the soil or discharged
through a 50-foot exhaust stack. Lockheed Martin will reinject between 50-70 per cent of
treated soil vapor. Based on three-dimensional vapor transport modeling and the
physical properties of the subsurface soil at the Plant B-1 site, 100 percent
reinjection cannot be achieved. The air reinjection system consists of blowers
at the treatment plant, a main injection line leading to the vent field, and an
automated valve to control the injection into each branch of the vent field
being used for reinjection. The capacity of the injection system is designed to
be 4,200 cubic feet per minute (cfm), or 70 percent of the capacity of the Soil
Vapor Extraction System. The injection system is capable of drawing air from
either the effluent side of the treatment unit or from the atmosphere; however,
in steady operations, any reinjection air shall be treated soil vapor. Lockheed
Martin plans to operate the reinjection system at a maximum feasible level. Air is processed by the treatment plant at a rate between 2,000 and 6,000
standard cubic feet per minute (SCFM) for removal of volatile organic compounds
(VOCs). The two independent Soil Vapor Extraction Systems designated as low
vacuum and high vacuum will have capacities of 3,600 and 2,400 SCFM
respectively. When an activated carbon bed is saturated with VOCs, it shall be
automatically taken off line with effluent immediately routed to the second
activated carbon bed. The activated carbon bed can also be manually taken off
line for routine maintenance.
The amount of VOC vapors emitted is minimized by controlling flow quantities,
shortening GAC adsorption times to two hours per day between regeneration cycles
(for at least the first six months of operation), diverting effluent flow
through a carbon polishing unit if mass concentration of stack discharge flow is
too high, and by re-injecting 50 to 70 percent of the gas stream back to the
well field.
Processed air is monitored for VOCs before exiting the plant. If total VOCs
exceed set point levels, the effluent air is automatically routed through a GAC
polishing unit. If effluent still approaches permit limits, vent field
extraction rates are automatically reduced. If effluent levels continue to
approach exceedence of permit limits with both of the above controls in place,
the plant is automatically shut down. At any of these points, the logic
controllers are automatically warning the operator and the City of Burbank.
The saturated activated carbon bed is regenerated by heating and stripping
with 15 psig steam. VOC-laden steam is condensed to two-phase liquid condensate
which is separated into a heavy liquid VOC layer (approximately 1.5 specific
gravity) and a lighter water phase. The VOC liquid is stored in a tank
temporarily, then it is transported off site. The VOC-saturated water is
processed on site through an air stripper. Off gas is routed through the vapor
phase filter. Water is passed through an activated carbon polishing beds to a
water neutralization unit where pH is adjusted to between 6.5 and 8. The water
is subsequently analyzed for VOCs and is discharged to the sewer if within
specifications. Water not meeting discharge specifications is stored temporarily
then transported off site.
A startup period of 90 days is required to bring the system on line. The
components of the system are started, tested, adjusted, and tuned by the
contractor and manufacturers to achieve maximum operational efficiency. Full
emissions monitoring occurs during the startup period to ensure emission
accedences are avoided. Any accedences associated with testing and adjusting
equipment are corrected, documented, and reported.
Processed wastewater to be discharged to the sewer include: 2,200 gallons/day
of process wastewater from the air stripper; 250 gallons/day boiler blowdown
water; 5,000 gallons/day of cooling tower blowdown; 10 gallons/day washdown
water from building drains; and 40 gallons/day of domestic wastewater. Reclaimed
PCE and TCE solvents produced are stored for removal by a licensed waste hauler
or recycler.
The Soil Vapor Extraction System is controlled and monitored by programmable
logic controllers. The controllers monitor and record data and manage automated
system shut downs in cases of component malfunctions or emission accedences. The
controllers monitor the Soil Vapor Extraction System through temperature,
pressure and/or flow sensors throughout the treatment plant. The controllers
automatically alter the facility configuration and throughput assuring that the
9.8 pounds per day maximum VOC limit is not exceeded. The carbon cycle time is
closely monitored and adjusted (during startup and when major changes are made
in the plant feed stream) to maintain the emissions rate of less than 9.8 pounds
per day maximum. If the daily emission rate approaches the established limit,
the polishing unit is automatically placed on line. If the effluent again
approaches the set point, the field extraction rate is reduced. If the
established limit is then reached, the facility is automatically shut down.
These automatic changes are recorded for system analysis and adjustment. The
operations monitoring system has an alarm system located at a City facility with
personnel on duty 24 hours per day. The alarm notifies City personnel if
emissions exceed 9.8 pounds per day of VOC. A second signal (supplied by
Lockheed Martin) indicates a facility shut down. Lockheed Martin provides
personnel on standby duty 24 hours per day to ensure manual shut down of the
plant within one hour of a breakthrough in the event that the automatic shut
down feature fails. Alarm and shutdown occurrences are documented (including
reason for alarm or shutdown) and maintained as a public record.
An emergency response plan is submitted to the City which specifies
deployment of emergency-response agencies in the event of a spill at the site or
in transport. The plan must be reviewed and approved by the Fire Chief prior to
project commencement.
Containment berms are constructed around the storage tanks to the
satisfaction of the Fire Chief.
Lockheed Martin will send the Independent Monitor bi-weekly written reports
indicating VOC emissions for each day that month. The Independent Monitor will
compare the Lockheed Martin data with its own independent monthly sample and
send a bi-weekly written report to the City which states whether or not the
system that month has operated within the limit of 9.8 pounds of VOCs per day.
During the first three months of operation, the Independent Monitor will
sample emissions once per week for the four contaminants (perchloroethylene,
trichloroethylene, vinyl chloride, and carbon tetrachloride). The Independent
Monitor will use these samples to perform two health risk assessments (HRAs).
Air samples will be taken according to a
schedule.
Using these samples, the Independent Monitor will perform the two HRAs to
determine whether the one per million risk threshold has been exceeded. For the
purpose of this requirement, these HRAs will be a spreadsheet calculation that
computes risks for monitored chemicals. This information will be included in the
Independent Monitor's bi-weekly report to the City.
In the event that the excess cancer risk calculated by the project life HRA
exceeds one in one million based on the analysis of any one monthly or quarterly
sample, the sampling frequency will be increased to at least one sample per week
for at least one month. The monthly average emission rate of the four
contaminants will be calculated from four consecutive weekly samples, one of
which will be the sample which triggered the increase in sampling frequency.
A 70-year HRA (in accordance with SCAQMD Rule 1401) will be conducted for
informational purposes.
When the monthly average emission rate results in a calculated risk over the
project life in excess of one per million, plant operations will be adjusted to
ensure that the monthly average emission rate for the next month is far enough
below the threshold to entirely compensate for the accedence in the prior month.
The monthly written report from the Independent Monitor will state whether or
not these adjustments, if needed, have achieved this requirement.
If the operational adjustments cause the expected project life to be
extended, the health risk assessments will use the extended project life rather
than the 8.5 years currently expected.
If the vinyl chloride limit of 0.14 pounds per day is exceeded in any month,
the emissions in the future months must be reduced so that the monthly average
for a three- month period which includes the month of violation meets the
emission limit.
The Independent Monitor will ensure that proper measures are incorporated
into the monitoring process. If the reports from the Independent Monitor
indicate a consistent pattern of failure to achieve these projects requirements,
the City will take appropriate enforcement action based on violations of
conditions of approval of the CUP.
The applicant can modify operational conditions and parameters so long as the
Independent Monitor's monitoring operations indicate compliance with target risk
calculations and emissions limits for daily VOCs and vinyl chloride.
|