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Hilliard Emission Controls, Inc. 888-621-3132 hank.hilliard@purgit.com |
Discussion of mobile equipment used for tank
vapor
control.
The object of vapor control is to reduce the volatile organic compounds
(VOC)
emitted during tank cleaning. Any improvement beyond that is a benefit.
PURGIT's
improvement is that we condense and our benefit is recovery. We are
proponents of using refrigeration and
condensers for controlling VOC from tank degassing. Our condensers
change tank vapors back
to liquid
suitable for recycling. When we condense and recover 1 pound of VOC, we
haven't just recovered 1 pound of VOC, we stopped 1 pound of greenhouse
gases from going into the atmosphere. The fact is that we recovered
over 85 tons of VOC condensate in
just 18
months. We are proud of our development of the mobile condenser system.
This paper shows how our proprietary refrigeration system is
different
from combustion systems.
States regulate the release of VOC vapors from sources like tank
cleaning. The
tanks could be barges, ships, rail cars, tank trucks, floating and
fixed roof
tanks, pipelines, etc. Tank farms require mobile equipment because of
the
remote tank locations. Shipyards may call for specialized control
equipment
from time to time for unusual cargoes. Many facilities use contractors
for
vapor control. PURGIT is a contractor that does vapor control with
mobile
equipment in
The following
is my
understanding of how the flow rates for these devices should be
calculated and
general information about devices used for tank vapor control. First
the
advantages of the refrigeration system followed by combustors, engines,
etc. The flow rate is very important because low flow rate contributes
to channeling in the tank vapors. That results in the heavy tank vapor
not coming out of the tank. Therefore the tank is not degassed.
The PURGIT Refrigerated Vapor Condenser
System has these important advantages.
* Liquid nitrogen is used for the refrigerant. Nitrogen is not a
pollutant and
it is not flammable.
* Refrigerated systems can handle concentrated vapors and can ramp up
quickly.
The condensers perform very well with rich input vapor.
* They do not
have
hot surfaces.
* It actually processes the rated flow. That means a 650 cfm unit will
process
650 cfm from the storage tank from minute #1 to the completion.
* PURGIT
uses a turbine flow meter to accurately measure flow and volume, not
pitot
tubes. The flow meter register is proof of flow.
* Temperature indicators send signals to control valves which adjust
the
temperature of the coils to as low as -200oF. We set the temperature to
match
the cargo.
* Condensers do not make NOx or CO or other pollutant. They do not have
exhaust
stacks.
* The diesel engine on the blower can be replaced with an
electric motor
for additional emission reduction.
* Credits may be available for the NOx
reduction.
* Detonation arresters protect the storage tank.
* The Hilliard Closed Loop configuration can add nitrogen gas to
prevent an
explosive mixture forming inside the storage tank by drawing in air.
* When degassing a storage tank, the tank vapors can be re-circulated.
In that
configuration, no emissions are emitted until the tank vapor space
meets the
rules for open venting. Even if the refrigeration system fails, vapors
are
circulated in the closed loop until the condition is fixed. There are
no
emissions.
* It recovers cargo, it does not destroy it. The recovered cargo can be
recycled. Humidity already in the tank is the only possible
contaminant. It
handles chlorinated solvents without scrubbing and returns the
condensate
liquid for recycling as cargo.
* An empty 150' dia. tank with a floating roof at 6' has 106,000 cu/ft
volume.
At 650 cfm a PURGIT dual condenser will take 11 hours for 4 volumes.
* An empty 40' dia. tank with a floating roof at 7' has 8,800
cu/ft
volume. At 650 cfm a PURGIT dual condenser will take 1 hour for 4
volumes. Set
up and knockdown not included (add 2 hours or so).
* Tanks can be degassed without opening. With the refrigerated
condenser unit,
the cargo tank does not open for additional work or venting until the
vapor
space meets the owners or regulatory specification.
Enclosed Mini Combustors:
Mini combustors are simply enclosed flares. The contractors who use
these
mini-combustor units claim they are rated at 1,000 cfm or more.
But a
mini-combustor can only handle 1,000 cfm with a very lean input
concentration
of tank vapor. The volume of the fire box in the mini-combustors limits
their
capacity. The industry standard nominal heat load rating in a
combustor
firebox is 500 btu per cubic foot per
minute. So if
the mini-combustor firebox is 4ft x 4ft x 6ft, then the capacity is 48,000 btu/min. Gasoline has 1,389 btu/cu/ft, so
in reality
the mini-combustor can only do a paltry 35 cfm, not the claimed 1,000
cfm, from
the storage tank. Contractors who claim they have a rate of 1,000 cfm
should
tell the other half of the truth which is that the vapors must be very
lean,
perhaps in the LEL range. High concentration will result in fire and
smoke
coming out of the stack. The volume of an empty 150' dia. storage tank
with a
floating roof at 6' is 106,000 scf. A mini combustor with a 4' x 4' x
6'
firebox will take 202 hours to complete 4 volumes at 35 cfm.
The informed tank owner will ask the contractor for a data sheet from
the
combustor manufacturer that shows the design BTU rating and the
combustion
chamber volume. Then insist on a gas flow meter between the tank and
the
control device to accurately measure the inlet flow and volume. Since
the
volume is one of the regulation requirements for vapor control, then
the flow
should be measured by a meter during the tank cleaning at actual flow
conditions.
Other disadvantages of the enclosed flares (mini-combustors):
* They are a source of ignition in the tank farm; they generate heat
and sparks
can come out of the exhaust stack. If you have ever seen one operating
at
night, you may have seen sparks coming out of the exhaust stack.
* They always create an explosive condition inside the storage tank by
drawing
in fresh air.
* They make
* They cannot
handle
chlorinated solvents without scrubbing the exhaust gas. Scrubbing makes
hazardous waste.
* The state of
* They require a source of supplemental fuel (propane) to start the
combustor
and when tank vapors are very lean it has to be added again to keep the
firebox
up to operating temperature. If the firebox isn't 1,200oF, all the VOC
may not
burn in the firebox and instead travel out of the stack.
Internal Combustion Engines:
ICE = internal combustion engine. PURGIT
had 3 of these units in
about 1997 which we tried to use for tank vapor control on the large
tanks here
in
Operators claim that hundreds of cubic feet per minute are controlled
with a
dual engine system. This infers that the flow rate from the storage
tank is in
the hundreds of cu/ft/min. Flow through the engines is limited to the
displacement in the cylinders. The engines are 460 cubic inches, so the
actual
flow is: 460 * the RPM (use 3,000) divided by 2 (four cycle engine)
divided by
1,728 (to get to cubic feet) = 400 cfm total gross displacement. A
stoichiometric fuel ratio that will pass an emission test is about 14.7
to 1.
That is a 6.8% flammable mixture for gasoline. Therefore 400 cfm flow *
6.8% =
27.2 scfm tank vapors per engine. Yes, they may be able to 'make' the
engine
run richer, but fuel will be coming out of
the
exhaust stack.
The volume of an empty 150' dia. storage
tank, with a floating roof
height at
6', is 106,000 scf. At 54.4 cfm (dual engine unit flow rate), it
will
take 129 hours for 4 volumes when the tank has 10% concentration by
volume,
which is not unusual. This is in line with meter readings from a flow
meter
PURGIT used on the units it operated. The operators
will say
they avoid the terrible performance by 'loading' the engine. What
parameter do
they change? Do they increase the RPMs or
do they put
more than 6.8% fuel in the engine?
The informed tank owner will ask for a detailed data sheet from the
manufacturer, but since the manufacturers
data seems
to be confusing or unavailable, he will simply insist on emission
test and a
flow meter between the tank and the ICE. Why is a flow meter so
important? Low
flow rates are hard to measure by pitot tubes that seem to be on some
devices.
It takes a positive displacement or turbine flow meter to have real
accuracy.
Only those types of meters have registers that prove flow and volume.
It is
possible to ask the ICE owner to provide a Wide Band - Air Fuel Ratio
Meter on
the manifold of the engine. None of them have that now because it would
show
the puny efficiency.
* The ICE units cannot handle rapid changes in concentration. When the
concentration changes rapidly, the engines flood or go lean with fuel
and they
shut off. So they are useless at truck loading racks or on pipelines.
ICE units
are complicated.
* The control system and engine is maintenance
intensive.
* The units have numerous sources of ignition. Red hot exhaust
manifolds,
distributors, etc. No gasoline engine is approved to work in a
classified area.
* Do they even have spark arresting mufflers?
* They will always create an explosive condition inside the storage
tank by
drawing in fresh air.
* They require a source of supplemental fuel (propane) to start the
engine and
when tank vapors are very lean it has to be added again to keep the
engines
running.
* They cannot be used to generate electricity as a
by-product
because of the limited time in operation and low horsepower.
* They do make
* Combustion devices like the ICE cannot handle chlorinated solvents
without
scrubbing the exhaust gas. Scrubbing makes hazardous waste.
Activated Carbon:
Activated carbon is a technique that is used occasionally. The handling
of
activated carbon is a nuisance. Carbon is delivered in large boxes and
has to
be transferred to the carbon/plenum container. The cost of carbon is
between $2
to $5 per pound considering disposal, handling, containers, etc. It may
take
anywhere from 2 to 5 pounds of carbon to control 1 pound of VOC. PURGIT
often
recovers 2,000 pounds of chlorinated or hydrocarbon liquids from a
tank. So the
carbon cost may be $8,000 or more for one tank.
* Carbon works best with high velocity vapor streams with low
concentration of
VOC (under 2,000 ppm) according to the Texas Natural Resource
Conservation
Commission Chemical Section Engineers, December, 1994
They also say it works best with high molecular weight compounds
rather
than low molecular weight compounds. And some carbon systems should not
be used
to control reactive compounds such as ketones and alcohols. Moisture
affects
the adsorptive capacity of carbon. They also point out that the
adsorptive wave
front through the carbon bed is curved and breakthrough VOC
concentrations may
occur before the bed has reached its theoretical capacity.
* Carbon can develop bed fires, especially when multiple cargoes are
used with
one carbon bed. Detonation arresters are a necessity.
* There should be at least 2 carbon containers, a primary and a
secondary. The
primary filters the vapor and the secondary is the backup. The vapor
stream
between the containers is monitored and when a sensor indicates
breakthrough,
the first box is shut off and the second becomes primary and a new box
is
brought in, or the process is shut down and the first box is changed
out.
* There is always the chance that some time in the future the discarded
carbon
will become a pollutant if it is put in a landfill.
* Regenerating carbon only transfers the problem since the VOC is
stripped out
by vacuum or heat. The collected liquid may be contaminated with other
products
in the carbon which may make it hazardous waste. If the stripped cargo
is
burned then NOx and CO are created.
Lean Oil Vapor Recovery System:
Lean oil is put in a tank and the cargo vapors are bubbled through it.
The
cargo tank vapors are absorbed into the lean oil and after a certain
point, the
lean oil will no longer absorb the cargo tank vapors. That makes rich
oil,
which must then, itself, have a vapor control system.
* The issue with lean oil is that it takes a simple problem and
compounds it,
because now there are many hundreds of gallons of contaminated oil. The
operators have the original vapor control problem and many hundreds of
gallons
of contaminated oil.
* The rich oil must be heated or vacuumed to drive out the VOC.
* If the lean oil is used for more than one cargo, then the problem is
magnified by having multiple compounds to recover.
There is a place for each of these vapor control devices. No one device
is
perfect for every application. In our experience, the refrigerated
system is
superior in speed and efficiency for MOST storage tank degassing
applications.
It is too bad this information is so
complicated. If you have gotten this far, you are one of the few. The
reason vapor control is so complicated is that the regulators make
rules and then the regulators disappear.
Hank Hilliard
PURGIT is a registered trademark
copyright 2008
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Note 1:
The rental unit
we used is on a 40', 18 wheeler trailer and has a 50 Hp
electric combustion air motor. The firebox on the rental unit isabout
1,500 cubic feet and the verified flow is 600 scfm.
Note 2: Gasoline has about 80 cubic feet of vapor in a gallon, so when
we recover 500 gallons, we have reduced 40,000 cubic feet of tank vapor
to liquid.