July1999
Concept
Alargeshop aircompressorwas used
for the initial tests. The regulated shop air
hose was connected
to a needle valve for
controlling
the
flow
rate,
and
then
to
a
silica-gel desiccator, and a flow meter for
measuring
the
flow rates
between
0
-
3
cubic
feet
per
minute.
The
flow
meter
output
was
connected
to
the
tank
input
port
with
the
dip
tube.
The
output
port
opened
at the top of the tank. The output
port was connected
to
a 10
foot length of
hose
with
the
flame
block
at
the
end.
Where
the
hose
was
connected
to
the
output port valve there was an instrument
tap used to samplethe gas exiting the tank.
The
instrument
connected
to
the
small
sampling hoseindicates when the gas is at
the
flammability
limits of
2% and
10%.
(See Figure 1 on
page 26.)
With this arrangement,airat aknown
flow rate
was
injected
into
a tank
full of
100% propane vapor at atmospheric pres-
sure and the resultant gas was monitored
for the time it took
to
reach
10% and 2%
propane
levels.
With
this
information
a
curve was calculated that defines the per-
cent propane for any number of tankvol-
umes.
Test
A ten gallon aluminum Worthington
vertical tank
was
used for the tank
under
test.
The
tank
was
prepared
by
filling
it
with 1/2 gallon of liquid propane and then
purging
the
air from
the tank
by
venting
vapor
from
the
tank
until
the
liquid
had
evaporated, the temperature was above 50
degrees
F., and
the pressure was zero.
An
area was chosen
for the test
that
had
controll ed
access,
no
structures
nearby, a 3 to 5 mph wind, and no ignition
source within 200 feet. The test setup was
laid out so the output hose was downwind.
The
test
data
produced
the
curve
shown in
Fig. 2. Four tank
volumes pro-
duces
a tank
content of 2% propane (the
lower flammability
limit).
By
extending
the curve, the percentage of propane can
be obtained to
10 tank
volumes.
The test
was
repeated
several
times
and produced the same results.
To
test
the
sensitivity
of
the
test
to
2, 3 cu. ft./min. The test
results were the
same.
IMPORTANT:
The
tank
inlet
and
outlet
ports
were
switched
and
the
tests
were
re-run
at
1
and
3
cu.
ft./min.
The
results
were
different
depending
on
the
tank
valve configuration.
There are sev-
eral valve configurations that open to the
top
of the tank. If air is
injected through
these,
they
will
cause different
amounts
of turbulence.
The
results
of
low turbu-
lence is incomplete purging. Injecting air
through the dip tube produced
consistent
results regardless of the valve configura-
tion at the top of the tank.. The conclusion
reached was that theturbulence in thetank
at 1 to 3
cu. ft./min., injected through the
dip
tube,
was
sufficient
to
provide com-
plete mixing of the propane and air in the
tank.
A 15
gallon tank was connected and
several
tests
were
run.
The
results
were

2% propane at
four tank
volumes.
Moisture
Out
of
the
Tank
During shipping one of the tank
ser-
vice valves must be open. At the comple-
tion
of the trip it is assumed that the tank
has some water vapor inside. This is usu-
ally corrected by the introduction of a few
ounces ofmethyl alcohol. However, there
are
restrictions
on
shipping
alcohol
with
the tank.
Aerostatic
Engineering
(San
Jose)
makes
a
small
desiccator
designed
with
propane fittings that can
be connected
to
the
open
tank
service valve. This
allows
the tank to “breathe” dry
air, meeting the
shipping requirements. The tank can then
be filled upon
arrival with
no problem.
The desiccator can be used to dry the
purge air for the return trip. A small can of
fresh
desiccant
can
be
shipped
with
the
July1999

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provides tags that are attached to the service valves indicating the
purge data.
The 12v
DC
Coleman
air mattress
compressor
was
tested
with
the small
desiccator on
a
10
gallon
tank. The
compressor
produced
1.33
Cu.Ft/Min
with
the
vehicle
engine
off
and
1.5
Cu.Ft./Min.
with
the engine
running
at
a fast
idle.
The
results
were the same. Remember the sparking brushes of the compres-
sor and the vehicle engine are sources
of ignition.
Since
there appear
to
be no
technical
purge criteria, it’s
a
matter
of
judgment
how
far
under
2%
propane
you
feel
is
required. You
will
note from
the curve,
8
tank
volumes
yields
.035%.With the1.33 Cu.Ft./min. portable air compressor it takes
9.98 minutes for a 10 gallon tank. For 10 tank volumes that yields
.0048%, and takes 12.48
minutes.
John Terry, after 35 years with IBM, principally in the field
of testing, now has his own balloon repair station and technical
design business, Aerostatic Engineering, in San Jose, California.
John has a number of Supplementary Type Certificates and
a Parts Manufacturing Authority. He has a commercial balloon
pilot’s certificate and has flown balloons for about 25 years.
For more info rmation contact Aerostatic Engineering, Joh n
Terry, 495 E Brokaw Rd, San Jose, CA 95112, phone 4 08-441-
1919, email: jterry@terry.com