An example using the PEAC tool:

Hydrogen Chloride is a common
chemical and is normally seen as an aqueous solution
that is typically labeled as Hydrochloric Acid.
The concentration can vary depending on the ultimate for
which the agent will be used. As most mineral
acids, it is very corrosive and should always be handled
with care and proper CPC should be utilized if exposure
to the Hydrochloric Acid is
possible.
Hydrogen Chloride is also
produced and shipped as a liquefied gas under its own
vapor pressure. In this form, it is referred to as
“Hydrogen Chloride, Anhydrous”, the anhydrous means it
is not in solution with water.
As a strong
acid, it has a number of industrial purposes. An
important use is the dissolving of certain metals, for
this reason hydrochloric acid is used extensively in the
industrial processing of metals and in the concentration
of some ores. It is also used in the production of
vinyl, cotton, and for etching semi-conductor
crystals.
Anhydrous Hydrogen Chloride by
itself is not corrosive, but it will react with any
moisture present to form concentrated Hydrochloric
Acid. Therefore, an individual exposed to
Anhydrous Hydrogen Chloride must be properly protected,
both to prevent inhalation and contact with the skin or
eyes. In either situation, the moisture present on
the skin or eyes will immediately form Hydrochloric Acid
that will lead to severe burns and potentially long term
effects. The inhalation will lead to reaction with
moisture in the airways and , which can lead to long-term health effects or
even death.
An interesting sidelight about
Anhydrous Hydrogen Chloride is that it is controlled by
the DEA (Drug Enforcement Administration) because of its
potential use in the manufacturing of
Methamphetamine. A domestic threshold of zero (0.0
kilograms) for anhydrous hydrogen chloride became
effective September 1, 2000, by a Final Rule published
on August 2, 2000 (65 FR 47309). Although the
threshold for anhydrous hydrogen chloride is established
at 0.0 kilogram, DEA has concluded that certain
transactions in anhydrous hydrogen chloride are not
sources for diversion. The Final Rule establishing
a zero threshold for anhydrous hydrogen chloride also
provided exemption, on an interim basis, from the record
keeping and reporting requirements for: (1) domestic
transactions involving pipeline distributions; and (2)
domestic distributions of 12,000 pounds (net weight) or
more in a single container.
For those not
familiar with the PEAC application and its various
features, the following is a brief description of how
information can be displayed in the PEAC
application. There are multiple methods to find a
hazardous material, it can be searched for by: (1) name,
(2) UN#, (3) CAS#, or if it is known to be in a certain
class of materials, it can be searched by selecting a
Quick Filter. Once the material is found, there
are multiple databases that can be displayed on the
screen. The default database always displayed is
the
Chemical Properties
information.
The following discussion
provides screen captures from
PEAC-WMD 2002 for
Windows application while viewing some of the
information available for Anhydrous Hydrogen
Chloride.

The Chemical Properties database screen
provides the responder with the basic information
required to start developing a plan of attack on the
problems that may be encountered in dealing with
Anhydrous Hydrogen Chloride. One concern is that
the material is going to be released as a gas and form a
vapor cloud.
This is obvious from
observing a couple of different pieces of information
found on the above screen capture. First, the
material is shipped as a liquefied gas under its own
vapor pressure plus it has a vapor pressure of 40+
atmospheres at 68
oF. In addition, the
boiling point is –121
oF so any material
released is going to be released as a vapor or it will
flash to a vapor very quickly if released as a
liquid.
Secondly, the vapor cloud is going to
behave as a dense-gas or heavier-than-air. This is
should be evident for two reasons: (1) the relative
vapor density is 1.3 since the molecular weight is 36
compared to air which is approximately 29, and (2) as we
have already seen, the material has a very low boiling
point (–121
oF), therefore when the material
is released from its container, particularly if released
as a liquid, it will flash to a vapor, and cool the
resulting vapor causing it to exhibit a dense-gas
behavior.
Third, the material is toxic
(with an IDLH of 50 ppm) therefore respiratory
protection is mandatory. As discussed earlier,
because of its reactivity with water or moisture, proper
selection of CPC is also critical for protecting
response personnel.
Finally, the material
is not combustible; therefore elimination of ignition
sources is not a critical factor.

By selecting the All Chemical Protective
Clothing database, all the entries in the PEAC database
for those products tested against Anhydrous Hydrogen
Chloride are listed by type of garment and breakthrough
times.
Depending on the incident and
other factors involved, such as fire, access to the DOT
ERG2000 “orange pages” may provide additional
guidance. In the next screen capture are displayed
the information for Evacuation. As shown, in
addition to the generic procedures provided in the
“orange pages”, the PEAC system will also provide the
evacuation distances found in the “green pages” of the
ERG2000. This screen also indicates the increasing
of isolation distance if fire is involved in the
incident. The other DOT ERG2000 listings can also
be displayed by selecting them in a similar
manner.

Since the PEAC tool displays the PAD icon
at the top of the screen when Hydrogen Chloride,
Anhydrous is selected, this means a PAD (Protective
Action Distance) can be generated based on information
provided by the user. To display the input screens
to allow generation of a PAD, click on the yellow PAD
icon at the top of the screen.
A
hypothetical incident has been used to demonstrate the
use of the PEAC PAD calculation. The incident
involves a railcar that has derailed and struck the
super structure of a bridge causing a hole to penetrate
the car. The hole can’t be seen but the portion of
the bridge that pierced the tank is approximately 3” in
diameter. Liquid is coming out the hole, but no
liquid pool is forming because all the liquid is forming
a vapor or fog cloud that is moving downwind. The
surrounding area is mostly wooded with a residential
area about 1 mile downwind. The time is about 2:00
PM, very light winds, outside temperature is in the mid
70’s, and no cloud cover.
Meteorology The
temperature is mid-70’s or about 75, light wind is
set for 2 mph, no cloud cover is 0%, and the
terrain is wooded with residential farther
downwind.
|
Container We select a railcar
from our list of containers and it fills in a
default size of the container. 95% full
assumes worst-case unless we know it is less, this
also allows for head-space. We have assumed
the tank is horizontal.
|
Source The exact size of
the hole is not known but since it looks like the
bridge structure element that made the hole is 3”,
we’ll go with 3”. We didn’t say where the
hole was but will assume it is close to the
bottom, at least we know liquid is coming out, so
it isn’t at the
top.
|

The PEAC built-in dispersion model
makes a calculation using the IDLH of 50 ppm as the
Level of Concern. This results in a
downwind distance of 2.4 miles. With a residential
area about a mile away from the incident, the call for
evacuation is probably in order. If the loss of
liquid was through a valve or some external line on the
container that might have some potential of being capped
or plugged, then perhaps an evacuation won’t be
required. In that case, perhaps only a “shelter in
place” might be the most prudent recommendation.
The thought being that the plugging or capping can be
accomplished fairly quickly and allowing the public to
close windows and shut off air-conditioners and
ventilation for a relatively short time should provide
enough protection. With the puncture scenario, the
time required to off load the contents means that the
vapor cloud is going to persist for quite some time
until the problem is
mitigated.