Today the DOT’s Pipeline and Hazardous Material Safety
Administration (PHMSA) published a notice of proposed rulemaking (NPRM) “Hazardous
Materials: Liquefied Natural Gas by Rail” in the Federal Register (84
FR 56964-56977). The rule would make changes to the Hazardous Materials
Regulations to allow for the bulk transport of Methane, refrigerated liquid,
commonly known as liquefied natural gas (LNG), in DOT-113C120W specification rail
tank cars. The rulemaking was initiated in response to a petition
for rulemaking [.PDF download link] from the Association for American
Railroads (AAR).
Tank Car Specification
The AAR petition requested that
PHMSA consider authorizing the use of current DOT-113C120W and a new DOT-113C140W
specification tank car for the transport of LNG by rail. In this rulemaking PHMSA
is only proposing
to authorize the use of the DOT-113C120W specification tank car which are
currently in service for the transportation of other flammable cryogenic liquids.
PHMSA notes
that they “anticipate that DOT-113 specification tank cars will need to be
manufactured to satisfy the demand for transporting LNG as the current fleet of
these tank cars is used for the transportation of ethylene and other cryogenic
liquids.”
The rulemaking would amend 49
CFR 179.319(d)(2) to add the following pressure relief requirements for
LNG:
• Maximum pressure when offered for transportation –
15 psig;
• Design service temperature – minus 216˚F; and
• Maximum start to discharge pressure – 75 psig
Operational Controls
The NPRM is not proposing to impose any additional
operational controls beyond those currently required for flammable cryogenic
liquids. It is, however, seeking comments on whether or not the following
controls should be considered in the final rule:
Incorporate by reference AAR Circular OT-55
key train and/or key route provisions;
LNG Characteristics
There is a lengthy discussion
in the preamble about the characteristics of LNG; particularly the
characteristics of LNG fires. The discussion of a
vapor cloud fire is important:
“If an LNG vapor cloud is ignited
before the cloud has been dispersed or diluted to below its lower flammability
limit, a flash fire will occur. Unlike other flammable liquids and gases, a LNG
vapor cloud will not ignite entirely at once. If ignited, the flash fire that
forms has a temperature of about 1,330 °C (2,426 °F). The resulting ignition
leads to a relatively slow (subsonic) burning vapor fire which travels
back to the release point producing either a pool fire or a jet fire
[emphasis added]. The radiant heat effects from such a flash fire does not
extend to distances significantly larger than the width of the flammable cloud.
The slow burning vapor fire will not generate damaging overpressures (i.e.,
explosions), if unconfined. To produce an overpressure event, the LNG vapors
need to be within the flammability range and ignited, and either be confined
within a structure or the travelling flame in the open encounters structural
obstructions (e.g., houses, trees, bushes, pipe racks, etc.) that can increase
the flame turbulence significantly when the flash fire reaches the source of
vapor (boiling LNG), if there is still a liquid pool of LNG evaporating at that
time, a pool fire will result.”
DOT 113 Accident History
The preamble includes a discussion of
the accident history of the DOT 113 tank car. It describes only
one incident in 37 years in which a fire occurred as a result of a derailment
involving flammable cryogenic liquids transported in DOT 113C120 tank cars. According
to a local
news report the fire was relatively unremarkable.
Public Comments
PHMSA is soliciting public comments on this NPRM. Comments
may be submitted via the Federal eRulemaking Portal (www.regulations.gov; Docket # PHMSA-2018-0025).
Comments need to be submitted by December 23rd, 2019.
Commentary
If the public
comments on PHMSA’s LNG by rail special permit are any indication (2,973
comments to date) there will be a large public outcry against this NPRM. It
will come mainly from people who have not read the NPRM and particularly did not
read the discussion on LNG characteristics and the accident history of the DOT
113 railcar.
We are seeing an increasing amount of natural gas being produced
in oil fields in the United States. It makes no economic sense nor
environmental sense to not use that methane as either a fuel or a chemical
feedstock. Either of those uses will require transporting the natural gas from
where it is produced to where it is used or to where it is shipped to our
trading partners via ocean going vessels. The pipeline infrastructure (the
safest way to ship either natural gas or LNG) is not in place to provide that
transportation. Currently the only other authorized way to ship the material is
by truck. That mode has more safety issues than does rail, and the dwindling
supply of hazmat qualified truck drivers provides an additional impediment to
transporting large quantities of LNG by truck.
Economically and environmentally this rulemaking is
necessary. There are some changes that I think need to be made and I will
address those in a separate blog post with subsequent submission as a comment
on this NPRM.
I urge everyone with an interest in this topic (pro and con)
to closely read this NPMR, consider what PHMSA is proposing (and missing) and
submit well-reasoned comments to help to improve this rulemaking.
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