Safety Advisory Guidance: Heating Rail Tank Cars To Prepare Hazardous Material for Unloading or Transloading, 41853-41856 [2013-16672]
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Federal Register / Vol. 78, No. 134 / Friday, July 12, 2013 / Rules and Regulations
CFR part 395. The guidance implicitly
imposes a recordkeeping requirement,
but relieves both the carrier and the
driver of any responsibility for
maintaining a copy of the instructions at
the principal place of business or on the
CMV.
In addition, the current guidance
includes an unenforceable performance
standard for assessing the validity of a
break that will be recorded as off-duty.
The guidance states the break must be
long enough to ensure that the
accumulated fatigue resulting from
driving the CMV will be significantly
reduced.
FMCSA’s Decision To Revise the
Regulatory Guidance
In consideration of the above, FMCSA
has determined the 1997 regulatory
guidance should be revised to eliminate
language that has the effect of
discouraging drivers from taking breaks
during the work day, or documenting
such breaks in their logbooks. The
FMCSA revises Question 2 to 49 CFR
395.2, to read as follows:
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Hours of Service for Commercial Motor
Vehicle Drivers Regulatory Guidance
for 49 CFR 395.2, Definitions
Question 2: What conditions must be
met for a commercial motor vehicle
(CMV) driver to record meal and other
routine stops made during a work shift
as off-duty time?
Guidance: Drivers may record meal
and other routine stops, including a rest
break of at least 30 minutes intended to
satisfy 49 CFR 395.3(a)(3)(ii), as off-duty
time provided:
1. The driver is relieved of all duty
and responsibility for the care and
custody of the vehicle, its accessories,
and any cargo or passengers it may be
carrying.
2. During the stop, and for the
duration of the stop, the driver must be
at liberty to pursue activities of his/her
own choosing.
Through the revision of the regulatory
guidance, FMCSA makes clear that the
motor carrier need not provide formal
guidance, either verbal or written, to
drivers with regard to the specific times
and locations where rest break may be
taken. The revised guidance also
emphasizes that periods of time during
which the driver is free to stop working,
and engage in activities of his/her
choosing, may be recorded as off-duty
time, irrespective of whether the driver
has the means or opportunity to leave a
particular facility or location. All
previously issued guidance on this
matter should be disregarded if
inconsistent with today’s notice.
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IV. Guidance for Heating of Rail Tank Cars
for Unloading or Transloading
Issued on: July 5, 2013.
Anne S. Ferro,
Administrator.
[FR Doc. 2013–16687 Filed 7–11–13; 8:45 am]
BILLING CODE 4910–EX–P
DEPARTMENT OF TRANSPORTATION
Pipeline and Hazardous Materials
Safety Administration
49 CFR Chapter I
[Notice No. 13–6]
Safety Advisory Guidance: Heating
Rail Tank Cars To Prepare Hazardous
Material for Unloading or Transloading
Pipeline and Hazardous
Materials Safety Administration
(PHMSA), DOT.
ACTION: Safety advisory guidance.
AGENCY:
This guidance provides safety
precautions and recommended guidance
for persons responsible for unloading or
transloading 1 hazardous materials from
rail tank cars, specifically those persons
heating a rail tank car to prepare its
hazardous material contents for
unloading or transloading. Further, this
guidance reminds such persons of
current regulatory requirements
addressing this type of operation.
PHMSA is issuing this guidance in
coordination with the Occupational
Safety and Health Administration
(OSHA) and the Environmental
Protection Agency (EPA), and in
consultation with the Federal Railroad
Administration (FRA).
FOR FURTHER INFORMATION CONTACT:
Cheryl West Freeman, Division of
Engineering and Research, Pipeline and
Hazardous Materials Safety
Administration, 202–366–4545. For
further information regarding OSHA
regulations, contact OSHA, Office of
Communications at 202–693–1999 and
for further information regarding EPA’s
Risk Management Plan, go to:
www.epa.gov/emergencies/rmp.
SUPPLEMENTARY INFORMATION:
SUMMARY:
I. Background
II. PHMSA’s Coordinated Response With
OSHA and EPA
III. Federal Regulations
A. Applicable PHMSA Regulations
B. Applicable OSHA Regulations or
Standards
C. Applicable EPA Regulations
1 As defined in § 171.8, Transloading means the
transfer of a hazardous material by any person from
one bulk packaging to another bulk packaging, from
a bulk packaging to a non-bulk packaging, or from
a non-bulk packaging to a bulk packaging for the
purpose of continuing the movement of the
hazardous material in commerce.
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I. Background
PHMSA’s mission is to protect people
and the environment from the risks of
hazardous materials transportation,
including those loading and unloading
operations covered under PHMSA
regulations. Our efforts to enhance the
safety of hazardous materials loading
and unloading operations include
development of standards for bulk
loading and unloading of hazardous
materials as part of our current strategic
plan. Towards this end, on May 24,
1999, the Research and Special
Programs Administration (PHMSA’s
predecessor agency) published a final
rule [Docket No. RSPA–97–2718 (HM–
225A), Hazardous Materials: Revision to
Regulations Governing Transportation
and Unloading of Liquefied Compressed
Gases] that revised regulations
applicable to the transportation and
unloading of liquefied compressed
gases. The revisions included new
inspection, maintenance, and testing
requirements for cargo tank discharge
systems, including delivery hose
assemblies, and revised attendance
requirements applicable to liquefied
petroleum gas and anhydrous ammonia.
Also, more recently, on March 11, 2011,
PHMSA published a Notice of Proposed
Rulemaking [Docket Number PHMSA–
2007–28119 (HM–247), Hazardous
Materials: Cargo Tank Motor Vehicle
Loading and Unloading] that proposes
to amend our regulations to require each
person (i.e., carrier or facility) who
engages in cargo tank loading or
unloading operations to perform a risk
assessment of the loading and unloading
operation and develop and implement
safe operating procedures based upon
the results of the risk assessment. We
received comments on the proposals in
this NPRM and are currently evaluating
the best course of action to address
them.
As part of our continuing efforts to
enhance the safety of hazardous
materials loading and unloading
operations, our combined effort with
other Federal agencies to protect the
public, and in response to the findings
from an NTSB investigation, PHMSA is
issuing this safety advisory guidance to
all entities responsible for unloading or
transloading of heated hazardous
material from a rail tank car. In 1999
and again in 2002, accidents occurred as
a result of the process of heating rail
tank cars for unloading hazardous
materials. On February 18, 1999, a rail
tank car, which was on the unloading
rack at the Essroc Cement Corporation
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(Essroc) Logansport cement plant near
Clymers, Indiana, sustained a sudden
and catastrophic rupture that propelled
the tank of the rail tank car an estimated
750 feet and over multistory storage
tanks. The 20,000-gallon rail tank car
initially contained about 161,700
pounds (14,185 gallons) of a toxic and
flammable hazardous waste that was
used as a fuel for the plant’s kilns. There
were no injuries or fatalities. Total
damages, including property damage
and costs from lost production, were
estimated at nearly $8.2 million. The
National Transportation Safety Board
(NTSB) determined that the probable
cause of the accident was the failure of
Essroc to develop and implement safe
procedures for heating rail tank cars for
unloading hazardous waste (i.e., toluene
diisocyanate matter wastes). This lack of
procedures resulted in the overpressurization of the rail tank car due to
chemical self-reaction and expansion of
the toluene diisocyanate matter wastes.
On September 13, 2002, a 24,000gallon-capacity rail tank car containing
about 6,500 gallons of hazardous waste
catastrophically ruptured at a transfer
station at the BASF Corporation
chemical facility in Freeport, Texas. The
rail tank car had been steam-heated to
permit the transfer of the waste to a
cargo tank motor vehicle for subsequent
disposal. The waste was a combination
of cyclohexanone oxime,
cyclohexanone, and water. As a result of
the accident, 28 people received minor
injuries. Residents living within one
mile of the accident site had to shelter
in place for five and one-half hours. The
rail tank car, cargo tank, and transfer
station were destroyed. The force of the
explosion propelled a 300-pound rail
tank car dome housing about 1⁄3 mile
away from the rail tank car. Two storage
tanks near the transfer station were
damaged; that resulted in the released
about 660 gallons of the hazardous
material oleum.2
The NTSB investigated the Freeport,
Texas accident and determined that the
probable cause of the rupture of the rail
tank car was over-pressurization
resulting from a runaway exothermic
decomposition reaction initiated by
excessive heating of the hazardous
waste material. The NTSB determined
that BASF’s failure to monitor the
temperature and pressure inside the rail
tank car while the hazardous waste was
heated in preparation for unloading
contributed to the accident. As a result
of its investigation of the Freeport,
Texas accident, the NTSB recommended
2 The Federal Railroad Administration has
identified three other incidents involving heating of
rail tank cars that did not result in death or injury.
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that PHMSA, in cooperation with the
OSHA and the EPA, develop regulations
that require safe operating procedures to
be established before hazardous
materials are heated in a rail tank car for
unloading; at a minimum, the NTSB
recommended that the procedures
should include the monitoring of
internal tank pressure and cargo
temperature (NTSB Recommendation
R–04–10; December 15, 2004).3
II. PHMSA’s Coordinated Response
With OSHA and EPA
PHMSA believes the current
regulations provide important
requirements for the safe unloading of
heated hazardous material from a rail
tank car. However, we believe it is
always beneficial to remind regulated
entities of their duties in affecting safe
transportation and to offer guidance in
furtherance of performing these duties,
and therefore, PHMSA, in coordination
with OSHA and EPA, and in
consultation with FRA, is issuing this
safety advisory guidance. This safety
advisory guidance is supplemental to
the regulations and is provided as
information for all entities responsible
for unloading or transloading heated
hazardous materials from a rail tank car,
including employees responsible for
overseeing the operation, inspecting and
maintaining equipment, establishing
emergency shutdown procedures, and
developing safe operating procedures.
Specifically, this safety advisory
guidance provides additional guidance
on the recommended safety precautions
affected entities should use when
heating a rail tank car to prepare its
hazardous material contents for
unloading or transloading. Employing
the recommended guidance summarized
in this guidance will enhance safety and
diminish the occurrence of incidents
resulting from the over-pressurization
and runaway exothermic decomposition
reactions initiated by heating of
hazardous material. We note, however,
that there is no binding regulatory
impact of the guidance offered in this
guidance.
III. Federal Regulations
A. Applicable PHMSA Regulations
PHMSA’s Hazardous Materials
Regulations (HMR; 49 CFR Parts 171–
180) specify requirements for the safe
transportation of hazardous materials in
commerce by rail car, aircraft, vessel,
and motor vehicle. Requirements in the
HMR apply to each person who offers a
hazardous material for transportation in
commerce, causes a hazardous material
to be transported in commerce, or
transports a hazardous material in
commerce (see 49 CFR 171.1(b) and (c)).
Transportation includes the movement
of property and loading, unloading, or
storage incidental to that movement (see
49 CFR 171.8).
In 49 CFR 172.700, PHMSA sets forth
training requirements to ensure a
hazmat employee has familiarity with
the general provisions of the HMR, is
able to recognize and identify hazardous
materials, has knowledge of specific
requirements of the HMR applicable to
functions performed by the employee,
and has knowledge of emergency
response information, self-protection
measures and accident prevention
methods and procedures. Any hazmat
employee (as defined in 49 CFR 171.8),
including the designated employee,
must be trained at least once every three
years in accordance with the existing
‘‘function specific’’ training
requirements in 49 CFR 172.704.
Unloading incidental to movement
includes rail tank car transloading
operations, such as the one that resulted
in the Freeport, Texas accident
described above (see 49 CFR 171.8). Rail
tank car unloading operations
conducted by consignee personnel after
the rail tank car has been delivered to
the consignee facility generally are not
regulated under the HMR (see 49 CFR
171.1(d)(2)).
The HMR requirements applicable to
rail tank car transloading operations are
in 49 CFR 174.67. The operator of a
facility at which transloading operations
are performed must maintain written
safety procedures governing
transloading operations and must make
the safety procedures immediately
available to the employee responsible
for rail tank car unloading. In addition,
persons conducting transloading
operations must take measures to
prevent movement of the rail tank car
and secure access to the track where the
transloading operation takes place.
During the transloading operation, the
rail tank car must be attended or
monitored at all times.
B. Applicable OSHA Regulations or
Standards
OSHA’s Process Safety Management
(PSM) standard (see 29 CFR 1910.119)
contains requirements for processes that
use, store, manufacture, handle, or
transport highly hazardous chemicals
3 See https://www.ntsb.gov/doclib/recletters/2004/
R04_10.pdf.
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on-site.4 Bulk 5 loading and unloading
operations involving PSM-covered
chemicals or other processes with PSMcovered chemicals are subject to the
requirements of the PSM standard.6 The
PSM standard requires employers to
compile process safety information (PSI)
to enable employers and employees to
identify and understand the hazards of
the process. The PSI must include: (1)
Physical and reactivity data of the
highly hazardous chemicals in the
process; (2) safe upper and lower limits
of the process such as temperatures,
pressures, flows and compositions; and
(3) an evaluation of the consequences of
deviation. Using the PSI, employers
must perform a process hazard analysis
to systematically identify, evaluate, and
control the hazards of the process. After
an employer completes a process hazard
analysis, the employer must develop
and implement written operating
procedures providing clear, written
instructions for safe operations of a
process, such as loading and unloading
operations to or from bulk containers
(see 29 CFR 1910.119(f)). After the
procedures are developed, each
employee, including a contract
employee, who is involved in loading
and unloading operations must be
trained in the required processes and
the procedures, in accordance with 29
CFR 1910.119(g).
The OSHA standards also include
requirements for the handling and
storage of specific hazardous materials,
including hazardous waste. Specifically,
29 CFR 1910.106(f) contains provisions
for loading and unloading facilities.
Additionally, the OSHA standard at 29
CFR 1910.120, pertaining to hazardous
waste operations and emergency
response, establishes requirements for
emergency response operations. When
there is a release of hazardous materials,
or a substantial threat of a release, then
emergency response operations must
comply with 29 CFR 1910.120(q).
In situations where an operation or a
material is not covered by the PSM
standard or the other OSHA standards,
employers are obligated under Section
5(a)(1)—‘‘the General Duty Clause’’—of
the OSH Act of 1970 to protect
4 29 CFR 1910.119(b), defines a highly hazardous
chemical as a substance possessing toxic, reactive,
flammable, or explosive properties and specified by
paragraph (a)(1) of § 1910.119.
5 The use of this term with respect to the PSM
standard is not the same as defined in the PHMSA
HMR.
6 Both of these processes may be covered by
OSHA’s PSM depending on the flash point of the
waste material and the other chemicals present in
the process. For operations with hazardous
materials, OSHA recommends implementation of
management systems such as those required by the
PSM standard, regardless of coverage.
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employees from serious ‘‘recognized’’
hazards.
Under OSHA’s Hazardous Waste
Operations and Emergency Response
(HAZWOPER) standards in 29 CFR
1910.120, an employer must train
workers exposed to hazardous
substances, health hazards, or safety
hazards before performing hazardous
waste operations and emergency
response. Specifically, 29 CFR
1910.120(e)(3) and (e)(4) detail the level
of training required of workers, who
perform cleanup operations or on-site
management and supervisors of
workers, and 29 CFR 1910.120(q)(6)
details the level of training required of
workers who perform emergency
response.
Section 29 CFR 1910.120(e)(3)(i)
specifies the training requirements for
general site workers engaged in
activities which expose or potentially
expose those workers to hazardous
substances and health hazards. These
workers are required to receive a
minimum of 40 hours of instruction off
the site, and a minimum of three days
actual field experience under the direct
supervision of a trained, experienced
supervisor.
Section 29 CFR 1910.120(e)(3)(ii)
specifies the training requirements for
workers on site only occasionally for a
specific limited task, who are unlikely
to be exposed to hazardous substances
and health hazards over defined
permissible limits. These workers are
required to receive a minimum of 24
hours of instruction off the site, and a
minimum of one day actual field
experience under the direct supervision
of a trained, experienced supervisor.
Section 29 CFR 1910.120(e)(3)(iii)
specifies training requirements for
workers who are regularly onsite in
areas that have been monitored and
fully characterized indicating that
exposures are under permissible
exposure limits and published exposure
limits where respirators are not
necessary, and the characterization
indicates that there are no health
hazards or the possibility of an
emergency developing. These workers
are required to receive a minimum of 24
hours of instruction off the site, and a
minimum of one day actual field
experience under the direct supervision
of a trained, experienced supervisor. In
accordance with 29 CFR 1910.120(e)(3),
on-site management and supervisors
directly responsible for, or who
supervise employees engaged in the
activities described above must receive
40 hours initial training, and three days
of supervised field experience and at
least eight additional hours of
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41855
specialized training at the time of job
assignment.
For all the levels of workers and their
on-site management and supervisors,
the OSHA training requirements
described in 29 CFR 1910.120(e) and (q)
would need to include training in all
aspects of the heating process if that
employee is responsible for performing
any such functions, including refresher
training every three years.
C. Applicable EPA Regulations
EPA regulations establish a general
duty for facility owners or operators of
facilities that produce, handle, process,
distribute, or store certain chemicals to
identify hazards associated with the
accidental releases of extremely
hazardous substances, design and
maintain a safe facility as needed to
prevent such releases, and minimize the
consequences of releases. In addition,
stationary sources with more than a
threshold quantity of a regulated
substance in a process are subject to
EPA’s accident prevention regulations,
including the requirement to develop a
Risk Management Plan (RMP) and
submit the RMP to EPA (see 40 CFR Part
68). EPA’s RMP requirements contain
accident prevention measures that are
virtually identical to those within the
OSHA PSM standard.
In addition to the accident prevention
requirements common to PSM, under 40
CFR Part 68, regulated facilities must
perform a hazard assessment consisting
of worst case and alternative release
scenarios and a five-year accident
history, implement an emergency
response program, implement a
management system, and develop and
submit an RMP to EPA. Further, 40 CFR
Part 112 establishes performance-based
training requirements that would apply
to any facility and covered operation,
including facility transfers that handle
certain chemicals in the specific
quantities listed in 40 CFR 68.130.
IV. Guidance for Heating of Rail Tank
Cars for Unloading or Transloading
Several Federal agencies share
responsibility for the safety regulations
of rail tank car unloading or
transloading operations involving
hazardous material—DOT (PHMSA and
FRA), OSHA, and EPA. PHMSA, in
coordination with OSHA and EPA, and
in consultation with FRA, is issuing this
safety advisory guidance to offer
guidance on heating of a rail tank car to
prepare solidified or viscous hazardous
material products contained in the rail
tank car for unloading or transloading.
Based on existing regulatory
requirements, we have assembled and
coordinated the following guidance to
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raise awareness of those requirements
and the risks associated with heating
rail tank cars. This guidance does not
include all of the aspects applicable to
the safe heating of rail tanks cars; rather,
it focuses on the issues raised in the
NTSB recommendations as a result of its
investigations into the two incidents
cited above.
Procedures. The shipper or facility
operator, if not the same, should
develop written safe operating
procedures to be used when hazardous
materials are heated in a rail tank car for
unloading or transloading. The
procedures should, at a minimum,
establish hazard controls necessary to
protect workers, the public, and the
environment from adverse
consequences, and include:
• Detailed information regarding the
chemical characteristics of the material
such as, melting temperature, flash
point, the degree to which the
hazardous material expands as a result
of heating, and additional risk if the
hazardous material reacts with air or
water.;
• The pressure created by heating the
rail tank car at which the material may
safely be unloaded or transloaded from
the rail tank car;
• Active monitoring and
recordkeeping requirements of the
internal tank pressure and material
temperature during the heating process.
The heating process should be
monitored with time intervals (such as
hourly) that are dependent upon the
nature and history of materials being
heated;
• Potential consequences of
deviations from standard operating
procedures and how to identify, control
and respond to those consequences; and
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• Training of all entities involved in
the unloading or transloading process.
These procedures should be
maintained in a location where they are
immediately available to employees
responsible for the heating, unloading or
transloading operation. These
procedures should clearly define
employees’ roles and responsibilities for
the heating of a rail tank car, as well as
the roles and responsibilities of
contractor personnel that are employed
at a facility to conduct the operations for
heating of a rail tank car.
Monitoring. The facility operator
should be knowledgeable of the
chemical properties of all of the
materials involved in the heating
process, including the reactivity of those
materials, and ensure that the heating
process (i.e., pressure, temperature, and
heating rate) applied to the rail tank car,
and the pressure and temperature inside
the rail tank car should be monitored to
ensure that it does not result in overpressurization of the rail tank car.
Monitoring should be conducted at
the necessary frequency as heating
continues until the material reaches its
recommended parameters (e.g., viscosity
and temperature) for safe unloading or
transloading. Certain chemicals, such as
a material that can undergo rapid
exothermic decomposition, may require
more frequent or even continuous
monitoring during heating. Monitoring
of the tank pressure and the temperature
of the hazardous material includes
measures to ensure that the heating rate
does not result in over pressurization of
the rail tank car.
As an additional aspect of monitoring,
the facility operator may, when practical
and safe, and the physical state of the
material allows, sample the material
that is in the rail tank car to verify the
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material and its chemical and physical
properties. The rail tank car contents
should be monitored at multiple times
as heating continues until the material
is determined to be at its recommended
parameters (e.g., viscosity and
temperature) for safe unloading or
transloading.
Designated Employee. The facility
operator should designate an employee
responsible for monitoring the heating
process. Prior to the onset of operation,
the designated employee should be
made thoroughly knowledgeable of the
nature and properties of the material
contained in the rail tank car and
procedures to be followed in the event
of an emergency. In the event of an
emergency, the designated employee
should have the ability and authority to
take responsive action.
Training. Hazardous materials
employees involved in heating rail tank
cars for unloading or transloading
operations should be trained in all
aspects of the heating process that each
employee is responsible for performing.
Further, the level of training for each
employee should correlate with that
employee’s level of exposure to
hazardous materials at the facility where
rail tank cars are heated for unloading
or transloading. Please refer to the
Section III for a discussion of specific
training obligations under applicable
Federal regulations.
Issued in Washington, DC, on July 8, 2013,
under authority delegated in 49 CFR Part
106.
Magdy El-Sibaie,
Associate Administrator for Hazardous
Materials Safety.
[FR Doc. 2013–16672 Filed 7–11–13; 8:45 am]
BILLING CODE 4910–60–P
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Agencies
[Federal Register Volume 78, Number 134 (Friday, July 12, 2013)]
[Rules and Regulations]
[Pages 41853-41856]
From the Federal Register Online via the Government Printing Office [www.gpo.gov]
[FR Doc No: 2013-16672]
-----------------------------------------------------------------------
DEPARTMENT OF TRANSPORTATION
Pipeline and Hazardous Materials Safety Administration
49 CFR Chapter I
[Notice No. 13-6]
Safety Advisory Guidance: Heating Rail Tank Cars To Prepare
Hazardous Material for Unloading or Transloading
AGENCY: Pipeline and Hazardous Materials Safety Administration (PHMSA),
DOT.
ACTION: Safety advisory guidance.
-----------------------------------------------------------------------
SUMMARY: This guidance provides safety precautions and recommended
guidance for persons responsible for unloading or transloading \1\
hazardous materials from rail tank cars, specifically those persons
heating a rail tank car to prepare its hazardous material contents for
unloading or transloading. Further, this guidance reminds such persons
of current regulatory requirements addressing this type of operation.
PHMSA is issuing this guidance in coordination with the Occupational
Safety and Health Administration (OSHA) and the Environmental
Protection Agency (EPA), and in consultation with the Federal Railroad
Administration (FRA).
---------------------------------------------------------------------------
\1\ As defined in Sec. 171.8, Transloading means the transfer
of a hazardous material by any person from one bulk packaging to
another bulk packaging, from a bulk packaging to a non-bulk
packaging, or from a non-bulk packaging to a bulk packaging for the
purpose of continuing the movement of the hazardous material in
commerce.
FOR FURTHER INFORMATION CONTACT: Cheryl West Freeman, Division of
Engineering and Research, Pipeline and Hazardous Materials Safety
Administration, 202-366-4545. For further information regarding OSHA
regulations, contact OSHA, Office of Communications at 202-693-1999 and
for further information regarding EPA's Risk Management Plan, go to:
---------------------------------------------------------------------------
www.epa.gov/emergencies/rmp.
SUPPLEMENTARY INFORMATION:
I. Background
II. PHMSA's Coordinated Response With OSHA and EPA
III. Federal Regulations
A. Applicable PHMSA Regulations
B. Applicable OSHA Regulations or Standards
C. Applicable EPA Regulations
IV. Guidance for Heating of Rail Tank Cars for Unloading or
Transloading
I. Background
PHMSA's mission is to protect people and the environment from the
risks of hazardous materials transportation, including those loading
and unloading operations covered under PHMSA regulations. Our efforts
to enhance the safety of hazardous materials loading and unloading
operations include development of standards for bulk loading and
unloading of hazardous materials as part of our current strategic plan.
Towards this end, on May 24, 1999, the Research and Special Programs
Administration (PHMSA's predecessor agency) published a final rule
[Docket No. RSPA-97-2718 (HM-225A), Hazardous Materials: Revision to
Regulations Governing Transportation and Unloading of Liquefied
Compressed Gases] that revised regulations applicable to the
transportation and unloading of liquefied compressed gases. The
revisions included new inspection, maintenance, and testing
requirements for cargo tank discharge systems, including delivery hose
assemblies, and revised attendance requirements applicable to liquefied
petroleum gas and anhydrous ammonia. Also, more recently, on March 11,
2011, PHMSA published a Notice of Proposed Rulemaking [Docket Number
PHMSA-2007-28119 (HM-247), Hazardous Materials: Cargo Tank Motor
Vehicle Loading and Unloading] that proposes to amend our regulations
to require each person (i.e., carrier or facility) who engages in cargo
tank loading or unloading operations to perform a risk assessment of
the loading and unloading operation and develop and implement safe
operating procedures based upon the results of the risk assessment. We
received comments on the proposals in this NPRM and are currently
evaluating the best course of action to address them.
As part of our continuing efforts to enhance the safety of
hazardous materials loading and unloading operations, our combined
effort with other Federal agencies to protect the public, and in
response to the findings from an NTSB investigation, PHMSA is issuing
this safety advisory guidance to all entities responsible for unloading
or transloading of heated hazardous material from a rail tank car. In
1999 and again in 2002, accidents occurred as a result of the process
of heating rail tank cars for unloading hazardous materials. On
February 18, 1999, a rail tank car, which was on the unloading rack at
the Essroc Cement Corporation
[[Page 41854]]
(Essroc) Logansport cement plant near Clymers, Indiana, sustained a
sudden and catastrophic rupture that propelled the tank of the rail
tank car an estimated 750 feet and over multistory storage tanks. The
20,000-gallon rail tank car initially contained about 161,700 pounds
(14,185 gallons) of a toxic and flammable hazardous waste that was used
as a fuel for the plant's kilns. There were no injuries or fatalities.
Total damages, including property damage and costs from lost
production, were estimated at nearly $8.2 million. The National
Transportation Safety Board (NTSB) determined that the probable cause
of the accident was the failure of Essroc to develop and implement safe
procedures for heating rail tank cars for unloading hazardous waste
(i.e., toluene diisocyanate matter wastes). This lack of procedures
resulted in the over-pressurization of the rail tank car due to
chemical self-reaction and expansion of the toluene diisocyanate matter
wastes.
On September 13, 2002, a 24,000-gallon-capacity rail tank car
containing about 6,500 gallons of hazardous waste catastrophically
ruptured at a transfer station at the BASF Corporation chemical
facility in Freeport, Texas. The rail tank car had been steam-heated to
permit the transfer of the waste to a cargo tank motor vehicle for
subsequent disposal. The waste was a combination of cyclohexanone
oxime, cyclohexanone, and water. As a result of the accident, 28 people
received minor injuries. Residents living within one mile of the
accident site had to shelter in place for five and one-half hours. The
rail tank car, cargo tank, and transfer station were destroyed. The
force of the explosion propelled a 300-pound rail tank car dome housing
about \1/3\ mile away from the rail tank car. Two storage tanks near
the transfer station were damaged; that resulted in the released about
660 gallons of the hazardous material oleum.\2\
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\2\ The Federal Railroad Administration has identified three
other incidents involving heating of rail tank cars that did not
result in death or injury.
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The NTSB investigated the Freeport, Texas accident and determined
that the probable cause of the rupture of the rail tank car was over-
pressurization resulting from a runaway exothermic decomposition
reaction initiated by excessive heating of the hazardous waste
material. The NTSB determined that BASF's failure to monitor the
temperature and pressure inside the rail tank car while the hazardous
waste was heated in preparation for unloading contributed to the
accident. As a result of its investigation of the Freeport, Texas
accident, the NTSB recommended that PHMSA, in cooperation with the OSHA
and the EPA, develop regulations that require safe operating procedures
to be established before hazardous materials are heated in a rail tank
car for unloading; at a minimum, the NTSB recommended that the
procedures should include the monitoring of internal tank pressure and
cargo temperature (NTSB Recommendation R-04-10; December 15, 2004).\3\
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\3\ See https://www.ntsb.gov/doclib/recletters/2004/R04_10.pdf.
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II. PHMSA's Coordinated Response With OSHA and EPA
PHMSA believes the current regulations provide important
requirements for the safe unloading of heated hazardous material from a
rail tank car. However, we believe it is always beneficial to remind
regulated entities of their duties in affecting safe transportation and
to offer guidance in furtherance of performing these duties, and
therefore, PHMSA, in coordination with OSHA and EPA, and in
consultation with FRA, is issuing this safety advisory guidance. This
safety advisory guidance is supplemental to the regulations and is
provided as information for all entities responsible for unloading or
transloading heated hazardous materials from a rail tank car, including
employees responsible for overseeing the operation, inspecting and
maintaining equipment, establishing emergency shutdown procedures, and
developing safe operating procedures.
Specifically, this safety advisory guidance provides additional
guidance on the recommended safety precautions affected entities should
use when heating a rail tank car to prepare its hazardous material
contents for unloading or transloading. Employing the recommended
guidance summarized in this guidance will enhance safety and diminish
the occurrence of incidents resulting from the over-pressurization and
runaway exothermic decomposition reactions initiated by heating of
hazardous material. We note, however, that there is no binding
regulatory impact of the guidance offered in this guidance.
III. Federal Regulations
A. Applicable PHMSA Regulations
PHMSA's Hazardous Materials Regulations (HMR; 49 CFR Parts 171-180)
specify requirements for the safe transportation of hazardous materials
in commerce by rail car, aircraft, vessel, and motor vehicle.
Requirements in the HMR apply to each person who offers a hazardous
material for transportation in commerce, causes a hazardous material to
be transported in commerce, or transports a hazardous material in
commerce (see 49 CFR 171.1(b) and (c)). Transportation includes the
movement of property and loading, unloading, or storage incidental to
that movement (see 49 CFR 171.8).
In 49 CFR 172.700, PHMSA sets forth training requirements to ensure
a hazmat employee has familiarity with the general provisions of the
HMR, is able to recognize and identify hazardous materials, has
knowledge of specific requirements of the HMR applicable to functions
performed by the employee, and has knowledge of emergency response
information, self-protection measures and accident prevention methods
and procedures. Any hazmat employee (as defined in 49 CFR 171.8),
including the designated employee, must be trained at least once every
three years in accordance with the existing ``function specific''
training requirements in 49 CFR 172.704.
Unloading incidental to movement includes rail tank car
transloading operations, such as the one that resulted in the Freeport,
Texas accident described above (see 49 CFR 171.8). Rail tank car
unloading operations conducted by consignee personnel after the rail
tank car has been delivered to the consignee facility generally are not
regulated under the HMR (see 49 CFR 171.1(d)(2)).
The HMR requirements applicable to rail tank car transloading
operations are in 49 CFR 174.67. The operator of a facility at which
transloading operations are performed must maintain written safety
procedures governing transloading operations and must make the safety
procedures immediately available to the employee responsible for rail
tank car unloading. In addition, persons conducting transloading
operations must take measures to prevent movement of the rail tank car
and secure access to the track where the transloading operation takes
place. During the transloading operation, the rail tank car must be
attended or monitored at all times.
B. Applicable OSHA Regulations or Standards
OSHA's Process Safety Management (PSM) standard (see 29 CFR
1910.119) contains requirements for processes that use, store,
manufacture, handle, or transport highly hazardous chemicals
[[Page 41855]]
on-site.\4\ Bulk \5\ loading and unloading operations involving PSM-
covered chemicals or other processes with PSM-covered chemicals are
subject to the requirements of the PSM standard.\6\ The PSM standard
requires employers to compile process safety information (PSI) to
enable employers and employees to identify and understand the hazards
of the process. The PSI must include: (1) Physical and reactivity data
of the highly hazardous chemicals in the process; (2) safe upper and
lower limits of the process such as temperatures, pressures, flows and
compositions; and (3) an evaluation of the consequences of deviation.
Using the PSI, employers must perform a process hazard analysis to
systematically identify, evaluate, and control the hazards of the
process. After an employer completes a process hazard analysis, the
employer must develop and implement written operating procedures
providing clear, written instructions for safe operations of a process,
such as loading and unloading operations to or from bulk containers
(see 29 CFR 1910.119(f)). After the procedures are developed, each
employee, including a contract employee, who is involved in loading and
unloading operations must be trained in the required processes and the
procedures, in accordance with 29 CFR 1910.119(g).
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\4\ 29 CFR 1910.119(b), defines a highly hazardous chemical as a
substance possessing toxic, reactive, flammable, or explosive
properties and specified by paragraph (a)(1) of Sec. 1910.119.
\5\ The use of this term with respect to the PSM standard is not
the same as defined in the PHMSA HMR.
\6\ Both of these processes may be covered by OSHA's PSM
depending on the flash point of the waste material and the other
chemicals present in the process. For operations with hazardous
materials, OSHA recommends implementation of management systems such
as those required by the PSM standard, regardless of coverage.
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The OSHA standards also include requirements for the handling and
storage of specific hazardous materials, including hazardous waste.
Specifically, 29 CFR 1910.106(f) contains provisions for loading and
unloading facilities. Additionally, the OSHA standard at 29 CFR
1910.120, pertaining to hazardous waste operations and emergency
response, establishes requirements for emergency response operations.
When there is a release of hazardous materials, or a substantial threat
of a release, then emergency response operations must comply with 29
CFR 1910.120(q).
In situations where an operation or a material is not covered by
the PSM standard or the other OSHA standards, employers are obligated
under Section 5(a)(1)--``the General Duty Clause''--of the OSH Act of
1970 to protect employees from serious ``recognized'' hazards.
Under OSHA's Hazardous Waste Operations and Emergency Response
(HAZWOPER) standards in 29 CFR 1910.120, an employer must train workers
exposed to hazardous substances, health hazards, or safety hazards
before performing hazardous waste operations and emergency response.
Specifically, 29 CFR 1910.120(e)(3) and (e)(4) detail the level of
training required of workers, who perform cleanup operations or on-site
management and supervisors of workers, and 29 CFR 1910.120(q)(6)
details the level of training required of workers who perform emergency
response.
Section 29 CFR 1910.120(e)(3)(i) specifies the training
requirements for general site workers engaged in activities which
expose or potentially expose those workers to hazardous substances and
health hazards. These workers are required to receive a minimum of 40
hours of instruction off the site, and a minimum of three days actual
field experience under the direct supervision of a trained, experienced
supervisor.
Section 29 CFR 1910.120(e)(3)(ii) specifies the training
requirements for workers on site only occasionally for a specific
limited task, who are unlikely to be exposed to hazardous substances
and health hazards over defined permissible limits. These workers are
required to receive a minimum of 24 hours of instruction off the site,
and a minimum of one day actual field experience under the direct
supervision of a trained, experienced supervisor.
Section 29 CFR 1910.120(e)(3)(iii) specifies training requirements
for workers who are regularly onsite in areas that have been monitored
and fully characterized indicating that exposures are under permissible
exposure limits and published exposure limits where respirators are not
necessary, and the characterization indicates that there are no health
hazards or the possibility of an emergency developing. These workers
are required to receive a minimum of 24 hours of instruction off the
site, and a minimum of one day actual field experience under the direct
supervision of a trained, experienced supervisor. In accordance with 29
CFR 1910.120(e)(3), on-site management and supervisors directly
responsible for, or who supervise employees engaged in the activities
described above must receive 40 hours initial training, and three days
of supervised field experience and at least eight additional hours of
specialized training at the time of job assignment.
For all the levels of workers and their on-site management and
supervisors, the OSHA training requirements described in 29 CFR
1910.120(e) and (q) would need to include training in all aspects of
the heating process if that employee is responsible for performing any
such functions, including refresher training every three years.
C. Applicable EPA Regulations
EPA regulations establish a general duty for facility owners or
operators of facilities that produce, handle, process, distribute, or
store certain chemicals to identify hazards associated with the
accidental releases of extremely hazardous substances, design and
maintain a safe facility as needed to prevent such releases, and
minimize the consequences of releases. In addition, stationary sources
with more than a threshold quantity of a regulated substance in a
process are subject to EPA's accident prevention regulations, including
the requirement to develop a Risk Management Plan (RMP) and submit the
RMP to EPA (see 40 CFR Part 68). EPA's RMP requirements contain
accident prevention measures that are virtually identical to those
within the OSHA PSM standard.
In addition to the accident prevention requirements common to PSM,
under 40 CFR Part 68, regulated facilities must perform a hazard
assessment consisting of worst case and alternative release scenarios
and a five-year accident history, implement an emergency response
program, implement a management system, and develop and submit an RMP
to EPA. Further, 40 CFR Part 112 establishes performance-based training
requirements that would apply to any facility and covered operation,
including facility transfers that handle certain chemicals in the
specific quantities listed in 40 CFR 68.130.
IV. Guidance for Heating of Rail Tank Cars for Unloading or
Transloading
Several Federal agencies share responsibility for the safety
regulations of rail tank car unloading or transloading operations
involving hazardous material--DOT (PHMSA and FRA), OSHA, and EPA.
PHMSA, in coordination with OSHA and EPA, and in consultation with FRA,
is issuing this safety advisory guidance to offer guidance on heating
of a rail tank car to prepare solidified or viscous hazardous material
products contained in the rail tank car for unloading or transloading.
Based on existing regulatory requirements, we have assembled and
coordinated the following guidance to
[[Page 41856]]
raise awareness of those requirements and the risks associated with
heating rail tank cars. This guidance does not include all of the
aspects applicable to the safe heating of rail tanks cars; rather, it
focuses on the issues raised in the NTSB recommendations as a result of
its investigations into the two incidents cited above.
Procedures. The shipper or facility operator, if not the same,
should develop written safe operating procedures to be used when
hazardous materials are heated in a rail tank car for unloading or
transloading. The procedures should, at a minimum, establish hazard
controls necessary to protect workers, the public, and the environment
from adverse consequences, and include:
Detailed information regarding the chemical
characteristics of the material such as, melting temperature, flash
point, the degree to which the hazardous material expands as a result
of heating, and additional risk if the hazardous material reacts with
air or water.;
The pressure created by heating the rail tank car at which
the material may safely be unloaded or transloaded from the rail tank
car;
Active monitoring and recordkeeping requirements of the
internal tank pressure and material temperature during the heating
process. The heating process should be monitored with time intervals
(such as hourly) that are dependent upon the nature and history of
materials being heated;
Potential consequences of deviations from standard
operating procedures and how to identify, control and respond to those
consequences; and
Training of all entities involved in the unloading or
transloading process.
These procedures should be maintained in a location where they are
immediately available to employees responsible for the heating,
unloading or transloading operation. These procedures should clearly
define employees' roles and responsibilities for the heating of a rail
tank car, as well as the roles and responsibilities of contractor
personnel that are employed at a facility to conduct the operations for
heating of a rail tank car.
Monitoring. The facility operator should be knowledgeable of the
chemical properties of all of the materials involved in the heating
process, including the reactivity of those materials, and ensure that
the heating process (i.e., pressure, temperature, and heating rate)
applied to the rail tank car, and the pressure and temperature inside
the rail tank car should be monitored to ensure that it does not result
in over-pressurization of the rail tank car.
Monitoring should be conducted at the necessary frequency as
heating continues until the material reaches its recommended parameters
(e.g., viscosity and temperature) for safe unloading or transloading.
Certain chemicals, such as a material that can undergo rapid exothermic
decomposition, may require more frequent or even continuous monitoring
during heating. Monitoring of the tank pressure and the temperature of
the hazardous material includes measures to ensure that the heating
rate does not result in over pressurization of the rail tank car.
As an additional aspect of monitoring, the facility operator may,
when practical and safe, and the physical state of the material allows,
sample the material that is in the rail tank car to verify the material
and its chemical and physical properties. The rail tank car contents
should be monitored at multiple times as heating continues until the
material is determined to be at its recommended parameters (e.g.,
viscosity and temperature) for safe unloading or transloading.
Designated Employee. The facility operator should designate an
employee responsible for monitoring the heating process. Prior to the
onset of operation, the designated employee should be made thoroughly
knowledgeable of the nature and properties of the material contained in
the rail tank car and procedures to be followed in the event of an
emergency. In the event of an emergency, the designated employee should
have the ability and authority to take responsive action.
Training. Hazardous materials employees involved in heating rail
tank cars for unloading or transloading operations should be trained in
all aspects of the heating process that each employee is responsible
for performing. Further, the level of training for each employee should
correlate with that employee's level of exposure to hazardous materials
at the facility where rail tank cars are heated for unloading or
transloading. Please refer to the Section III for a discussion of
specific training obligations under applicable Federal regulations.
Issued in Washington, DC, on July 8, 2013, under authority
delegated in 49 CFR Part 106.
Magdy El-Sibaie,
Associate Administrator for Hazardous Materials Safety.
[FR Doc. 2013-16672 Filed 7-11-13; 8:45 am]
BILLING CODE 4910-60-P