enTTi ra miac* f ti
Compl i an t
U.S. Department of Labor -
Occupational Saf e ty and Healt h Admini s tration
OSHA3133 -
1994 (R e print e d) -
Report Documentation Page
Report Date Report Type
00001994 N/A
Dates Covered (from... to)
Title and Subtitle
Contract Number
Process Safety Management Guidelines for Compliance
Grant Number
Program Element Number
Author(s)
Project Number
Task Number
Work Unit Number
Performing Organization Name(s) and Address(es)
U.S. Dept of Labor Occupational Safety & Health
Administration 200 Constitution Avenue Washington,
DC 20210
Performing Organization Report Number
OSHA-3133
Sponsoring/Monitoring Agency Name(s) and
Sponsor/Monitor’s Acronym(s)
Address(es)
Sponsor/Monitor’s Report Number(s)
Distribution/Availability Statement
Approved for public release, distribution unlimited
Supplementary Notes
Abstract
The major objective of process safety management (PSM) of highly hazardous chemicals to prevent
unwanted releases of hazardous chemicals especially into locations that could expose employees and
others to serious hazards. An effective process safety management program requires a systematic
approach to evaluating the whole chemical process. Using this approach, the process design, process
technology, process changes, operational and maintenance activities and procedures, nonroutine activities
and procedures, emergency preparedness plans and procedures, training programs, and other elements that
affect the process are all considered in the evaluation.
Subject Terms
Report Classification
unclassified
Classification of this page
unclassified
Classification of Abstract
unclassified
Limitation of Abstract
UU
This informational booklet provides a generic,
non-exhaustive overview of OSHA standards-
related topics. This publication does not itself
alter nr determine compliance responsibilities,
which are set forth in OSHA standards them¬
selves and the Occupational Safety and Health
Act. Moreover, because interpretations and
onfnrr<ampnt nnlirv/ mpv rh;^nnA ovpr timP fnr
I. W. ..w. -..—
additional guidance on OSHA compliance
requirements, the reader should consult current
administrative interpretations and decisions by
the Occupational Safety and Health Review
Commission and the courts.
Material contained in this publication is in the
niihlic domain and mav be reoroduced. fuliv or
partially, without permission of the Federal
Government. Source credit is requested but not
required.
This information will be made available to
sensory impaired individuals upon request.
Voice phone; (202) 219-8045;
Telecommunications Device for the Deaf (TDD)
message referral phone; 1-800-326-2577
Procsss Sststy
ManauemGnt
Tor
1^1 i o n
v#v/i I ipiioii I
U.S, Department of Labor
Robert B. Reich, Secretary
Occupationai Safety and Health Administration
Joseph A. Dear, Assistant Secretary
OSHA 3133
1994 (Reprinted)
E
K^\Jl lid liO
Purpose.
ADDlication.
■ 'i“ I--
Exceptions.
Process Safety Information.
Hazards of the Chemicals Used in the Process
Technology of the Process.
Equipment in the Process.
Emolovee Involvement.
— I' - ^ -
Process Hazard Analysis.
Operating Procedures.
i;^iii|yPiwy^^ iiaiiiiii^ .
Contractors.
rage
1
O
2
2
3
5
5
..8
in
I w
12
Dr-a-Qtartim Rc^vipiUf
----- ^ ^ j ■ ■ w « ■ • •
I W '
12
Mechanical Integrity of bquipment.13
Process Defenses.13
Written Procedures.14
Inspection and Testing.14
Quality Assurance.15
Nonroutine Work Authorizations.15
Managing Change.16
incident Investigation.17
Emergency Preparedness.
Compliance Audits.
Planning.
Staffing.
Conductino the Audit.
— ^
Evaluation and Corrective Action
27
27
27
28
28
Conclusion
Aooendix
" T r -
States with Approved Plans.
OSHA Consultation Project Directory
OCUA
WWI mi WlllWd^
29
30
/%/S
36
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liiustrations
Figure 1. Process Flow Diagram.4
Figure 2. Request for Change Form.18
Figure 3. Incident Investigation Report.20
Purpose
The major objective of process safety management (PSM) of highly
hazardous chemicals is to prevent unwanted releases of hazardous
chemicals especially into locations that could expose employees and
others to serious hazards. An effective process safety management
nrnnram renuires a svstematic aooroach to evaluatino the whole
-— ” ^ J ---- - -- - ^ .
chem.ical process. Using this approach, the process design, process
technology, process changes, operational and maintenance activities
and procedures, nonroutine activities and procedures, emergency
nrandfo/Hnoee nianc anH rirnroHiiroc traininn nronramc anri nthpr
Qlamante that affopt the nrpr>aoe ara all ppnciHprorl in tho o\/aliiatinn
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n|i./pilWCll.lWI I
The various lines of defense that have been incorporated into the
design and operation of the process to prevent or mitigate the
release of hazardous chemicals need to be evaluated and strength¬
ened to ensure their effectiveness at each level. Process safety
management is the proactive identification, evaluation and mitigation
or prevention of chemicai releases that could occur as a result of
failures in processes, procedures, or equipment.
The process safety management standard targets highly hazardous
chemicals that have the potential to cause a catastrophic incident.
The purpose of the standard as a whole is to aid employers in their
efforts to prevent or mitigate episodic chemical releases that could
lead to a catastrophe in the workplace and possibly in the surround¬
ing community.
To control these types of hazards, employers need to develop the
necessary expertise, experience, judgement, and initiative within
their work force to properly implement and maintain an effective
orocess safetv manaoement orooram as envisioned in the Occuoa-
tional Safetv and Health Administration fOSHA) standard.
- — _ — - .. . . ^ ^
The OSH.A standard is required by the Clean Air Act Amendments,
as is the Environmental Protection .Agency’s Risk Management Plan,
which will be proposed in 1992. Employers who merge the two sets
nf roni lirnmontc intn thoir nrnr'occ cafot\/ mananomont nrnnram will
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/niiiiuuyii ir\ uciiovoo oaioiy iiianay^iiicsiu win iicavc? a
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puijilivc? uii Lilt? tiaiciy ui eiiipiuyctJt) aiiu win uiit;i uiiici [juLt?ii-
tial banefits to ernpioysrs, such as incrGased productivity, smalisr
businsssGS that may havG iimitGd rssourcGS availabiG to thorn at this
1
time, might consider alternative avenues of decreasing the risks
associated with highly hazardous chemicals at their workplaces.
One method that might be considered is reducing inventory of the
highly hazardous chemical. This reduction in inventory will result in
reducing the risk or potential for a catastrophic incident. Also,
employers, including small employers, may establish more efficient
inventory control by reducing, to below the established threshold, the
quantities of highly hazardous chemicals onsite. This reduction can
be accomplished by ordering smaller shipments and maintaining the
minimum inventory necessary for efficient and safe operation. When
reduced inventory is not feasible, the employer might consider
dispersing inventory to several locations onsite. Dispersing storage
into locations so that a release in one location will not cause a
release
in another location is also a practical way to reduce the risk
or potential for catastrophic incidents.
Pvr'ontinnc
The PSM standard does not apply to the following:
• Oil or gas well drilling or servicing operations;
• Normally unoccupied remote facilities;
• Hydrocarbon fuels used solely for workplace consumption as a fuel
(e.g., propane used for comfort heating, gasoline for vehicle
refueling), if such fuels are not a part of a process containing
another highly hazardous chemical covered by this standard; or
• Flammable liquids stored in atmospheric tanks or transferred,
which are kept below their normal boiling point without benefit of
chilling or refrigerating and are not connected to a process.
Process Safety Information
Hazards of the Chemicals Used in the Process
Complete and accurate written information concerning process
chemicals, process technology, and process equipment is essential
to an effective process safety management program and to a pro¬
cess hazard anaivsis. The comoiled information will be a necessary
resource to a variety of users including the team performing the
process hazard analysis as required by PSM; those developing the
2
E
training programs and tha operating procedures; contractors whose
Amployees will be working with, the process; those conducting the
pre-sta.hup reviews; as well as local emergency preparedness
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corrosion and erosion effects on the process equipment and monitor¬
ing tools. Current materia! safety data sheet (MSDS) information can
be used to help meet this requirement but must be supplemented
with process chemistry information, including runaway reaction and
over-pressure hazards, if applicable.
I echnoiogy of the process
Process technology information will be a part of the process safety
information package and should include employer-established
criteria for maximum inventory levels for process chemicals; limits
beyond which would be considered upset conditions: and a qualita¬
tive estimate of the consequences or results of deviation that could
occur if operating beyond the established process limits. Employers
are encouraged to use diagrams that will help users understand the
process.
A block flow diagram is used to show the major process equipment
and interconnecting process flow lines and flow rates, stream
composition, temperatures, and pressures when necessary for
claritv. The block flow diaaram is a simolified diaaram.
Process flow diagrams are more com.plex and show all main flow
streams including valves to enhance the understanding of the
process as well as pressures and tem'^eratu.''es on all feed a.nd
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luico die oiiuwii wild I I ic?oci>iacii y lui uictiiiy. in duuiuuii, }jiuv^C 5 »i> iiuw
uidyrduis LisUdlly show majOf compORGnts of control loops along with
i\fc?y uiiiiutJb.
4
Wastewater
Treatment
System
Equipment in the Process
Piping and instrument diagrams (P&IDs) may be the more appropri¬
ate type diagrams to show some of the above details as well as
display the information for the piping designer and engineering staff.
The P&IDs are to be used to describe the relationships between
equipment and instrumentation as well as other relevant information
that will enhance clarity. Computer software programs that do P&IDs
or other diagrams useful to the information package may be used to
help meet this requirement.
The information pertaining to process equipment design must be
documented. In other words, what codes and standards were relied
on to establish good engineering practice? These codes and
standards are published by such organizations as the American
Society of Mechanical Engineers, the American Petroleum Institute,
American National Standards Institjjte, National Fire Prot^tion
Association, American Society for Testing and Materials, The
National Board of Boiler and Pressure Vessel inspectors. National
Association of Corrosion Engineers, American Society of Exchange
Manufacturers Association, and Model Building Code groups.
For existing equipment designed and constructed many years ago in
accordance with the codes and standards available at that time and
no longer in general use today, the employer must document which
cooes ana stanoaros were useo ana tnat tne aesign ana construction
along with the testing, inspection, and operation are still suitable for
the intended use. Where the process technology requires a design
that departs from the applicable codes and standards, the employer
iiiust document that the design and construction are suitable for the
intended purpose.
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r 0 pr 0 C 0 ntgti\/ 0 s informed about relevant safety and health issues and
may be able to adapt these practices a.nd procedui'es to meet their
obligations under PSM.
5
Employers who have not implemented an occupational safety and
health program may wish to form a safety and health committee of
employees and management representatives to help the employer
meet the PSM obligations. Such a committee can be a significant
ally in helping the employer implement and maintain an effective
process safety management program for all employees.
Process Hazard Analysis
A process hazard analysis (PHA), or evaluation, is one of the most
important elements of the process safety management program. A
PHA is an organized and systematic effort to identify and analyze the
significance of potential hazards associated with the processing or
handling of highly hazardous chemicals. A PHA provides information
that will assist employers and employees in making decisions for
improving safety and reducing the consequences of unwanted or
unplanned releases of hazardous chemicals.
A PHA analyzes potential causes and consequences of fires, explo¬
sions, releases of toxic or flammable chemicals, and major spills of
hazardous chemicals. The PHA focuses on equipment, instrumenta¬
tion, utilities, human actions (routine and nonroutine), and external
factors that might affect the process.
The selection of a PHA methodology or technique will be influenced
by many factors including how much is known about the process. Is
it a process that has been operated for a long period of time with little
or no innovation and extensive experience has been generated with
its use? Or, is it a new process or one that has been changed
frequently by the inclusion of innovation features? Also, the size and
complexity of the process will influence the decision as to the appro¬
priate PHA methodology to use. All PHA methodologies are subject
to certain limitations. For example, the checklist methodology works
well when the process is very stable and no changes are made, but it
is not as effective when the process has undergone extensive
change. The checklist may miss the most recent changes and
consequently they would not be evaluated. Another limitation to be
considered concerns the assumptions made by the team or analyst.
The PHA is dependent on good judgement and the assumptions
made during the study need to be documented and understood by
the team and reviewer and kept for a future PHA.
The team conducting the PHA needs to understand the methodology
that is going to be used. A PHA team can vary in size from two
people to a number of people with varied operational and technical
backgrounds. Some team members may be part of the team for only
6
a limited time. The team leader needs to be fully knowledgeable in
the proper implementation of the PHA methodology to be used and
should be impartial in the evaluation. The other full or part-time team
members need to provide the team with expertise in areas such as
process technology: process design; operating procedures and
practices; alarms; emergency procedures; instrumentation; mainte¬
nance procedures, both routine and nonroutine tasks, including how
the tasks are authorized; procurement of parts and supplies; safety
and health; and any other relevant subjects. At least one team
member must be familiar with the process.
The ideal team will have an intimate knowledge of the standards,
codes, specifications, and regulations applicable to the process
being studied. The selected team members need to be compatible
and the team leader needs to be able to manage the team and the
PHA study. The team needs to be able to work together while
benefiting from the expertise of others on the team or outside the
team to resolve issues and to forge a consensus on the findings of
the study and recommendations.
The application of a PHA to a process may involve the use of
different methodologies for various parts of the process. For ex¬
ample, a process involving a series of unit operations of varying
sizes, complexities, and ages may use different methodologies and
team members for each operation. Then the conclusions can be
integrated into one final study and evaluation.
A more specific example is the use of a PHA checklist for a standard
boiler or heat exchanger and the use of a Hazard and Operability
PHA for the overall process. Also, for batch-type processes like
custom batch operations, a generic PHA of a representative batch
may be used where there are only small changes of monomer or
other ingredient ratio and the chemistry is documented for the full
range and ratio of batch ingredients. Another process where the
employer might consider using a generic type of PHA is a gas plant.
Often these plants are simply moved from site to site, and therefore,
a generic PHA may be used for these movable plants. Also, when
an employer has several similar size gas plants and no sour gas is
being processed at the site, a generic PHA is feasible as long as the
variations of the individual sites are accounted for in the PHA.
Finally, when an employer has a large continuous process with
several control rooms for different portions of the process, such as
for a distillation tower and a blending operation, the employer may
wish to do each segment separately and then integrate the final
results.
7
Small businesses covered by this rule often will have processes that
have less storage volume and less capacity and may be less compli-
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anticipate that the less complex methodologies would be used to
meet the process hazard analysis criteria in the standard. These
process hazard analyses can be done in less time and with fewer
peopie being involved. A less complex process generally means that
less data, P&lDs, and process information are needed to perform a
process hazard analysis.
Many small businesses have processes that are not unique, such as
refrigerated warehouses or cold storage lockers or water treatment
facilities. Where employer associations have a number of members
with such facilities, a generic PHA, evolved from a checklist or what-
if questions, could be developed and effectively used by employers
to reflect their particular process; this would simplify compliance for
them.
When the employer has a number of processes that require a PHA,
the employer must set up a priority system to determine which PHAs
to conduct first. A preliminary hazard analysis may be useful in
ooiLiM^ ^iiuiiifob lui iMc; pivjoooooo ii id.i it lo i iGo 11 m lou
are subject to coverage by the process safety management stan¬
dard. Consideration should be given first to those processes with the
potential of adversely affecting the largest number of employees.
This priority setting also should consider the potential severity of a
chemical release, the number of potentially affected employees, the
operating history of the process, such as the frequency of chemical
releases, the age of the process, and any other relevant factors.
Together, these factors would suggest a ranking order using either a
weighting factor system or a systematic ranking method. The use of
a preliminary hazard analysis will assist an employer in determining
which process should be of the highest priority for hazard analysis
resulting in the greatest improvement in safety at the facility occur¬
ring first.
W Q+^ r pn I ^/-i
Detailed guidance on the content and application of process hazard
analysis methodologies is available from the American Institute of
Chemical Engineers’ Center for Chemical Process Safety, 345 E.
47th Street, New York, New York 10017, (212) 705-7319. Also, see
the discussion of various methods of process hazard analysis
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Operating Procedures
Operating procedures describe tasks to be performed, data to be
recorded, operating conditions to be maintained, samples to be
8
collected, and safety and health precautions to be taken. The
nrocfidura.s need to be technicallv accurate, understandable to
j_ _______ ___ — - .
employees, and revised periodically to ensure that they reflect
current operations. The process safety information package helps to
ensure that the operating procedures and practices are consistent
with the known hazards of the chemicals in the process and that the
operating parameters are correct. Operating procedures should be
reviewed by engineering staff and operating personnel to ensure
their accuracy and that they provide practical instructions on how to
actually carry out job duties safely. Also the employer must certify
annually that the operating procedures are current and accurate.
Operating procedures provide specific instructions or details on what
steps are to be taken or followed in carrying out the stated proce¬
dures. The specific instructions should include the applicable safety
precautions and appropriate information on safety implications. For
example, the operating procedures addressing operating parameters
will contain operating instructions about pressure limits, temperature
ranges, flow rates, what to do when an upset condition occurs, what
alarms and instruments are pertinent if an upset condition occurs,
and other subjects. Another example of using operating instructions
to properly implement operating procedures is in starting up or
shutting down the process. In these cases, different parameters will
be required from those of normal operation. These operating
instructions need to clearly indicate the distinctions between startup
and normal operations, such as the appropriate allowances for
heating up a unit to reach the normal operating parameters. Also,
the operating instructions need to describe the proper method for
increasing the temperature of the unit until the normal operating
temperatures are reached.
Computerized process control systems add complexity to operating
instructions. These operating instructions need to describe the logic
_XI_
OT irie soiiware as wen as [ne reiauonsnip oexween me equipmeru
and the control system; otherwise, it may not be apparent to the
upeiaiui.
Operating procedures and instructions are important for training
operating personnel. The operating procedures are often viewed as
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9
maintenance department (like changing a valve from steel to brass
or other subtle changes) need to be evaluated to determine whether
operating procedures and practices also need to be changed. All
management of change actions must be coordinated and integrated
with current operating procedures, and operating personnel must be
alerted to the changes in procedures before the change is made.
When the process is shut down to make a change, then the operat¬
ing procedures must be updated before re-starting the process.
Training must include instruction on how to handle upset conditions
as well as what operating personnel are to do in emergencies such
as pump seal failures or pipeline ruptures. Communication among
operating personnel and workers within the process area performing
nonroutine tasks also must be maintained. The hazards of the tasks
are to be conveyed to operating personnel in accordance with
established procedures and to those performing the actual tasks.
When the work is completed, operating personnel should be in¬
formed to provide closure on the job.
Employ66 Trsiniiiy
All employees, including maintenance and contractor employees
iiivuivt^u wiui Hiyiiiy iia^^aiuuu:) iiecu lu luiiy uiluctoiailu
the safety and health hazards of the chemicals and processes they
v¥wir\ vviiii ov^ II loy woi i u loiiuvv i ipi\^y
and the citizens of nearby communities. Training conducted in
compliance with the OSHA Hazard Communication standard {Title
2Q nf Forloral Roniilatinnc Part 1010 1900^ will infnrrn
em.ployees about the chem.icals they work with and familiarize them
with reading and understanding MSDSs. However, additional
traininn in .«;nhiflr:tc; siioh a?? nneratinn nrnraHiirp*? and work
.C? —J -- p,. --
oractices. emeraencv evacuation and resoonse. safetv orocedures.
I-»- ’if -V --- ----,---^ i- ----»
routine and nonroutine work authorization activities, and other areas
pertinent to process safety and health need to be covered by the
emolover’s trainina orooram.
In establishing their training programs, employers must clearly
identify the employees to be trained, the subjects to be covered, and
the goals and objectives they wish to achieve. The learning goals or
objectives should be written in clear measurable terms before the
training begins. These goals and objectives need to be tailored to
each of the specific training modules or segments. Employers
should describe the important actions and conditions under which
the employee will demonstrate competence or knowledge as well as
what is acceptable performance.
10
Hands-on training, where employees actually apply lessons learned
in simulated or real situations, will enhance learning. For example,
ooeratino oersonnel. who will work in a control room or at control
oanels. would benefit bv beina trained at a simulated control oanel.
W I
Upset conditions of various types could be displayed on the simula¬
tor, and then the employee could go through the proper operating
procedures to bring the simulator pane! back to the normal operating
parameters. A training environment could be created to help the
trainee feel the full reality of the situation but under controlled
conditions. This type of realistic training can be very effective in
teaching employees correct procedures while allowing them also to
see the consequences of what might happen if they do not follow
established operating procedures. Other training techniques using
videos or training also can be very effective for teaching other job
tasks, duties, or imparting other important information. An effective
training program will allow employees to fully participate in the
training process and to practice their skills or knowledge.
Employers need to evaluate periodically their training programs to
see if the necessary skills, knowledge, and routines are being
properly understood and implemented by their trained employees.
The methods for evaluating the training should be developed along
with the training program goals and objectives. Training program
evaluation will help employers to determine the amount of training
their employees understood and whether the desired results were
obtained. If, after the evaluation, it appears that the trained employ¬
ees are not at the level of knowledge and skill that was expected, the
employer should revise the training program, provide retraining, or
provide more frequent refresher training sessions until the deficiency
is resolved. Those who conducted the training and those who
ro/^oi\/oH tho traininn alcn chniilH ho rnnciiltoH ac tn hnw hoct tn
I W ITWSk* IIIW WW I WAW
imnrnvo tho traininn nrnoocic; If thoro Iq a lanniiano harrior tho
. .jj .. ^ •'-■••a—a'' . ..
language known to the trainees should be used to reinforce the
training messages and information.
Careful consideration must be oiven to ensure that emolovees.
includina maintenance and contract emolovees. receive current and
w I y '
updated training. For example, if changes are made to a process,
affected employees must be trained in the changes and understand
the effects of the changes on their job tasks. Additionally, as already
discussed, the evaluation of the employee’s absorption of training
will certainly determine the need for further training.
11
Contractors
Employers who use contractors to perform work in and around
processes that involve highly hazardous chemicals have to establish
a screening process so that they hire and use only contractors who
accomplish the desired job tasks without compromising the safety
and health of any employees at a facility. For contractors whose
safety performance on the job is not known to the hiring employer,
the employer must obtain information on injury and illness rates and
experience and should obtain contractor references. In addition, the
employer must ensure that the contractor has the appropriate job
skills, knowledge, and certifications (e.g., for pressure vessel weld¬
ers). Contractor work methods and experience should be evaluated.
For example, does the contractor conducting demolition work swing
loads over operating processes or does the contractor avoid such
hazards?
Maintaining a site injury and illness log for contractors is another
method employers must use to track and maintain current knowledge
of activities involving contract employees working on or adjacent to
processes covered by PSfvi. injury and illness logs of both the
employers employees and contract employees aiiow the employer to
have full knowledge of process injury and illness experience. This
log contains information useful to those auditing process safety
management compliance and those involved In incident investiga¬
tions.
Contract employees must perform their work safely. Considering
thot r>Qrfr\rm \/£^r\/ or^^r*!lallTcaW ranW rarv+on+foll\/
1.1 lUl WUI III OVLV./I O Oil 1V.4 I III 04.11
ha'^iarWriMe tacLre eimh ae r»nnfin^H enar'o ontr\/ ar*ti\/itiQC qhH
I I OXWI II 11 lO.'V 4 VI V « VAIIS<«
nnnrnntino ronair artix/itioe thoir mi ict ho pnntrnlloH \A/hiio thov
llV/IIIWVJVillW V«VO/VI VII.IV.AWf VllWiI «VVi/ll\ IIIWWV WW WW ItVIWIlWW VVIIIIW VI
are on or near a process covered by PSM. A permit system or work
authorization system for these activities is helpful for all affected
employers. The use of a work authorization system keeps an
employer informed of contract employee activities. Thus, the em¬
ployer has better coordination and more management control over
the work beino oerformed in the orocess area. A well-run and well-
W I I
maintained orocess. where emolovee safetv is fully recoonized,
I ' I ^ ^ ^ w *
benefits all of those who work in the facility whether they are employ¬
ees of the employer or the contractor.
Pre-Startup Safety Review
For new processes, the employer will find a PHA helpful in improving
the design and construction of the process from a reliability and
quality point of view. The safe operation of the new process is
enhanced by making use of the PHA recommendations before final
19
rnctallatinnc aro
.•r'*.
IW bV« 4 l IMfci W I iw Ml M WM •
PAIHc chniilH ho rnmnlotoH
*... ... .......-- .... ....... j
W< IMVIIW* MW WWI
tho nnorat-
VI IW Wf^WI w«v
ing procedures put in place, and the operating staff trained to run the
process, before startup. The initial startup procedures and normal
operating procedures must be fully evaluated as part of the pre¬
startup review to ensure a safe transfer into the normal operating
mode.
For existing processes that have been shutdown for turnaround or
modification, the employer must ensure that any changes other than
“replacement in kind” made to the process during shutdown go
through the management of change procedures. P&IDs will need to
be updated, as necessary, as well as operating procedures and
instructions. If the changes made to the process during shutdown
are significant and affect the training program, then operating
personnel as well as employees engaged in routine and nonroutine
work in the process area may need some refresher or additional
training. Any incident investigation recommendations, compliance
audits, or PHA recommendations need to be reviewed to see what
affect they may have on the process before beginning the startup.
Mechanical integrity of Equipment
Employers must review their maintenance programs and schedules
to see if there are areas where “breakdown” maintenance is used
rather than the more preferable on-going mechanical integrity
piuyiciin. cquipiiitti iL ubfcju iu pfuuwyb, biurt?, ui iiciiiuitJ iiiyniy
hazardous chemicals has to be designed, constructed, installed, and
mciiniciinBu lu ilui ihu 1 15r\ ui iOi buun ui i@ii iludiS. 1 1 ilS
requires that a mechanical integrity program be in place to ensure
II ^UIIIIIIU^U llll^^iliy piWOOOO I II.
Pliamiante ni a m£i/^hQnir>' 5 l int/ 3 nrit\/ nronrom ir>r>li iHo iHontif\/in/-i anH
I—.IWi I IV./I IVv7 Wi M I I IMMI IMI IIWMI lltLW^Illjr IIIWIWMW (W W I I VI > ^ J ■ ■ ^ MIIW*
categorizing equipment and instrumentation, inspections and tests
anH thair fronnannw maintonanra nmraHitrac traininn nf mainta-
ViAl IW VllWfl liw^wwiiwy^ II I W.I I I V W I • V.VI IWW ^IWWWWWIWWf VI M.I I I I I 1^ W • II ■ Vi>VI I • V w
na.nce personnel; criteria for acceptable test results; documentation
of test and inspection results; and documentation of manufacturer
mnommanriationfi for enuinmont and in.«;trtjmentation.
Process Defenses
The first line of defense an employer has is to operate and maintain
the process as designed and to contain the chemicals. This is
backed up by the second line of defense which is to control the
release of chemicals through venting to scrubbers or flares, or to
surge or overflow tanks designed to receive such chemicals. This
also would include fixed fire protection systems like sprinklers, water
r\r rlr^li nrio i-*i irnr* r^iL^QC» ricic*rlr'aim^/^/n
o|jiciy, ui ucjluyc; oyotcjiiio, iiiwiitiwi ^ui lo, wirv^o, u^oi^i ic7v^ vuiciiiici^o
systems, and other systems to control or mitigate hazardous chemi-
i^ole nn^Q Qn tmu/antoH rolosca nr'r'iire
\/l IV/Sm' V<l I V I ■ V* Wil • VV'V^ I N.^lV'ViOi.^S.^ V/WN^^l W*
Writton PrnroHiir^Q
«*ia%«w«a • ■ w w%r« ^ ■ ^iir%iir
THa first stp»n nf an affantiva manhanirial intanritv nrnnram is tn
nnmnile and oateoorize a list of nrocess eouioment and instrumenta-
--I-— - -- ^ ~ - ---- I--1— I--- -*--- -—---
tion to include in the program. This list includes pressure vessels,
storage tanks, process piping, relief and vent systems, fire protection
svstem comoonents. emeraencv shutdown systems and alarms, and
J I ' w ^ ^
interlocks and pumps. For the categorization of instrumentation and
the listed equipment, the employer should set priorities for which
pieces of equipment require closer scrutiny than others.
Inspection and Testing
The mean time to failure of various instrumentation and equipment
parts would be known from the manufacturer’s data or the
employer’s experience with the parts, which then influence inspec¬
tion and testing frequency and associated procedures. Also, appli¬
cable codes and standards—such as the National Board Inspection
Code, or those from the American Society for Testing and Materials,
American Petroleum institute. National Fire Protection Association,
American National Standards institute, American Society of Me¬
chanical Engineers, and other groups—provide information to help
establish an effective testing and inspection frequency, as well as
appropriate methodologies.
The applicable codes and standards provide criteria for external
II Id^J^UllUI lO lUI OUUI I KOI i lO 0.0 l\JUI lUOllUI I Oi lU OU|J|.^UI lO^ Ol lUI IWI
r\r /^i ix/ rc* rMr%Q
V^UliUiCLO UI Ol^^l OU}^|JUllO, ^uy VVII^O, l lU^^lOO OMU opi II ir\lUI O,
/>rxofin/^o onH ir»oi
1 lOi Oy UUI lull 1^ UUI II lUUliUI lO, pi UlUUll VU UUOLII 1^0 Ol lU 11 lOUIOLIUI ly
and external metal surfaces of piping and vessels. These codes and
ctanrlarrlc alor\ nrnv/irlo infnrmatinn nn mothn/Hnlnnioc fnr intornal
«^LOI iV,.<Oi VIW II ii W I I I I V>'i • V/ii I I i-s-^Vi iwawiwy iww »wi iiiwiiiViAi
inspection and a frequency formula based on the corrosion rate of
the materials of construction. .Also, i.nternal and e.xterna! erosion
must be considered along with corrosion effects for piping and
vfllvpc; Whpirfl thft cnrrn.«;inn ratp i.c; not known, e maximum insoec-
tion frpouencv is recommended (methods of develooino the corro-
-.... 1 _— —.. . _ -- _ ^
sion rate are available in the codes). Internal inspections need to
cover items such as the vessel shell, bottom and head; metallic
linings; nonmetallic linings; thickness measurements for vessels and
piping; inspection for erosion, corrosion, cracking and bulges;
internal equipment like trays, baffles, sensors and screens for
erosion, corrosion or cracking and other deficiencies. Some of these
14
inspections may be performed by state or local government inspec¬
tors under state and local statutes. However, each employer must
develop procedures to ensure that tests and inspections are con¬
ducted properly and that consistency is maintained even where
different employees may be involved. Appropriate training must be
provided to maintenance personnel to ensure that they understand
the preventive maintenance program procedures, safe practices, and
the proper use and application of special equipment or unique tools
that may be required. This training is part of the overall training
program called for in the standard.
Quality Assurance
A quality assurance system helps ensure the use of proper materials
of construction, the proper fabrication and inspection procedures,
and appropriate installation procedures that recognize field installa¬
tion concerns. The quality assurance program is an essential part of
the mechanicai integrity program and wiii help maintain the primary
and secondary lines of defense designed into the process to prevent
unwanted chemical releases or to control or mitigate a release. “As
built” drawings, together with certifications of coded vessels and
other equipment and materials of construction, miust be verified and
retained in the quality assurance documentation.
Equipment installation jobs need to be properly inspected in the field
for use of proper materials and procedures and to ensure that
qualified craft workers do the job. The use of appropriate gaskets,
packing, bolts, valves, lubricants and welding rods needs to be
vorifiorl in fho fiolH Alcn nrnnorli iroc fnr inctallinn cafcit\/ rlo\/inoo
V V./1 i I is^VhI 111 li i\«/ ii>^i\.4. ^1 Vi^O iv«ii li tO li I 1^ %.7<^iv^i.jr \.<iv^vivxwO
nood tn ho \/orifipH ci irh ac tho tnrniio on tho hnitc nn riintnro Hicn
inctallatinni; imjfnrm tnrniio nn flanno hnltQ and nrnnor incitallatinn nf
I I 1V V liwy VIIIIWIIII V*l l WI»V) ^^1 'V P^IV^VI fiiv hMI I VII VI
pump seals. If the quality of parts is a problem, it may be appropri¬
ate for the employer to conduct audits of the equipment supplier’s
facilities to better ensure orooer ourchases of reauired eouioment
suitable for intended service. Anv chanoes in eouioment that mav
-- - _ -- - — _____ __ _ .. —
become necessary will need to be reviewed for management of
chanae orocedures.
Nonroutine Work Authorizations
Nonroutine work conducted in process areas must be controlled by
the employer in a consistent manner. The hazards identified involv¬
ing the work to be accomplished must be communicated to those
doing the work and to those operating personnel whose work could
affect the safety of the process. A work authorization notice or
permit must follow a procedure that describes the steps the mainte-
15
nance supervisor; contractor representative, or other person needs
to follow to obtain the necessary clearance to start the job. The work
authorization orocedures must reference and coordinate, as aoDli-
I * I I
cable, lockout/tagout procedures, line breaking procedures, confined
space entry procedures, and hot work authorizations. This proce¬
dure also must provide clear steps to follow once the job is com¬
pleted to provide closure for those that need to know the job is now
completed and that equipment can be returned to normal.
Managing Change
To properly manage changes to process chemicals, technology,
equipment and facilities, one must define what is meant by change.
In the process safety management standard, change includes all
moaiTications to equipment, proceoures, raw materials, ano process¬
ing conditions other than “replacement in kind.” These changes
must be properly managed by identifying and reviewing them prior to
implementing them. For example, the operating procedures contain
\irr\ 'rr\}r\nr\e^
LI 1 C upciaiiiiy paiaiMcicid ^{jicoouic iiinuo, iciii}jci aiuic laii^co, iiwvv
rates, etc.) and the importance of operating within these limits. While
+h^ mi let ha\/n fhz:i flnviKilit\/ +r\ mQin+ain eofo r\r\oratir\n
il QilVi/l MlUOi IIUV^ kl I IW I I ICail ItUiil I OUIW ULiWI I
within the established parameters, any operation outside of these
parameters requires review and approval by a written management
of change procedure. Management of change also covers changes
in process technology and changes to equipment and instrumenta¬
tion. Changes in process technology can result from changes in
production rates, raw materials, experimentation, equipment unavail¬
ability, new equipment, new product development, change in cata¬
lysts, and changes in operating conditions to improve yield or quality.
Equipment changes can be in materials of construction, equipment
specifications, piping pre-arrangements, experimental equipment,
computer program revisions, and alarms and interlocks. Employers
must establish means and methods to detect both technical and
mechanical changes.
Temporary changes have caused a number of catastrophes over the
years, and employers must establish ways to detect both temporary,
and permanent changes. It is important that a time limit for temporary
changes be established and monitored since otherwise, without
control, these changes may tend to become permanent. Temporary
changes are subject to the management of change provisions. In
addition, the management of change procedures are used to ensure
+ i r\r
Li lai LI ic; I loi iL ai lu pi u^c:;uui oo aic; ic;lumiou lu Liic;ii wii^iiiai ui
designed conditions at the end of the temporary change. Proper
imontati/^n anri m\/i£i\A/ nf thoco r^hanncio Jnx/csli iqKIo in
WV/V>V^I I IWI li.Ci.LIV/1 I i\jt IV^^VIWW Wl lUI ^ II i V III
ensuring that safety and health considerations are incorporated into
16
operating procedures and processes. Employers may wish to
develop a form or clearance sheet to facilitate the processing of
changes through the management of change procedures. A typical
change form may include a description and the purpose of the
change, the technical basis for the change, safety and health consid¬
erations, documentation of changes for the operating procedures,
maintenance procedures, inspection and testing, P&IDs, electrical
classification, training and communications, pre-startup inspection,
duration (if a temporary change), approvals, and authorization.
Where the iiiipact of the change is minor and well understood, a
check list reviewed by an authorized person, with proper communi-
uauuH Lu uuicio wiiu aic? aiicuicu,
oaiiipio lov^uooi lui
pi UUOVJUl o.y
Ul 10.1 1^0 lUi II 1
Midy ouiiiot?. (occ; riyuid lur d
♦ ^\y^ ^\y*\lr^^i li I y^i iiWir^y^ + 1 - 1 !/^
u loi uoi I uc? i loipiui 111 yululi ly ii ii;d
Pr>r a mnr£i r'nmnlciv nr einnifi^ont Hcioiyin hr>\A#Q\/Qr a hoTorrl
1 V/l U I I ivyi ^ WWI ll|...lV^r\ Wl ^1^1 III IV..UI IL W^OI^I I OIIUII^^, IIWVV^VWI, GL I lUA-Cil \J
o\/aliiatinn nrn^oHiiro w/ith annrn\/alc h\/ nnoratinnc maintonanr'Q
W V I WWWWI>4I W fVIbll W V 1.41 wjr 1 <^LI W I lO ^ I I I Ul I I VVy I i Ui I Vi/j
and safety departments may be appropriate. Changes in documents
such as P&IDs, raw materials, operating procedures, mechanical
intenritv nrnnrams. and plartrioal rlaaaifiratinn.Q ahniilH hp nntpH an
.. ..wg. ..y p,. W.. . . —, ---- ----- ww
that these revisions can be made pe.rmanent when the drawings and
procedure manuals are updated. Copies of process changes must
be keot in an accessible location to ensure that desion chanoes are
available to operating personnel as well as to PHA team members
when a PHA is being prepared or being updated.
Incident investigation
Incident investigation is the process of identifying the underlying
causes of incidents and implementing steps to prevent similar events
from occurring. The intent of an incident investigation is for employ¬
ers to learn from past experiences and thus avoid repeating past
mistakes. The incidents OSHA expects employers to recognize and
to investigate are the types of events that resulted in or could rea¬
sonably have resulted in a catastrophic release. These events are
sometimes referred to as “near misses,” meaning that a serious
consequence did not occur, but could have. (See Figure 3 for
sample incident investigation report form.)
tmpioyers must oeveiop in-nouse capaoiiity to investigate mcioents
that occur in their facilities. A team should be assembled by the
_
ernpiuyer anu ira'iiea in me lecnniques oi invesiigaiion inciuomg now
to conduct interviews of witnesses, assemble needed documenta¬
tion, and write reports.
A iiiulti-discipiinary team is better able to
gather the facts of the event and to analyze them and develop
piauDiuic ou^iianuo ao ikj vviiai iiaypciicu, emu vviiy.
1 ^Cll i I 11 lOi I lU^l O
17
> rTiM^lriid'
Infomiation about the ChanBe:
Originator
Date of Origination
Proposed Date of Change
Area
a Permanent o Temporary From
To
Descriotion and Location of Chanoe fScooe)
Ttv^nirval Qaeie fnr
ICV^tUllWCU Wgjtj IVA W(>CU<^D
Nature of the Change:
Change affects;
□ Safety □
Loss Prevention
□
Type of Change:
a Alarm d
Shutdown Point
□
u ripiiiy niuuiiiudijufi u
CnemlCSi
U
D Job Procedure Q
Instrument
□
□ Other
Environment □ Health
Addition or Removal of Equipment
Pro(^33 CciTipufsr Control
Equipment/Material Modification
PremodHleation
Applicable NA
Chaekllste ^
Ini^S \ ■’
Q
o
□
n
a
c
Q
□
n
Q
O
a
□
□
□
n
□
□
□
□
□
c
□
□
□
□
Q
O
□
□
□
□
Consiit piping and equipment specfi^Jons.
Perform reactive chemicals testing. □ In process?
Add involved maiehais to Toxic Substance Control Act (TSCA) inventory.
Cateilata impact on F&Ei and CEi.
Complf «ritti Engineering Practices.
Con^ with Technology Center guidelines.
Comply vifitt) Dow Enyironmental Protecdon Guideline for Qper^ons.
Comply with Safety ani Loss Prevention requirements.
Consult mantenaritslname)_
Consult inswmentand efearical technician (name)_
Consult parts' technician (name)_
Evaluate and modify relief ^stem (name)_
Consult Industrial Hy^'ene (name)_
Consult Process En^eering (name)_
Complete required reviews (name reviews)_
Other_~ ■ _
PostmodHication Checklist (Before Startup):
Applicable
n/A
initials
n
□
_Pprfnfmad nfP<aartirn audit
□
a
Completed or updated training program.
□
□
Wrote and obtained approval tor job procedures.
□
Q
llnriatpd PRID."; nrorp^i; flow ?hAPt$ and pint plane
□
□
Trained personnel on the change.
□
□
Updated cntical instrument checklist.
□
□
Ch.ar!Q6(3 Gornoutsf cods snd doojmsntstiQn.
Approvals: Name Date
Originator _
First Reviewer _
Department Head/Superintendent _
CotporaW S/LP/S
• iwc.
Reprinted with permission of Dow Chemical U$A,
2020 Dow Center. Midland, Mi 48762.
Figure 2
National Safety Council
ACCIDENT INVESTIGATION REPORT
COMPANY_
DEPARTMENT_
1. NAME of INJURED
6. HOME ADDRESS
_ADDRESS_
. LOCATION (if different from mailing address)_
I 2. SOCIAL SECURITY NUMBER | 3. SEX
3. SEX
4 AGE
CM OF
7 EMPLOYEE'S USUAL OCCUPATION 8. OCCUPATION at TIME of ACCIDENT
11- EMPLOYMENT CATEGORY
□ RegiMar, fulPttme □ Temoorary □ Nonemoioyee
□ Regular, part-time □ Seasonal
13, NATURE of INJURY and PART of BODY
9, LENGTH Of EMPLOYMENT 10. TIME m OCCUP at TIME Of ACCIDENT
D Less man i mo. G 6 mo$. to S yrs. G Less man 1 mo. G 6 mos. to 5 yrs
□ 1-5 mos C More than 5 yrs. □ 1-5 mos. D More than 5 yrs
12. CASE NUMBERS and NAMES of OTHERS INJURED in SAME ACCIDENT
14, NAME and ADDRESS of PHYSICIAN
15. NAME and ADDRESS of HOSPITAL
18. SPECIFIC LOCATION of ACCIDENT
ON EMPLOYER'S PREMISES? G Yes □ No
20. DESCRIBE HOW the ACCIDENT OCCURRED
16. TIME of INJURY 17. SEVERITY of INJURY
AM □ Fatality
A PM
■ ——— □ Lost workdays—days away from work
_ D Lost workdays—days of restncied activity
B. Time within shift
‘ - G Medical treatment
ot $mn D First aK)
^ □ Other, soecily_
19. PHASE.OF EMPLOYEE'S WORKDAY at TIME ot INJURY
During rest penod C Entenng or leaving plant
During meaf period □ Performing work duties
U Woddng ovemmt. G Other,
21. ACCIDENT SEQUENCE. Describe in reverse order of occurrence events preceding the injury and accident. Starting
with the injury and moving backwanf in time, reconstrita the sequence ot events that led to the injury.
A. Injury Event . .. _ _ ..
B. /tecident Event_ . .
C. Prweding Event #1 _
0. Preceding Event #2. #3, etc _ .
Figure 3
1
ro
l\3
22. TASK and ACTIVITY at TIME of ACCIDENT
A. General type of task_
23. POSTURE of EMPLOYEE
B. Specific acpvify
C. cffipjOim ws working:
n Aicne With crsw cr fsHcw wcrksf O Cttfw sj^cify
24 SUPERVISION at TIME ot ACaOENT
3 Directly superveed □ N« supensed
□ Indirectly supervised □ Supervisian not feasiHe
2S. CAUSAL FACTORS. Events and conditions tnat contributed to the accident include tnose
identiiied by use oi tne Guide tor Idenotyino causal Factors and Corrective Actions
€ %
26. CORRECTIVE ACTIONS. TTiose tnat nave oeen. or will be. taken to prevent recurrenctr include those
indcntiSed by use of tbe Guide for loemifying Causal Factors and Corrective Acuons.
PRFPARFn RY
APPROVFD
TITLE
TITLE
DATE
npnannai*aiT
n*Te
Roonnwcn
Heprinted with permissiQn frvm ihs NsUonst
TITLE
DArt
Safety Council. 1121 Spnng Lake Diive.
iiasca. iL SG14S-32G1
IV^
c5
Figure 3 (Continued)
should be selected on the basis of their training, knowledge, and
ability to contribute to a team effort to fully investigate the incident.
Employees in the process area where the incident occurred should
be consulted, interviewed or made a member of the team. Their
knowledge of the events represents a significant set of facts about
the incident that occurred. The report, its findings, and recommen¬
dations should be shared with those who can benefit from the
information. The cooperation of employees is essential to an effec¬
tive incident investigation. The focus of the investigation should be
to obtain facts and not to place blame. The team and the investiga¬
tive process should clearly deal with all involved individuals in a fair,
open, and consistent manner.
Emergency Preparedness
Each employer must address what actions employees are to take
when there is an unwanted release of highly hazardous chemicals.
Emergency preparedness is the employer’s third line of defense that
will be relied on along with the second line of defense, which is to
i OIWUOO Wl Wl I I IIWOIIO. N^WIILIWt Cil iv«i
preparedness will take place when the first line of defense to operate
and maintain the process and contain the chemicals fails to stop the
release. In preparing for an emergency chemical release, employers
will need to decide the following:
• Whether they want employees to handle and stop small or minor
incidental releases;
• Whether they wish to mobilize the available resources at the plant
and have them brought to bear on a more significant release;
• Whether employers want their employees to evacuate the danger
area and promptly escape to a preplanned safe zone area, and
then allow the local community emergency response organizations
to handle the release; or
• Whether the employer wants to use some combination of these
actions.
Fmninworc will noaH tn ctslart hnvA/ man\/ Hifforont omornonrs/ nro-
paredness or third lines of defense they plan to have, develop the
necessary emergency plans and procedures, appropriately train
employees in their emergency duties and responsibilities, and then
inipidltCUL U lilies Ul
24
Employers, at a minimum, must have an emergency action plan that
will facilitate the prompt evacuation of employees when there is an
unwantfid release of a hiohlv hazardous chemical. This means that
the emolover’s oian will be activated bv an alarm svstem to alert
employees when to evacuate, and that employees who are physi¬
cally impaired will have the necessary support and assistance to get
them to a safe zone. The intent of these requirements is to alert and
move employees quickly to a safe zone. Delaying alarms or confus¬
ing alarms are to be avoided. The use of process control centers or
buildings as safe areas is discouraged. Recent catastrophes indi¬
cate that lives are lost in these structures because of their location
and because they are not necessarily designed to withstand over¬
pressures from shock waves resulting from explosions in the process
area.
When there are unwanted incidental releases of highly hazardous
chemicals in the process area, the employer must inform employees
of the actions/procedures to take. If the employer wants employees
to evacuate the area, then the emergency action plan will be acti¬
vated. For outdoor processes, where wind direction is important for
selecting the safe route to a refuge area, the empioyers shouid place
a wind direction indicator, such as a wind sock or pennant, at the
highest point visible throughout the process area. Employees can
move upwind of the release to gain safe access to a refuge area by
knowing the wind direction.
If the employer wants specific employees in the release area to
control or stop the minor emergency or incidental release, these
Krt rils
0 0+
tion
- rni *ct
o H luol III civj
van
WO Cll fW \Jl wwow
I trc
ul ^
wovoiV.
l^ow oi iw
\nnr\\Qm^nfQA UIpn/HIlnn Inr'IHpntpl ir>ir minr»r pmpmonr»icsQ in
III I ^lO I 1 iOi ILO w > I II iVii«iv«40i iLcli iwiodoOo iwi iiiiiiwi Oi i lOi iwioo hi
the process area must include pre-planning, providing appropriate
oni linmont fnr thd ha-7arHc and rnnHi ir'tinn traininn fnr thnco omninu-
IWI bllV./ II Vi« W y I ^ WW blUMIIII^ IWI
ees who will pe.dorm the emergency work before they respond to
handip an artiial rfllpa.c;p, Tha amnlnvar’a traininn nrnnram- inr:lud-
ing the Hazard Communication standard training, is to address,
identify, and meet the training needs for employees who are ex-
oected to handle incidental or minor releases.
Preplanning for more serious releases is an important element in the
employer’s line of defense. When a serious release of a highly
hazardous chemical occurs, the employer, through preplanning, will
have determined in advance what actions employees are to take.
The evacuation of the immediate release area and other areas, as
necessary, would be accomplished under the emergency action
plan. If the employer wishes to use plant personnel—such as a fire
brigade, spill control team, a hazardous materials team—or employ¬
ees to render aid to those in the immediate release area and to
control or mitigate the incident, refer to OSHA’s Hazardous Waste
OpGrations and Emergency Response (HAZWOPER) standard (Title
29 CFR Part 1910.120). If outside assistance is necessa.'y, suc.h as
thrniinh mutual aid anroamontc hatwocm amnlnv/Arc and Inral
Vilivw^ll IIIWI i.vi* fciAl Wi W I I I V./ i • VW • V« IW WKiAl
nri\/ornmont omornonm/ rAcnnnco nrnaniTatinnc thoco £imarnQnA\/
^WVSyllllliWIIb WIIIWI^WI I t tKJSm* bllVi^WV>i> VirrlllWI^Vi^i t\^y
raenonricire ^Icri K\/ UiA^XA/^^PPD XHq c^afcitx/ 'anH hciral+K
i IVi4V/l ^ uiow WV./ V w j 1 l/~\^ VVWt i.ll« lll^ ly di IW I 1^:7 Ql II i
rM'/^+z:ir»tir\n rcir<iiJrciH -frvr r^r*rM^r^Wj!^r«> io r^ac^rnr^rkr^iKili-fx/ r\4^
1^1 wi^OLivyi I i^v^uiic^vj iwi C7II i^i ^^1 i\^y t ^opvji ivj^i o JO 11 iC7 i ^opwi loiuiiiiy VJl
4-k rvi r^l /^\A rxf nrt ^ *•
li iT 7 ii ^11 i|jiwyc;i o ai lu ut u lu ui I'ouci ic it luiuoi u v^ui i it iiai luoi.
RGSpondGfs may ug working undGr vary hazardous conditions;
tharGforG, thG objGCtivG is to havG tham competantiy iGd by an on-
scene incident commander and the commanders staff, properiy
equippeo lo oo ineir assigneo worK sareiy, ana ruiiy irainea lo carry
out their duties safely before they respond to an emergency. Drills,
training exercises, or simulations with the local community emer¬
gency response planners and responder organizations is one means
to obtain better preparedness. This close cooperation and coordina¬
tion between plant and local community emergency preparedness
managers also will aid the employer in complying with the Environ¬
mental Protection Agency’s Risk Management Plan criteria.'*
An effective way for medium to large facilities to enhance coordina¬
tion and communication during emergencies within the plant and with
local community organizations is by establishing and equipping an
emergency control center. The emergency control center should be
located in a safe zone so that it could be occupied throughout the
duration of an emergency. The center should serve as the major
communications link between the on-scene incident commander and
plant or corporate management as well as with local community
officials. The communications equipment in the e.mergency control
center should include a network to .'"eceive and transmit informatio.n
h\/tAipnhnnp rarlin nr nthpr mpanc It ic imnnrtant tn hp\/p p hanln in
J < «««%<■ 'Wj V' VVtIW* 111%^ IW« fV IW * b W I V bA ^
rommi ininptinnc nptu/nrU in naco nf nnw/or faili irp nr if nnp nni-nmnni.
wwiliiliwi II Vi/b^bl S./ Ilb^ IIN^bVTWII'V III WbAW Vi/ \./l ^V^VVWI IVAIIViilV^ V/l II S/lIVi/ WVa/1 I I 1 I I Vi< I M
natlnn moanc failc "Tha oontor plen chr»i ilrl ]r\ci Qrtnlrxncirl \A/lth
V./VAklV./l I IIIV./U4IIWI iVAIIV,^* IIIV^ Vi/V^ tlbV^I QiOV./ OllV^ViJlV^ ki/Vi/ Willi Llt^
r^l^nt l'3\/nMt* r'nmmi init\/ morvo* i itill+v/ innli
piai IL iClJV./UL, WVi/l I II IIUI Mljr IIIO^O, Ollllliy VUIClWltt^O) lllOlU^lIf^ VVCIIOI IWI
^\re\ mmrw *•!
liic cAiii i^uioi ill 1 ^, 17111^1 iwy ci}.^pi vjpi lai^ i oi luc;
<“*! rm rv%11/^+ i/i^/-b
aio ouwi I ao a ^uvci i ii i loi ii iwy i iwiiiiv^aiiwi \ uui i i|jai ly \jx:^\^ui i~
ir\ I ... 11 A I I A T".+1... Ill ........ ^ ..+.. .. .. A I... ^^.....aI ^ ..f..+« . A ... ^ n A U. A A ^ A
I ici [ji lui 1C iipi, o/nnr\ i me iii lepui is di lu iiidiciidi sdiciy udid t>i iccib,
emergency plans and procedures manual; a listing with the location
of emergency response equipment and mutual aid information; and
access to meteorological data and any dispersion modeling data.
'EPA is required by the Clean Air Act Amendments of 1990 to develop regulations that
will require companies to make available to the public information on the way the
companies manage Jhe risks of the chemicals they handle. These regulations will be
developed in 1992. The OSHA PSM standard, which meets similar Clean Air
Amendment requirements and the forthcoming EPA ruies, will apply only to specified
Irt J^l lr^OLJA + ta/ill /b/'ll*» + I
v/t 1711 iiuaio 111 iioi 7 u v^uai iiiuco. Nwwr ai lu u-r r*v o iidid win i lui i icucoocii ny uc luei iiiudi.
Compliance Audits
An audit is a technique used to gather sufficient facts and informa¬
tion, including statistical information, to verify compliance with
standards. Employers must select a trained individual or assemble a
trained team to audit the process safety management system and
oroaram. A small orocess or olant mav need onlv one knowledae-
I" '*-/' “• I ^ w
able oerson to conduct an audit. The audit includes an evaluation of
the design and effectiveness of the process safety management
system and a field inspection of the safety and health conditions and
practices to verify that the em.ployer’s systems are effectively imple-
montoH The ai iHit chniilH ho onnHiiotoH nr lort hv n norenn knnwl-
I f IW I I kW W • I I IW I V WW I «W Wi W VS^ W IWSta ^ J IXIIWWI
oHnoohlo in ai iHit tonhniniioc \A/hn ie imr\artial tnwarHc tho fanilitv/ nr
ViTUK/IV/ 111 VAI><<S4I W kW Wi V«IIW l«kJ III t ^IMI tW VV Ul WIW hi IW i j W f
K^ilnrt -ai rvf on oi iHit nrnnrcim
Cll ^Cl won 1^ dUWIIlOW. I I lO OOOOI ILlCll OIOI i lot no Wl C4.1 I UWWn 1^1 Vk/^I C4I I 1
Imnli iHn nlrannin/-i nnnWi mflnr^ oi iHif m/oliiotinn KoTorHo
it luiuuo pidi II Hi 1 ^, ocaiiiii^, oui iuuwlii i^ ii to ouuil, ovaiuaiiii^ iici^.ciiwo
ai lu uoi luici iooo ai lu iar\ii wuiic/ouvc auiiuii, jjoi lui 11 iii a luiiuw-up
and documenting actions taken.
Planiiirig
Planning is essential to the success of the auditing process. During
planning, auditors should select a sufficient number of processes to
give a high degree of confidence that the audit reflects the overall
level of compliance with the standard. Each employer must establish
the format, staffing, scheduling, and verification methods before
conducting the audit. The format should be designed to provide the
lead auditor with a procedure or checklist that details the require¬
ments of each section of the standard. The names of the audit team
members should be listed as part of the format as well. The check¬
list, if properly designed, could serve as the verification sheet that
provides the auditor with the necessary information to expedite the
review of the program and ensure that all requirements of the
standard are met. This verification sheet format could also identify
those elements that will require an evaluation or a response to
correct deficiencies. This sheet also could be used for developing
the follow-up and documentation requirements.
Staffina
The selection of effective audit team m.em.bers is critical to the
success of the program. Tea.m members should be chosen for t.heir
OYnarionro knnxA/lArlnp anH traininn anH QhniilH hp familiar with thp
W^^WIIV/IIWV/y ^ H • I » • 1^ • ... w w • hf • fc • • w
nroAPcoAc anH ai iHitinn tophnini loc nraptippc anH nroporii irpc Thp
WWWWWWW (.AI IV4 (UWVIIlil 1^ &WWI II 11I.J V.,/W y ^1 (..AWIIWV/Wy Ul lVi« WW* I I
r»l tHci \a/I!I \/on/ rIan/an/Hinn nn tho oi *70 canH nnmr^Iovitx/ nf
OI4.W Wl ll IW iWUI i I will VUijr WW^WI IWII Wl I II IW ^l^w Ml IVI V/N/l I l|>-^IVr/\ibjr V/*
ir\rr\r^£soo i /'/^n€?iHorotir\n o lorno r'omr^lov hinhh/
Ll
1 Uil IViWi WWI lOiVI^I ClllWI !•
Wi n ICAI^V^y WWIII^iW/\y I ll^i Ii j
if r»-»o\/ h/^ trv t^Ti-rarri \A/ith
ii iOLi ui I lOi now picii ll, ll iiiay wo uooiiciwio iw iiavo loaiii iiioiiiwoio wii^ii
OApoi u^o ill piuwooo oi lyii lool li ly ai lu uooi^ii, piwuooo Wl loi I noil y ,
KlbU Ui I lOMLdUUM Cti lU WUili|JUL 01 WUliUUIO, OlOWLf IWdl lia^aiUO Cll lU
27
w
h
classifications; safaty and health disciplines; maintenance; emer-
npnnv nrpnprpHnp*?*;' wprphni i<;inn nr Qhinninn- anri nrnnp*;*; Qafptx/
WV-. .WWW, .. W.. W. .WW.W.. w. w« . .p. ^ p^.wwwww w^.wvj
^inrlitinn Thp tppm mpv iiqp nprt-timp mpmhprQ tn nrnwirlp thp
Wil i liW I. W V^l • ■ I • WSi/ !«'«..«« b bllS.'
ovnorticp rpniiirpH anH tn nnmnaro \A/hat ic antiiallx/ Hnno nr fnlln\*/Q/H
LIWW I W V.f W4 I I V/V4 U4.IIV.il tV/ WWIIi^VAlV/ fWItVAL IW U4WLUIU4lljr V4V/ilW V# I 1 V./11W V V O V»l
\A/ifh th^ \A/ritton PQ^^ r^rr^nram
YVIVII LI tw ¥VIILL\..«il I WIVI W ^1 Ul I I •
i/%4in4^ Aiirli4
wwi iviuwiii muviii
A
rvi I
ciicuiivc auuii II iuiuu« 3 a a icvicw ui me icicvaiii uueuiiici iictuuii
and process safety information, inspection of the physical facilities,
and interviews with all levels of plant personnel. Utilizing the audit
procedure and checklist developed in the preplanning stage, the
audit team can systematically analyze compliance with the provi¬
sions of the standard and any other corporate policies that are
relevant. For example, the audit team will review ail aspects of the
training program as part of the overall audit. The team will review
the written training program for adequacy of content, frequency of
training, effectiveness of training in terms of its goals and objectives
as well as to how it fits into meeting the standard’s requirements.
Through interviews, the team can determine employees’ knowledge
and awareness of the safety procedures, duties, rules, and emer¬
gency response assignments. During the inspection, the team can
observe actual practices such as safety and health policies, proce¬
dures, and work authorization practices. This approach enables the
team to identify deficiencies and determine where corrective actions
or improvements are necessary.
Evaluation and Corrective Action
The audit team, throuoh its svstematic anaivsis, should document
areas that require corrective action as well as where the process
safety ma.nagement system is effective. This provides a record of
thA audit nrnnpdiirPA and findinnQ and Qpn/pc ac a hacpiinp nf
• w 1 >I% w w.«. piT.wwwww.ww iw ••••willow * V* W» » W VAU» V% V *
nnpratinn data fnr fiitiirp aiiditc It \A/ilI accict in dotarmlninn nhannoc
W ^ W I V 4 . Wl V • • V«U« VVA I V/ • I V« VV« I U 4 W WllkAiJ* Will VA^WI W V III V.* V^bWIIIIIIIIll^ \yl I VAI 1 ^
nr trondc in fi iti iro ai idite
Wl LlWiiVIW III IVIVVJIV^ UAVJVJIkW*
rr*£i/^+l\//::i Oi^+i/^rt io fh/ri rr^z-vof imrM^r+or-»+ r-N^r+r* tKri oi iHit •nr-iH
V.y Wl I V ^ aWLlWI I lO Wl IW Wf LI IIIWOL IllipWILdill l^dl lO Wl II Id dUWIi dl IW
II iwiuwdo ludiiiiiyiii^ udMwidi iwido, diiw fjidiiiiiii^, iwiiwvvii i^’up, ai lu
wuwui I idi iiii ly II Id wwi I dWLiwi ici. I I Id uui i duuvd duuui 1 ULid:^;:) i lui i i iciiiy
udyins With a managGiTient rGviGw of ths audit findings. Th© purposG
of this rsviGW IS to detorminG what actions ar© appropriate, and to
establish priorities, timetables, resource allocations and require¬
ments, and responsibilities, in some cases, corrective action may
involve a simple change in procedures or a minor maintenance effort
to remedy the problem. Management of change procedures need to
be used, as appropriate, even for a seemingly minor change. Many
of the deficiencies can be acted on promptly, while some may
Oft
require engineering studies or more detailed review of actual proce¬
dures and practices. There may be instances where no action is
necessary; this is a valid response to an audit finding. All actions
taken, including an explanation when no action is taken on a finding,
need to be documented.
The employer must assure that each deficiency identified is ad¬
dressed, the corrective action to be taken is noted, and the respon¬
sible audit person or team is properly documented. To control the
corrective action process, the employer should consider t.he use of a
trarlfinn cuctom Thic trarkinn cwctom minht inrliiHo norinHir ctati ic
VI WWI Mli^ wjwvwill* • IllViy VI VAV./I I W j W VW III llll^ltv IIIWIWAV^S.' ^WIIWWIIWW VVA vw* w
ronnrtc charoH \A/ith affor'toH lov/olc nf manonomont rcsnnrtc
I W i WIIUlWVxl VVIVII l^ll^WWiiWI IV^tVS^IO V^I It IVAI W I IIV^IIV) IW^WI Vv-f
Cl i/^h oc nf on onninonrinn cti irl\/ onH o finol Imnlomonto-
OUW/I I I LIWI 1 Wl Ul I ^ I i^ll 11 1^ OLUW Jf y QXt IVU Ci MItCil llll|N/IV>ifl^l liU.
+inn tn nlnciirzri frM* +Ko+
LiUI I LW piWVIWC? UIVJOUl^ lUI ClUV^IL 11 ICIL IICIV^
+ ^^ I I i-* rv^'"I ^ vn/i+K
u II uuyi I 11 lai la^oi i loi u vji ui lai i^c, ii afjpi ujji laio, anu ii ic;m oi lai cu vvui i
rv% i>N I « y ^ rv^ ^ rv>% I t ^ I ^ />%+ rv^
dit^wit^u ciiipiuyctro anu inai layci^iilai ii. i i it^ ly>>■ ciur\ii ly ::>yc>Lc;iii
provid©s thiG GmpioyGr with tuG status of tnG conGCiivG action. It also
proviuGS the documGntation required to verify that appropriate
corrective actions were taken on deficiencies identified in the audit.
Conclusion
OSHA believes the preceding discussion of PSM should help small
employers to comply more easily with the new requirements the
standard imposes. The end result can only be safer more healthful
workplace for all employees—a goal we all share.
29
ADDendix - Methods of Process Hazards Analysis
■ ■ -- — ---- j -
On July 17,1990, OSHA issued a proposed rule for the rnanagement
nf hfl7arri<; a.csRnriiatfiri with nrnnfn;Qei<; iicinn hinhlv hayarrlniic
w • • ■ ■ ww W W V « a k( * WWWWWW l ( VA>in«.iAI Wt W ^ W
nhfaminaLQ Thic riilp ralloH tho Pmoocc .Qafptu K^annnomont
WI a WI a 11 wa^aw • a a a aw a a.« a w ) 'ip'• * Si)'Na< hi I W I I W WW WW WWhl W I VIM4 I W I f I W I i h
ctanHarH wac finaliTorl nn Pphrnarx/ OA. ■iQQO
WhWh* I'.iMV.hlSptl VAW * l« «WAi I^W WII I Vp'la./lh.i WhI y Um~r^ I
In an sannonWIv tn tho nrnnnociH nil^ OQUIA HJe*m
III I u|«/|i^wi ivpti/N hVp# hi m> pi i uiOy \^\j% i/~v v.<ioouoo^v4 oc;yc;icii
nf nmnnoc» ho"y<ar*W *T"Pm+ /'lir'm ir^oi/^rh
iii^Liiwwo wi pi wK^^oo I la^ai u di laiyoio. i i icii \jiouuooiv./i i, vviiium iiiciy uc
hninfi li fni* ■fl^non Wnmn mP\
iicjipiui iwi LI iwod uwiii^ jvju iia^aiu aiiaiyooo, lutiuwd.
\A/i^ l-f I la ■ ■ ■ an MM M I I A A J mmmmmmmmm a^Ma a^Ma.a A Lk m aaa. aa m m m ... m
vviiai-ii. rui iciauvBiy uiluuiM|jiiu<dit:!u piuufcJbbeti, review me pruuess
from raw matei'ials to product. At each (handling or processing step,
‘ w'hat if” questions are formulated and answered, to evaluate the
effects of component failures or procedural errors on the process.
Checkiist. For more complex processes, the “what if” study can be
best organized through the use of a “checklist,” and assigning certain
aspects of the process to the committee members having the
greatest experience or skill in evaluating those aspects. Operator
practices and job knowledge are audited in the field, the suitability of
equipment and materials of construction is studied, the chemistry of
the process and the control systems are reviewed, and the operating
and maintenance records are audited. Generally, a checklist evalua¬
tion of a process precedes use of the more sophisticated methods
described below, unless the process has been operated safely for
many years and has been subjected to periodic and thorough safety
inspections and audits.
What-lf/Checklist. The what-if/checklist is a broadly based hazard
assessment technique that combines the creative thinking of a
selected team of soecialists with the methodical focus of a nrenared
checklist. The result is a comprehe.nsive hazard analysis that is
extremely useful in training operating pe-^sonne! on t.he hazards of
thp» nartimlar nn^ratinn
,..w pr^. wpr W. ..
Xho ro\/io\A/ tocjm ic coIon+oH tr\ r^srvrcie^nt a xa/iHz^ ronnc^ r\f r^rriHi
i I I w V IV./ vv I.WV.AI ii iVi/ v/Vp/iV/V^CSi/V^ I ^v^Vi/l IL CA VVI\.4^ V./i |«/IV,/ViiCI\M'LIVii/lly
mor'hianir*2jl tQ/^hnir*ol onW oof^tx/ r\/r%rr»rxr» Jr' o
I I iv./\./i IVAI XSip/X^l If liwc«iy Ul iVJ OCllXi^Ly WIOOI^III IC70. I_CIL./I I p^lOWtl lO^iV^ll Cl
u/uoiw II fiwi 11 ICILIWI 1 }MrciL./r\Cl^C7 IIIC? L^^UiailUII lU UC OLUUIC/U.
"Thio l>v/^-»/^**^/»* rwl/v
I i iio pcLwrxQ^c; ly pi^any ii luiuvjco ii ihji i t lauui i ui i i idJLCH Ud ui i i ictici icti^,
piv/»wc 7 oo icLyiIIluluyy, jjiuucuuitjyuipiiit^ni utJijiyii, ni 5 :iuuint?iilclliun
controi, incidGnt GXpenencG, and previous hazards rGviGws. A fisid
tour of the operation also is conducted at this time.
nitj review leam meinoaicaiiy examines me operation trom receipt or
raw materials to delivery of the finished product to the customers
site. At each step, the group collectively generates a listing of %hat-
if questions regarding the hazards and safety of the operation.
When the review team has completed listing its spontaneously
generated questions, it systematically goes through a prepared
checklist to stimulate additional questions.
Subsequently, answers are developed for each question. The
review team then works to achieve a consensus on each question
and answer. From these answers, a listing of recommendations is
developed specifying the need for additional action or study. The
recommendations, along with the list of questions and answers,
become the key elements of the hazard assessment report.
Hazard and Operability Study (HAZOP). HAZOP is a formally
structured method of systematicaiiy investigating each element of a
system for all of the ways in which important parameters can deviate
from the intended design conditions to create hazards and operability
problems. The hazard and operability problems are typically deter-
Hill it^u uy cx OLUuy ui u it:; pip" cxi lu li i^ii ui i \k^i ii uici^i ai i lo \u\ jjiai il
I i luuci; uy CL i^ai 11 wi \J^ \ oui ii i^i vvi lu ui iiiv,/Ciiiy ai laiy^c ^ii^wlo ui
pui^i llldt UUIdl I lO Cll ion 1^ il I ddUl I pipoill Id dl lU ddUl I VdOOdl UI 11 id
operation.
Portinont naramotorc am colnntorl fr>r ovamnio fln\A/ tomnoratiim
f LW 1 KJ Ml I W W4WV4 f < W I W/XMl IIWW)
nmccliro anri timo Then tho effort nf Howintinnc frrm Hocinn
!%■« biatis.^* btiw waiwWvwi Sdiwv i»«cki w »tw iiwii* waWWt^t*
conditions of each parameter is examined. A list of key words, for
example, “more of,” “less of,” “part of,” are selected for use in de¬
scribing each potential deviation.
The system is evaluated as designed and with deviations noted. All
causes of failure are identified. Existing safeguards and protection
are identified. An assessment is made weighing the consequences,
causes, and protection requirements involved.
Failure Mode and Effect Analysis (FMEA). The FMEA is a methodi¬
cal study of component failures. This review starts with a diagram of
the operation, and includes all components that could fail and
conceivably affect the safety of the operation. Typical examples are
instrument transmitters, controllers, valves, pumps, rotometers, etc.
These components are listed on a data tabulation sheet and individu¬
ally analyzed for the following:
• Potential mode of failure, (i.e., open, closed, on, off, leaks, etc);
• Consequence of the failure; effect on other components and
effects on whole system;
• Hazard class, (i.e., high, moderate, low);
31
• Probability of failure;
• Detection methods; and
• Remarks/compensating provisions.
Multiple concurrent failures also are included in the analysis. The
last step in the analysis is to analyze the data for each component or
multiple component failure and develop a series of recommendations
appropriate to risk management.
Fault Tree Analysis. A fault tree analysis can be either a qualitative
or a quantitative model of all the undesirable outcomes, such as a
toxic gas release or explosion, that could result from a specific
initiating event. It begins with a graphic representation (using logic
symbols) of all possible sequences of events that could result in an
incident. The resulting diagram looks like a tree with many branches
listing the sequential events (failures) for different independent paths
to the top event. Probabilities (using failure rate data) are assigned
to each event and then used to calculate the probability of occur¬
rence of the undesired event.
This technique is particularly useful in evaluating the effect of alter¬
native actions on reducing the probability of occurrence of the
undesired event.
32
States with AoDroved Plans
■ I
COMMISSIONER
Alaska Department of Labor
I
■4 A O+U 0+^,-<^+
I I I I VVt!£>l Oil I Oil CCl
Room 306
Juneau, AK 99801
(907) 465-2700
niDPrrnn
Industrial Commission of Arizona
SOOW.Washinaton
- - - ^
ni_A"7ocnA"7
riiueiiiA, MZ.OOOU/
(602) 542-5795
DIRECTOR
California Department
of Industrial Relations
455 Golden Gate Avenue
4th Floor
ban rrcinuisjuu,
(415)703-4590
COMMISSIONER
Connecticut Department of Labor
200 Folly Brook Boulevard
Wethersfield, CT 06109
/nr\o\ c-ioo
DIRECTOR
riciwcm Lytfpcai ii i it?i ii ui uauui
and Industrial Relations
Q<5A Di inAhKnu/l QirAot
I W4I IV>I V^LI WWfc
Honolulu, Hi 96813
F;flfi-Rft44
-/--- -
B «« AS ^ ir~r^
Indiana Department of Labor
Qi iilHinn
OidlC willow L^UIIIXUM
402 West Washington Street
Room W195
I_If_iki Ar^r\/\A
maianapoiis, iin
(317) 232-2378
COMMISSIONER
Iowa Division of Labor Services
1000 E. Grand Avenue
Des Moines, lA 50319
/CHc\ no-\,'iAA~r
\sjj C^KJ I t /
SECRETARY
Kentucky Labor Cabinet
1049 U.S. Highway, 127 South
Pranlrfnrt l^V AnfiOi
(502) 564-3070
MM
looiv^i^c^n
Maryland Division of Labor
nnH InHi ictn/
IW II j
Department of Licensing
and Reaulation
— -- ^
i-r\A ni_
ou I cji. raui riaue, t^iiu nuui
Baltimore, MD 21202-2272
lA-\n\ <5'3'3_/H7Q
I I t
niRFCTOR
Michigan Department of Labor
Victor Office Center
4L.W I I V VCIOI 111 I OV^UCll KS
RO. Box 30015
Lansing, Ml 48933
(o I /; *s/,3-yDuu
niDcoTr^D
I v/i~i
Michigan Department
of Public Health
3423 North Logan Street
Box 30195
I.C11 toil 1^, IVII
(517)335-8022
COMMISSIONER
Minnesota Department of Labor
and Industry
443 Lafayette Road
Qt Dpill c;c;i CC
Oi. I dui, IVII V I sjsj
(612)296-2342
DIRECTOR
Nevada Department of Industrial
Relations
Capitol Complex
H <57n o r'lii-M/Ot
I I \j \j, Vv/uiiy Oil oc^i
Carson City, NV 89710
(702) 687-3032
QC^DCTADV
l^*«l I ■
New Mexico Environmental
Department
Occuoational Health
I.— —
and Safety Bureau
1190 St. Francis Drive
PO R/^v OA1 io
• » I I w
Santa Fe, NM 87502
f5051827-2850
\ / - — — - - -
COMMISSIONER
M « t
I MOW loi L/o^cii II noi 11 ui (.duui
state Office Building - Campus
12
Room 457
Albany, NY 12240
(518) 457-2741
COMMISSIONER
North Carolina Department
of Labor
4 West Edenton Street
Km 07cnH
Haioiyi I, iMV^ \jyj i
(919) 733-0360
ADMINISTRATOR
Department of Consumer
dPid BuSiPiGSS SGPviCGS
Labor and Industries Building
Wintor Qtroot MR Di^omytQn
...I IV/V-/I I I "TWV/
VVIIIIWI Wit w \i^ i ,
Salem, OR 97310
(503) 378-3272
34
SECRETARY
nutil lU niuu L^cpcil II i iCI li \Jl LXIL^WI
and Human Resources
PriiHonrin Riuora MartinA7
I I va w wi iwiw • !• * wi %•« ■ w ••« WM.
Ri lilHinrt
|^V4IIUII 1^
505 Munoz Rivera Avenue
Hato Rev. PR 00918
/n/^rv\ TC A r\M A r\
(oua) / I I »
COMMISSIONER
South Carolina Department
of Labor
ocnn Pi-ir£sot ririxyo
WWWW I Wl U.ril«w
RO. Box 11329
Columbia, SC 29211-1329
A r\^r\ a
(ouo) /
COMMISSIONER
Tennessee Department of Labor
710 James Robertson Parkway
S I ii+rt ‘‘A” „ Or\A Clrvi^r
Nashville, TN 37243-0659
(615)741-2582
COMMISSIONER
Industrial Commission of Utah
RO. Box 146600
I _i,_ . I IT o >1 -I ^ rx cic.r\f\
oaii i_aNe oiiy, u i o^t i i w-uuww
(801) 530-6898
COMMISSIONER
Vermont Department of Labor
and Industry
i OA Qfotzi Qf
\C^\J
Montpelier. VI 05620
(802) 828-2288
COMMISSIONER
\/Srr«5in le^lfariHe FA^martm^nt
V II ^11 i lOICil %i I iwi •%
of Labor
2131 Hospital Street
Christiansted
St. Croix, VI 00840-4666
/QAQ\ TTO-HQAyl
COMMISSIONER
V II yil llct L^t^pai III Id II Ul UCILA^I
and Industry
Pn\A/orc.Ta\/lnr Ri lilHinn
I K^VVWaW Miawaa* ■ ^
13 South 13th Street
Richmond, VA 23219
(OLKf) 7 00-^0/ /
DIRECTOR
Washington Department of Labor
and Industries
Genera! Administration Building
RO. Box 44001
Olympia. W.A 98504-4001
(206) 956-4213
AnH/IIMICTDATriD
I I mi V^l I
Occupational Safety and Health
Ad.ministration
Herschler Building, 2nd Fbor
East
122 West 25th Street
\M\/ nr^r\r\n
i^neyenne, vv i o^iuuii
(307) 777-7672
OSHA Consultation Project Directory
state
Telephone
Alabama.
Alaska.
Arizona.
Arkansas.
California.
Colorado.
Connecticut.
Delaware.
District of Columbia
Florida.
Georgia.
Guam.
Hawaii.
Idaho.
Illinois.
Indiana.
Iowa.
Kansas.
Kentucky.
Louisiana.
Maine.
Maryland.
Massachusetts.
Michigan.
Minnesota.
Mississippi.
Missouri.
Montana.
Nebraska.
.... (205)348-3033
.... (907)269-4939
.... (602) 542-5795
.... (501)682-4522
.... (415) 703-4441
... (303)491-6151
... (203) 566-4550
... (302) 577-3908
... (202) 576-6339
... (904) 488-3044
... (404) 894-8274
... (671) 647-4202
... (808)586-9116
... (208) 385-3283
... (312)814-2337
... (317)232-2688
... (515)281-5352
... (913)296-4386
... (502) 564-6895
... (504) 342-9601
... (207) 624-6460
.... (410)333-4218
.... (617)969-7177
(517)322-8250(H)
(517)322-1809(8)
.... (612)297-2393
.... (601)987-3981
.... (314)751-3403
....(406)444-6418
.... (402)471-4717
36
Nevada.
i>icw nciiii|jo< lilt;
New Jersey.
Mow Mexico.
New York.
North Carolina..
INUr III UciNUlid ...
Ohio.
OHahoma
>.< I XfUAI I Wl I IVA ...••••.
Oregon.
Pennsvivania...
r^i IT J •
r ud lu PMuu.
Rhode Island ...
S Ai ith Hamlina
W«%l I V./III •
South Dakota...
Tennessee .
Texas .
Utah.
Vermont.
Virginia.
Virgin Islands...
Washington.
West Virginia ...
Wvnminn
.O
(702) 486-5016
/cnoN 07^ ono>4
(609) 292-3923
(505) 827-2877
(518) 457-2481
(919) 733-2360
/"7A-I \ C-lOO
^ / U I ; C^C. I I oo
(614)644-2631
(405)528-1500
(412) 357-2396
/OAn\ ICA o^7^
I / I
(401)277-2438
(803) 734-9599
(605) 688-4101
(615) 741-7036
\ /
(512) 440-3834
(801) 530-6868
(802) 828-2765
(804) 786-8707
(809) 772-1315
\ f
tr\r\f>\ r\rf> r a Ary
(304) 558-7890
(Ci.r\&\ 0 «A-fi£; 7 Q('U\
\mf^ I •/
(608) 266-1818(8)
. .. (307) 777-7786
- \- - f ..
(H) - Health
(S) - Safety
37
03HA Ar63 Officss
Area Telephone
Albany, NY...(518)464-6742
MiDuquerque, imivi.......(quo) /od-o#i i
Allentown, PA.(215)776-0592
AAl^ /QHT^ 07i
iwi r-\f V .. w / / ^ I '•Jft-m
Appleton, Wl.(414) 734-4521
Auausta. ME.^2071622-8417
' —^-».... \— ■ /- _ . -
A.._i.i__ Tw /nMrs\ Arsr\
Ausiin, IA.(oi^:)^o^:-o/oo
Avenel, NJ.(908) 750-3270
K^n //nn\ QftO-OQ/in
LJCIIIII I IWI C, IVIL^..... \-T I \JJ </WC.'£.l_r-rw
Baton Rouge, LA.(504) 389-0474
Bay-side, NY...(718)279-9060
tjeiievue, vva.(riuo) ooo-/o*iu
Billings, MT.(406) 657-6649
Birmingham, AL.(205) 731-1534
Bismarck. ND.(701)250-4521
Boise, ID.(208)334-1867
Bowmansville, NY.(716)684-3891
Braintree, MA.(617) 565-6924
B nrir’O'-'nrt PT /ono\ C70 CCTQ
Calumet City. IL.(708) 891-3800
Carson City, NV.(702) 88-5-6963
unar lesion, wv.iJ4/-oy;3/
Cincinnati, OH.(513) 841-4132
/^i 1 /n-» coo oo-« o
«^ifciVtii<di lu, wn . uc^-oo I o
Columbia, SC.(803) 765-5904
roiiimhiic ni-i rfi14^4nQ-!^c;ft9
Concord, NH.(603)225-1629
Corous Christi. TX.^5121888-3257
--,...-.-. . .^ ,
r-l_ll_TV/ /04 X\ OOO 0^00
uaiias, IA.(4 1^)
Denver, CO.(303) 844-5285
Hoo Dioiooo II ^7nft^ fln'^./iflnn
LyV70 I lail 1^0, H_..... \f wwy WWW -rwww
38
Des Moines, lA.
Enalewood. CO.
— ^ -
ET-I/-. nA
C.I le, rM.
Fort Lauderdale, FL.
Fort Worth, TX.
error. k'V
I I Of ir\i wi i, IV I .
Harrisburg, PA.
Hartford, CT.
Hachroi irW Hoinhtc M. I
I I W«WfXi IWI^IIAWy IVW
Hato Rey, PR.
Honolulu, HI.
Houston, TX.
Houston, TX.
Indianapolis, IN.
Jackson, MS.
Jacksonville, FL.
Kansas City, MO.
Lansing, Ml.
Little Rock. AR.
Lubbock, TX.
Madison, Wl.
M r!krlf/vr\ Kl I
Ol liWI I, I ...
Methuen, MA.
Milwaukee, Wl.
K/IKI
IVIII 11 iVIl ^.
Mobile, AL.
Nashville, TN.
M ciiA/VXrl/' KIV
I i\^i rv, I ^ I ...
Norfolk, VA.
North Aurora, IL.
wrviuiiuitia oiiy, wrv..
Omaha, NE.
Parsippany, NJ..
Peoria, IL.
Philadelohia. PA
I
(515)284-4794
(3031843-4500
/O-l A\ ooo CTrO
(305) 424-0242
(817) 885-7025
/c.no\ ooy.ynoA
~t V/C.’~T
(717)782-3902
(203)240-3152
(201)288-1700
(809) 766-5457
(808) 541-2685
(713)286-05a3
(713)591-2438
(317)226-7290
(601) 965-4606
(904)232-2895
(816)426-2756
(517)377-1892
(501)324-6291
(806)743-7681
(608)264-5388
/CnQ\ TCT.Ci D^
J f I I
(61/) 565-8110
(414)297-3315
/CION 0/IQ_iQQy1
\\J l£^J W/fW" I
(205)441-6131
(615) 781-5423
/O-ION OC/1_QQyin
\c^j
(804) 441-3820
(708) 896-8700
/yinCN oo^ coc^
£.<3 I I
. (402)221-3182
. (201)263-1003
. (309) 671-7033
. (215)597-4955
> /
39
Phoenix, AZ.
Pittsburgh, PA.
Portland, OR.
Providence, Rl.
Raleiah. NC..
^ *
i . I IT"
csaii LaKe u i .
San Francisco, CA
Savannah, GA.
Smyrna, GA.
Springfield, MA.
St. Louis, MO.
r^.__i\/
Syracuse, in t .
Tampa, FL.
Tarrytown, NY.
Toledo, OH.
Tucker, G A.
Westbury, NY.
Wichita, KS.
Wilkes-Barre, PA...
(6Q2) 640-2007
(412) 644-2903
(503) 326-2251
(401) 528-4669
r9191 8.56-4770
(801) 524-5080
f4151744-7120
\ ' / ..
(912) 652-4393
f4041984-8700
(413) 785-0123
rSI 41425-4249
\ • /--- ~
(315) 451-0808
f8131626-1177
\ / — ' - - - -
(914) 682-6151
f4191259-7542
(404) 493-6644
(516) 334-3344
(316) 269-6644
(717)826-6538
40
Related Publications
OSHA-2056 All About OSHA
OSHA-3084 Chemical Hazard Communication
OSHA-3047 Consultation Services for the Employer
OSHA-3088 How to Prepare for Workplace Emergencies
O-SHA-209S OSHA Ins'^ections
nQUA.'^noi
1/ ^ I
DQl-IA ■ Fmnlnuoa VUnrlenlano Hinhtc
imm! I » ^ J ^ ^ W 9 ! t t t I • «W
^QI-JA_On 7 T C?/arc*r»no/ P^rtt t!r\nr»/^nf
/^OLJA 0*4 00 D f»/n ^ A A ^
^^J4L nuL^aoo c>ca/c?i/ ivianaycru/atii
/^r»LJA on“7n ^
v-^onM-ou/3 nfij/^z/dzu/y rtuL&uuun
HaZcira LyUfTirnufnuciuuf} OLunuaru, nu^ uuue? u/ rfue^/d/
HeguiBiions (c^rn; ran /y/c/. /^c/u.
Process Safety Management of Highly Hazardous Chemicals
Standard, Title 29, Code of Federal Regulations (CFR) Part
1910.119 FR 57, P. 6356. This contains the actual text of the PSM
rule.
(A single free copy of the above materials can be obtained from
OSHA Publications Office, Room N3101, Washington, DC 20210,
(202) 523-9667).
OS HA-3104 Hazard Communication - A Compliance Kit
(A reference guide to step-by-step requirements for compliance
with the OSHA standard.)
OS HA-3071 Job Hazard Analysis
(OSHA 3104 and OSHA 3071 are available from the Superintendent
of Documents. U.S. Government Printino Office, Washinaton, DC
20402, (202) 783-3238. OSHA 3104 - GPO Order No. 929-022-
000009,' $18-domestic; $22,50-foreign. OSHA 3071 - GPO Order No.
029-016-00142-5, $1.00.)
1994 Q _ 154-969 : QL 3
Regional Offices
Region 1
Region VI
coc (Sriffin Street
1 1 1 wl i icll IvJ i 1 w w 1
1 oi riuor
riL/UI 11
DOolUii, IVIM 1 1^
L/ciUcio, 1 A /
Tnlonhnnn- (9iA\ 7f\7 A7^i
iGiepnone. v^i /j uoo-/ i04
IGicpi lOI Ic. /D/“M'/OI
1 Kegion ii
Region VII
(NJ,NY,*PR,*Vn
(lA * KS MO NE)
201 Varick Street
911 Walnut Street Room 406
Room 670
Kan<?a*i Citv MO 64106
NewYork. NY 10014
Telenhnne- (8161 4'56-5861
Telephone: (21 2) 337-2378
1 It7. \Q> 1 iJOW 1
1 . Region VIII
1 Kegion iii
(CO^ MX, ND, sn, UT,* WY*)
(DC, DE, MD,* PA, VA,* WV)
Federal Building Room 1576
1 Gateway Building, Suite 2100
1961 Stout Street
1 3535 Market Street
Denver CO 80294
1 Philadelphia. PA 19104
/OOOX Q/1/l-30Ai
1 Telephone: (215) 596-1201
1 .... Region IX
1 Region iv
(American Samoa, AZ* CA,*
1 (AL, FL, GA, KY,* MS, NC,
Guam, HI,* NV,‘TrustTemtories
1 SC,*TN*)
of the Pacific)
1 1375 Peachtree Street, N.E.
71 Stevenson Street Room 420
1 , .Suite 587
San Franeiseo C A 94105
1 Atlanta GA 30367
Atlanta GA 30367
1 TfilonhnnA- (AnA.\ 347-3573
MUCtI IlCl, \Jir\ OUOU/
/AH Ci\
■ I y .w .y w .. w*' • w 1 tricrpi iv-^i ic. y-t i uj 1 i Tj
1 Region V
Region X
1 (IL,IN,*MI,* MN,*OH,WI)
(AK*ID OR *WA*)
Room 3244
1111 Third Avenue
Suite 715
Chicago, IL 60604
Telephone: (312) 353-2220
S e attl e . WA 98101 - 3212
Telephon e : (206) 553 - 5930
*Th6se states and territories operate their own OSHA-approved job safety
and health programs (Connecticut and New York plans cover public
employees only). States with approved programs must have a standard
that is identical to, or at least as effective, as the federal standard.