HomeMy WebLinkAbout1.17 Emergency response planEMERGENCY RESPONSE PLAN ETC CANYON PIPELINE, LLC Beaver Creek Pipeline IN THE EVENT OF: • Accidental Release of Regulated Substance (e.g., hydrocarbons), Fire, or Bodily Injury (e.g.,
heart attack) of Property Damage. ~ Evacuate degree of non-incidental release. ~ If Non-Catastrophic, notify Superintendent, District Manager and the Manager of Safety, Health, and Environment
to determine the course of action and make appropriate reporting contacts. ~ If Catastrophic, conduct Emergency Shutdown (ESD), make appropriate notifications, evaluate impact of release
to employees and public, and evacuate facility per Emergency Evacuation Plan as necessary. Notify Superintendent and District Manager to engage Emergency Response Plan. • Need For Emergency
Response Support: Alan McDermott, Engineering Manager of Projects (720) 225-4020Phone Scott Pierce, Operations Superintedent Jimmy Smith, Construction Manager Wagon Wheel Consulting,
Inc. Gregory Norton, Lead Inspector Garfield County Sheriff Rifle Fire Department • Need for Emergency Health Care: ~ Grand River Medical Center Located at: 501 Airport Rd., Rifle, Colorado
~ Ambulance 911 (970) 263-0934 Phone (970) 216-1750 Mobile (970) 625-8433 Phone (303) 726-9070 Mobile (970) 625-8433 Phone (435) 621-0285 Mobile (970) 625-1899 or 911 911 Designated
employees trained in Medic 1 st Aid are to perform 1 st Aid procedures on injured employees as applicable.
EVACUATION AND ESCAPE INFORMATION NOTE: All personnel are responsible for their own evacuation, and should actively solicit evacuation assistance if needed. Escape Route: o PRIMARY ROUTE
Proceed county road 317 north to county road 320. Muster at intersection. Post-Evacuation Employee Accounting: o Employees are to report by phone (970-625-8433), or in person to the
Inspection Office located in Rifle, Colorado. o The incident Commander will alert emergency responders of any employees who are unaccounted for after an emergency evacuation, so that
rescue operations can be addressed. Reporting Emergencies: o Emergency Phone Contact List on attached page. Critical Duties All employees will evacuate during a catastrophic ESD emergency.
The Construction Engineering Manager, Operations Superintendent or Construction Manager, or Construction Supervisor are the only qualified persons to issue permission to enter the facility,
or response area. o Activate Emergency Shutdown (ESH) system. o Activate Emergency Response System by notifying Superintendent or Engineering Manager of your emergency. o Render medical
assistance to any injured employees. Only persons trained in First Aid and CPR are qualified to render aid. o Evacuate right-of-way per this Emergency Evacuation Plan. o Make appropriate
notifications of emergency conditions. Additional Emergency Plan Information o Emergency Responses shall occur as follows: ~ First responder notification: Any facility or field personnel
noticing a release or other potentially hazardous situation shall notify the person in charge immediately of the nature of the hazardous occurrence. Location, product involved, release
quantity, and status of personnel in the area shall be communicated. ~ Personnel identifying the emergency shall evacuate the area as necessary. Only personnel designated and trained
for the particular function may take actions required to combat the emergency. ~ The Person in charge will assume the functions of the Site Commander until emergency responders (EMS)
arrive on scene and coordinated this role. The Site Commander possesses the ability, and has been granted the authority, to assume control and make decisions when an emergency arises.
The Emergency Coordinator will: • Notify potentially affected personnel of the emergency . • Sound any applicable emergency alarms (describe alarm system, if any, used to alert on-site
personnel).
• Determine if Emergency Shutdown (ESD) and/or Evacuation are/is applicable. o Take immediate measures as possible to prevent contamination of waterways or other mechanisms that might
impact public safety. • Determine when off-site emergency responders are needed. • Notify the Engineering Manager, Operations Manager, Construction Manager, Lead Inspector, and Construction
Superintendent. o Designate personnel to remain in the vicinity of the incident to monitor the area for further problems and to assist emergency response personnel with necessary facility
functions/site layout. o Designate appropriate personnel to coordinate meeting emergency response vehicles in order to guide them to the site. o Utilize appropriate section, township,
and range as well as nearest access roads and landmarks or other applicable information when reporting incident. • Insure that access is maintained to the right-of-way at all times.
Alarm System (Pipeline) • Two-way radio or cellular phone • Note that direct verbal communication of an emergency i§. satisfactory for the pipeline if this can be effective in alerting
all personnel who may be on-site. Non-Evacuation emergency (Pipeline) • Activate Emergency Shutdown (ESD) • Notify Person in charge -Site Commander, Lead Inspector and Construction Superintendent.
Updating Emergency Plan • This Evacuation Plan will be reviewed at least annually and revised to reflect relevant changes. Employee Training • This Evacuation Plan will be reviewed with
all new employees during their orientation (or first week of employment), and with all employees on an annual basis. Cost Reimbursement • ETC Canyon Pipeline, LLC with be responsible
for the reimbursement of any cost associated with the emergency response of any and all agencies or departments contacted as a result of an incident requiring services.
SPECIFIC ACTION PLAN FOR ACCIDENTAL RELEASE Emergency plan decision tree Hydrocarbon Release Non-Catastrophic 1. 911 (if required) 2. Notify Superintendent and Foreman 3. Notify Engineering
Manager 4. Notify EH&S 5. Assist & assume Site Commander lead until relieved by Foreman or Superintendent Catastrophic 1. 911 (if required) 2. ESO Pipeline Operations 3. Notify Foreman,
Superintendent 4. Notify Engineering Manager 5. Notify EH&S 6. Assume Role of Site Commander -until relieved by Foreman or Superintendent
Energy Transfer Company Incident Reporting
INCIDENT REPORTING PURPOSE To specify essential reporting and documentation of on the job injurics to sotisfy Company alld Insurance Company requirements; to identify and implement methods
to prevent similar incidents; and to communicate prcvention methods and recommendations to all workforce< WHAT MUST BE REPORTED The following occurrences and incidents must be reported<
Sample fonns can be found under a separate tab< A. On-the-Job Injuries and Illnesses -Any on-the-job injury or illness must be documented at the time they OCCUI. R Vehicle Accidents
-Any accident while operating any vehicle on the job or while on ETC company business< C General Liability Accidents -Any occurrence, excluding vehicle-related accidents, injury to others,
or damage to the property of others< Example: A contractor's employee is seriously injured on Company property< D< Other Accidents or Losses -Any theft, accident, or losses such as fire,
vandalism or damage to company property< E. Near Miss -File a report on near misses in order to analyze, perform and communicate measures necessary to prevent a reoccurrence at alliocations<
Use the Accident Report Form and mark "NEAR MISS" at the top< F< Any occurrence which has the potential to cause or result in regnlatory agency, mass media visit, inspection, or request
for information STANDARDS: I) This procedure provides guidance for reporting and conducting Incident Investigations< 2) The company considers all documents (notes, records, drawings,
photographs, videotapes, reports) and physical evidence prepared as part of an incident investigation to be confidential. 3) External requests for information concerning Incidents or
Incident investigations shan be immediately referred to the Safety and Legal Department 4) All requests for information from the media (newspapers, television, and radio) shall be referred
to Corporate Communications and the Legal Department DEFINITIONS: Incident: An event meeting the criteria described by "Reportable Incident Class" m this document involving: I) Contract
personnel while performing Company business, 2) Company equipment, 3) Company assets, or 4) Other Third Party personnel or equipment while on Company business 5) An event that will attract
media attention Note: Property damage/loss due to nonnal wear and tear and/or mechanical equipment failure without potential for hann to personnel or the environment is not covered by
this procedure but should be reviewed by facility management Page 1 of 3
INCIDENT REPORTING REPORTABLE INCIDENT CLASSES: Incident Class or Category: The mnking of iHl Incident based upon the level of actual and/or potential consequences. Class 1: • OSHA-Recordable
injury or substantial first aid injury to a Contractor or Third Pal1y. • Company, Contractor, or Third Party property damage or environmental remediation estimated to cost between $10,000
to $50,000 • Near miss incident with the potential to generate Class I consequences Class 2: • Lost Time Injury to a Contractor or Third Party o Company, Contractor or Third Party property
damage/loss or environmental remediation estimated to cost between $50,000 and $250,000 o Fires which are immediately controlled, but have the potential to generate Class 2 consequences
o Explosions that generate Category 2 consequences o Spills or releases that exceed Reportable Quantities under CERCLA; excluding spills less that 10 gallons into waters of the US, or
international equivalent. o Near miss incident with the potential to generate Category 2 consequences Class 3: o Employee or Third Party fatalities or lost time injuries resulting in
a loss of consciousness or requiring overnight hospitalization o 2 or more OSHA Recordable injuries related to an Incident o Company, Contractor, or Third Party property damage/loss
or environmental remediation estimated to exceed $250,000 o Explosions and fires which cannot be immediately controlled, contained or extinguished o Near miss incident with potential
to generate Class 3 PROCEDURE: The following steps provide guidance for conducting Incident Investigations. INITIAL INCIDENT ASSESSMENT The Inspector or other company representative
at the scene of an Incident is responsible for the initial assessment, which includes: o Care for the injured and protect people/public o Initiate notification procedures. o Assess the
general condition of and secure the site. o Protect equipment and assets o Preserve any physical evidence and collect names, addresses, and telephone numbers of personnel on site. •
Gather information necessary to complete the Initial Report of Incident. Page 2 of 3
INCIDENT REPORTING DOCUMENTATLQN: Inspector will: Have Contractor docllment basic information concel11ing the Incident on an initial report of Incident. A completed copy of the contractor's
initial incident report is due within 48 hours (or two business days) and a copy is to be sent to the Safety Department. The Contractor does not have to use ETC's report fonnat or ETC's
f01111S. ETC's forms will be provided if requested but the contractor is not required to use any special ETC fonn. Contractors can use a format or fom1 of their choice as long as all
required information is provided. The initial report of incident will be used by the Safety Department, Operations, and/or Engineering to determine scoping or other requirements for
additional infonnation and reports. REPORTING TREE Project Manager or struction Coordi I' F incident Affects pipeline Operation Qascont~~ Contract Inspector Field EH&S Page 3 of 3 Ops
Manager Director . Other ETC
Energy Transfer Company Reporting Forms
(Form A) Date of incident: ETC FIRST REPORT OF INJURY Contraclor or Third Pm[y ______ Time: ___ AM/PM Name of injured person: Address: Phone Number(s): ___________________ _ Date of
birth: Male ---Female Employing Company: Address: Phone Number(s): __________________________ _ Injured person job classification: What was injured doing at time of incident: __________________
_ Location ofIncident: __________________________ _ Typeofi~ury: ________________________________ _ Details of incident: Injury requires physicianlhospital visit? Yes No Name of ph ysici
ani hospital: ________________________ _ Address: Physicianlhospital phone nnmber: Person preparing this report Date Contact Information Return this fonn to Safety Department within
48 hours of incident. Attn: Safety Department Fax to !R321IiIiR-1129 ANO 121m 401-7110
Form -B First Report ETC PROPERTY DAMAGE Dept. _____ _ Dept. Location: ______ _ Date of Loss: __ _ Time: a.m.lp.m. Date of this Report: ______ _ Reporting Employee: __________ _ Phone:
( Reporting SupelVisor: __________ _ Phone: ( LOSS INFORMATION Type of Loss: o Mechanical Damage o Storm Damage o Other Location of Loss: ---=:--,--,-,-,------=----------ooc-c------=---street
Address City State Zip Description of Loss: Cost to Repair/Replace: $ ________ _ PREPARED BY Prepared By: ____________ _ Date: ____ _ Phone: ______ _ Return this form to Safety Department
within 48 hours of incident. Attn: Safety Department Fax to (832) 668-1129 AND (210) 403-7530
Form C FIRE OR EXPLOSION FIRST REPORT Dept. Dept. Location: ______ ~ Date of Loss. Time: a.m./p.m. Date of this Report: ___________ _ Reporting Employee: ___________ _ Phone: ( Reporting
Supervisor: Phone: ( LOSS INFORMATION Type of Loss: o Explosion Damage o Fire Damage o Other Location of Loss: ---====-,-----------;o=---------,=c:----~ Street Address City State Description
of Loss: Cost to RepairfReplace: $ _________ _ PREPARED BY Prepared By: ____________ _ Date: ____ _ Phone: Return this form to Safety Department within 48 hours of incident. AUn: Safety
Department Fax to (832) 668-1129 AND (210) 403-7530 Zip
(Form D) Dale of Accident Location FIRST REPORT Vehicle Accident If you're in an accident Call Police if 2 If applicable, forward copies 01 your completed form [0 your insurance agent,
supervisor or appropriate organization contact • A person is injured. There is more than $1,000 damage \0 the vehicle(s). • Your vehicle has been vandalized or subjecllo a hit and run
or thefl • The other driver is uninsured or driving with a suspended license • The other driver is impaired. A. Your Organization Organization/Branch I C,,'ame, Nombe, lif app""ble)
Address Phone I Fa, I E-mail B. Vehicle Unit Number License Plate Number Make/Model C. Driver Name Driver's License Number Driver's License Expiration Date Day Phone Fa> E-mail D. Occupants
-Total Number of Occupants: __ (not including driver) (Please attach a separate sheet if more than one occupant was involved) Name Day Phone I Fa> E. Other Vehicles and Drivers -Total
Number of Vehicles Involved: __ (including your vehicle) (Please attach a separate sheet if more than two vehicles were involved) License Plate Number {State of Plale License Expiration
Date Name 01 Insurance Company Policy Number Name of Agent and Address Year and Make J MadellSody Type, Sedao, Miol Vao, etc.) Driver's Name Driver's License Number Driver's License
Expiration Date Address Day Phone I E,eolog Phooe I Fa> I E-mail Vehicle Owner's Name (if not Driver) Address l Day Phone I E,eoiog Phaoe I Fa> I E-mail Return this form to Safety Department
within 48 hours of incident. Attn: Safety Department F::IY tn (~i?) fifiJL 11?Q ANn (') 1 m A.01_ 7"lO
(Form 0) Return this fonn to Safety Department within 48 hours of incident. Attn: Safety Department F:1X to (R1?) fihR_ll?Q ANn f? I m .dfl1_ 7(j1fl
(Form D) F. The Accident I , Date Time (AM/PM) Location Al the lime of the accident was the vehicle being used lor o Business o Personal use ---.-~-Light Conditions (Dawn, Day, Dusk,
Dark) Weather at Time of ACCident Type 01 Road Surface Road Condition Name of Witnesses (other than occupants) Witness Phone Witness Address --Had You Consumed any Alcohol? If so, How
Much When DYes DNa Did the Other Driver Appear to Have Been Drinking? Give any Details DYes o No O'lf€cllon of Vehicle On What Road? What Side of Road? Speed Direction of Other Vehicle
On What Road? What Side of Road? Speed What Traffic Signals Were Present? Did you Give A Warning Signal? What Kind? Which lights Did You Have On (if any)? DYes DNa Did the Other Driver
Give A Warning Signal? What Kind? Did the Other Driver Have their Headlights On? DYes DNo DYes DNo Has the ACCident been Reported to Police? Did Police Attend the Scene of the Accident?
Name of Police Force DYes DNa DYes DNa Police Officer's Name Police Phone Police File Number Have the Police Charged Anyone? Name of Person Charged Nature of Charge DYes DNa G Injuries
and Damage (please attach a separate sheet if you require more room) Nature of Damage to oIherVehicies Nature of Injuries to Drivers or Occupants Nature of Damage to Unit H. Driver's
Detailed Description of How Accident, Loss or Mechanical Damage Occurred Who Do You Think Was 10 81a me? Why? Driver Signature Date If helpful, Hlustrate the accident at right. Be sure
to nole: • The name of all streets, • Course of all cars involved, and • Position of vehicles al inslant of accident Return this fonn to Safety Department within 48 hours of incident.
Attn: Safety Department l<~v tn fSn.'J) ,c;,c;SL11'1Q doNn f'11m t1(YL7.1\':t.t1
(Form D) Return this fann to Safety Department within 48 hours of incident. Attn: Safety Department F~v tn (~':I.,),\ hhSL 11 ')Q ANn ('J 1 m dO'L 7 I:; 1.f'I
Form· E Type of Loss: o Theft Was Theft Reported to Police: DYes Police Contact information: o Date First Report ETCPROPERTYTHEFT~OSS o Vandalism o No Agency contact Person Loss Location:
Time/Date Loss Was Discovered Last Known Time/Date before Loss Description of Loss: Initial Cost City State Street Address City Time Time $---------------Cost to Repair/Replace: $ ________
_ PREPARED BY State Date Date o Other Phone Zip Prepared By: ____________ _ Date: ____ _ Phone: ______ _ Return this fonn to Safety Department within 48 hours of incident. Attn: Safety
Department Fax to (832) 668-1129 AND (210) 403-7530
Form -E Return this form to Safety Department within 48 hours of incident. Attn: Safety Department Fax to (832) 668-1129 AND (210) 403-7530
Energy Transfer Company Hot Work Procedures and Hot Work Permitting
Inspector Permit Qualification Process Safety Principle: Total job safety is the objective. Energy Transfer Company has developed and put in place Safety Management Systems which work
to prevent accidents and flres, eliminate personal injury, and protect the environment and general public. An example of one such system is the Hot Work Permit System. This system is
designed with specific requirements as to who has the authority to issue permits and approve work. The Inspector qualification program is used to authorize non-operations, and in some
cases non-Company, personnel to issue certain types of hot work pem1its. Application: This process applies to existing pipeline facilities owned and/or operated by Energy Transfer Company.
This process covers the issuance of Hot Work Permits and Confined Space Work Pennits related to excavation work associated with pipeline activities. This also inclndes general pipeline
and right-of-way work activities that do not require depressurization or opening process or pipeline equipment containing hydrocarbons. Applicability Note: This process is not intended
for and does not apply to "Greenfield" engineering and construction activities which are new construction and gas free and are not yet connected to any Energy Transfer Company pipe or
facility. Pennitting activities for "Greenfield" operations and projects are the responsibility of project contractors. Procedure: Local pipeline operations supervision and Safety representatives
may authorize qualified construction or contract inspectors to issue hot work pennits in accordance with this process as a designated Operation representative. In order to serve as the
designated Operation representative, non-operations Energy Transfer Company employee or contract inspector must be approved by Operations Manager and the local Safety Coordinator from
the area in which the person is to perfonn as a Designee. The Operation Representati ve Designee must: L Be qualified to recognize and address abnonnal operating conditions and other
required job tasks in accordance with the Energy Transfer Company Operator Qualification (OQ) program, as it applies to the work being conducted. This includes the ability to effectively
coordinate the mitigation of an unplanned release of the product in the system being worked. 2. Have a thorough understanding of the equipment (piping, valves, etc.) in the system where
the work is being conducted. This includes the physical location and access routes of associated isolation valves upstream and downstream of the work site and other associated equipment
that may be involved. 3. Be familiar with the operating conditions of the system on which the work is being conducted. 4. Be familiar with and be in possession of the Emergency Action
Plan covering the area where the work is being conducted, or have the necessary emergency contacts for the area if it is not covered by an existing Emergency Action Plan (i.e., new project).
5. Demonstrate understanding of Energy Transfer Company's Safety Policies and Procedures, including the use and calibration of portable gas detection equipment, and all other precautionary
measures outlined in the various pennitting processes. 6. Have a thorough knowledge of applicable OSHA regulations pertinent to the work being conducted.
Inspector Permit Qualification Process The following is provided CiS clarification regarding the Issuance of permits by a Company Representative Designee. Hot Work Permits Any hot work
involving welding or other spark producing activities on any opened j depressurized process equipment or piping containing hydrocarbons j chemicals requires a hot work permit issued
by an Energy Transfer Company Operations Employee. A Operation Representative Designee(s) who is not an Energy Transfer Company employee can not issue a hot work permit for work that
requires the process or piping containing the hydrocarbons j chemicals to be opened to the atmosphere. New pipeline construction projects (i.e., well ties) where hydrocarbons are not
introduced into the system do not require a hot work permit. Hot Work Permits for Pipeline Integrity Excavations j Repairs Outside of Compressor/Pump Stations and Processing Facilities
(Anomaly Investigations) All initial excavations on in-service or depressurized lines with evidence of leaking hydrocarbon /chemicals require the issuance of a Hot Work Penmit, the completion
of the Excavation Checklist, and the presence of an Energy Transfer Company Operations Employee. For other pipeline integrity excavations and repairs (clock spring installation, bolt
on clamps, weld on sleeves) when there is no evidence of a hydrocarbon j chemical leak, and the job plan does not call for the piping or equipment to be opened to the atmosphere, the
hot work penmit may be issued by a Operation Representative Designee. Confined Space Entry Permits As defined in the Confined Space Policy, an excavation with a depth of four (4) feet
or more is initially classified as a confined space. Confined space excavations in which physical and atmospheric hazards are eliminated and a means of egress is provided within every
twenty-five (25) feet may be re-classified as Non-Penmit Required (non-regulated) confined spaces by the Operation Company Representative Designee. Non-Penmit Required confined space
entries such as excavations do not require the continuous presence of an operations representative or designee. However, the nonpenmit required spaces must be inspected daily (prior
to entry, or if conditions change) by a "competent person" to ensure physical and atmospheric conditions at the work site have not changed (e.g., water or hydrocarbon accumulation, sloughing
of walls, fissures in walls, etc.). While this inspection is required on a daily basis, the job does not require continuous oversight by the operations representative or designee. All
Permit-Required Confined Space Entry Permits must be issued by an Energy Transfer Company Operations Representative.
Inspector Permit Qualification Process Appendix A -Supplemental Reference Material and Definitions Air Mover -A portable lightweight device for securing a positive forced movement of
air or gas, either into or out of a closed area. It requires compressed air or gas to operate and has no I110Vlllg parts. The device converts the pressure of a compressed air or gas
by expansion at a high velocity through an annular orifice, and produces a powerful venturi or jet effect. This causes a large volume of the gas in the pipeline to be drawn through the
bell of the air mover, and be delivered with the expanded air or gas supply through the outlet ho11l. Auto-ignition Temperature -The lowest temperahlre at which a flammable gas or vapor-aIr
mixture will igni te from its own heat source or a contacted heat surface without the necessity of spark or name. Blanking or Blinding -The absolute closure of a pipe, line or duct by
fastening across its bore a solid plate or "cap" which completely covers the bore. Combustible Liquids -Liquids with a flash point at or above lOO°F. When these liquids are heated to
or above their flash point, they may have some of the same characteristics and hazards of a flammable liquid. Combustion -The act or process of continuous burning that follows after
ignition, which involves rapid oxidation accompanied by the evolution ofheat and usually light. Convection -The transfer of heat or electricity by means of mixing or circulating heated
or electrified particles. Double Block and Bleed -The closure of a line, duct or pipe by locking open and tagging a drain or vent valve which is open to the atmosphere in the line between
two closed and locked valves. Explosion -A rapid increase of pressure in a confined space followed by its sudden release due to the rupture of the container. Explosive Limits -The minimum,
Lower Explosive Limit (LEL), and maximum, Upper Explosive Limit (UEL), concentration of vapor or gas in air below the LEL or above the VEL which explosion or propagation of flame does
not occur in the presence of ignition. Explosive Range -The difference between the lower (LEL) and upper (VEL) flammable (explosive) limits, expressed in terms of percentage by volume
of vapor or gas in air. Explosive Mixture -A miXhrre of flammable vapor or gas and air within the lower (LEL) and upper (UEL) limits of the explosive range. Extinguishing Agent -Material
or substance which performs a fire extingnishing function. Fire -Rapid oxidation with the evolution of heat and light. Flame -The visible heat rays which appear when the ignition of
a material is reached. Flame Propagation -The spread of flame throughout a combustible vapor area which may be in a container or across a surface, independently of the ignition source.
Generally used in connection with the capability and rate of such movement.
Inspector Permit Qualification Process Flammable -Any substance that is easily ignited, bums intensely, or has a rapid rate of flame spread. Flammable and inflammable are identical in
meaning. Flammable Limits -(See Explosive Limits) Flammable Liquids -Liquids having a flash point below 100uF and having vapor pressure nol exceeding 40 PSIA at 100°F. A flammable liquid
does not bum, rather, the vapors /i'om the liquid bum. Flammable Range -(See Explosive Range) Flammable Vapor -A concentration, by volume, of vapors in the air from a flammable liquid
within the lower (LEL) and upper (UEL) flammable limits. Flash Point -The lowest temperature of a liquid at which it gives off sufficient vapor to fOim an ignitable mixture with the
air near the surface of the liquid or within the vessel used. Hazardous Atmosphere -An atmosphere exposing employees to risk of death, incapacitation, or injury or acute illness due
to: • Flammable gas, vapor or mist in excess of 10% ofthe LEL. • Oxygen concentration below 19.5% or above 23.5%. • Atmospheric concentration of a hazardous substance above its Permissible
Exposure Limit (PEL). • Atmospheric condition recognized as Immediately Dangerous to Life or Health (IDLH). Hot Work -Any operation that produces sufficient heat or has the potential
for developing sufficient heat to cause ignition of flammable materials. Examples: Open flame, welding, grinding, gas or diesel engine, electric equipment, sandblasting, dynamiting,
static electricity, jack out/draw out/drop out of electrical disconnect switches, hot taps. Hot Work Permit -The employer's written authorization to perfonn welding, cutting, heating
or other operations which could serve as a source of ignition in a restricted area. Ignition Temperature -The minimum temperature to which a substance in air must be heated in order
to initiate or cause self-sustaining combustion independent of the heating source. Interior Line Breaking -The intentional opening of a pipe, line or duct that is or has been in service
carrying flammable, corrosive or toxic material, or carrying any fluid at a pressure greater than atmospheric or temperature greater than II0aF, or cold enough to cause a severe flinch
reaction or thennal injury. Lockout and Tagout -A means of isolating a pipeline or system by securing all energy sources and placing a padlock or tag on the control (valve, switch, etc.)
to assure that all employees are aware that the condition or placement of the valve or switch should not be changed. Oxidation -The combination of a substance with oxygen. Restricted
Area -Those areas or activities which have been designated by location supervision as requiring the Hot Work Pennit procedure. These include all areas where hydrocarbons, are handled,
Inspector Permit Qualification Process stored, piped or processed. Example: Compressor Stations, NG Treating Plant, Gasoline Plants, LPG Pump Stations, LPG Tank Farl11s, LPG Loading
Areas, API Separators, and Hydrocarbon Pipelines. Spontaneous Ignition -Ignition resulting frolll a chemical reaction in which there is a generation of heat from oxidation of organic
compounds until the combustion or ignition temperanJre of the matenallS reached. Technician -The employee designated to render technical safety infollnatioll pertaining to specialized
job operations plior to the execntion of some work perl11its. Examples would include the employee who operates a pipe locator. Operations Representative Designee -The appointed person
for the unit/area where that pennit is issued and has been designated, in writing, by the location Supervisor and the Safety & Health as capable (by education and experience) of anticipating,
recognizing and evaluating worker exposure to hazards/unsafe conditions and will use good judgment in aniving at their decision. The Designee shall be capable of specifYing necessary
control and/or protective action to insure worker and equipment safety. This person authorizes and issues the Work Pennit. Vapor -The gaseous phase of a substance which is a liquid at
normal temperature and pressure. Vapor Density -Weight ofa vapor per unit volume at any given temperature and pressure. Vapor Pressure -The pressure exerted at any given temperature
by a vapor either by itself or in a mixture of gases. It is measured at the surface of an evaporating liquid. FIRE THEORY FIRE is made up of the four following components: 1. Fuel -The
most common fuels contain hydrogen and carbon. 2. Heat -A necessary condition for ignition to occur. 3. Oxygen -Oxygen plays a key role in regulating the speed of burning for most fuels
and is a necessary element for combustion to initiate and continue. 4. Chemical Chain Reaction -A chemical reaction in which intermediate products are formed which are necessary for
the existence and continuation of flames. CLASSIFICATIONS OF FIRES The National Fire Protection Association has broken all fires into four separate classes based on the type of extinguishing
media necessary to combat each. l. Class A Fires -Fires that occur in ordinary combustible materials such as wood and paper. Water is the recommended media for cooling and quenching
Class A fires. 2. Class B Fires -Fires that occur in a vapor-air mixture above the surface of flammable liquids. 3. Class C Fires -Fires that occur in or near electrical equipment where
no-conductive extinguishing agents are required. 4. Class D Fires -Fires that occur in combustible metals such as magnesium, titanium, lithium and sodium. Each flammable metal requires
its own extinguishing agent. The following is a classification system established by the National Fire Protection Association: Flammable Liquids Class I -Flash points below 100°F Class
IA -Flash points below 73°F and boiling points below 100°F
Inspector Permit Qualification Process Class [8 -Flash points below 73°F and boiling points above 100°F Class IC -Flash points at or above 73°F and below 100°F Combustible Liquids -Liquids
with flash points at or above 100°F Class]] -Flash points at or above 100°F and below 140"F Class !II A -Flash points at or above 140°F and below 2000p Class !II B -Flash points at or
above 2000p COMMON FLAMMABLE AND COMBUSTIBLE MATERIALS WITHIN THE GAS INDUSTRY Various flammable and combustible materials, including solids, liquids and gases, exist within the gas
industry. This section is dedicated to the identification of the more common of these and where they exist in the work place. GASES Methane -Methane, in various concentrations, exists
in virtually all processes within the industry. Methane is also referred to as natural gas, sweet gas or marsh gas. It is the main product in marketable or commercial gas. Natural gas
containing high concentrations of methane (87-95%) has the following properties: Specific Gravity (AIR = 1.0) ....................................... 590 -.614 Ignition Temperature ..................
............................ 900 -11700F Limits of Flammability ............................................ 04.7 -15.0% From these properties, it is easily concluded that methane is
an extremely flammable gas. It is lighter than air and is easily ignited. High concentrations of methane are found in all pipelines (main and field gas gathering), mainline and field
compressor stations, treating and gasoline plants. Hydrogen Sulfide -H2S also exists in various concentrations in most processes within the industry. Hydrogen sulfide is a highly flammable
and toxic gas. H2S of98% or more has the following properties: Specific Gravity (AIR = 1.0)...................................... 1.2 Ignition Temperature ............................................
.. 500°F Limits of Flammability............................................ 4.3 -46.0% Hydrogen sulfide is an extremely flammable and poisonous gas. It exists in high concentrations
in sulfur plants, treating plants, flare lines, many gathering lines and some compressor stations. Work with or around H2S should not be attempted without a thorough knowledge of the
compound. Iron Sulfide -(A by-product of H2S) -Iron sulfide is formed in a finely divided state as a film or sludge whenever H2S is in contact with iron or steel. It may also be formed
in the presence of iron, sulfur and heat. Spontaneous combustion may take place on exposure of iron sulfide to the oxygen in the air, thus providing an unwanted ignition source. Steaming
of vessels containing iron sulfide is the most effective way to remove carbon vapors and liquids. If this is not possible, iron sulfide should be kept wet during work activities.
Inspector Permit Qualification Process LP Gas -(Propane, Butane, Ethane) -LP Gas is a mIxture of materials all comprised of carbon und hydrogen. In commerce, LP gas is mainly either
propane or normal butane or mixtures of these with smaller amounts of ethane, ethylenes, propylene and butylene Propane has the following properties: Specific Gravity (AIR = 1.0) ....................
................. 1.5 Ignition Temperature.................................... .......... 842°F Limits of Flammability ............................................ 2.15 -9.60% Butane
has the following propeliies: Specific Gravity (AIR = 1.0) ...................................... 2.0 Ignition Temperature... ................... .................... .... 550°F Limits
of Flammability ............................................ 1.55 -8.60% LP Gas vapor is nonnally 1-1/2 -2 times heavier than air, therefore it will tend to spread along the ground sometimes
associated with a visible fog of condensed water vapor LPG is extremely flammable and is most commonly fonnd in gasoline and fractionation plants, liqnid storage and loading facilities.
LIQUIDS Natural Gasoline (C5 +) -An extremely flammable liquid hydrocarbon. Gasoline is a product of the distillation process in most gasoline plants. Drip gasoline may also be found
in field operations. This liquid has the following properties: Specific Gravity (WATER= l.0) ....................................... 72 -.76 Flash PoinL ..............................................
...... 45°F Auto-ignition Temperature .......................................... 536 -850'F Limits of Flammability ............................................ 1.4 -7.6% Vapor Density
(AIR = l.0) ......................................... 3.0 -4.0 Gasoline -A dangerous fire and explosion hazard when exposed to heat and flames. Vapors are three to four times heavier
than air and can flow along surfaces, reach distant ignition sources and flash back. This liquid may be found in gasoline plants, storage and loading facilities, field gathering pipelines,
scrubbers and drips. Gasoline can react violently with oxidizing agents. Glycol -Glycol readily absorb moisture and are widely used in dehydration of natural gas. Di-ethylene and tri-ethylene
glycol have been used to dehydrate natural gas since the 1940's. Glycol is a combustible liquid with a low fire hazard unless heated, and has the following properties: Boiling Point
................................ , 446°F Flash Point .................................. , 230°F Auto-ignition Temperature ..................... 442°F Limits of Flammability ........................
, 0.9 -6.2% Glycol is a colorless, sweet tasting, poisonous liquid. This combustible is mainly found in field treating operations and treating plants. Caution should be exercised when
hot work is perfonned near glycol.
Inspector Permit Qualification Process OTHER COMBUSTIBLE LIQUIDS Many liquids exist in various areas in the industry. Before any "Hot Work" is attempted in or around facilities containing
liquids, knowledge of that substance and its properties should be acquired. Lubrication Oil -A low fire hazard, unless heated. Many different types of oils are used on various equipment.
Most lube oils have high flash points and auto-ignition temperatures. Amine Treating Solutions -The various treating amines (DEA, MEA, DGA) are made up mainly of water. However, after
tbe treating process has taken place and the treating solutions absorb hydrocarbons, these hydrocarbons may cause a fire hazard when heat is applied. Safety Solvent -A petroleum type
solvent used for cleaning that has replaced Varsol at most all of EPNG's locations. This solvent goes by the name of Lube Rite and Solvent 140-66. Safety solvent is an NFPA class IIIA
combustible liquid. Like lubricating oil, this solvent can become explosive if heated. Flash Point.. .......................................... 142-150 deg. F Auto-ignition Temperature...............
....... No Data Limits ofFlamrnability............................ 1.0 -6.0% Vapor Density (Air = 1.0)...... .................... 5.48 Specific Gravity (Water = \.0) ......................
780 Establishing Hot Work Areas This appendix provides guidance on determining and establishing hot work areas in a facility inside which a hot work pennit would be required to conduct
hot work. The work product is intended to serve as a training and resource tool to ensure consistent and safe application of the hot work procedure. Class I Locations Class I locations
are those in which flammable gases or vapors are or may be present in the air in quantities sufficient to produce explosive or ignitable mixtures. Class I locations shall include those
specified in (a) and (b) below. (a) Class I, Division I. A Class I, Division I location is a location (1) in which ignitable concentrations of flammable gases or vapors can exist under
normal operating conditions; or (2) in which ignitable concentrations of such gases or vapors may exist frequently because of repair or maintenance operations or because of leakage;
or (3) in which breakdown or faulty operation of equipment or processes might release ignitable concentrations of flammable gases or vapors, and might also cause simultaneous failure
of electric equipment. (b) Class I, Division 2. A Class I, Division 2 location is a location (I) in which volatile flammable liquids or flammable gases are handled, processed, or used,
but in which the liquids, vapors, or gases will normally be confined within closed containers or closed systems from which they can escape only in case of accidental rupture or breakdown
of such containers or systems, or in case of abnormal operation of equipment; or (2) in which ignitable concentrations of gases or vapors are normally prevented by positive mechanical
ventilation, and which might become hazardous through failure or abnormal operation of the ventilating equipment; or (3) that is adjacent to a Class I, Division 1 location, and to which
ignitable concentrations of gases or vapors might occasionally be
Inspector Permit Qualification Process communicated unless sdch communication IS prevented by adequate positive-pressure velltilation from a sourCG lIf clean aIr, and effective safeguards
against ventilation failure are provided. Class II and Class III -definitions are summarized below but are not normally expected to occur. Issuers of hot work permits should be aware
of these hazards from combustible materials when issuing pel111its. Class II locations are those that are hazardous because of the presence of combustible dust. Class III locations are
those that are hazardous because of the presence of easily ignitable fibers or flyings, but in which such fibers or flyings are not likely to be in suspension in the air in quantities
sufficient to produce ignitable mixtures. WORK SITUATIONS REQUIRING HOT WORK PERMIT Operations or work situations requiring the Hot Work Permit are those creating or capable of creating
sufficient heat to cause the ignition of flammable materials. Welding 0 perations Arc The most common type of arc welding is shielded metal arc (sometimes called stick welding). The
intense heat from an electrical arc is used to melt and fuse metals to form a weld. The heat created by this operation is sufficient to cause the ignition of virtually all flammable
materials in the gas industry. Welding can also create enough heat that the flash point of many other materials can be reached. Gas Gas welding is a manual fusion welding process similar
to arc welding except welds are made with a very hot gas flame instead of with the heat from an electrical arc. The metal surfaces to be joined are melted by the gas flame so they merge
or mingle and, after cooling, form a strongly bonded joint. Oxygen and acetylene are the gases most widely used for gas fusion because they produce a hotter flame than other gas mixtures.
The Oxyacetylene flame has a maximum temperature of about 6,300°F, which is more than sufficient heat to cause the ignition offlammable materials. Oxygen and Acetylene Cutting Operations
When fitted with a special cutting torch, an oxyacetylene welding outfit is quickly converted to an oxygen cutting outfit. The gas and oxygen mixture is regulated so that the temperature
is sufficient to melt the metal and added oxygen pressure blows the molten metal from the cut. This operation, like the welding flame, reaches temperatures in excess of 6,OOO°F. Grinding
Operations Portable and table grinders are among the most helpful power tools used by a maintenance craftsman. These tools are also capable of creating sufficient heat to ignite many
flammable materials. The mechanical energy used in overcoming the resistance to motion when two solids are rubbed together is known as frictional heat. Any friction generates heat. Friction
sparks include the sparks which result from the impact of two hard surfaces, at least one of which is usually metal. Although the temperatures generated vary with different types of
metal, in most cases they are sufficient to cause ignition of flammable materials. Other operations creating friction sparks include steel tools. Static Electricity
Inspector Permit Qualification Process Static electricity (sometimes called frictional electricity) is an electrical charge that accumulates on the surfaces of two materials that have
been brought together and then separated. Olle surface becomes charged positively, the other negatively. If the substances are not bonded or grounded, they will eventually accumulate
a sufficient electrical charge so that a spark discharge may occur. Static arcs are ordinarily of very short duration, and do not produce sufficient heat to ignite ordinary combustible
matelials such as paper. Some, however, are capable of igniting flammable vapors, gases, and clouds of combustible dust. Sand blasting operations are capable of producing such an electrical
charge and static discharge. Other operations capable of creating a static spark include: LPG loading operations, tank filling, liquid transfer etc. Electricity ElectJicity is capable
of creating sufficient heat, in many situations, to ignite flammable liquids and vapors. The heat from arcing electrical CUlTent is file most common source of electJical ignition of
flammables. Arcing occurs when an electrical circuit which is carrying current is intentionally or accidentally interrupted. The arc temperatures are very high, and the heat released
may be sufficient to ignite flammable materials. Arcing may be caused by improperly wired tools or equipment, switches and plugs, fi'ayed wiring, etc. EQUIPMENT The equipment and accessories
used in order to assure safe working conditions involving hot work must be understood and demonstrated. Explosive-meter -Eagle, MSA, Scout, Gas Scope, Etc. H2S Detection -When working
in areas where H2S may be present, it is extremely important to test for this highly toxic gas. Not only is the extreme flammability of the substance a concern, but also its toxic effect
on workers. Fire Extinguishers It is important when monitoring hot work to select a fire extinguisher that is suitable for the flammable or combustible materials involved and the nature
of the work area. The selection of the extinguishing mefilod should be made with caution. Each work situation should be evaluated individually, with consideration placed on the type
of fife that may be encountered. • Carbon dioxide, dry chemical, foam and vaporizing liquid (halon) type extinguishing agents have proven to be effective for use on flammable liquid
fires of moderate size. • CO2 and halon extinguishers are normally used for electJical fires in the work area. Due to the nonconductivity of these agents and easy clean-up, these have
been found to be suitable. • For fires involving natural gas, where little or no liquids are involved, dry chemical and halon have proven to be the most effective. It should be noted
that fire extinguishers combat fire by breaking the chain reaction and displacing the oxygen. Therefore, caution should be taken not to displace the oxygen within a work area, making
the environment unsuitable for workers. • Water spray is particularly effective on Class A fires and fires involving flammable liquids having flash points above lOO°F. Water may be ineffective
fighting fires in low flash point liquids.
Inspector Permit Qualification Process • It is always preferable to create a hot work situation where 110 fire is involved. However, due to gas leakage from valves, flammable liquids
and other factors, this is not always possible. When supervising hot work, always anticipate these problems and be ready .to react.
Hot Work Permit Issued to __ :=--___ -:-_c--______ to perform work in (Department or Company) area -;-_--;--:;--_ _ ______ section, _______ _ Work description, ______ --:::-_~::_:_:_c-------Work
Order No, ,--__ _,_-,-Permit Ref, No, ______ _ • Date • Permit valid from ______ to ___ _ Revalidation Date Time to ___ _ Revalidation Authorization: * Permit valid only for the date
and time stated, Revalidation good for one shift or maximum of 12 hours, Yes No 1, Is the equipment properly isolated or blinded? 0 0 2, Is the instrumentation tubing disconnected, depressured,
and capped? 0 0 3, Is the equipment depressured and drained? 0 0 4, Have all valves been properly closed, blinded, locked, and tagged? 0 0 5, Has equipment been steamed or flushed? 0
0 6, Has equipment been purged? Type 0 0 7, Is equipment free of flammables? 0 0 8, Have sewers been covered? 0 0 g, Is the proper electrical breaker locked, tagged, and start test tried?
0 0 10, Is fire extinguisher available? 0 0 11, Is firewatch required and assigned? 0 0 12. Has toxicity of hazardous atmospheres been tested for? 0 0 13. Special instructions to be
followed are: The following protective equipment is required but not restricted to: o Faceshields 0 Goggles 0 Gloves o Boots 0 Chemical Suit 0 Chemical Apron o Breathing Apparatus 0
Welding Goggles 0 Leather Gloves/Gauntlets o Fall Protection 0 Other ______________ _ Verified By: __ -=-_-::-_-=_--,--________________ _ Operations Signature Explosimeter test results
% LEL (Reading must be 10% LEL or lower). If above 10% LEL, management must approve and sign the permit Other Pertinent Tests Substance Tested for: Result _____ _ Firewatch: --------;-::,--;-;---:-~_
_::_:____:_c:-------------(Fulf name-No initials) Permit issued to: -----=c------,---.,------------(Full name-No initials) Permit issued by: -----;:=----:----:----:::-:;----:-:--:__::_:____:_c:------
-(Person in charge, FulJ name-No initials) To be filled out by a Permit Worker, signed, and retumed to the Person-In-Charge. Yes No Initials 1. Locks and tags (Deisolation) have been
removed. o 0 2. Work area and equipment have been cleaned, o 0 3. Work has been completed. o 0 Permit Worker Signature Date Initials ---This permit is automatically canceled when any
emergency alarm is sounded.
Energy Transfer Company Gas Detection I nstru mentation
Hazardous Atmosphere Testing Qualification Training Training Expectation To ensure that the hazardons atmosphere (gas) testing program is implemented properly. And to explain the generall"oles
and responsibilities of those Employees and Contractors involved in the hazardous atmosphere testing program. Responsibilities for Equipment Preparation Designation and preparation of
equipment for work including any associated hazardous atmosphere testing is responsibility of Operations and/or a designated Contract Inspector. In defining the job to be done it may
be necessary to consult with persorUlel from other departments, i.e. group performing work. When equipment has been selected and job defined, the responsible person ensures proper preparations
of equipment, which may include items listed below: Isolation Depressurization Lockout Blinding Washing with water Ventilating with air Steaming Purging Cleaning Hazardous Atmospheres
Depending upon a worker's background, the term "Hazardous Atmosphere" can range from toxic air contaminants to flammable atmospheres. For purposes of this training an atmosphere is hazardous
if it meets the following criteria. Mixture of any flammable material in air whose concentration is within the material's flammable range (i.e. between the material's lower flammable
limit and its upper flammable limit). Hazardous substance has potential of exceeding permissible exposure limit. Page I
Atmosphere has potential to become an oxygen deficient or an oxygen enriched atmosphere. Types of Direct Reading Instruments There are several types of instrumentation for detecting
hazardous atmospheres. Oxygen Indicators Oxygen indicators are used to evaluate an atmosphere. Oxygen content for respiratory purposes in nomlal air is 20.9% oxygen. If oxygen content
decreases below 19.5% it is considered oxygen deficient and special respiratory protection is needed. Increased risk of combustion; concentrations above 23.5% are considered oxygen enriched
and increase the risk of combustion. Some instruments require sufficient oxygen for operation. For example, some combustible gas indicators do not give reliable results at oxygen concentrations
below 10%, the inherent safety approvals for instnllnents are for nonnal atmospheres and not for oxygen enriched atmospheres. We can not over emphasize importance of conducting testing
for oxygen deficient/enriched atmospheres first. Combustible (Gas) Atmosphere Indicators Combustible gas indicators (CGIs) measure the concentration ofa flammable vapor or gas in air,
indicating results as a percentage of the lower flammable limit ofthe calibration gas. The LEL (lower explosive limit) or LFL (lower flammable limit) of a combustible gas or vapor is
the minimum concentration of material in air that will propagate flame on contact with an ignition source. The UFL (upper flammable limit) is the maximum concentration. Above the UFL
the mixture is too rich to support combustion so ignition is not possible. Below the LFL there is insufficient fuel to support combustion. The LEL and VEL for natural gas are approximately
5% and 15% respectively. NOTE: The lower explosive limit (LEL) and lower flammable limit (LFL) have the same meanmg. Toxic Atmosphere Monitors Along with oxygen concentration and flammable
gases or vapors there is a concern about chemicals present at toxic concentrations. This usually involves measurements at . concentrations lower than would be indicated by oxygen indicators
or combustible gas indicators. There is a need to detennine if toxic chemicals are present and identify so the environmental concentration can be compared to exposure guidelines. Toxic
atmosphere monitoring is done to: Identify airborne concentrations that could pose a toxic risk to workers and the public. Set up work zones or areas where contaminants are or are not
present. Page 2
Evaluate need for and type of personal protective equipment including respiratory protection. There are several different instruments used for these pUllJoses Color metric Indicator
Tubes (Detector Tubes) Colormetric indicator tubes consist of a glass tube impregnated with an indicating chemical. The tube is connected to a piston or bellows type pump. A known volume
of contaminated air is pulled at a predetermined rate through the tube, by the pump. The contaminant reacts with the indicator chemical in the tube, producing a change in color whose
length is proportional to the contaminant concentration. Detector tubes are nonnally chemical specific. Thete are different tubes for different gases; for example, chlorine detector
tube for chlorine gas, etc. Some manufacturers do produce tubes for groups of gases, e.g. aromatic hydrocarbons, alcohols. Detector tubes can not be mixed. An MSA tnbe can not be nse
with a Drager pump, etc. Multi-Gas indicators Mnlti-purpose instrument designed to monitor areas for flammable/combustible vapor and oxygen deficiency as well as other gases such as
H2S or CO. These indicators function the same as those described above, but allow the operator to sample the atmosphere for all hazards using one instrument. In today's environment the
multi-gas indicator is llsed for most applications. These indicators, depending on manufacturer have visual and audio alanns for each chaIlIlel to wam the operator or worker of atmospheric
hazards. The multi-gas indicator requires a calibration gas containing a standard for each contaminate the indicator is capable of testing, only calibration gas specifically manufactured
for the instrument can be used. Atmospheric Testing Requirements There are several sections of the ETC Safety Handbook that may require atmospheric testing, including Confined Space
Entry, H2S, Respiratory Protection, and Excavation. When equipment has been properly prepared, the "Job Site" is ready for testing. Atmospheric testing to fulfill requirements of the
Work Pennit Program must be performed, i.e. hot work pennit, and/or confined space entry penuit. Periodic gas tests may be required to assist persoIlI1el with the various steps of equipment
preparation. Hot Work Permit If hot work is to be perfonned in an area where flammable mixtures may be present, a gas test for flammable vapors must be perfonued. Ideally zero LEL should
be obtained before proceeding with hot work, but hot work can perfonned up to a 10% LEL level, if 10% or less can not be achieved, the work can only be perfonued with management approval
and signature. Page 3
Tests for toxic or cOll"osive substances must also be perfolllled when their presence is suspected. Permit Entl"y Confined Space When entry into a permil entry confined space is required,
gas tests for flammable vapors and oxygen content must be perfOimed. Entry into a Pennit Required Confined Space has extensive safety and regulatory requirements which must be met. Every
reasonable effort needs to be made to remove hazards and downgrade the confined space to the "safest" state. If the space can not be downgraded to a "non pe1111it" required confined
space ETC employees will enter only as a last resoli and then only with Safety DepaiLment approval after all regulatory requirements have been met. If a Pennit Entry is required, ETC
will contract the entry to a qualified and experienced Contractor and defer to that Contractor's PECS program. Tests for toxic or corrosive substances must also be perfonned when their
presence is suspected. Performing Atmospheric Tests When a hazardous atmosphere test is required, the issuing authority notes this fact on pennit and specifies particular gas test needed.
In most cases the permit issuer will also perform the testing. Before going to work on site the person performing the test must: • Understand specific equipment involved and tests to
be preformed. • Ensure testing instrument is functioning. • Select correct Drager tube (detector tube) when tests for toxic substances are specified. Perform atmospheric tests stipulated
on work permit in accordance with guidelines. Confined Space When entry into a pennit entry confined space is necessary for testing, the person performing the test must be provided with
supplied air respiratory protection and any other protective equipment that may be needed such as impervious boots, chemical resistant slicker suit, gloves, etc. Ventilation must be
stopped 15 minutes prior to conducting the gas test, except when continuously monitoring. Perform tests throughout large spaces such as tanks, drums, towers, or excavations where it
may be possible for gas to be trapped in dead end nozzles, plugged downcomers, structnral members, etc. Perform tests at many levels in taller vessels since some gases are heavier than
air and tend to fall to the bottom and some which are lighter rises to the top. Page 4
Inert Atmospheres Using a gas tester to analyze an inert gas atmosphere can produce a false read mg. Always consult with the manufacturer about special requirements. Open Areas The primary
concern in open areas is flammable/combustible gas, however; gas tests for toxic substances 'should also be conducted if presence of toxic substances is suspected. Checks should be made
around and at all openings of equipment where work is to be done. Tests at sewer openings, open vents, bleeds, and at any other possible locations in area where leaks may be suspected.
General It is recommended gas testing be continued throughout the course of work or at specified intervals, i.e. hot work in an area when conditions could change or tank cleaning when
work may cause a change in conditions (agitating sludge or other by products). For a gas test to be valid it should be performed as close as possible to the time work in the tested aTea
begins. At a minimum gas tests must be repeated when: Two or more hours pass between test and start of 1V0rk. Work is stopped and resumes at a later time. Conditions change. Record results
of gas tests and sign work permi t. If at anytime during the course of work the instrument alarm sounds, warn other workers to exit the area, the permit is cancelled. Take the instrument
to clean air to clear the instrument, and re-test and assess the area before returning. Ignition Sources Examples of ignition sources include but are not limited to: Acetylene/gas burning
Welding Use of open flames Grinding Drilling Page 5
Gasoline engines driving equipment such as pumps, generators etc. Ignition sources must not be introduced into an area that may contain a flammable concentration in air without !irst
performing atmospheric testing. Hot Work Permits are required when ignition sources are to be used within 40 feet of any threaded or flanged pipe connection, vent source, flammable liquid
storage/dispensing area, process equipment, tanks etc., that handles flammable products or within any facility containing such products. Maintenance and Calibration of Monitors To ensure
proper operations and meter responses, it is important to maintain and calibrate all instruments. The following establishes responsibilities and methods by which maintenance and calibration
will be accomplished: Have available a calibration kit from vendor and use them to verify meter calibration at least monthly or in accordance with the manufacturers recommendations.
Calibration is performed by using a known gas/air mixture to ensure the meter response is accurate. Place a calibrated sticker on instruments immediately after calibration. Include date
and initials of person performing calibration. Calibration checks should be recorded in an appropriate log. Carry out battery and meter adjustment checks each time an instrument is used.
Functional checks of oxygen and combustible gas meters should be carried out each day before use. Functional or bump test is defined as a brief exposure of the monitor to a known concentration
of gases for the purpose of verifying sensor and alarm operation and is not intended to be a measure of the accuracy of the instrument. Any instrument not operating properly or out of
calibration should be tagged "DANGER DO NOT OPERATE" and sent to the appropriate vendor for necessary repair. Drager/MSA Type Gas Detector This hand operated bellows pump draws measured
amounts of air through a gas tube which contains a variety of substances that react selectively with certain chemicals to change colors of the materials in the tube. The concentration
of the particular chemical in sampled area is measured as parts per million, PPM, by volume and is indicated by color change within a selected tube. Permissible exposure limits for these
contaminants may be found in Federal Regulations Code 29 eFR 1910.1000. Tests for over two hundred of these contaminants can be made with this instrument. In today's environment this
instrument is seldom used due to availability of the Multi-gas monitor, but it is important that personnel understand that this device can be used for testing when necessary. Page 6
Permit Responsibilities Permit Issuer/Company Representative Conduct pre-job safety meeting with ETC and contract personnel. Inspect the work site and conduct gas tests for flammable
and/or other hazardous conditions. Ensure a minimum oftwo fire extinguishers and other necessary safety and communication equipment is available. Identity any special precautions necessary
and list on the permit. Complete and sign the permit veri tying the pennit conditions have been met and monitor the work as it progresses ensuring the conditions have not changed. Stop
the work if a change occurs which creates an unsafe condition. Work will not resume until a safe condition is restored. Designate a safe area for all personnel to meet in case of an
emergency. Person doing the work (permit worker): Read, understand, and sign the Hot Work permit. Advise other works of any special precautions or conditions pertain to the job. Know
where the nearest fire extinguisher and other necessary safety and communication equipment are located. Provide necessary equipment, such as: combustible gas detectors, dry chemical
fire extinguishers, oxygen meters, safety belts, respiratory equipment, barricades, shoring, etc., as required. Clean up and secure work area after completion of work. When any emergency
announcement is made, stop all work and proceed to a safe area. Do not resume work until notified by an ETC representative. Fire Watch Observe an area of at least 50' around the hot
work site, and maintain the area free of combustibles and tripping hazards. Have no other duties assigned while on watch. Sign the Hot Work permit and adhere to the conditions listed
on the permit. Be properly trained in the use of the fire extinguisher and other safety equipment. Call for emergency assistance and extinguish any small fires. Page 7
Fire watch will remain on watch for 30 minutes after completion of cutting or welding to make certain no ignition takes place from residual heat. Hands On Training To operate specific
atmospheric test equipment the candidate wiII need access to that instrument, instrument calibration equipment and the operator's manual. Page 8
Hazardous Atmosphere Testing Direct Reading Instruments Genet'al Knowledge • Responsibilities for Equipment/Vessel Preparation o Describe what is required to prepare equipment or the
job site, for gas testing. • Hazardous Atmospheres o Describe three types of hazardous atmospheres. • Types of Direct Reading Instmments o Describe the following: • Combustible Atmosphere
Indicators • Oxygen Indicators • Toxic Atmosphere Monitors • MuIti'gas indicators o Describe LEL and VEL in relation to flammable concentrations in the atmosphere. o Identify the LEL
and VEL of natural gas. • Atmosphere Testing Requirements o Describe when atmospheric testing is required. o Describe how Often testing is required. o Describe when re-testing is required.
• Ignition Sources o Describe why ignition sources must be limited. o Describe types of ignition sources. Periodic instrument calibration • Describe and demonstrate instmment calibration
according to manufacturer's recommendations. • Describe the recordkeeping requirements for instmment calibration. Bump testing • Describe when bump testing is required. • Demonstrate
bump testing. Performing atmospheric testing • Describe and Demonstrate hazardous atmospheric testing. Issuing Hot Work Permits • Describe the role of the pemlit issuer/authorizer. •
Describe the role of the worker receiving the permit (permit worker). • Describe the fire watch requirements. • Describe when a Hot Work Permit is cancelled. • Demonstrate completion
of a "Hot Work Permit". Page 1
Hazardous Atmosphere Testing Qua lifica tion This is to certify that . _____ has satisfied the qualification requirements to perform hazardous atmospheric testing related to the completion
of "Hot Work Pennits" for Energy Transfer Company. The person named above has completed training and demonstrated the physical ability to conduct the necessary tests required by the
Energy Transfer Company Hot Work Permit program. Qualification Evaluator Signature Date _____ _ I have completed the training required for hazardous atmosphere testing. I understand
the importance of hazardous atmospheric testing and the Hot Work Pennit program and will fulfill those duties to the best of my ability. Candidate Signature _________________ Date ____
_ Page 2
Energ.y Transfer Company Lock-Out Tag-Out
ENERGY ISOLATION Lock ouUTag out Energy Transfer Company requires compliance with applicable Energy Isolation Standards. This is accomplished through the use of appropriate engineering
controls, management controls, employee training, personal protective equipment, recordkeeping, and safe work practices. Application: A!lmachines and equipment are isolated and rendered
inoperative by locking out and tagging all applicable energy isolating devices that physically prevent the transmission or release of energy to the machine or equipment while work is
being performed. A positive means of isolation must be implemented and verified before work commences. This section is applicable when any ETC employee or contractor is required to work
on various sources of energy, including electrical, mechanical, hydraulic, and pneumatic or stored pressure. Examples of work activities as described above include, but are not limited
to maintenance and service of pumps and compressors; repair anciJor replacement of valves or pipelines; motor repairs; tower and tray work; filter change-out; equipment and vessel cleaning;
etc. Acceptable Energy Isolation Devices There are six types of mechanical energy isolating devices used to isolate equipment and prevent the unexpected release of stored energy while
service and maintenance work is being performed: I. Electrical source disconnects. 2. Double block-and-bleed valves (i.e., twin seal valves or valve arrangement; two single in-line block
valves with a bleeder; sample or vent outlet between the valves). 3. Single block valves that provide a positive seal and can be verified. 4. Air gapping with blind flanges or spool
piece removal. 5. Isolation blinds 6. Stopples Important Note: , The use of "stopples" as isolation devices requires the development of a detailed job safety plan and approval. Pipeline
Operation must provide procedures for clearing the line segment down stream ofthe stopple fitting as well as procedures to verifY all liquids have been removed to verifY the stopple
fitting has properly sealed preventing any leaking of hydrocarbons past the stopple fitting. The use of these devices is an integral part of our established safety practices and procedures
for preparation of equipment for maintenance. However, under this policy, these devices are locked out and tagged prior to any work being perfonned in the upstreal11ldownstream de-energized
side of these devices. Requirement Guidelines: 1. Workers will be trained and qualified 2. Perform an initial evaluation of the equipment being isolated to determine any hazard
ENERGY ISOLATION Lock out/Tag out 3. Use locks for energy isolation controls which are user-identified and uniquely keyed which add protection against tampering with locked or tagged
systems, and ensure others do not tamper with LOTO devices. 4. Resolve any Company/Contractor energy isolation control differences or conllicts that may create a hazard before work begins.
5. Notify Affected Employees of the application of energy isolation devices. 6. Isolate and/or lockout all identified energy sources. 7. Tag devices with tags identifying the Authorized
Employee and date applied. 8. Clear the area sUlTounding the equipment of personnel. 9. Test the equipment to verify energy sources are controlled before beginning work 10. Immediately
stop unsafe activities and report them to location snpervision. 11. Make notification to Affected Employees of the removal of LOTO devices. 12. Remove locks /tags used to control hazardous
energy. Procedures: General Energy Isolations Procedures The responsibility for compliance with LockoutiTagout procedures rests with the supervisors and workers performing the LockoutiTagout
procedures. This can include Operations, Engineering, Inspectors, Construction or Contract persormel performing and authorizing the work. The operations supervisor/designee authorizing
the work and the individuals of each crew performing the work are required to follow all safety procedures outlined. The following basic procedures apply in all LockoutiTagout situations.
Detailed Procedures The following guidance applies to all pipeline operations. Refer all questions regarding the application of these procedures to the operations supervisor or a safety
department representative. l. Pipeline operations personnel must notifY all employees and contractors when LockoutiTagout procedures are required prior to the work being performed. 2.
Ensure that all necessary notifications regarding equipment isolation and decommissioning are made to the facility control room or pipeline control.. 3. Review the most current flow
or equipment diagrams to assist in locating all isolation points. 4. Survey the work area and equipment to identifY isolation points and the proper methods of energy isolation. S. In
compression/pump stations, render safe the equipment being worked on by isolating and relieving any stored hazardous energy, by closing valves or switchgear, opening vents, disconnecting,
restraining or blinding. Blinds are installed when the release of flammable or toxic liquids, vapors or gases into the work area cannot be controlled. 6. On pipeline operations, close
all block valves that feed into the line where work is performed. Chain, lock, and tag the isolation valves with a DANGER: DO NOT OPERATE or other appropriate tag. Blinds (where applicable)
are installed when the introduction of flammable materials into the work area is not controlled.
ENERGY ISOLATION Lock out/Tag out 7. Pipeline Operations prepares the isolation and/or blinds identifying all electrical and/or mechanical isolation points associated with the equipment/machine
taken out-of service. The following guidelines are presented to assist ill prepanng the "Isolation/Blind List", and implementing these procedures: • All piping is physically traced and
verified by single line drawings, if possible, to determine all sources of pressure such as pumps, hydrostatic head pressure, and manifold lines, and to identify which valves and pressure
sources need to be blinded, closed, disconnected and/or depressurized. • Valves that stop the flow of material to the equipment being opened are closed, locked and tagged. Single block
valves in hydrocarbon service must provide a positive seal. If a positive seal is not achieved, a thorough hazard evaluation must be conducted and a Job Plan developed to make the work
safe. Precautionary measures may include installation of blinds behind leaking valves or use of stopples. In addition air movers may be utilized to pull hydrocarbons out of the lines
or equipment to clear the work zone. In some cases, where the use of one of these methods is not feasible or is ineffective, it may be necessary to de-pressure upstream of the isolation
valve to prevent the escape of hydrocarbon vapors while the work is being performed. Where possible, two valves on the upstream side of the point of work are closed, and both valves
are locked and tagged in the closed position. Any residual pressure between the two valves is bled from the line and a positive means of keeping the line vented is maintained by means
of locking and tagging a valve (bleed) in the opened position, or by means of spool removal. • If the equipment being opened is connected to a common header, it may be necessary to blind,
lock out and tag the valves on the downstream side of the work point. Never depend on check valves to prevent backflow of contents in the pipelines. • Verify the equipment is ready for
maintenance and/or servicing by such methods as checking pressure gauges downstream of the isolation points; "sniffing" the line for hydrocarbons or checking for other materials; opening
bleed valves; and checking on/off switches or other normal operating controls. Operations personnel ensure the equipment is totally de-energized and isolated from any potential energy
sources. • NotifY all personnel (Company and contractors) involved in the work to be performed of the type and magnitude of the energy hazard involved. This information includes the
electrical current/voltage; hazardous characteristics of the product, potential pressure involved, mechanical action or other energy potential, emphasizing the significance of proper
implementation and compliance of these procedures. 8. In the process of decommissioning the equipment, pipeline operations first locks out and tags each isolation device as it is closed,
de-energized, and/or installed in such a manner that renders the equipment inoperative and/or totally isolates it from any potential energy source. Operations places the first lock and
tag "on" and take the last lock and tag "off" the equipment being isolated.
ENERGY [SOLATION Lock out/Tag out 9. When servicing and/or maintenance is performed by a crew, craft, department or other group, they utilize a procedure which affords personnel a level
of protection equal to that provided by the implementation of a personal lockout or tagout device. 10. As a minimum, one lock and tag for each craft, group, or contractor working on
the equipment is attached to the lockout device at each energy isolation point. The use of the "lock box" methodology may be followed in some cases where the direct application of the
lock is not practical. When this methodology is used, it must be compatible with the contractor's energy isolation procedure. The contractor has the right to verify and place their locks
on each isolation point. II. Pipeline Operations ensures all additional procedures are completed for decommissioning the equipment and all requirements of the Pelmit System are implemented
prior to work commeucing. 12. Before lockout or tagout devices are removed and energy is restored to the machine or equipment, the authorized employee(s) will ensure the work area is
inspected and that nonessential items have been removed and that machine or equipment components are operationally intact. In addition, the work area shall be checked to ensure that
all employees have been safely positioned or removed from the equipment being energized. Blinding Procedures for Pipeline Operations (Compression and Pump Stations): Blinds are installed
to control the release of combustible or toxic liquids, vapors or gases during maintenance or construction. Full-rated blind meeting ANSI standards shaH be installed. All "shop built
or home made" blinds must be approved by Engineering and meet ANSI standards. In addition to this the following guidelines apply: I. Blinds are tagged for identification. 2. All blinds
are removed when work is complete. 3. During hydro-test applications (line, vessel, drum, etc.), only a rated blind flange is used. 4. During a confined space entry, a skillet blind
is inserted at each flange closest to the vessel. 5. A skillet blind (vendor manufactured, shop built, or on-site manufactured) is used ONLY if a tagged vent to atmosphere is located
between a closed and locked block valve and the blind. Preparation Guideliues for Isolating Electrical Equipment The following procedures are applicable when maintenance/service work
is performed directly on any electrically-operated equipment where the potential exposure of electrical current andlor equipment activation (startup) may result in injury to employees
and/or contractors. I. Qualified personnel prepare the equipment for repair and disconnect the electrical circuit from its source of power by means of the circuit breaker or disconnect
switch. 2. The following are conducted by qualified personnel: all power circuit disconnects of600 Volts and above; any de-energizing activities that require the opening of
ENERGY ISOLATION Lock out/Tag out the switchgear door, cover or other protective devices; and allY reaching into and/or entering the equipment in any manner. • Disconnection of the electrical
power is done at the main power or disconnect switch and never through an "off-on" push button, selector switch or electrical interlocks that de-energize electric power circuits indirectly
through contacts, controllers or other electrically-operated disconnecting devices. • Once the power source is disconnected, locked out and tagged, personnel verify the equipment/machine
operating controls (such as push button selector switches and electrical interlocks or other operating mechanism) are properly de-energized to ensure the equipment/machine is not restarted
and/or activated 1Il any manner. • Electrical circuits to machine/equipment worked on directly are checked with appropriate test equipment by qualified personnel to verify the equipment
and circuits are totally de-energized. (Safety procedures for checking "test equipment" are followed in accordance to NFP A 70E). • Where it is not possible to lock open a circuit, the
removal of a fuse or buss is an acceptable method of isolation. The fuse or buss in the switchgear is removed by a qualified person/electrician. Both operations' personnel and the qualified
person are required to place their "Danger" tag at this point of power disconnect. Where it is neither possible to remove a fuse or buss nor to lockout disconnects at the power source,
qualified personnel disconnect from the power source and place a "Danger" tag on the electrical wires to the equipment. • All "on-off' switches andlor control points between the one
locked out and the equipment being worked on must be in the "off' position so that when power or utility is restored, no damage occurs from auxiliary control panels being in the "on"
position. Note: Some automatic equipment has a built-in memory and in many instances may cycle or be activated in some manner when power is restored to the equipment. This is applicable
to "timed" andlor remotely activated equipment such as pumps, cooler fans and computer-controlled equipment. Work Activities NOT Requiring Lockout /Tagout 1. Employee controlled cord-and
plug-connected electrical tools. 2. Hot tapping operations where continuity of service is essential and shutdown of the system is impractical and the work is perfonned in accordance
with the existing established safe operating procedures that do not involve any type of maintenance/service work which exposes the individual or others to potential injury when performing
"hot tap" procedures. 3. Normal operating duties and functions routinely perfonned by operations personnel in accordance with established safe operating procedures and do not involve
any type of maintenance work that exposes the individual to the release of unexpected energy. 4. Welding on in-service pipelines conducted in accordance with specific engineering standards,
procedures, and safety requirements developed for this type of work.
ENERGY ISOLA nON Lock ouUTag out 5 Any job and/or work activities tbat meet the criteria of this policy, but are not locked out and tagged in accordance to these procedures due to abnormal
situations and/or conditions, are reviewed by the respective location supervisor and safety personnel to determine acceptable alternatives (hat protect against employee exposure to potential
injury.