Class IIIA Liquids

Class IIIA Liquids

Definition(s)


Class IIIA Liquids

Liquids having flash points at or above 60 °C (140 °F) and below 93 °C (200 °F. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Class II Liquids

Class II Liquids

Definition(s)


Class II Liquids

Liquids having flash points at or above 37.8 °C (100 °F) and below 60 °C (140 °F). API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Combustible Liquid (Class II, IIIA, and IIIB Liquids)

Combustible Liquid (Class II, IIIA, and IIIB Liquids)

Definition(s)


Combustible Liquid (Class II, IIIA, and IIIB Liquids)

Any liquid that has a closed-cup flash point at or above 37.8 °C (100 °F), as determined by the test procedures and apparatus outlined in NFPA 30. Combustible liquids are subdivided as follows: Class II liquids - Liquids having flash points at or above 37.8 °C (100 °F) and below 60 °C (140 °F). Class IIIA liquids - Liquids having flash points at or above 60 °C (140 °F) and below 93 °C (200 °F). Class IIIB liquids - Liquids having flash points at or above 93 °C (200 °F). API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Unclassified Locations (Non-hazardous Location)

Unclassified Locations (Non-hazardous Location)

Definition(s)


Unclassified Locations (Non-hazardous Location)

Locations determined to be neither Class I, Division 1 nor Class I, Division 2; or any combination thereof. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Hazardous (Classified) Location

Hazardous (Classified) Location

Definition(s)


Hazardous (Classified) Location

A location where fire or explosion hazards may exist due to flammable gases or vapors, flammable liquids, combustible dust, or ignitable fibers or flyings. Unless specifically indicated otherwise, locations containing combustible dust, ignitable fibers or flyings are outside the scope of this recommended practice. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Class I Material Groups

Class I Material Groups

Definition(s)


Class I Material Groups

For the purpose of testing, approval, and area classification, various air mixtures (not oxygen enriched) are subdivided into Groups A, B, C, or D for Class I, Division 1 and Class I, Division 2 locations. Group A—Atmospheres containing acetylene. Refer to Section 5.5, NEC Article 500.6(A)(1) and NFPA 497:3.3. Group B—A typical Class I Group B material is hydrogen. Refer to Section 5.5, NEC Article 500.6(A)(2), and NFPA 497:3.3 for a more complete definition. Group C—A typical Class I Group C material is ethylene. Refer to Section 5.5, NEC Article 500.6(A)(3), and NFPA 497:3.3 for a more complete definition. Group D—Atmospheres containing butane, gasoline, hexane, methane, natural gas, propane, and many other hydrocarbon gases and vapors encountered in oil and gas production, refining and pipeline operations. Refer to Section 5.5, NEC Article 500.6(A)(4), and NFPA 497:3.3 for a more complete definition. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Class I, Division 2 Location

Class I, Division 2 Location

Definition(s)


Class I, Division 2 Location

A Class I, Division 2 location is a location: 1) in which volatile flammable liquids or flammable gases are handled, processed, or used, but in which the hazardous liquids, vapors, or gases will normally be confined within closed containers or closed systems from which they can escape only if accidental rupture or breakdown of such containers or systems or abnormal operation of equipment occurs; or 2) in which hazardous concentrations of gases or vapors are normally prevented by positive mechanical ventilation but that 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 hazardous concentration of gases or vapors might occasionally be communicated unless such communication is prevented by adequate positive-pressure ventilation from a source of clean air, and effective safeguards against ventilation failure are provided. (See NEC Article 500 and API 500.) Source: API Recommended Practice 14FZ, Recommended Practice for Design, Installation, and Maintenance of Electrical Systems for Fixed and Floating Offshore Petroleum Facilities for Unclassified and Class I, Zone 0, Zone 1, and Zone 2 Locations, Second Edition, May 2013. Global Standards

Class I, Division 2 Location

A location in which flammable gases or vapors may be present, but normally are confined within closed systems; are prevented from accumulating by adequate ventilation; or the location is adjacent to a Division 1 location from which ignitable concentrations might occasionally be communicated. Reference 6.2.1.1.b and NEC Article 500.5(B)(2) for a more complete definition. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Class I, Division 1 Location

Class I, Division 1 Location

Definition(s)


Class I, Division 1 Location

A Class I, Division 1 location is a location: 1) in which ignitable concentrations of flammable gases or vapors exist continuously, intermittently, or periodically under normal operating conditions; or 2) in which ignitable concentration 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 electrical equipment (see NEC Article 500 and API 500). Source: API Recommended Practice 14FZ, Recommended Practice for Design, Installation, and Maintenance of Electrical Systems for Fixed and Floating Offshore Petroleum Facilities for Unclassified and Class I, Zone 0, Zone 1, and Zone 2 Locations, Second Edition, May 2013. Global Standards

Class I, Division 1 Location

A location in which ignitable concentrations of flammable gases or vapors are expected to exist under normal operating conditions or in which faulty operation of equipment or processes might simultaneously release flammable gases or vapors and also cause failure of electrical equipment. Reference 6.2.1.1.a and NEC Article 500.5(B)(1) for a more complete definition. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Class I Location

Class I Location

Definition(s)


Class I Location

A Class I location is one in which flammable gases or vapors are or may be present in the air in quantities sufficient to produce explosive or ignitable mixtures. (See NEC Article 500 and NEC Article 505 and API 500 and API 505.). Source: API Recommended Practice 14FZ, Recommended Practice for Design, Installation, and Maintenance of Electrical Systems for Fixed and Floating Offshore Petroleum Facilities for Unclassified and Class I, Zone 0, Zone 1, and Zone 2 Locations, Second Edition, May 2013. Global Standards

Class I Location

A location in which flammable gases or vapors are, or may be, present in the air in quantities sufficient to produce explosive or ignitable mixtures. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Building, Purged

Building, Purged

Definition(s)


Building, Purged

See enclosure, purged and purged and pressurized. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Barrier, Vaportight

Barrier, Vaportight

Definition(s)


Barrier, Vaportight

A wall or other obstruction that will limit the passage of gas or vapor at atmospheric pressure, thus preventing the accumulation of vapor-air or gas-air mixtures in concentrations above 25 % of their lower flammable (explosive) limit, LFL (LEL). NOTE Barrier, non-vaportight applies to any wall or other obstruction that will not meet the criteria for barrier, vaportight. API RP 500, Recommended Practice for Classification of Locations for Electrical Installations at Petroleum Facilities Classified as Class I, Division 1 and Division 2, Third Edition, December 2012, Global Standards
Maximum Use Concentration

Maximum Use Concentration

Definition(s)


Maximum Use Concentration (MUC)

means the maximum atmospheric concentration of a hazardous substance from which a responder can be expected to be protected when wearing a respirator. This is determined by using the APF of the respirator or class of respirators and the exposure limit of the hazardous substance. The MUC can be determined mathematically by multiplying the APF specified for a respirator by the required OEL, STEL, or ceiling limit. When no OSHA exposure limit is available for a hazardous substance, an employer shall determine an MUC on the basis of relevant available information and informed professional judgment. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
UTV

UTV

Definition(s)


UTV

Utility-terrain vehicle Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
UC

UC

Definition(s)


UC

Unified Command Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
SDS

SDS

Definition(s)


SDS

Safety data sheet [formerly known as material safety data sheet (MSDS)]. Source: API RP 2D, Operation and Maintenance of Offshore Cranes, Seventh Edition, December 2014. Global Standards

SDS

Safety Data Sheets. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards Source:API RP T-1, Creating Orientation Programs for Personnel Going Offshore, Fifth Edition, November 2016. Global Standards
SCBA

SCBA

Definition(s)


SCBA

self-contained breathing apparatus. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
PAPR

PAPR

Definition(s)


PAPR

powered air-purifying respirator. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
OVM

OVM

Definition(s)


OVM

organic vapor monitor. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
OSRO

OSRO

Definition(s)


OSRO

oil spill removal organization Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
ATV

ATV

Definition(s)


ATV

all-terrain vehicle. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
VOC

VOC

Definition(s)


VOC

volatile Organic Compound. Source: API STD 521, Pressure-relieving and Depressuring Systems, Sixth Edition, January 2014. Global Standards Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards

VOC

Organic compound that participates in atmospheric photochemical reactions. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Tarballs

Tarballs

Definition(s)


Tarballs

Discrete, and usually pliable, globules of weathered oil, ranging from mostly oil to highly emulsified with varying amount of debris and/or sediment. NOTE Tarballs may vary in size from millimeters to 20–30 centimeters across, and depending on exactly how “weathered,” or hardened, the outer layer of the tarball is, sheen may or may not be present. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Time-weighted Average

Time-weighted Average

Definition(s)


Time-weighted Average

Average airborne exposure in any 8-hour work shift of a 40-hour workweek that shall not be exceeded (see 29 CFR 1910.1000, Table Z2). Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Particulate Matter

Particulate Matter

Definition(s)


Particulate Matter

Suspension of fine solid or liquid particles in air, such as dust, fog, fume, mist, smoke, or sprays. NOTE Particulate matter suspended in air is commonly known as an aerosol. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Oil Spill Removal Organization

Oil Spill Removal Organization

Definition(s)


Oil Spill Removal Organization

Any person or persons who owns or otherwise controls oil spill removal resources that are designed for, or are capable of, removing oil from the water or shoreline, providing response equipment and services, individually or in combination with subcontractors or associated contractors, under contract or other means approved by the President, directly to an owner or operator of a facility or tank vessel required to have a response plan under 33 USC 1321(j)(5). NOTE 1 Control of such resources through means other than ownership includes leasing or subcontracting of equipment or, in the case of trained personnel, by having contracts, evidence of employment, or consulting agreements. NOTE 2 OSROs must be able to mobilize and deploy equipment or trained personnel and remove, store, and transfer recovered oil. NOTE 3 Persons such as sales and marketing organizations (e.g. distributorships and manufacturer's representatives) that warehouse or store equipment for sale are not OSROs. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
OEL

OEL

Definition(s)


OEL

occupational exposure limit Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards

OEL

Upper limit of the acceptable concentration of a hazardous substance in the environment for a particular material or substance typically established by an authority having jurisdiction (AHJ). Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Occupational Exposure Limit

Occupational Exposure Limit

Definition(s)


Occupational Exposure Limit

Upper limit of the acceptable concentration of a hazardous substance in the environment for a particular material or substance typically established by an authority having jurisdiction (AHJ. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Nonroutine Responder

Nonroutine Responder

Definition(s)


Nonroutine Responder

Individual responders who do not have experience in oil spill response, who are not affiliated with an oil spill removal organization (OSRO), and who have not received training in accordance with OSHA regulation under 29 CFR 1910.120 prior to introduction to response theater. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Lower Explosive (Flammable) Limit

Lower Explosive (Flammable) Limit

Definition(s)


Lower Explosive (Flammable) Limit

Minimum concentration of combustible gas or vapor in air (expressed in percent of gas or vapor in air by volume) below which propagation of flame does not occur on contact with an ignition source. NOTE Lower flammable limit (LFL) is synonymous with lower explosive limit (LEL. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards
Job Hazard Analysis

Job Hazard Analysis

Definition(s)


Job Hazard Analysis

Safety management technique that is used to anticipate and identify hazards in order to make decisions to appropriately control the hazards associated with a process, job, or procedure. NOTE Any job that has actual or potential hazards is a candidate for a JHA. Source: API RP 98, Personal Protective Equipment Selection for Oil Spill Responders, First Edition, August 2013. Global Standards