FUEL OIL
HAZARDTEXT ®
Information to help in the initial response for evaluating chemical incidents
-IDENTIFICATION
SYNONYMS
FUEL OIL API NO. 2 FUEL OIL DIESEL FUEL MARINE DIESEL OIL FUEL OIL NO. 2 FUEL OIL, NO. 2 GAS OIL HOME HEATING OIL NO. 2 NUMBER 2 BURNER FUEL NUMBER 2 FUEL OIL NO. 2 HOME HEATING OILS
IDENTIFIERS
1202-Fuel oil, no. 1,2,4,5,6 1202-Fuel oil 1993-Fuel oil
SYNONYM REFERENCE
- (AAR, 1994;(Lewis, 1996; OHM/TADS , 1996; RTECS , 1996)
USES/FORMS/SOURCES
Fuel oil No. 2 (diesel oil) is a straight-run or cracked distillate. It is used in atomizing-type burners as a general purpose domestic or commercial fuel (Lewis, 1993). Fuel oil is utilized in domestic and industrial heating, as power for heavy units (ships, trucks, trains), and as a source of synthesis gas (Lewis, 1993).
Fuel oil is any liquid petroleum product burned in a furnace to generate heat or used in an engine to generate power. (Oils having a flash point of approximately 100 degrees F (37.7 degrees C) and oils burned in cotton or wool-wick burners are not classified as fuel oil.) Fuel oil may be a distillated fraction of petroleum, a residuum from refinery operations, a crude petroleum, or a blend of these (Lewis, 1993). Different grades of fuel oil are required for use with various types of burners having various capacities. ASTM has developed specifications for six grades of fuel oil: Numbers 1, 2, 4, 5 (light), 5 (heavy), and 6 (Lewis, 1993).
-CLINICAL EFFECTS
GENERAL CLINICAL EFFECTS
- Fuel oil No 2 will cause taste and odor problems before reaching toxic levels.
- The following clinical effects information is for HYDROCARBONS in general:
The most serious toxic effect following ingestion is aspiration pneumonitis (especially low viscosity hydrocarbons). Aspiration of hydrocarbons may also result in transient central nervous system depression or excitement. Secondary effects may include hypoxia, infection, pneumatocele formation, and chronic lung dysfunction. Specific clinical effects and associated severity from ingestion depends on the physical and chemical properties of individual hydrocarbons and the amount ingested. In general, the low viscosity (less than 100 S.U.S.) hydrocarbons pose the greatest risk of pulmonary aspiration and toxicity. Inhalation may result in euphoria, cardiac dysrhythmia, respiratory arrest, and central nervous system toxicity. Cardiovascular and neurologic toxicity are the major concerns following hydrocarbon inhalation. Inhalation of high concentrations of hydrocarbon vapors may be accidental, usually in a closed environment, or intentional (eg, "huffing" or "bagging" gasoline, paint solvents, glue solvents, etc). Cardiac dysrhythmia has accounted for sudden death after "sniffing" halogenated hydrocarbons in inhalation abusers. Ventricular arrhythmias have also been reported after inhalation of toluene.
- POTENTIAL HEALTH HAZARDS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
Inhalation or contact with material may irritate or burn skin and eyes. Fire may produce irritating, corrosive and/or toxic gases. Vapors may cause dizziness or suffocation. Runoff from fire control or dilution water may cause pollution.
-MEDICAL TREATMENT
LIFE SUPPORT
- Support respiratory and cardiovascular function.
SUMMARY
- FIRST AID - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
Move victim to fresh air. Call 911 or emergency medical service. Give artificial respiration if victim is not breathing. Administer oxygen if breathing is difficult. Remove and isolate contaminated clothing and shoes. In case of contact with substance, immediately flush skin or eyes with running water for at least 20 minutes. Wash skin with soap and water. In case of burns, immediately cool affected skin for as long as possible with cold water. Do not remove clothing if adhering to skin. Keep victim warm and quiet. Ensure that medical personnel are aware of the material(s) involved and take precautions to protect themselves.
SUMMARY INHALATION EXPOSURE INHALATION: Move patient to fresh air. Monitor for respiratory distress. If cough or difficulty breathing develops, evaluate for respiratory tract irritation, bronchitis, or pneumonitis. Administer oxygen and assist ventilation as required. Treat bronchospasm with an inhaled beta2-adrenergic agonist. Consider systemic corticosteroids in patients with significant bronchospasm. In symptomatic patients (coughing, choking, tachypnea, etc) monitor blood gases to assure adequate ventilation. Admit the patient for observation. Observe patient for 6 hours. If vital signs become abnormal or symptoms develop admit patient to the hospital and obtain a chest x-ray. Asymptomatic patients can be discharged. SEIZURES: Administer a benzodiazepine; DIAZEPAM (ADULT: 5 to 10 mg IV initially; repeat every 5 to 20 minutes as needed. CHILD: 0.1 to 0.5 mg/kg IV over 2 to 5 minutes; up to a maximum of 10 mg/dose. May repeat dose every 5 to 10 minutes as needed) or LORAZEPAM (ADULT: 2 to 4 mg IV initially; repeat every 5 to 10 minutes as needed, if seizures persist. CHILD: 0.05 to 0.1 mg/kg IV over 2 to 5 minutes, up to a maximum of 4 mg/dose; may repeat in 5 to 15 minutes as needed, if seizures continue). Consider phenobarbital or propofol if seizures recur after diazepam 30 mg (adults) or 10 mg (children greater than 5 years). Monitor for hypotension, dysrhythmias, respiratory depression, and need for endotracheal intubation. Evaluate for hypoglycemia, electrolyte disturbances, and hypoxia.
Pulmonary edema may be managed with PEEP and supplemental oxygen. Antibiotics are indicated only if bacterial superinfection of the lungs occurs. Steroids have not been shown to be of benefit for hydrocarbon pneumonitis.
DERMAL EXPOSURE DECONTAMINATION: Remove contaminated clothing and jewelry and place them in plastic bags. Wash exposed areas with soap and water for 10 to 15 minutes with gentle sponging to avoid skin breakdown. A physician may need to examine the area if irritation or pain persists (Burgess et al, 1999). Barrier creams may be useful in preventing defatting dermatitis.
EYE EXPOSURE DECONTAMINATION: Remove contact lenses and irrigate exposed eyes with copious amounts of room temperature 0.9% saline or water for at least 15 minutes. If irritation, pain, swelling, lacrimation, or photophobia persist after 15 minutes of irrigation, the patient should be seen in a healthcare facility.
ORAL EXPOSURE Based on hydrocarbon exposure, prehospital GI decontamination is not recommended because of the risk of aspiration. Once admitted to the hospital, studies fail to show if gastric emptying improves outcomes in patients with oral hydrocarbon ingestions. However, if a patient has ingested a large amount of hydrocarbon that causes significant systemic toxicity shortly prior to presentation, it is reasonable to insert a small NG tube and aspirate gastric contents. Activated charcoal should NOT be used it does not adsorb hydrocarbons well and increases the likelihood of vomiting and aspiration. In symptomatic patients (coughing, choking, tachypnea, etc) monitor blood gases to assure adequate ventilation. Admit the patient for observation. Observe patient for 6 hours. If vital signs become abnormal or symptoms develop admit patient to the hospital and obtain a chest x-ray. Asymptomatic patients can be discharged. SEIZURES: Administer a benzodiazepine; DIAZEPAM (ADULT: 5 to 10 mg IV initially; repeat every 5 to 20 minutes as needed. CHILD: 0.1 to 0.5 mg/kg IV over 2 to 5 minutes; up to a maximum of 10 mg/dose. May repeat dose every 5 to 10 minutes as needed) or LORAZEPAM (ADULT: 2 to 4 mg IV initially; repeat every 5 to 10 minutes as needed, if seizures persist. CHILD: 0.05 to 0.1 mg/kg IV over 2 to 5 minutes, up to a maximum of 4 mg/dose; may repeat in 5 to 15 minutes as needed, if seizures continue). Consider phenobarbital or propofol if seizures recur after diazepam 30 mg (adults) or 10 mg (children greater than 5 years). Monitor for hypotension, dysrhythmias, respiratory depression, and need for endotracheal intubation. Evaluate for hypoglycemia, electrolyte disturbances, and hypoxia.
Pulmonary edema may be managed with PEEP and supplemental oxygen. Antibiotics are indicated only if bacterial superinfection of the lungs occurs. Steroids have not been shown to be of benefit for hydrocarbon pneumonitis.
-RANGE OF TOXICITY
MINIMUM LETHAL EXPOSURE
MAXIMUM TOLERATED EXPOSURE
Several studies in which an unspecified amount of fuel oil No. 2 was applied to the shell surfaces of bird eggs resulted in decreased hatchability, deformed bills, and dead embryos (HSDB , 1996). A dose of 243 g/kg for 97 weeks intermittently applied to the skin produced tumors in mice (RTECS , 1996).
- Carcinogenicity Ratings for CAS68476-30-2 :
ACGIH (American Conference of Governmental Industrial Hygienists, 2010): A3 ; Listed as: Diesel fuel, as total hydrocarbons A3 :Confirmed Animal Carcinogen with Unknown Relevance to Humans: The agent is carcinogenic in experimental animals at a relatively high dose, by route(s) of administration, at site(s), of histologic type(s), or by mechanism(s) that may not be relevant to worker exposure. Available epidemiologic studies do not confirm an increased risk of cancer in exposed humans. Available evidence does not suggest that the agent is likely to cause cancer in humans except under uncommon or unlikely routes or levels of exposure.
EPA (U.S. Environmental Protection Agency, 2011): Not Listed IARC (International Agency for Research on Cancer (IARC), 2016; International Agency for Research on Cancer, 2015; IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, 2010; IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, 2010a; IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, 2008; IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, 2007; IARC Working Group on the Evaluation of Carcinogenic Risks to Humans, 2006; IARC, 2004): Not Listed NIOSH (National Institute for Occupational Safety and Health, 2007): Not Listed MAK (DFG, 2002): Not Listed NTP (U.S. Department of Health and Human Services, Public Health Service, National Toxicology Project ): Not Listed
TOXICITY AND RISK ASSESSMENT VALUES
- EPA Risk Assessment Values for CAS68476-30-2 (U.S. Environmental Protection Agency, 2011):
-STANDARDS AND LABELS
WORKPLACE STANDARDS
- ACGIH TLV Values for CAS68476-30-2 (American Conference of Governmental Industrial Hygienists, 2010):
Editor's Note: The listed values are recommendations or guidelines developed by ACGIH(R) to assist in the control of health hazards. They should only be used, interpreted and applied by individuals trained in industrial hygiene. Before applying these values, it is imperative to read the introduction to each section in the current TLVs(R) and BEI(R) Book and become familiar with the constraints and limitations to their use. Always consult the Documentation of the TLVs(R) and BEIs(R) before applying these recommendations and guidelines.
- AIHA WEEL Values for CAS68476-30-2 (AIHA, 2006):
- NIOSH REL and IDLH Values for CAS68476-30-2 (National Institute for Occupational Safety and Health, 2007):
- OSHA PEL Values for CAS68476-30-2 (U.S. Occupational Safety, and Health Administration (OSHA), 2010):
- OSHA List of Highly Hazardous Chemicals, Toxics, and Reactives for CAS68476-30-2 (U.S. Occupational Safety and Health Administration, 2010):
ENVIRONMENTAL STANDARDS
- EPA CERCLA, Hazardous Substances and Reportable Quantities for CAS68476-30-2 (U.S. Environmental Protection Agency, 2010):
- EPA CERCLA, Hazardous Substances and Reportable Quantities, Radionuclides for CAS68476-30-2 (U.S. Environmental Protection Agency, 2010):
- EPA RCRA Hazardous Waste Number for CAS68476-30-2 (U.S. Environmental Protection Agency, 2010b):
- EPA SARA Title III, Extremely Hazardous Substance List for CAS68476-30-2 (U.S. Environmental Protection Agency, 2010):
- EPA SARA Title III, Community Right-to-Know for CAS68476-30-2 (40 CFR 372.65, 2006; 40 CFR 372.28, 2006):
- DOT List of Marine Pollutants for CAS68476-30-2 (49 CFR 172.101 - App. B, 2005):
- EPA TSCA Inventory for CAS68476-30-2 (EPA, 2005):
SHIPPING REGULATIONS
- DOT -- Table of Hazardous Materials and Special Provisions for UN/NA Number 1202 (49 CFR 172.101, 2005):
Hazardous materials descriptions and proper shipping name: Diesel fuel Symbol(s): I Hazard class or Division: 3 Identification Number: UN1202 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: 144, B1, IB3, T2, TP1 144: If transported as a residue in an underground storage tank (UST), as defined in 40 CFR 180.12, that has been cleaned and purged or rendered inert according to the American Petroleum Institute (API) Standard 1604 (IBR, see sxn. 171.7 of this subchapter), then the tank and this material are not subject to any other requirements of this subchapter. However, sediments remaining in the tank that meet the definition for a hazardous material are subject to the applicable regulations of this subchapter. B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T2: Minimum test pressure (bar): 1.5; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Gas oil Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: UN1202 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: 144, B1, IB3, T2, TP1 144: If transported as a residue in an underground storage tank (UST), as defined in 40 CFR 180.12, that has been cleaned and purged or rendered inert according to the American Petroleum Institute (API) Standard 1604 (IBR, see sxn. 171.7 of this subchapter), then the tank and this material are not subject to any other requirements of this subchapter. However, sediments remaining in the tank that meet the definition for a hazardous material are subject to the applicable regulations of this subchapter. B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T2: Minimum test pressure (bar): 1.5; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Heating oil, light Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: UN1202 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: B1, IB3, T2, TP1 B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T2: Minimum test pressure (bar): 1.5; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
- DOT -- Table of Hazardous Materials and Special Provisions for UN/NA Number 1993 (49 CFR 172.101, 2005):
Hazardous materials descriptions and proper shipping name: Diesel fuel Symbol(s): D D: identifies proper shipping names which are appropriate for describing materials for domestic transportation but may be inappropriate for international transportation under the provisions of international regulations (e.g., IMO, ICAO). An alternate proper shipping name may be selected when either domestic or international transportation is involved.
Hazard class or Division: 3 Identification Number: NA1993 Packing Group: III Label(s) required (if not excepted): None Special Provisions: 144, B1, IB3, T4, TP1, TP29 144: If transported as a residue in an underground storage tank (UST), as defined in 40 CFR 180.12, that has been cleaned and purged or rendered inert according to the American Petroleum Institute (API) Standard 1604 (IBR, see sxn. 171.7 of this subchapter), then the tank and this material are not subject to any other requirements of this subchapter. However, sediments remaining in the tank that meet the definition for a hazardous material are subject to the applicable regulations of this subchapter. B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP29: A portable tank having a minimum test pressure of 1.5 bar (150.0 kPa) may be used provided the calculated test pressure is 1.5 bar or less based on the MAWP of the hazardous materials, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Combustible liquid, n.o.s Symbol(s): D, G D: identifies proper shipping names which are appropriate for describing materials for domestic transportation but may be inappropriate for international transportation under the provisions of international regulations (e.g., IMO, ICAO). An alternate proper shipping name may be selected when either domestic or international transportation is involved. G: identifies proper shipping names for which one or more technical names of the hazardous material must be entered in parentheses, in association with the basic description. (See 40 CFR 172.203(k).)
Hazard class or Division: Comb liq Identification Number: NA1993 Packing Group: III Label(s) required (if not excepted): None Special Provisions: IB3, T1, T4, TP1 IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T1: Minimum test pressure (bar): 1.5; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(2). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 241
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, cleaning liquid Symbol(s): D, G D: identifies proper shipping names which are appropriate for describing materials for domestic transportation but may be inappropriate for international transportation under the provisions of international regulations (e.g., IMO, ICAO). An alternate proper shipping name may be selected when either domestic or international transportation is involved. G: identifies proper shipping names for which one or more technical names of the hazardous material must be entered in parentheses, in association with the basic description. (See 40 CFR 172.203(k).)
Hazard class or Division: 3 Identification Number: NA1993 Packing Group: I Label(s) required (if not excepted): 3 Special Provisions: T11, TP1 T11: Minimum test pressure (bar): 6; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 201 Bulk packaging: 243
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, cleaning liquid Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: NA1993 Packing Group: II Label(s) required (if not excepted): 3 Special Provisions: IB2, T7, TP1, TP8, TP28 IB2: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130kPa at 55 °C (1.3 bar at 131 °F) are authorized. T7: Minimum test pressure (bar): 4; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP8: A portable tank having a minimum test pressure of 1.5 bar (150 kPa) may be used when the flash point of the hazardous material transported is greater than 0 °C (32 °F). TP28: A portable tank having a minimum test pressure of 2.65 bar (265 kPa) may be used provided the calculated test pressure is 2.65 bar or less based on the MAWP of the hazardous material, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 202 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, cleaning liquid Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: NA1993 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: B1, B52, IB3, T4, TP1, TP29 B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. B52: Notwithstanding the provisions of sxn. 173.24b of this subchapter, non-reclosing pressure relief devices are authorized on DOT 57 portable tanks. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP29: A portable tank having a minimum test pressure of 1.5 bar (150.0 kPa) may be used provided the calculated test pressure is 1.5 bar or less based on the MAWP of the hazardous materials, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, tree killing, liquid or Compounds, weed killing, liquid Symbol(s): D, G D: identifies proper shipping names which are appropriate for describing materials for domestic transportation but may be inappropriate for international transportation under the provisions of international regulations (e.g., IMO, ICAO). An alternate proper shipping name may be selected when either domestic or international transportation is involved. G: identifies proper shipping names for which one or more technical names of the hazardous material must be entered in parentheses, in association with the basic description. (See 40 CFR 172.203(k).)
Hazard class or Division: 3 Identification Number: NA1993 Packing Group: I Label(s) required (if not excepted): 3 Special Provisions: T11, TP1 T11: Minimum test pressure (bar): 6; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 201 Bulk packaging: 243
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, tree killing, liquid or Compounds, weed killing, liquid Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: NA1993 Packing Group: II Label(s) required (if not excepted): 3 Special Provisions: IB2, T7, TP1, TP8, TP28 IB2: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130kPa at 55 °C (1.3 bar at 131 °F) are authorized. T7: Minimum test pressure (bar): 4; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP8: A portable tank having a minimum test pressure of 1.5 bar (150 kPa) may be used when the flash point of the hazardous material transported is greater than 0 °C (32 °F). TP28: A portable tank having a minimum test pressure of 2.65 bar (265 kPa) may be used provided the calculated test pressure is 2.65 bar or less based on the MAWP of the hazardous material, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 202 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Compounds, tree killing, liquid or Compounds, weed killing, liquid Symbol(s): Not Listed Hazard class or Division: 3 Identification Number: NA1993 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: B1, B52, IB3, T4, TP1, TP29 B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. B52: Notwithstanding the provisions of sxn. 173.24b of this subchapter, non-reclosing pressure relief devices are authorized on DOT 57 portable tanks. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP29: A portable tank having a minimum test pressure of 1.5 bar (150.0 kPa) may be used provided the calculated test pressure is 1.5 bar or less based on the MAWP of the hazardous materials, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Flammable liquids, n.o.s Symbol(s): G Hazard class or Division: 3 Identification Number: UN1993 Packing Group: I Label(s) required (if not excepted): 3 Special Provisions: T11, TP1, TP27 T11: Minimum test pressure (bar): 6; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP27: A portable tank having a minimum test pressure of 4 bar (400 kPa) may be used provided the calculated test pressure is 4 bar or less based on the MAWP of the hazardous material, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 201 Bulk packaging: 243
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Flammable liquids, n.o.s Symbol(s): G Hazard class or Division: 3 Identification Number: UN1993 Packing Group: II Label(s) required (if not excepted): 3 Special Provisions: IB2, T7, TP1, TP8, TP28 IB2: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130kPa at 55 °C (1.3 bar at 131 °F) are authorized. T7: Minimum test pressure (bar): 4; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP8: A portable tank having a minimum test pressure of 1.5 bar (150 kPa) may be used when the flash point of the hazardous material transported is greater than 0 °C (32 °F). TP28: A portable tank having a minimum test pressure of 2.65 bar (265 kPa) may be used provided the calculated test pressure is 2.65 bar or less based on the MAWP of the hazardous material, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 202 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Flammable liquids, n.o.s Symbol(s): G Hazard class or Division: 3 Identification Number: UN1993 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: B1, B52, IB3, T4, TP1, TP29 B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. B52: Notwithstanding the provisions of sxn. 173.24b of this subchapter, non-reclosing pressure relief devices are authorized on DOT 57 portable tanks. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP29: A portable tank having a minimum test pressure of 1.5 bar (150.0 kPa) may be used provided the calculated test pressure is 1.5 bar or less based on the MAWP of the hazardous materials, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
Hazardous materials descriptions and proper shipping name: Fuel oil (No. 1, 2, 4, 5, or 6) Symbol(s): D D: identifies proper shipping names which are appropriate for describing materials for domestic transportation but may be inappropriate for international transportation under the provisions of international regulations (e.g., IMO, ICAO). An alternate proper shipping name may be selected when either domestic or international transportation is involved.
Hazard class or Division: 3 Identification Number: NA1993 Packing Group: III Label(s) required (if not excepted): 3 Special Provisions: 144, B1, IB3, T4, TP1, TP29 144: If transported as a residue in an underground storage tank (UST), as defined in 40 CFR 180.12, that has been cleaned and purged or rendered inert according to the American Petroleum Institute (API) Standard 1604 (IBR, see sxn. 171.7 of this subchapter), then the tank and this material are not subject to any other requirements of this subchapter. However, sediments remaining in the tank that meet the definition for a hazardous material are subject to the applicable regulations of this subchapter. B1: If the material has a flash point at or above 38 °C (100 °F) and below 93 °C (200 °F), then the bulk packaging requirements of sxn. 173.241 of this subchapter are applicable. If the material has a flash point of less than 38 °C (100 °F), then the bulk packaging requirements of sxn. 173.242 of this subchapter are applicable. IB3: Authorized IBCs: Metal (31A, 31B and 31N); Rigid plastics (31H1 and 31H2); Composite (31HZ1 and 31HA2, 31HB2, 31HN2, 31HD2 and 31HH2). Additional Requirement: Only liquids with a vapor pressure less than or equal to 110 kPa at 50 °C (1.1 bar at 122 °F), or 130 kPa at 55 °C (1.3 bar at 131 °F) are authorized, except for UN2672 (also see Special Provision IP8 in Table 3 for UN2672). T4: Minimum test pressure (bar): 2.65; Minimum shell thickness (in mm-reference steel) (See sxn.178.274(d)): sxn.178.274(d)(2); Pressure-relief requirements (See sxn.178.275(g)): Normal; Bottom opening requirements (See sxn.178.275(d)): sxn.178.275(d)(3). TP1: The maximum degree of filling must not exceed the degree of filling determined by the following: [Degree of filling = 97/1+alpha(tr - tf)], where tr is the maximum mean bulk temperature during transport, and tf is the temperature in degrees celsius of the liquid during filling. TP29: A portable tank having a minimum test pressure of 1.5 bar (150.0 kPa) may be used provided the calculated test pressure is 1.5 bar or less based on the MAWP of the hazardous materials, as defined in sxn. 178.275 of this subchapter, where the test pressure is 1.5 times the MAWP.
Packaging Authorizations (refer to 49 CFR 173.***): Exceptions: 150 Non-bulk packaging: 203 Bulk packaging: 242
Quantity Limitations: Vessel Stowage Requirements:
- ICAO International Shipping Name for UN1202 (ICAO, 2002):
Proper Shipping Name: Diesel fuel UN Number: 1202 Proper Shipping Name: Gas oil UN Number: 1202 Proper Shipping Name: Heating oil, light UN Number: 1202
- ICAO International Shipping Name for UN1993 (ICAO, 2002):
LABELS
- NFPA Hazard Ratings for CAS68476-30-2 (NFPA, 2002):
-PERSONAL PROTECTION
SUMMARY
- RECOMMENDED PROTECTIVE CLOTHING - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
RESPIRATORY PROTECTION
- Refer to "Recommendations for respirator selection" in the NIOSH Pocket Guide to Chemical Hazards on TOMES Plus(R) for respirator information.
PROTECTIVE CLOTHING
- CHEMICAL PROTECTIVE CLOTHING. Search results for CAS 68476-30-2.
-PHYSICAL HAZARDS
FIRE HAZARD
POTENTIAL FIRE OR EXPLOSION HAZARDS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004) HIGHLY FLAMMABLE: Will be easily ignited by heat, sparks or flames. Vapors may form explosive mixtures with air. Vapors may travel to source of ignition and flash back. Most vapors are heavier than air. They will spread along ground and collect in low or confined areas (sewers, basements, tanks). Vapor explosion hazard indoors, outdoors or in sewers. Those substances designated with a "P" may polymerize explosively when heated or involved in a fire. Runoff to sewer may create fire or explosion hazard. Containers may explode when heated. Many liquids are lighter than water. Substance may be transported hot. If molten aluminum is involved, refer to GUIDE 169.
Fuel oil is flammable and when exposed to heat, flame, or oxidizers it is a dangerous fire hazard (Lewis, 1996). According to OHM/TADS 1996, fuel oil's flammability level is moderate.
- FLAMMABILITY CLASSIFICATION
- NFPA Flammability Rating for CAS68476-30-2 (NFPA, 2002):
- FIRE CONTROL/EXTINGUISHING AGENTS
- FIRE PRECAUTIONS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
CAUTION: All these products have a very low flash point: Use of water spray when fighting fire may be inefficient. CAUTION: For mixtures containing a high percentage of an alcohol or polar solvent, alcohol-resistant foam may be more effective.
- SMALL FIRE PRECAUTIONS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
- LARGE FIRE PRECAUTIONS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
Water spray, fog or regular foam. Use water spray or fog; do not use straight streams. Move containers from fire area if you can do it without risk.
- TANK OR CAR/TRAILER LOAD FIRE PRECAUTIONS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
Fight fire from maximum distance or use unmanned hose holders or monitor nozzles. Cool containers with flooding quantities of water until well after fire is out. Withdraw immediately in case of rising sound from venting safety devices or discoloration of tank. ALWAYS stay away from tanks engulfed in fire. For massive fire, use unmanned hose holders or monitor nozzles; if this is impossible, withdraw from area and let fire burn.
- NFPA Extinguishing Methods for CAS68476-30-2 (NFPA, 2002):
Listed as: Diesel Fuel Oil No Extinguishing Method(s): Not Listed Listed as: Fuel Oil No Extinguishing Method(s): Not Listed
DUST/VAPOR HAZARD
- Fuel oil produces acrid smoke and irritating fumes when heated to decomposition (Lewis, 1996).
- Fuel oil is considered to be a stable substance (OHM/TADS , 1996).
REACTIVITY HAZARD
- Fuel oil emits acrid smoke and irritating fumes when heated to decomposition (Lewis, 1996).
EVACUATION PROCEDURES
- Editor's Note: This material is not listed in the Table of Initial Isolation and Protective Action Distances.
- LARGE SPILL - PUBLIC SAFETY EVACUATION DISTANCES - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
- FIRE - PUBLIC SAFETY EVACUATION DISTANCES - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
If tank, rail car or tank truck is involved in a fire, ISOLATE for 800 meters (1/2 mile) in all directions; also, consider initial evacuation for 800 meters (1/2 mile) in all directions.
- PUBLIC SAFETY MEASURES - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
CALL Emergency Response Telephone Number on Shipping Paper first. If Shipping Paper not available or no answer, refer to appropriate telephone number: MEXICO: SETIQ: 01-800-00-214-00 in the Mexican Republic; For calls originating in Mexico City and the Metropolitan Area: 5559-1588; For calls originating elsewhere, call: 011-52-555-559-1588.
CENACOM: 01-800-00-413-00 in the Mexican Republic; For calls originating in Mexico City and the Metropolitan Area: 5550-1496, 5550-1552, 5550-1485, or 5550-4885; For calls originating elsewhere, call: 011-52-555-550-1496, or 011-52-555-550-1552; 011-52-555-550-1485, or 011-52-555-550-4885.
ARGENTINA: CIQUIME: 0-800-222-2933 in the Republic of Argentina; For calls originating elsewhere, call: +54-11-4613-1100.
BRAZIL: PRÓ-QUÍMICA: 0-800-118270 (Toll-free in Brazil); For calls originating elsewhere, call: +55-11-232-1144 (Collect calls are accepted).
COLUMBIA: CISPROQUIM: 01-800-091-6012 in Colombia; For calls originating in Bogotá, Colombia, call: 288-6012; For calls originating elsewhere, call: 011-57-1-288-6012.
CANADA: UNITED STATES:
For additional details see the section entitled "WHO TO CALL FOR ASSISTANCE" under the ERG Instructions. As an immediate precautionary measure, isolate spill or leak area for at least 50 meters (150 feet) in all directions. Keep unauthorized personnel away. Stay upwind. Keep out of low areas. Ventilate closed spaces before entering.
- AIHA ERPG Values for CAS68476-30-2 (AIHA, 2006):
- DOE TEEL Values for CAS68476-30-2 (U.S. Department of Energy, Office of Emergency Management, 2010):
Listed as Diesel fuel marine (Fuel oil No.2) TEEL-0 (units = mg/m3): 100 TEEL-1 (units = mg/m3): 125 TEEL-2 (units = mg/m3): 500 TEEL-3 (units = mg/m3): 500 Definitions: TEEL-0: The threshold concentration below which most people will experience no adverse health effects. TEEL-1: The airborne concentration (expressed as ppm [parts per million] or mg/m(3) [milligrams per cubic meter]) of a substance above which it is predicted that the general population, including susceptible individuals, could experience notable discomfort, irritation, or certain asymptomatic, nonsensory effects. However, these effects are not disabling and are transient and reversible upon cessation of exposure. TEEL-2: The airborne concentration (expressed as ppm or mg/m(3)) of a substance above which it is predicted that the general population, including susceptible individuals, could experience irreversible or other serious, long-lasting, adverse health effects or an impaired ability to escape. TEEL-3: The airborne concentration (expressed as ppm or mg/m(3)) of a substance above which it is predicted that the general population, including susceptible individuals, could experience life-threatening adverse health effects or death.
- AEGL Values for CAS68476-30-2 (National Research Council, 2010; National Research Council, 2009; National Research Council, 2008; National Research Council, 2007; NRC, 2001; NRC, 2002; NRC, 2003; NRC, 2004; NRC, 2004; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; United States Environmental Protection Agency Office of Pollution Prevention and Toxics, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2009; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2008; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2007; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2005; National Advisory Committee for Acute Exposure Guideline Levels for Hazardous Substances, 2006; 62 FR 58840, 1997; 65 FR 14186, 2000; 65 FR 39264, 2000; 65 FR 77866, 2000; 66 FR 21940, 2001; 67 FR 7164, 2002; 68 FR 42710, 2003; 69 FR 54144, 2004):
- NIOSH IDLH Values for CAS68476-30-2 (National Institute for Occupational Safety and Health, 2007):
CONTAINMENT/WASTE TREATMENT OPTIONS
SPILL OR LEAK PRECAUTIONS - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004) ELIMINATE all ignition sources (no smoking, flares, sparks or flames in immediate area). All equipment used when handling the product must be grounded. Do not touch or walk through spilled material. Stop leak if you can do it without risk. Prevent entry into waterways, sewers, basements or confined areas. A vapor suppressing foam may be used to reduce vapors. Absorb or cover with dry earth, sand or other non-combustible material and transfer to containers. Use clean non-sparking tools to collect absorbed material.
RECOMMENDED PROTECTIVE CLOTHING - EMERGENCY RESPONSE GUIDEBOOK, GUIDE 128 (ERG, 2004)
To treat oil spills, use sorbents, sinking agents, gelling agents, combustion promoters, dispersants, or mechanical systems (OHM/TADS , 1996). If fuel oil is spilled on land, contain it by digging a holding area such as a pit, pond, or lagoon. Use soil, sand bags, foamed polyurethane, or foamed concrete to dike the surface flow. Then, to absorb bulk liquid, apply fly ash, cement powder, or commercial sorbents (AAR, 1994). To limit fuel oil spilled in water use natural barriers or oil spill control booms. Use suction hoses to remove trapped material (AAR, 1994). Knock down fuel oil vapors with water spray or mist (AAR, 1994). SRP (Science Review Panel): "At the time of review, criteria for land treatment or burial (sanitary landfill) disposal practices are subject to significant revision. Prior to implementing land disposal of waste residue (including waste sludge), consult with environmental regulatory agencies for guidance on acceptable disposal practices." (HSDB , 1996) Waste management activities associated with material disposition are unique to individual situations. Proper waste characterization and decisions regarding waste management should be coordinated with the appropriate local, state, or federal authorities to ensure compliance with all applicable rules and regulations.
To soak up an oil spill, use straw, polyurethane foam, activated carbon, or peat (OHM/TADS , 1996). To dispose, spray into an incinerator (OHM/TADS , 1996).
-ENVIRONMENTAL HAZARD MANAGEMENT
POLLUTION HAZARD
- Fuel oil may be released to the environment during its production, formulation, or use as fuel for trucks, ships, and other automotive equipment (HSDB , 1996).
- It may be released to waterways during shipping. It is intentionally released to aquatic environments where it serves to prevent mosquito breeding by coating the waters (HSDB , 1996).
ENVIRONMENTAL FATE AND KINETICS
SURFACE WATER Fuel oil will volatilize quickly from water: Half-lives for major components are between 4.4 and 4.8 hours. This process is attenuated, however, by the compound's tendency to adsorb to sediment and suspended solids in the water (HSDB , 1996).
OTHER In air, fuel oil, with an average hydroxyl radical concentration of 5X10+5 molec/cm(3), has a half-life of approximately 1 day or less (HSDB , 1996).
BIODEGRADATION
- Fuel oil in soil will biodegrade in the presence of microorganisms; however, the compound's tendency to adsorb to soil and sediments in water will slow the biodegradation process (HSDB , 1996).
BIOACCUMULATION
The bioconcentration factors (BCFs) for C16-C19 unbranched alkanes, the primary components of fuel oil, were estimated at 10,000 to 14,000. Thus, these components have a high potential to bioconcentrate in aquatic organisms. However, some evidence suggests that metabolism may offset the problems normally associated with such high BCFs (HSDB , 1996).
ENVIRONMENTAL TOXICITY
- No information found at the time of this review.
-PHYSICAL/CHEMICAL PROPERTIES
MOLECULAR WEIGHT
DESCRIPTION/PHYSICAL STATE
- Fuel oil is a straw yellow to dark colored liquid. It has a petroleum-like odor (AAR, 1994).
- Fuel oil No 2 is a brown, slightly viscous liquid (Lewis, 1996).
- In water, fuel oil No 2 is iridescent and will create a dark blue-purple slick (OHM/TADS , 1996).
SPECIFIC GRAVITY
- OTHER TEMPERATURE AND/OR PRESSURE
DENSITY
- TEMPERATURE AND/OR PRESSURE NOT LISTED
FREEZING/MELTING POINT
BOILING POINT
- 232 degrees C (OHM/TADS , 1996)
FLASH POINT
- 52-96 degrees C; 126-204 degrees F (NFPA, 1994)
AUTOIGNITION TEMPERATURE
- 257 degrees C; 494 degrees F (Lewis, 1996)
SOLUBILITY
Fuel oil is insoluble in water (AAR, 1994). It is slightly soluble in water (OHM/TADS , 1996).
OTHER/PHYSICAL
-REFERENCES
GENERAL BIBLIOGRAPHY- 40 CFR 372.28: Environmental Protection Agency - Toxic Chemical Release Reporting, Community Right-To-Know, Lower thresholds for chemicals of special concern. National Archives and Records Administration (NARA) and the Government Printing Office (GPO). Washington, DC. Final rules current as of Apr 3, 2006.
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