Help with Board Question (No Word Count), and Research Paper. APA Format Throughout to include Reference Page.
Board Question
Share with the class some common oxidizers that you might have in your home (e.g., under the counter, in the kitchen or bathroom, or out in the garage). Do you think any of these products should be outlawed from home use? Why, or why not?
Unit Research Paper
OSHA issued the Process Safety Management of Highly Hazardous Chemicals Standard (PSM) (29 CFR 1910.119) which contains requirements for the safe management of chemicals for companies that exceed OSHA’s threshold quantities for highly hazardous substances. This standard requires the establishment of a management program that includes conducting process hazard analyses, establishing detailed operating procedures, and includes other important requirements to mitigate the possibility of a serious, chemical related incident occurring at the facility.
For this assignment, suppose you are a safety manager at a chemical manufacturing facility that manufactures concentrated nitric acid. You have heard that employees who load nitric acid into rail tank cars have been checking the pre- inspection checklist from the rail shipping office instead of actually inspecting the vehicles with the checklist in hand as
required by the operating procedure. This has not been the first time the shipping crew has been lax about process safety related work rules. Based on this scenario, please compose a research paper which includes the following information:
Identify the chemical properties, uses, and primary hazards associated with common oxidizers including concentrated nitric acid.
Identify important occupational exposure limits (OELs) associated with at least 3 common oxidizers.
Identify PSM requirements that would be useful for preventing or minimizing the consequences of a significant oxidizer related incident.
Using the OSHA Standard and your own experience, justify and validate the importance of the PSM standard to your facility (if it stores and processes highly hazardous materials) or a facility that may impact your community or a near-by community. Examples might include a water treatment facility that utilizes liquefied chlorine gas, a coal fired power plant that utilizes liquefied chlorine gas for water treatment, a food processing plant with a large ammonia refrigeration system, a fertilizer manufacturing or storage facility, a chemical manufacturing facility, etc.
Your research paper must be at least two pages in length. You are required to cite the OSHA Standard 29 CFR 1910.119 in your response as well as at least two other sources. All sources used, including the textbook, must be referenced. Paraphrased and/or quoted materials must have accompanying citations in APA format.
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By Standard Number / 1910.119 – Process safety management of highly hazardous chemicals.
Part Number: 1910
Part Number Title: Occupational Safety and Health Standards
Subpart: 1910 Subpart H
Subpart Title: Hazardous Materials
Standard Number: 1910.119
Title: Process safety management of highly hazardous chemicals.
Appendix: A; B; C; D
GPO Source: e-CFR
Purpose. This section contains requirements for preventing or minimizing the consequences of catastrophic releases of toxic, reactive, flammable, or explosive chemicals.
These releases may result in toxic, fire or explosion hazards
1910.119(a)
Application.
1910.119(a)(1)
This section applies to the following:
1910.119(a)(1)(i)
A process which involves a chemical at or above the specified threshold quantities listed in appendix A to this section;
1910.119(a)(1)(ii)
A process which involves a Category 1 flammable gas (as defined in 1910.1200(c)) or a flammable liquid with a flashpoint below 100 °F (37.8 °C) on site in one location, in a
quantity of 10,000 pounds (4535.9 kg) or more except for:
1910.119(a)(1)(ii)(A)
Hydrocarbon fuels used solely for workplace consumption as a fuel (e.g., propane used for comfort heating, gasoline for vehicle refueling), if such fuels are not a part of a
process containing another highly hazardous chemical covered by this standard;
1910.119(a)(1)(ii)(B)
Flammable liquids with a flashpoint below 100 °F (37.8 °C) stored in atmospheric tanks or transferred which are kept below their normal boiling point without benefit of chilling or
refrigeration.
https://www.osha.gov/laws-regs/regulations/standardnumber
https://www.osha.gov/laws-regs/interlinking/standards/1910.119
https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119AppA
https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119AppB
https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119AppC
https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119AppD
https://www.ecfr.gov/cgi-bin/text-idx?SID=65b279ee2e7530009034c1f152d451e5&tpl=/ecfrbrowse/Title29/29tab_02.tpl
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(1)(ii)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(1)(ii)(B)
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1910.119(a)(2)
This section does not apply to:
1910.119(a)(2)(i)
Retail facilities;
1910.119(a)(2)(ii)
Oil or gas well drilling or servicing operations; or,
1910.119(a)(2)(iii)
Normally unoccupied remote facilities.
1910.119(b)
Definitions. Atmospheric tank means a storage tank which has been designed to operate at pressures from atmospheric through 0.5 p.s.i.g. (pounds per square inch gauge, 3.45
Kpa).
Boiling point means the boiling point of a liquid at a pressure of 14.7 pounds per square inch absolute (p.s.i.a.) (760 mm.). For the purposes of this section, where an accurate
boiling point is unavailable for the material in question, or for mixtures which do not have a constant boiling point, the 10 percent point of a distillation performed in accordance
with the Standard Method of Test for Distillation of Petroleum Products, ASTM D-86-62, which is incorporated by reference as specified in §1910.6, may be used as the boiling
point of the liquid.
Catastrophic release means a major uncontrolled emission, fire, or explosion, involving one or more highly hazardous chemicals, that presents serious danger to employees in
the workplace.
Facility means the buildings, containers or equipment which contain a process.
Highly hazardous chemical means a substance possessing toxic, reactive, flammable, or explosive properties and specified by paragraph (a)(1) of this section.
Hot work means work involving electric or gas welding, cutting, brazing, or similar flame or spark-producing operations.
Normally unoccupied remote facility means a facility which is operated, maintained or serviced by employees who visit the facility only periodically to check its operation and to
perform necessary operating or maintenance tasks. No employees are permanently stationed at the facility.
Facilities meeting this definition are not contiguous with, and must be geographically remote from all other buildings, processes or persons.
Process means any activity involving a highly hazardous chemical including any use, storage, manufacturing, handling, or the on-site movement of such chemicals, or
combination of these activities. For purposes of this definition, any group of vessels which are interconnected and separate vessels which are located such that a highly
hazardous chemical could be involved in a potential release shall be considered a single process.
Replacement in kind means a replacement which satisfies the design specification.
Trade secret means any confidential formula, pattern, process, device, information or compilation of information that is used in an employer’s business, and that gives the
employer an opportunity to obtain an advantage over competitors who do not know or use it. See Appendix E to §1910.1200—Definition of a Trade Secret (which sets out the
criteria to be used in evaluating trade secrets).
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(a)(2)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(b)
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1910.119(c)
Employee participation.
1910.119(c)(1)
Employers shall develop a written plan of action regarding the implementation of the employee participation required by this paragraph.
1910.119(c)(2)
Employers shall consult with employees and their representatives on the conduct and development of process hazards analyses and on the development of the other elements
of process safety management in this standard.
1910.119(c)(3)
Employers shall provide to employees and their representatives access to process hazard analyses and to all other information required to be developed under this standard.
1910.119(d)
Process safety information. In accordance with the schedule set forth in paragraph (e)(1) of this section, the employer shall complete a compilation of written process safety
information before conducting any process hazard analysis required by the standard. The compilation of written process safety information is to enable the employer and the
employees involved in operating the process to identify and understand the hazards posed by those processes involving highly hazardous chemicals. This process safety
information shall include information pertaining to the hazards of the highly hazardous chemicals used or produced by the process, information pertaining to the technology of
the process, and information pertaining to the equipment in the process.
1910.119(d)(1)
Information pertaining to the hazards of the highly hazardous chemicals in the process. This information shall consist of at least the following:
1910.119(d)(1)(i)
Toxicity information;
1910.119(d)(1)(ii)
Permissible exposure limits;
1910.119(d)(1)(iii)
Physical data;
1910.119(d)(1)(iv)
Reactivity data:
1910.119(d)(1)(v)
Corrosivity data;
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(c)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(c)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(c)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(c)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(v)
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1910.119(d)(1)(vi)
Thermal and chemical stability data; and
1910.119(d)(1)(vii)
Hazardous effects of inadvertent mixing of different materials that could foreseeably occur.
Note: Safety data sheets meeting the requirements of 29 CFR 1910.1200(g) may be used to comply with this requirement to the extent they contain the information required by
this subparagraph.
1910.119(d)(2)
Information pertaining to the technology of the process.
1910.119(d)(2)(i)
Information concerning the technology of the process shall include at least the following:
1910.119(d)(2)(i)(A)
A block flow diagram or simplified process flow diagram (see Appendix B to this section);
1910.119(d)(2)(i)(B)
Process chemistry;
1910.119(d)(2)(i)(C)
Maximum intended inventory;
1910.119(d)(2)(i)(D)
Safe upper and lower limits for such items as temperatures, pressures, flows or compositions; and,
1910.119(d)(2)(i)(E)
An evaluation of the consequences of deviations, including those affecting the safety and health of employees.
1910.119(d)(2)(ii)
Where the original technical information no longer exists, such information may be developed in conjunction with the process hazard analysis in sufficient detail to support the
analysis.
1910.119(d)(3)
Information pertaining to the equipment in the process.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(vi)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(1)(vii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)(B)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)(C)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)(D)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(i)(E)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)
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1910.119(d)(3)(i)
Information pertaining to the equipment in the process shall include:
1910.119(d)(3)(i)(A)
Materials of construction;
1910.119(d)(3)(i)(B)
Piping and instrument diagrams (P&ID’s);
1910.119(d)(3)(i)(C)
Electrical classification;
1910.119(d)(3)(i)(D)
Relief system design and design basis;
1910.119(d)(3)(i)(E)
Ventilation system design;
1910.119(d)(3)(i)(F)
Design codes and standards employed;
1910.119(d)(3)(i)(G)
Material and energy balances for processes built after May 26, 1992; and,
1910.119(d)(3)(i)(H)
Safety systems (e.g. interlocks, detection or suppression systems).
1910.119(d)(3)(ii)
The employer shall document that equipment complies with recognized and generally accepted good engineering practices.
1910.119(d)(3)(iii)
For existing equipment designed and constructed in accordance with codes, standards, or practices that are no longer in general use, the employer shall determine and
document that the equipment is designed, maintained, inspected, tested, and operating in a safe manner.
1910.119(e)
Process hazard analysis.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(B)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(C)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(D)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(E)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(F)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(G)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(i)(H)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(d)(3)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)
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1910.119(e)(1)
The employer shall perform an initial process hazard analysis (hazard evaluation) on processes covered by this standard. The process hazard analysis shall be appropriate to the
complexity of the process and shall identify, evaluate, and control the hazards involved in the process. Employers shall determine and document the priority order for conducting
process hazard analyses based on a rationale which includes such considerations as extent of the process hazards, number of potentially affected employees, age of the
process, and operating history of the process. The process hazard analysis shall be conducted as soon as possible, but not later than the following schedule:
1910.119(e)(1)(i)
No less than 25 percent of the initial process hazards analyses shall be completed by May 26, 1994;
1910.119(e)(1)(ii)
No less than 50 percent of the initial process hazards analyses shall be completed by May 26, 1995;
1910.119(e)(1)(iii)
No less than 75 percent of the initial process hazards analyses shall be completed by May 26, 1996;
1910.119(e)(1)(iv)
All initial process hazards analyses shall be completed by May 26, 1997.
1910.119(e)(1)(v)
Process hazards analyses completed after May 26, 1987 which meet the requirements of this paragraph are acceptable as initial process hazards analyses. These process
hazard analyses shall be updated and revalidated, based on their completion date, in accordance with paragraph (e)(6) of this standard.
1910.119(e)(2)
The employer shall use one or more of the following methodologies that are appropriate to determine and evaluate the hazards of the process being analyzed.
1910.119(e)(2)(i)
What-If;
1910.119(e)(2)(ii)
Checklist;
1910.119(e)(2)(iii)
What-If/Checklist;
1910.119(e)(2)(iv)
Hazard and Operability Study (HAZOP);
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(1)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(iv)
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1910.119(e)(2)(v)
Failure Mode and Effects Analysis (FMEA);
1910.119(e)(2)(vi)
Fault Tree Analysis; or
1910.119(e)(2)(vii)
An appropriate equivalent methodology.
1910.119(e)(3)
The process hazard analysis shall address:
1910.119(e)(3)(i)
The hazards of the process;
1910.119(e)(3)(ii)
The identification of any previous incident which had a likely potential for catastrophic consequences in the workplace;
1910.119(e)(3)(iii)
Engineering and administrative controls applicable to the hazards and their interrelationships such as appropriate application of detection methodologies to provide early
warning of releases. (Acceptable detection methods might include process monitoring and control instrumentation with alarms, and detection hardware such as hydrocarbon
sensors.);
1910.119(e)(3)(iv)
Consequences of failure of engineering and administrative controls;
1910.119(e)(3)(v)
Facility siting;
1910.119(e)(3)(vi)
Human factors; and
1910.119(e)(3)(vii)
A qualitative evaluation of a range of the possible safety and health effects of failure of controls on employees in the workplace.
1910.119(e)(4)
The process hazard analysis shall be performed by a team with expertise in engineering and process operations, and the team shall include at least one employee who has
experience and knowledge specific to the process being evaluated. Also, one member of the team must be knowledgeable in the specific process hazard analysis methodology
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(vi)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(2)(vii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(vi)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(3)(vii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(4)
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experience and knowledge specific to the process being evaluated. Also, one member of the team must be knowledgeable in the specific process hazard analysis methodology
being used.
1910.119(e)(5)
The employer shall establish a system to promptly address the team’s findings and recommendations; assure that the recommendations are resolved in a timely manner and
that the resolution is documented; document what actions are to be taken; complete actions as soon as possible; develop a written schedule of when these actions are to be
completed; communicate the actions to operating, maintenance and other employees whose work assignments are in the process and who may be affected by the
recommendations or actions.
1910.119(e)(6)
At least every five (5) years after the completion of the initial process hazard analysis, the process hazard analysis shall be updated and revalidated by a team meeting the
requirements in paragraph (e)(4) of this section, to assure that the process hazard analysis is consistent with the current process.
1910.119(e)(7)
Employers shall retain process hazards analyses and updates or revalidations for each process covered by this section, as well as the documented resolution of
recommendations described in paragraph (e)(5) of this section for the life of the process.
1910.119(f)
Operating procedures.
1910.119(f)(1)
The employer shall develop and implement written operating procedures that provide clear instructions for safely conducting activities involved in each covered process
consistent with the process safety information and shall address at least the following elements.
1910.119(f)(1)(i)
Steps for each operating phase:
1910.119(f)(1)(i)(A)
Initial startup;
1910.119(f)(1)(i)(B)
Normal operations;
1910.119(f)(1)(i)(C)
Temporary operations;
1910.119(f)(1)(i)(D)
Emergency shutdown including the conditions under which emergency shutdown is required, and the assignment of shutdown responsibility to qualified operators to ensure that
emergency shutdown is executed in a safe and timely manner.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(5)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(6)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(e)(7)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(B)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(C)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(D)
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emergency shutdown is executed in a safe and timely manner.
1910.119(f)(1)(i)(E)
Emergency Operations;
1910.119(f)(1)(i)(F)
Normal shutdown; and,
1910.119(f)(1)(i)(G)
Startup following a turnaround, or after an emergency shutdown.
1910.119(f)(1)(ii)
Operating limits:
1910.119(f)(1)(ii)(A)
Consequences of deviation; and
1910.119(f)(1)(ii)(B)
Steps required to correct or avoid deviation.
1910.119(f)(1)(iii)
Safety and health considerations:
1910.119(f)(1)(iii)(A)
Properties of, and hazards presented by, the chemicals used in the process;
1910.119(f)(1)(iii)(B)
Precautions necessary to prevent exposure, including engineering controls, administrative controls, and personal protective equipment;
1910.119(f)(1)(iii)(C)
Control measures to be taken if physical contact or airborne exposure occurs;
1910.119(f)(1)(iii)(D)
Quality control for raw materials and control of hazardous chemical inventory levels; and,
1910.119(f)(1)(iii)(E)
Any special or unique hazards.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(E)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(F)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(i)(G)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(ii)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(ii)(B)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)(A)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)(B)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)(C)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)(D)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iii)(E)
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1910.119(f)(1)(iv)
Safety systems and their functions.
1910.119(f)(2)
Operating procedures shall be readily accessible to employees who work in or maintain a process.
1910.119(f)(3)
The operating procedures shall be reviewed as often as necessary to assure that they reflect current operating practice, including changes that result from changes in process
chemicals, technology, and equipment, and changes to facilities. The employer shall certify annually that these operating procedures are current and accurate.
1910.119(f)(4)
The employer shall develop and implement safe work practices to provide for the control of hazards during operations such as lockout/tagout; confined space entry; opening
process equipment or piping; and control over entrance into a facility by maintenance, contractor, laboratory, or other support personnel. These safe work practices shall apply
to employees and contractor employees.
1910.119(g)
Training—
1910.119(g)(1)
Initial training.
1910.119(g)(1)(i)
Each employee presently involved in operating a process, and each employee before being involved in operating a newly assigned process, shall be trained in an overview of the
process and in the operating procedures as specified in paragraph (f) of this section. The training shall include emphasis on the specific safety and health hazards, emergency
operations including shutdown, and safe work practices applicable to the employee’s job tasks.
1910.119(g)(1)(ii)
In lieu of initial training for those employees already involved in operating a process on May 26, 1992, an employer may certify in writing that the employee has the required
knowledge, skills, and abilities to safely carry out the duties and responsibilities as specified in the operating procedures.
1910.119(g)(2)
Refresher training. Refresher training shall be provided at least every three years, and more often if necessary, to each employee involved in operating a process to assure that
the employee understands and adheres to the current operating procedures of the process. The employer, in consultation with the employees involved in operating the process,
shall determine the appropriate frequency of refresher training.
1910.119(g)(3)
Training documentation. The employer shall ascertain that each employee involved in operating a process has received and understood the training required by this paragraph.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(1)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(f)(4)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(g)(3)
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The employer shall prepare a record which contains the identity of the employee, the date of training, and the means used to verify that the employee understood the training.
1910.119(h)
Contractors—
1910.119(h)(1)
Application. This paragraph applies to contractors performing maintenance or repair, turnaround, major renovation, or specialty work on or adjacent to a covered process. It
does not apply to contractors providing incidental services which do not influence process safety, such as janitorial work, food and drink services, laundry, delivery or other
supply services.
1910.119(h)(2)
Employer responsibilities.
1910.119(h)(2)(i)
The employer, when selecting a contractor, shall obtain and evaluate information regarding the contract employer’s safety performance and programs.
1910.119(h)(2)(ii)
The employer shall inform contract employers of the known potential fire, explosion, or toxic release hazards related to the contractor’s work and the process.
1910.119(h)(2)(iii)
The employer shall explain to contract employers the applicable provisions of the emergency action plan required by paragraph (n) of this section.
1910.119(h)(2)(iv)
The employer shall develop and implement safe work practices consistent with paragraph (f)(4) of this section, to control the entrance, presence and exit of contract employers
and contract employees in covered process areas.
1910.119(h)(2)(v)
The employer shall periodically evaluate the performance of contract employers in fulfilling their obligations as specified in paragraph (h)(3) of this section.
1910.119(h)(2)(vi)
The employer shall maintain a contract employee injury and illness log related to the contractor’s work in process areas.
1910.119(h)(3)
Contract employer responsibilities.
1910.119(h)(3)(i)
The contract employer shall assure that each contract employee is trained in the work practices necessary to safely perform his/her job.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(2)(vi)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)(i)
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1910.119(h)(3)(ii)
The contract employer shall assure that each contract employee is instructed in the known potential fire, explosion, or toxic release hazards related to his/her job and the
process, and the applicable provisions of the emergency action plan.
1910.119(h)(3)(iii)
The contract employer shall document that each contract employee has received and understood the training required by this paragraph. The contract employer shall prepare a
record which contains the identity of the contract employee, the date of training, and the means used to verify that the employee understood the training.
1910.119(h)(3)(iv)
The contract employer shall assure that each contract employee follows the safety rules of the facility including the safe work practices required by paragraph (f)(4) of this
section.
1910.119(h)(3)(v)
The contract employer shall advise the employer of any unique hazards presented by the contract employer’s work, or of any hazards found by the contract employer’s work.
1910.119(i)
Pre-startup safety review.
1910.119(i)(1)
The employer shall perform a pre-startup safety review for new facilities and for modified facilities when the modification is significant enough to require a change in the process
safety information.
1910.119(i)(2)
The pre-startup safety review shall confirm that prior to the introduction of highly hazardous chemicals to a process:
1910.119(i)(2)(i)
Construction and equipment is in accordance with design specifications;
1910.119(i)(2)(ii)
Safety, operating, maintenance, and emergency procedures are in place and are adequate;
1910.119(i)(2)(iii)
For new facilities, a process hazard analysis has been performed and recommendations have been resolved or implemented before startup; and modified facilities meet the
requirements contained in management of change, paragraph (l).
1910.119(i)(2)(iv)
Training of each employee involved in operating a process has been completed.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(h)(3)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(2)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(i)(2)(iv)
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Page 13 of 18https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119
Training of each employee involved in operating a process has been completed.
1910.119(j)
Mechanical integrity—
1910.119(j)(1)
Application. Paragraphs (j)(2) through (j)(6) of this section apply to the following process equipment:
1910.119(j)(1)(i)
Pressure vessels and storage tanks;
1910.119(j)(1)(ii)
Piping systems (including piping components such as valves);
1910.119(j)(1)(iii)
Relief and vent systems and devices;
1910.119(j)(1)(iv)
Emergency shutdown systems;
1910.119(j)(1)(v)
Controls (including monitoring devices and sensors, alarms, and interlocks) and,
1910.119(j)(1)(vi)
Pumps.
1910.119(j)(2)
Written procedures. The employer shall establish and implement written procedures to maintain the on-going integrity of process equipment.
1910.119(j)(3)
Training for process maintenance activities. The employer shall train each employee involved in maintaining the on-going integrity of process equipment in an overview of that
process and its hazards and in the procedures applicable to the employee’s job tasks to assure that the employee can perform the job tasks in a safe manner.
1910.119(j)(4)
Inspection and testing.
1910.119(j)(4)(i)
Inspections and tests shall be performed on process equipment.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(1)(vi)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(4)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(4)(i)
3/15/20, 2:38 PM1910.119 – Process safety management of highly hazardous chemicals. | Occupational Safety and Health Administration
Page 14 of 18https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119
Inspections and tests shall be performed on process equipment.
1910.119(j)(4)(ii)
Inspection and testing procedures shall follow recognized and generally accepted good engineering practices.
1910.119(j)(4)(iii)
The frequency of inspections and tests of process equipment shall be consistent with applicable manufacturers’ recommendations and good engineering practices, and more
frequently if determined to be necessary by prior operating experience.
1910.119(j)(4)(iv)
The employer shall document each inspection and test that has been performed on process equipment. The documentation shall identify the date of the inspection or test, the
name of the person who performed the inspection or test, the serial number or other identifier of the equipment on which the inspection or test was performed, a description of
the inspection or test performed, and the results of the inspection or test.
1910.119(j)(5)
Equipment deficiencies. The employer shall correct deficiencies in equipment that are outside acceptable limits (defined by the process safety information in paragraph (d) of this
section) before further use or in a safe and timely manner when necessary means are taken to assure safe operation.
1910.119(j)(6)
Quality assurance.
1910.119(j)(6)(i)
In the construction of new plants and equipment, the employer shall assure that equipment as it is fabricated is suitable for the process application for which they will be used.
1910.119(j)(6)(ii)
Appropriate checks and inspections shall be performed to assure that equipment is installed properly and consistent with design specifications and the manufacturer’s
instructions.
1910.119(j)(6)(iii)
The employer shall assure that maintenance materials, spare parts and equipment are suitable for the process application for which they will be used.
1910.119(k)
Hot work permit.
1910.119(k)(1)
The employer shall issue a hot work permit for hot work operations conducted on or near a covered process.
1910.119(k)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(4)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(4)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(4)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(5)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(6)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(6)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(6)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(j)(6)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(k)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(k)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(k)(2)
3/15/20, 2:38 PM1910.119 – Process safety management of highly hazardous chemicals. | Occupational Safety and Health Administration
Page 15 of 18https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119
1910.119(k)(2)
The permit shall document that the fire prevention and protection requirements in 29 CFR 1910.252(a) have been implemented prior to beginning the hot work operations; it shall
indicate the date(s) authorized for hot work; and identify the object on which hot work is to be performed. The permit shall be kept on file until completion of the hot work
operations.
1910.119(l)
Management of change.
1910.119(l)(1)
The employer shall establish and implement written procedures to manage changes (except for “replacements in kind”) to process chemicals, technology, equipment, and
procedures; and, changes to facilities that affect a covered process.
1910.119(l)(2)
The procedures shall assure that the following considerations are addressed prior to any change:
1910.119(l)(2)(i)
The technical basis for the proposed change;
1910.119(l)(2)(ii)
Impact of change on safety and health;
1910.119(l)(2)(iii)
Modifications to operating procedures;
1910.119(l)(2)(iv)
Necessary time period for the change; and,
1910.119(l)(2)(v)
Authorization requirements for the proposed change.
1910.119(l)(3)
Employees involved in operating a process and maintenance and contract employees whose job tasks will be affected by a change in the process shall be informed of, and
trained in, the change prior to start-up of the process or affected part of the process.
1910.119(l)(4)
If a change covered by this paragraph results in a change in the process safety information required by paragraph (d) of this section, such information shall be updated
accordingly.
1910.119(l)(5)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(k)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(2)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(4)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(5)
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Page 16 of 18https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119
1910.119(l)(5)
If a change covered by this paragraph results in a change in the operating procedures or practices required by paragraph (f) of this section, such procedures or practices shall be
updated accordingly.
1910.119(m)
Incident investigation.
1910.119(m)(1)
The employer shall investigate each incident which resulted in, or could reasonably have resulted in a catastrophic release of highly hazardous chemical in the workplace.
1910.119(m)(2)
An incident investigation shall be initiated as promptly as possible, but not later than 48 hours following the incident.
1910.119(m)(3)
An incident investigation team shall be established and consist of at least one person knowledgeable in the process involved, including a contract employee if the incident
involved work of the contractor, and other persons with appropriate knowledge and experience to thoroughly investigate and analyze the incident.
1910.119(m)(4)
A report shall be prepared at the conclusion of the investigation which includes at a minimum:
1910.119(m)(4)(i)
Date of incident;
1910.119(m)(4)(ii)
Date investigation began;
1910.119(m)(4)(iii)
A description of the incident;
1910.119(m)(4)(iv)
The factors that contributed to the incident; and,
1910.119(m)(4)(v)
Any recommendations resulting from the investigation.
1910.119(m)(5)
The employer shall establish a system to promptly address and resolve the incident report findings and recommendations. Resolutions and corrective actions shall be
documented.
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(l)(5)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)(i)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)(ii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)(iii)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)(iv)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(4)(v)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(5)
3/15/20, 2:38 PM1910.119 – Process safety management of highly hazardous chemicals. | Occupational Safety and Health Administration
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documented.
1910.119(m)(6)
The report shall be reviewed with all affected personnel whose job tasks are relevant to the incident findings including contract employees where applicable.
1910.119(m)(7)
Incident investigation reports shall be retained for five years.
1910.119(n)
Emergency planning and response. The employer shall establish and implement an emergency action plan for the entire plant in accordance with the provisions of 29 CFR
1910.38. In addition, the emergency action plan shall include procedures for handling small releases. Employers covered under this standard may also be subject to the
hazardous waste and emergency response provisions contained in 29 CFR 1910.120 (a), (p) and (q).
1910.119(o)
Compliance Audits.
1910.119(o)(1)
Employers shall certify that they have evaluated compliance with the provisions of this section at least every three years to verify that the procedures and practices developed
under the standard are adequate and are being followed.
1910.119(o)(2)
The compliance audit shall be conducted by at least one person knowledgeable in the process.
1910.119(o)(3)
A report of the findings of the audit shall be developed.
1910.119(o)(4)
The employer shall promptly determine and document an appropriate response to each of the findings of the compliance audit, and document that deficiencies have been
corrected.
1910.119(o)(5)
Employers shall retain the two (2) most recent compliance audit reports.
1910.119(p)
Trade secrets.
1910.119(p)(1)
Employers shall make all information necessary to comply with the section available to those persons responsible for compiling the process safety information (required by
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(6)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(m)(7)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(n)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)(1)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)(2)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)(3)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)(4)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(o)(5)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(p)
https://www.osha.gov/laws-regs/interlinking/standards/1910.119(p)(1)
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Page 18 of 18https://www.osha.gov/laws-regs/regulations/standardnumber/1910/1910.119
Employers shall make all information necessary to comply with the section available to those persons responsible for compiling the process safety information (required by
paragraph (d) of this section), those assisting in the development of the process hazard analysis (required by paragraph (e) of this section), those responsible for developing the
operating procedures (required by paragraph (f) of this section), and those involved in incident investigations (required by paragraph (m) of this section), emergency planning and
response (paragraph (n) of this section) and compliance audits (paragraph (o) of this section) without regard to possible trade secret status of such information.
1910.119(p)(2)
Nothing in this paragraph shall preclude the employer from requiring the persons to whom the information is made available under paragraph (p)(1) of this section to enter into
confidentiality agreements not to disclose the information as set forth in 29 CFR 1910.1200.
1910.119(p)(3)
Subject to the rules and procedures set forth in 29 CFR 1910.1200(i)(1) through 1910.1200(i)(12), employees and their designated representatives shall have access to trade
secret information contained within the process hazard analysis and other documents required to be developed by this standard.
[57 FR 23060, June 1, 1992; 61 FR 9227, March 7, 1996; 77 FR 17776, March 26, 2012; 78 FR 9313, Feb. 8, 2013]
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1
Course Learning Outcomes for Unit
Upon completion of this unit, students should be able to:
6. Determine strategies for dealing with chemical properties of specific types of hazardous substances.
6.1 Identify the chemical properties, uses, and primary hazards associated with common oxidizers
6.2 Identify workplace exposure concentrations associated with common oxidizers.
6.3 Identify PSM requirements that would be useful for preventing or minimizing the consequences
of a significant oxidizer-related incident.
Course/Unit
Learning Outcomes
Learning Activity
6.1
Unit V Lesson
Chapter 5 Reading
Chapter 11 Reading
Unit V Research Paper
6.2
Unit V Lesson
Chapter 11 Reading
Unit V Research Paper
6.3
Unit V Lesson
Chapter 11 Reading
PSM Standard Reading
Unit V Research Paper
Reading Assignment
Chapter 5:
Principles of Chemical Reactions, pp. 140-142
Chapter 11:
Chemistry of Some Oxidizers, pp. 421-463
Additional Reading Assignment(s):
Please review the information regarding the Process Safety Management of Highly Hazardous Chemicals at
the following link:
https://www.osha.gov/pls/oshaweb/owadisp.show_document?p_table=STANDARDS&p_id=9760
Unit Lesson
In this unit, we still study the chemistry of some oxidizers as discussed in Chapter 11 of our textbook. Most or
all of you have heard of oxidizers or even oxidation-reduction reactions (redox in short). These reactions,
when controlled, can benefit our society. Examples are combustion of fuels, disinfection of water, household
cleaning, and bleaching of fabrics. However, when the reactions become uncontrolled, fire, and/or an
explosion could result that may result in loss of life and property.
Before we get into these reactions, we will review what an oxidizer is. According to Meyer (2014), the
Department of Transportation (DOT) defines an oxidizer as a substance that may enhance or support
combustion of other materials, generally by yielding its oxygen. However, an oxidizer does not necessarily
have oxygen to give up. A substance that removes electrons from other substances is also an oxidizer (also
known as an oxidizing agent). So, an oxidizer can consist of elements, acids, or salts that are separated into
UNIT STUDY GUIDE
Chemistry of Some Oxidizers
https://www.osha.gov/pls/oshaweb/owadisp.show_document?p_table=STANDARDS&p_id=9760
2
UNIT x STUDY GUIDE
Title
different families. These families each have specific hazards associated them (Burke, 2003). The elements
include oxygen, chlorine, fluorine, bromine, and iodine. If you recall from the periodic table in Unit I, these
elements belong to the same family.
To learn oxidation-reduction reactions, we have to know what an oxidation number or oxidation state is. This
is defined as the ability of an ion or atom to combine with another ion or atom (Meyer, 2014). It provides a
way to keep track of electrons in redox reactions. In practice, there are rules for assigning oxidation numbers.
In Section 5.4 of our textbook, oxidation-reduction is also discussed in more detail. Basically, in an oxidation
process, there is an increase in oxidation number and loss of electrons. In reduction, there is a decrease in
oxidation number and gain of electrons.
In redox reactions, the equation should be written as the following:
oxidizing agent + reducing agent → products.
A good example of a redox reaction between iron chloride and tin chloride is shown on pages 424-425 of the
textbook.
The National Fire Protection Agency (NFPA) lists oxidizers in four classes (Classes 1 to 4), with Class 1
having the lowest activity. Class 4 has the highest activity where the materials may undergo explosive
reactions when catalyzed or exposed to heat, shock, or friction (Meyer, 2014).
Common Oxidizers: Many household products used to sanitize indoor/outdoor surfaces and swimming pools
contain oxidizers such as calcium or sodium hypochlorite. Hydrogen peroxide is used to help heal insect
bites, burns, and scrapes, and is also used in hair color products.
Fireworks are entertaining but inherently dangerous. Used in the production of all fireworks is a mixture of an
oxidizing agent and a reducing agent. The oxidizing agent could be sodium chlorite/chlorate or perchlorate,
and the reducing agent could be sulfur, pulverized magnesium, or aluminum flakes (Meyer, 2014).
There are only a few ammonium compounds that are thermally stable, so the use of them is limited. A
common compound that is used commercially is ammonium nitrate, which is used as a fertilizer. Another
example of an ammonium compound used is ammonium perchlorate, which accounts for, “70% of the solid
propellants used by the aerospace industry to propel space shuttles” (Meyer, 2014, p. 445).
Notable incidents involving ammonium compounds include the following:
1947 SS Grandcamp incident in Texas City, Texas: The ship was carrying nearly 2280 tons of
fertilizer grade ammonium nitrate when it caught fire. The heat generated by the fire resulted in the
decomposition of the ammonium nitrate (Meyer, 2014). The decomposition products, oxygen and
nitrogen dioxide, supported combustion in the storage hold of the ship, a confined space, resulting in
an explosion.
1995 Oklahoma bombing of the Murrah Federal Building: Fertilizer grade ammonium nitrate and
diesel fuel were mixed and detonated (Dougherty, 2001).
Other common oxidizers include the following:
oxidizing chromium compounds (more commonly called hexavalent chromium with +6 oxidation
state),
sodium or potassium permanganate,
metallic nitrite or nitrates,
metallic peroxides and superoxides,
potassium persulfate and sodium persulfate, and
matches.
Oxidation–reduction reactions, also called redox reactions, greatly benefit our modern lifestyle. When
oxidation–reduction reactions are conducted in a controlled fashion, the energy they release can be
harnessed to our advantage. However, when redox reactions occur in an uncontrolled fashion, the generated
3
UNIT x STUDY GUIDE
Title
energy is released into the immediate environment where it can initiate or intensify fire and explosion,
resulting in the loss of life and property. This necessitates the study of redox reactions by EHS and FS
professionals responding to hazardous materials incidents.
References
Burke, R. (2003). Hazardous chemistry for emergency responders (2nd ed). Washington DC: Lewis.
Dougherty, J. (2001, May). McVeigh diagrams ANFO bomb. Retrieved from
Meyer, E. (2014). Chemistry of hazardous materials (6th ed.). Upper Saddle River, NJ: Pearson.
11 n hts,de (J _ 1-+ 2) Ba lance oxygen byinsertmgal ,nfr on the left s. oe 01 1~ arrow but six on th~ }so b3lances the nurnber of potassium ato ms on eac h 1.:1 Cl~ •ormu•.i fot potdSS um b,c,1rbon: 1:01:s e 01 a,.,ow TheeQu,monnowlookS a .., ~ … Di’.S)-‘ .;,(Oils;_ Hi0\.9)., C0 2(gl
Perlorm,ng a rin.tf checl: 0/’I the numbe r of atom\;”;~::t:~ !~:~es~~: :7~h=1~:,t i~~~:si~hm , tv,a a~
of h}drogen. rv.o atoms of caroon, an d 51,: ato ms , rs @Q~~~ ,
REDUCTION
5.4·8 .
11
is a lways associa ted ,_vith the acc~mpa nyi ng p rocess ca ll ed reduction . An}’ o ne
o~;d:}~iowing p roc esses co n stitut es redu ct io n: .
ofl
1
11
o und s redu ce w hen they lose oxyge n atom s. For exa mpl e, when sod rnm p er-
• ~~~r:te is hc a red , it loses oxygen atoms.
ii , ___________ “ow_bdl.Jn,~c,=d~——————– NaCJO”(s) NaCl(~) …. 20,1(gJ Sod1ump,:n.h lvr:Ul”‘ Sod ,um chlo n,k O,) gc n
OJfid.1 tio n-rl!-duction
rNCtion (re-dox re«tion)
A chem ical react ion
betwee n one or more
01Cid iz ing and reducing
agents
oxidatio n • A ch emical
process during wh ich a
substance reacts as an
oxid izing agent
5 .4 OXIDATION- REDUCTION REACTIONS
. 1 ocess in rerm s of whether it represe nts an OXid .
Chemi~rs also cl? ssi~ a c~:~:t
1
/:i~ed a redox react_ion. Comb! nation, decom po:i~11-
redu’:1on reaction , re~ rea c:io ns involve oxi darion-reducnon processes, whe/ll,
a nd s im ple replaec:;nr:crions do not. Although we s.rudy redox reactio ns in m:;s
double replac em b . d standi ng is now required, because we will enco ‘
deprh in Chapter 11 , a as 1c un er · unr~
th em frequentl y.
5 .4 -A OXIDATION
Oxidation is an y of th e fo llowing processes:
Elemencs and compounds oxidize when th ey gain oxygen ,1to ~1 s. W~en a compound
is o xidized, eac h rype of atom within the ~o.mpou n d co~_bmes _wnh oxygen. Fot
exa mple, carbon, hydroge n, and methane ox1d1ze by combm mg w1rh oxygen.
C (s) + 0 1(g) – C01(g)
caroon 0Aygrn
2H1(g) O,(g)
Hydrogrn o,n:rn
CH.J(g) + 20 2(8)
Mrlhl!IIC- O.\ygrn
Cwbontl 10;0Jt”
WaJc- r
CO,(g) + 2H10 (g)
Ca.rbou J1o~id,: Wa te1
Compounds also oxidize when rhey Jose hydrogen ato m s. When methanol decon,.
p oses, for insta nce, formalde hyde and hyd roge n form.
C H30H(g) – , HCHO(g) + H ,(g)
Mcth.lnol Fonna/dch)de l·l)drvgc n
Beca use methanol loses hydrogen aro ms, iris sa id to be oxidized.
An element or ion o xi dizes when it become s less affi liated w ith its electrons. for ionK
s ub sta nces, this is accomplished by the loss of one o r more electron s.
.:-•.r:t {s) – Na-(aq) + e –
Mg (s) Mg,-(aq ) + 2, –
Cu (s) —–. Cu 2 … (aq ) + 1l’ –
Fe2- (aq ) —-+ Fe3 … (aq ) + e-
2Cr-{aq) Cl1(g ) + 2e –
ln th e firs t three examples, neut ral atoms of sodium, mag nesium, and copper, rt~pc(·
ri vel y, Jose eit her one o r two electrons as indicated and become posi tively charged t~!Hi
in the fo urth example, rh e iron (II J ion loses an electron and becomes th e iron (IIIJ ion;
a nd in th e fifth example, eac h of two c hl o ride ions loses a n electron ro form 3 nruiul
mo lecu le of chlorine.
f re sodium perchlorate is sa id to be reduced. .
Th~e :u nds a lso reduce when th ey ga in h ydroge n a toms. For example, t he organic
1 ~~n:O und erh ene combines wi th h yd roge n to beco me et ha ne.
C2H°'(g) + H 2(g) – C2Ho(g)
E1hcnc Hydroge n E1hanc
B se it ga ins hr drogen atoms, eth ene is redu ced.
• S~~~~nces reduce w he? th ey ~ecome n~ore affi lia ted with elecuons. For ionic sys –
tems, redu ction is assoctated with the gain of electrons.
C l,(g) + 2, – – lCl – (aq )
s,1,1 + 16, – – ss1 – 1aq )
Fe3 .. {aq) + e- – Fc 2-(aq)
Fe 2~(aq) + l e- – Fe(s)
In che firs t rwo examples, n.eucral _elemen ts gain electro n s and for1:1 n ega ti_ve ions; ~n the
third example, th e iron (fII ) 10n gams a n electron and beco mes th e 1ron (U) 10n; and 1~ the
final exa mpl e, rh e iron (II ) ion gains two electrons and becomes an a to m of elementa l iro n.
The molecu les a nd ions on the left of th ese a rrows are said to be reduced.
Oxid.1tion and , eduction a lso occur in cova lent sys tem s, but here, an actual t ransfe r-
ence of electrons d oes not occur. For insta nce, co nsider th e c he mi ca l react io n represented
by 1he combi nation of hydroge n and ch lo r ine.
H1(.~) + Cl :2(~) – 2HCl(g)
l-l )Jrogcn Chlorine l·l}drogc-nchlondc
In th e hydrogen a nd ch lo rin e mo lec ules, the electron pa irs in the cova len t bonds arc
sha red eq uall y br their res pecti\’e atoms. In th e hr drogen chloride molec ule , ho wever, the
chlorin e atom shar es the pair of bond in g electrons 10 a greate r d eg ree than does th e
hydrogen a tom. This un equa l s harin g of the electro n pai r is illustrated in Figure 5.1. h
causes a n unsymm etri ca l electron di stribution in the molecule of h ydroge n chloride. Thi s
unsymme tric a l distribution of el ec trons is t y pical of oxidation in co val e nt sys tems .
Hydroge n has been oxidized a nd c hlorin e has been reduced .
00 GXi)
Hydrogen Chlorine H yd rogen ch loride
flG URE S.1 Whe n the ox1dat1on- reduct ron phenomenon occurs between cova lently bonded substances,
e’ee1rons are not comp letely transfer red from one rea ctan t to th e oth er In the hydrogen an d chlorine m olecules
shown here ro the left of the arrow, the electron pairs are mu t ually sh ared between th e tvvo hke atoms But 1n
t/-te hydrogen chl ori de molecule shown to th e rig ht of the arrow, the electronic d1stnbu t1on is asymmetric about
th e center of th e molecule Th is pa n 1al loss and gain of electron density 1s typical of t he oXJd at1on-reduct 1on
redct ron s 11wo!wn g covalen tly bonded substances
red u ction • A chem ical
process during which a
substance reacts as a
reducing agent
140 Chapter 5 Principles of Chemica l Reactions
Chapter 5 Principles of Chemica l Reactions 141
I reduci ng ag ent The substance oxidized
during an oxidation-
reduct ion reaction
oxidiz ing agent {oxi-
dizer) The substance
reduced dur ing an
oxidat ion-reduction
react ion
rate of reaction The
speed at which a
chemical transformation
occurs; the amount of a
product formed, or
reactant consumed, per
unit of time
igni tion source Any
purposeful or inciden-
tal means by which
self-sustained combus-
tion is initiated
Any oxidized substance is called a reducing agent, and any reduced substance is
called an oxidizing agent, or oxidizer. These names result from the effect that the agent
ha s on other substances. In the combination of hydrogen and chlorine, chlorine is th,
oxidizing agent and hydrogen is the reducing agent.
Consider another example. Decades ago, cameras used flashb~lbs to generate a bril-
liant blaze to lighten a darkened scene. The brilliance was ~ssociated with a chemical
reaction in which metallic magnesium burned to form magnesmm oxide.
2Mg(s) + O!(g) —> 2MgO (s)
ivlagncs iurn Oxygen r..fagnc sium o:c;idc
During this reaction, a magnesium atom loses two electrons to_ become a_ magnesium
ion. It also combines with oxygen. For both reasons, magnesium ts ox1d1zed. Each
atom of an oxygen molecule gains two electrons and becomes an oxide ion. The oxy-
gen is reduced. Magnesium is the reducing agent, and oxygen is the oxidizing agent,
or oxidizer.
5.5 FACTORS AFFECTING THE RATE OF REACTION
Each chemical reaction occurs at a definite speed called its rate of reaction. Sometimes
the rate of reaction is referenced by correlating it to a chemical phenomenon, as in the use
of terms such as the rate of combustion, rate of corrosion, or rate of explosion. Chemists
establish these rates of reaction by experimentally noting the change in concentration of a
reactant or product over time.
The speed at which a given substance undergoes a chemical change is often associated
with its hazardous nature. This is clearly illustrated by the detonation of nitroglycerin.
Several grams can completely decompose within a millionth of a second. Fortunately, nm
all chemical reactions occur as rapidly, or we would have even greater problems when
responding to emergencies involving hazardous materials.
The rate of reaction depends on at least seven factors, each of which will be discussed
independently in the sections that follow. When appropriate, the influence of each factor
is noted as it bears on the rate of combustion.
5 .S· A NATURE OF THE MATERIAL
When exposed to air, some substances do not burn at all. Examples of such substances are
water, carbon dioxide, nitrogen, and the noble gases, Other substances, like hydrogen,
magnesium, and sulfur, do not begin burning in air until they are first exposed to a source
of ignition. Common ignition sources include open flames, sparks (static, electrical, and
mechanical), lightning, smoking, cutting and welding, hot surfaces, physical and chemical
reactions, electrical arcs, radiant heat, and the accumulation of electrical charges (friction)
generated by the movement of materials (e.g., liquids through a pipe or hose or powders
through chutes or conveyors).
Still other substances burn spontaneously in air, even without exposure to an ignition
source. An example is elemental white phosphorus, which bursts into flame on exposu~e
to the air. These rates of combustion vary from zero to some finite value. It is their indt·
vidual chemical nature that causes some substances not to burn at all, others to burn only
when kindled, and others to burn spontaneously.
5.5-B SUBD IVISION OF THE REACTANTS
Wooden logs do not burn spontaneously. Initially, they must first be kindled, perhaps b;
the heat generated from the b~rni_ng of smaller pieces of wood. By contrast, when the dus
from the same type of wood 1s dispersed or suspended in air within a confined area and
142 Chapter 5 Principles of Chemical Reactions
CHAPTER
,
Courtesy of FEMA.
,,Nfoi4
1
available chlorine, p. 433
chlorine bleach, p. 433
dasses of oxidizers, p. 427
fireworks, p. 438
Fireworks 1.3G (special fireworks,
display fireworks), p. 439
Fireworks 1.4G (common fireworks,
consumer fireworks), p. 439
flare,p.443
fM!HM!
I
11
Chemistry of Some Oxidizers
half-reaction, p. 425
hexavalent chromium compounds, p. 452
high-test hypochlorite (HTH), p. 434
ionic equation, p. 424
nonchlorine bleach, p. 432
oxidation number, p. 423
oxidizer (Don, p. 422
oxidizer (NFPA), p. 427
oxidizer (OSHA), p. 422
oxidizing agent (oxidant), p. 422
safety matches, p. 461
signaling smoke, p. 443
smoke bomb, p. 443
spectator ion, p. 424
strike-anywhere matches, p. 461
Associate the physical and health hazards of the oxidizers noted in this chapter with
the information provided by their hazard diamonds and GHS pictograms.
Determine the oxidation numbers of the atoms and ions in a given substance .
1 Describe how NFPA distinguishes the degree of hazard potentially posed by different
oxidizers.
Identify the primary industries that use the oxidizers noted in this chapter.
1
Identify commercial products that contain oxidizers.
1
Describe the OSHA and OHS regulations that pertain to the handling, storage,
stowing, loading, unloading, or discharge of bulk quantities of ammonium nitrate.
ld~ntify the labels, markings, and placards that DOT requires on the packaging of
oxidizers and the transport vehicles used for their shipment.
Identify the resp onse actions to be executed when oxidizers are released fro m th ei
r
Packaging into th e enviro nm ent.
ox id izing agen t
(oxida nt) An oxygen•
rich substance capable
of read ily yield ing
some of its oxygen; the
substance reduced
during an oxidation-
reduction react ion
oxi dizer For the
purposes of DOT
regulations, any
substance that may
enhance or support the
combustion of other
mater ials, generally by
yielding its oxygen
oxidizer (O SH A) Any
gas, l iqu id, or sol id that
read ily yields oxygen or
other oxid izing gas, or
that readily reacts to
promote or initiate
combustion of combus•
t ible materials and,
under some circum•
stances, can undergo
vigorous self.sustained
decomposition due to
contamination or heat
exposure
Certain chemical reacrio~s s:ea rly benefit modern li~esryles. They ~nclude the c tion of fue- 1s, the ch_lo n n:Hlon of_ water, the ex.plos1on of dy~?mne, the bleaco~ fabrics, and the tbrm ~ o f recre~nom l fireworks . These spe~1f1c phenomena a; utgflf
ciared wit h oxidarion-rcducuon reacuons, also call~d red ox rea~ttons. These rea crio e a.sSo-
the ha zardous m~Herials associa ted with_ chem consmure the s~1b1ec r matter of thischansa~
\Vhen oxidation-reduction rcac11ons are conducted m a controlled fash · Pttr.
ene rgy rh ey release can be harnessed to advantage. For example, the reaction hion, tht
in devices such as barteries, dry cells, a nd fuel ce lls provide a suppl y of pona~ t ar 0ctlir
energy. Howe\’er, whe n redox reactions occu r in an uncontrolled fashion th e elect~
energy is relea sed into the immediate _environment, where_ it can initiate ~r i:t:~~era~
and explosion and cause the loss of life an~ property. This potential for destructi~ firt
necess iraces the examination of redox reaction s as a component of the st ud y of ha llC\s
o us materials. lard.
11 . 1 W HAT IS AN OXIDIZER?
Ir was noted in Chapter 7 that ~ydroge n burns in o~ygen an~ chlorine to produce \\’ite
and hydrogen chloride, res pecnvely. These combustion reacuons a re represe nted b · h’
fo llowing equations: ) 1 e
2H,(g) + 0 2(g)
H~drogcn
H,(g) + Cl 2(g)
H~drogcn Chlonnc
2H 20(g)
Water
2HC l(g)
H)drogen ch londe
The subs tances supporting these independent combustion processes are examples of oKi-
dizers, o xidants, or oxidizing agents. The first two terms a re u sed by emergency respond-
e rs, bur the third term is used by chemists. H ydroge n is an example of a reducing agrnt.
Oxidizing agents always react wit h reduci ng agents in concert.
Because hydrogen burns in a chlorine atmosphere, it is evident chat oxygen is not tbr
sole substance that s upports the combustion of other materials . Like oxygen, chlorine is
an example of an oxidizer.
11 .1-A DOT CLASSIFICATION OF OXIDIZERS
In the DOT regulati o ns, an ox idize r is defined as a subsrance that may enhance or sup-
port the combustion of othe r mat e ri a ls, generally by yie lding its oxygen. DOT al so
distinguishes berween two cla sses of oxidizers: inorganic (or metallic ) oxidizers, which
are si mpl y called oxidizers, and o rganic peroxides. Their properties arc nocrd in 1lu5
chapter and Section 13.9, respectively.
11 .1-B OSHA/GHS IDENTIFICATION OF OXIDIZERS
Formerly, OSHA defined an oxidizer as a substance other rhan a blasting agent ore~pt
sive that initiates or promotes combu stion in other materials, thereby causing _fire e~t :
of itself or through the relea se of oxygen or ocher gases . Following the adoption ° ~
GHS, OSHA no w considers oxidizers as any of the three cl asses, oxidizing gases, oxi ·
ing liquids, or oxidizing solids. As oxidizers, each of rh e latter stares of mat1cr ca use cw
contribute to the combustion of ocher materia l, generally by providing oxygen. _ ht
Except for oxidizers that are organic compo und s, OSHA minimally req uires~
manufacturers, distributors, and importers of oxidizers ro post the GHS flain e•_o~•er• I :
letter- .. 0 ” pictogram ro the labels of chemical products consisting of an oxidizi~g:rr
liquid, or solid, in addition to appropriate signal words and hazard and precauuo
sta temenrs.
422 Chapter 11 Chemistry of Some Oxidizers
1
1
_2 OXIDATION NUMBERS
emists use ch e_ ~oncept 0 ~ an ox1dat1on ~umber, or oxidation state, to describe the
Ch ibining capability of on~ ion for anorh_er ion or of one atom for another atom. In prac-
c~ 11 an oxida tion number 1s formally ass igned to the atoms 1hat make up a substa nce by ::~~;g ihe following rules:
The oxidation number of each atom in an element is zero; rhus, the oxidation number
1 f each atom in the element~ H 2_, O z, Na , and Mg is O.
~h algebraic su m of the ox1dat1on numbers of the atoms in any substance is zero.
1 Th~ hydrog en acorn in hydrogen-containing compounds other than metallic hydri?es
1 has an oxidation number of +1. The hydrogen in a hyd ride ion (l-r) has an oxidation
number of -1 .
The oxygen acorn in OX)’gen-containing compounds other than peroxides and super-
xidcs ha s an oxidation number of – 2. Each oxygen atom in a peroxide ion (O t )
\d a superoxide ion (O l ) has an oxidation number of-I and – 0.5, respectively.
~he oxidation number of a monatomic ion (i.e., ha vi ng one atom) is the same as its
1
net ionic charge; thus, the oxidation number of sodium is +1; of magnesium, +2; of
the chloride ion, – 1; and of the sulfide ion, -2.
1 The algebraic sum of the oxidation numbers of the atoms in a polyatomic ion is equal
to its ionic charge .
The chemical formula of a substance must be known to use these rules and determine the
oxida tion numbers of its component atoms. As an example, let’s use them to determine the
oxidation number of each atom in sodium chlorate, an oxidizing agent used in fireworks and
signaling flares. The chemical formula of sodium chlorate is NaCI03. This formula indicates
that the compound is composed of two ions, the sodium ion (N a + ) and the chlorate ion
(CIOj”) . The oxidation number of each element in sodium chlorate is determined as follows:
OXIDATION
CONSTITUENT NUMBER
Sodium ion, Na• +1
Orygenatom -2
Chlorat e ion, (10 3
_,
Chlorine atom +5
RELEVANT RULE
The 01tidation number of a monatomic ion is the same as its
ionic charge.
Other than in peroxides, the oxidation number of oxygen is -2 .
The algebra ic sum of the oxidation numbers of the atoms in a
polyatomic ion is equal to its ionic charge; that is, -1 = +S + [3 x
(-2)] = +5 + (-6) ,
The algebraic sum of the oxidation numbers in any substance is
zero; that is, 0 = + 1 +5 + {3 x (-2)] = +6 + (-6).
Additio nal examples of determining the oxidation numbers of the atom s in some com-
po unds a re noted in Tab le I 1.1.
11.3 OXIDATION- REDUCTION REACTIONS
Brcause a redox reaction occurs between an ox idi zing ~1gent and a reducing agent, the
~quation illustrating a rcdox reaction is always written in the following generalized form:
O xidi zing agen t + Redu c in g age nt –t Produ c- L::,
~,S Pec_ific example of this is the reaction between iron (lll ) chloride and tin (ll ) chloride.
r Wrn c the eq uation for this reaction as follows:
2FeC l3(aq ) + SnC l2(aq) 2F(‘C 12(aqJ + S nCl.i(w1)
lrun1 lll 1 ch lun,k Tin( l ll chlomlc lr0n ( II Jch londc Ti n
\
lV)chlonJ,:
oxi dation number
(o xid ation state) • A
number assigned to an
atom or ion by follow •
ing established rules
that aim to reflect its
capacity for combining
with other atoms or ions
Chapter 11 Chemistry of Some Oxidizers 423
spectator io n One or
more o f the ions t h at
do not participate in an
oxidatio n-reduction
re action
ion ic equation An
equation th at dep icts
only the ions that par•
t icipate in an oxidation-
reduction reaction
Mllhiiil
SYMBOL OF ELEMENT OXIDATION NUMBER
0
Cl
– 1
I -2 so 2
1 H 20 2
—–~:3——- ~ N;:H-, —–
– 2 Ni H4
-1 NH20H
+1 N20
+2 NO
+3 HN02
+4
+5 _,
+1
+3
+5
+ 7
HN0 3
HCI
HCIO
KC I02
KCI0 1
HCI04
Because the chloride ions do not parricipare in this redox reactio n, they often are called
spectator ions. We can eliminate them and write an ionic equation fo r the reaction as follows:
2Fc3 .. (aq) + Sn 2+(aq ) – 2Fc 2+(aq) + Sn-l+(aq)
In an ionic equation, only rhe symbo ls of the ions cont ributing to the reaction are wm·
ten . In this rep resentat ion , electrons have si mpl y been transferred between the iron ions
a nd tin ions. The informa tion conveyed by chis equation is summa rized as foll ows:
The iron (ll1 ) ions become iro n(ll ) ions. The ox idation number of iron dec reases from
+3 to +2; thus, rhe iron {III ) ions are reduced. lron (III ) chloride is ca lled rhe oxid,zmg
agent, because it oxidizes tin (II ) chloride.
The rin (Il) ions become rin (IV) ions. The oxidation number of tin increa ses from +l
to +4; thus, the tin (Il) ions are oxidized . Tin (ll) chlor ide is ca ll ed the redu cing agttll,
because it reduces iron (IJI ) chloride.
Because a simultaneous increa se and decrea se in oxidation numbers alwa )’S accomP’.1·
oxidation and reduction , respecti vel y, we can summarize the natu re of this process in
1omc systems as follows:
Oxidation is the ph enomeno n associated wi th an increase in oxidation num~r and
loss of electrons from an ion, a tom, or group of atoms . d
Re~uction is the phenomenon associated with a decrease in oxidation number 30
gam of electrons from an ion, atom, or group of atoms.
424 Cha pter 11 Chemistry of Some Oxidizers
Some Common Ox1dmng Agents
ox101z1NG AGENT
~m pero)(ide
~ Ilic .
nypocn to rItes
;;i’allic chlorates
Nitric ac id
(concentrated)
Nitric acid (dilute)
Metallic
peroxydisulfates
ELEMENT T HAT
CHANGES
OXI DAT I ON
NUM BER
Oxygen
Chlorine
Chlorine
Nitrogen
Nitrogen
Sulfur
OXIDATION N UMBER
IN IN
REACTANT PRODUCT
-1 -2
+1 -1
+5 -1
+5 +4
+5 +2
+7 +6
EQUATION I LLU ST RAT I NG
HA LF·REACTION
Na 20 2(aq) + 2H 20(f) – 2e
– 2Na · (aq) ..,. 40H (aq)
00 (aq) + 2W(aq) + 2e
– Cl (aq) _.. H 20(f)
CI0 3 (aq) ..,. 6W(a q ) ..,. 6e
– Cl (aq) – 3H 20(f)
N 0 1 {aq) – 2W(aq) -r- e
– N02{g) – H 20 (f)
N0 3 (aq) -r- 4W(aq) -r- 3e~
– NO(g) + 2H 20(f)
S20 .2 (aq) + 2e
– 2so / (aq)
1 The substance that accepts electrons during a redox reaction is ca lled the oxidizing
agent.
The substance that lo ses electrons during a redox reaction is called the reducing agent .
Oxida tion and reduct ion phenomena can also be represented sepa ratel y by equations
like the fo llowing:
Sn 2— (aq ) – Sn4 .. (aq ) + 2r
Fe3 .. (t,q ) + c- – Fc::! +- (a q )
The phenomenon illu strated by each equation is ca lled a h a lf-re action . One half.reaction
repre sents oxidation, whereas the other represents reduction. The processes represented
b)’ half.reactions always occur simu ltaneo usly.
Se ve ral 01hcr exa mpl es o f oxidation-red uction phenomena ~ue provided in Table l l .2.
h alf.reacti o n
An equ ation that
sepa rately depicts
eithe r oxidation o r
reduction
SOLVED EXERCISE 11.1
ft
de ntify the element ox1d1zed, the element red uced. the ox1d1z1ng ag ent , and the reducing agen t in th e re dox
reaa,on denoted by the following equation
6Fe50,:(aq) • Na 2Cr20 1(a q ) -r- 7H 2504(.:iql –
lronill)\ulfd tf’ So d,umd,c!uoma:.:- Su! fur,ca<•d
3Fe2(S0,1)]1a ql -r- Na2 SO.daq1 .,. Cr 2(SO.;l/aq -r- 7H 10 ri
lron{llI) sul fate <,oo,um ~ull.u c ( t- ·,w uIr,,111> sul f,11 (.’ \\ a\er
t this equat,on, the sodium and su lfate ions are 1dent1f1ed as spectator ions, because th e oxi dat ion
! ,minate: 1: d;~I:~I
~~u
I
~n~;:q~:t~i~
I
~r:r:~:~.ame on each ~1de of the arrow . W hen the spect at or ,ans are
Chapte r 11 Chemistry of Some Oxidizers 425
:\
\
1,
I I
I
!!It r1
fl f I
I 1; I II
I/ Ii’
I I
I
I /I
i I
ii
FI GURE 1 1.1 The
cn m1na/ act of detonating
awea.oon ofmass
destruction at th e
Oldahoma City federa l
bu ildin g resulted ,n 168
iatal1t1esand8 S0m1u ri es
The w ea pon was a 4000-
po und ( 1800-kg) mtXture
of amm onium nJtrate fer-
ti lizer and fuel 01I (ANFO }
Th e detonation occurred
atth e rat e ofapproXJ•
mat ely 13,000 ft.ls (4000
mis) (Courresyof FEMA /
ro aeterm,nt’ the a,o: uat,on nu,.,ber of chrom um ,n the d ch romate on. reca ll that the aiget ra c sum of
~~~~r.,…o~c~r~~t::at~~; n a 001yatom •c ,on 1s equa l to ,ts 1on,c cha rge We thus de1erm ,ne that ll’ie~~
– 2 = /2 X ( .. 6)) -t- /7 X (- 2))
– 2 = – 2
Theo~ oat or number of the monatom ,c ,eris is the s.!lme as the ir 1on1c Ch.!lrge ;~:~:%~:,~~r~;d;io~~ ;3!’ ;~,’:;/ /~;n~:;~~l~;t!’ ~;~~~s:~:;,~;~;:n~n ox,da;,on :~! 11 .4 COMMON FEATURES OF OXIDIZ ERS Di ffe r e nt o xidiz er s ca n hav e di ss imilar srrengrh s . This va ri atio n in rhe strength of 426 Chapter 11 Chemistry of Some Oxidizers
Relative Strength of Ox1d1zing Agents ..
Fluor ine Oxygen •u11ed In aescend,ng orde r of ox idi zing power In its codes and standards, N FPA us es the term oxidizer to denote a substance that I Class I oxidi zer. This is a subs ta nce th at does nor moderatel y increase the burning rate 1 Cla ss 4 oxidizer. This is a substance that can undergo an explosive reaction due co Some specific o xidize rs are denoted in Table 11.4 using this system of classification.
11.5 HY DROGEN PEROXIDE Solut ions ha ving a concentration from 1% co 3 % by mass are used as top ical ~ :.ardou.s M,ttenals uxle (Qui ncy, M.iss;a chUSfflS: N:1 tioru l Fire Protccuon ~ation), 2009.
o x idize r (NF PA) • As cl as se s o f o x i d ize r s • Hydrogen peroxide, Chapter 11 Chemistry of Some Oxid izers 427
I I ~ I CLASS 1 Ca lci um hypochtorite (66 % or less av.t ,l able ch lor,ne and a total water content of ,tt least 1 7% by mass) Bar ,umbromate Sodium persulfate CLASS2
N1troc acid (more than 40% but Jess than 86 % by mas~ Hydrogen pero1Ude (greater than .27.5 % up to 52% by mass) Sod11Jm perox ide Lrth1um chlorate Ammonium d 1chromate 9t %byma1s) Per ch/or,, ac id solutions. 60 % to 72 .5% by mass
Strontium perchlorate CLASS3
Potass1umbromat e CLASS4
Ammonium perch!o r.;1te (part rd e size greater than Guar11 dme nitrate Ammonium perma n ga na te —
‘ ilepnmPd w~h pe,m~1or1 from “-FPA .:00-10 11, ~nra~ M,1tpn,1/s CodP. Copyrig ht C 201). N4t!Ofl.tl f ire Prote,ct,on Assoc;,;rtlon, Qui~ M-‘- i’- 428 Ch apte r 11 Chemistry of Some Oxidizers
nir11onl y av.111.iblc a s ovcr-1~e -co unter produc ts in drug s1ores. They ;1.re a lso wi~dy O s.iln: “; 0
1::dons h.1ving co n~entra rio n of 6% by mass a re used m bl e.1c h ha ir. In the ~roJu cr-1 {ions having a conceniration from 30% 10 50% by mass are use d in th e chem!- O l;, w sy nthesize peroxo-organic co mpound s (Sec1io n I 3. 9 ). T he JO% so lu110n rs 5 rr • Sol ut ions ha ving a concentrauon _of 70 % by ma ss ar c use d by th e chem ica l 111du s JS J!o/~~1~ ~:: ~o:~t~;n:. concentr.Hio n of 90 % by vo lu me a re use d b y the aerospa ce roxide so lution s a re no ted in Table I 1.5. Alth ough anh yd rou s h ydro ge n perox id e k, brc n p roduced, it is unava ilabl e commerciall y becau se ir is li kel y to decompo se CH , C!-1 1- C – l·l(/J …- O~ (x) O H CH3-n – CH 3(/J – H_-O~({J
0 The h>drogen pe ro xi de and ace tone a re se para1ed b y dis till ation. T h e h ydr oge n iiiiiiiii Phys ical Properties of Some Hydrogen Peroxide Solutions Bo ,lo11gpoin t S?tc,f1c~v, tyat68•F(20 “0
Vapo, preuure at 68″F (2_.:.0 “_:C:_) -‘-“‘—–‘ Chapter 11 Chem istry of Some Oxidizers 429 H)drogen peroxide is an inherend y unstable substance. It slowly decomposes as fo!IO\\,: ll ~ds”o~cn ~nn1J~ \\ ,,tn O, )gcn
The r.m:- of the decomposition reaction is c:1t~l yze d by sun lig ht as w~ll as certain metal Conce nrrat c-d so luc io ns of hydrogen pe roxide (>6 Y~ 1110 i l beco me intensdy heat d deco~:n::i~~~:;ed hydroge n pero xide solutions ha ve rhe following properties:
Whe n co ncentrated hydrogen peroxide soluti o ns decompo_se, ample hcac may be FI GU RE 11 .2 In comp hancewith DOT regulatoons, !he 430 Chapter 11 Chemistry of Some Oxidize rs
11 .5-A THE KURSK 11 .5-B WORKPLACE REGULATIONS INVOLVING When hydrogen peroxide is us ed in the workp lace, OSHA requires 11 .5-C TRANSPORTING HYDROGEN PEROX IDE 20!i, to40’/o
;;;60¾ -,60¾
Shipping Oescnpt,ons of Aqueou s Hydroge n SHIPPING DESCRIPTION•
-t UN2984, Hydrogen pero)( ide, aqueous solut ion UN2014, Hydrogen perox i de. aqueous solution (stabilized) UN201 4. Hydrogen perox ide, aqueous solut ion (stabilized) UN2 015, Hydrogen perox ide, stab ili zed) ‘l!tlOff sh ipmtnl, OO T requ ires the adC1 1tlon of a subrtan.te to hydrog en pero• ldt to Inhibit In de co mP05!tl on.
When shippers offer a hydrogen peroxide solutio n for tran sportation, DOT require s t ei;hipping pape r. DOT a lso requires s hippers and car riers to comply wit h a ll applicable SOLVED EXERCISE 11 .2
Whtn a sh, ppe r offers a carrier 2 500 pound s (1135 kg) of an aaueous solut,on containing 30% to 3 2 % hydrogen (al What sh ,pp,ng descnpt,on does DOT requ ire the sh ipper to provide for th ,s chem ical commod i ty 7 Solution: mg 30% to 32 % hydrogen pero)(1de so lution on the accompanying sh ,ppmg paper
I (1DENT1F1CAr1o~H:~:;E~~!~~1::~0s~1PP1NG NAME. f UNITS HM HAZARD CLASS OR DIVISION, AND PACKING GROUP)
1 cargo X UN2014. Hydrogen pero 1C i de. aqueous solut ion
tank I ~:::!lr~:ts~~~7~~i ;~3 1 WEIGHT 2500
(b) Beca use more th an 100 1 pounds (454 kg) of the hy drogen pero -.ide solution 1s offere d for transporta • 0 s1de and each end F,nall y, as p1evIousl y noted In Table 6 7, because the solu tion contai ns more than 10% hydrogen
~Za~~~E~ch end of the ta nk HYDROGEN PEROXIDE . r I 11 I
:/ I I
ii’
I I no nth lotin e blea ch • 11 .5 -D RESPONDING TO INCID ENTS INVOLVING \,? hen eme rgency- res pons e team s encou nt ~r h ~·d rog en _pe r~x id e so lutio ns at ace· 11 .5 – E NONCHLORINE BLEACHES An exampl e of a no nch lo rine bleach is Ox1Clean. Its active component is an dd 2Na_.,C03·J H:,0 1(aql (‘iod1ur11p1:rcarb,m.Ut)
2Na_.,C 0 3(aq) + 3H_., 0 2foq1 Sodmm ca rbon :i te perox yhydrat e 1s also 3 component of T;de Lau11dry Detergent anj [
HO 0 – 0 0 111′ “‘Na· 8 U j ·-l ll 10 110 0 – 0 Oil When sodiu m peroxoborate is di ssoln:d in cold wat er, it di ssociates and form s h)·drogru N .1_., 8 2(O1)l O H )4 -H-!2O(aq! — 2Na l3 0 ](aq 1 ,_ 2H20 z(a11) – ~l l10tfl When sodium peroxoborat e is dissolve d in hot w:i ter, th e hrdrogen peroxide dN”omposts 11 .6 METALLIC HYPOCHLORITES 432 Chapter 11 Chemistry of Some Oxidizers
Il l.i s arc N.1CI O and CJ (CI_O )1 ,. re specti vel y. When 1he y a re used a s bleach(n~ 1 Jf tilorine bleaches . 15 1tJ\ fr or11 co u on and hn ~n, ~ut not w~I , silk, ;ind nr lon. N? nchcmtsrs generall_y c?n – l ,anufacturers post on th e fabric’s 13bel the open triangular sy mbol shown below The effectiveness of the hypochlorite bleaching agents is commercially described h)’ The available chlorine in any chlorine bleach is determined by using rhe reaction C i(CIOh(~) + -t HC l(oq) — CaClz(aq) … 2H~O(1) ..,. 2Cl ~(g) The percentage of chlorine produced from the gi\’en amount of calcium hypochlorite is So me hypochlorite bleaching agents are solids at room temperature, but they are also Cnlci11 mh)pc… hlonte C:ik1u m ,hlon dc o~) p:n
When thi s decomposition reaction occurs at a fire scene, the oxygen suppo rts combustion 11 .6-A SODIUM HYPOCHLORITE \X’e are mos t familiar wi1h sodium hypochloritc solutions that are used as bleaches So lu1 ions th at contain from 10 % to 12 .5% sodium hypochlorite arc also av ai la ble chlorine bl ea ch • availabl e chlorine Sodium
hypochlorite
Chapter 11 Chemistry of Some Oxi di zers 433
Ii rr- 11 I l/1
Potable Vent
Ched( val~,
Q=..::J:_=::Hy=~~ softener Potable To,~ … Calcium high-tu t hy pochlorit e so lution havin g 12.5 % a va ilable chlorine. It is used as a disinfectant and sa niriurfortht Sodium hypoc hlor icc formerl y wa s ma nu factured for commercial use by pa ssinggu. ~N aOH(aq) + Cl;(I.’ • – NaCJO(nq) + NaCl (aqJ ..- H10)
S00 111 mh) Jnn1Jc Chlonn~ S0J1u111 h)P•><.hk,mc 'ioJ111rn .:hfonJe \ \Jl(T
Today, citing the de sire to 1mpro\’e security, Clorox dilu1es high-strength (15 %) bleJQ Sodium hypochlorire may also be generated fo r use on demand. In the system sbot.’I ‘ ./:J. C Haq) …- H 2O (ll – N .tClO(a qJ + H z(g ) 11 .6-B CALC IUM HYPOCHLORITE Calcium hypochlorire is manufacrured b)’ reacting chlor in e wirh a lime sl urry. AII\IJ 2Ca(Oli )1(aq) + 2Cl ~(x) – C a(CIO l~((lqJ + C:1C l2((1q ) + 2H 2CX/) Sodium chloride is 1hen added 10 th e so lution. This ca uses the calci um hyp0chlon1tlO 434 Chapter 11 Chem istry of Some Oxidizers
Contact of calciu m hypochlorite wit h Oa mmab le and combustible mat er ials causes 11.6-C TRANSPORTING METALLIC HYPOCHLORITES FI GURE 11 .4 Th ,s test 1/li!IIW Shipp ing Oescn pt1ons o f Some Re p rese ntative Me t a lhc Hypochlontes Ca lci um hypochlor, te, dry, and c.a ldum hypochlorite dry mixtures ClltJum hypoc h lonte, hydrated and calc ium hypochtorite Ca k 111m hypoc h lor1te, dry (contains more than 10% but not UN1748, Ca lcium hypochlor1te, dry, 5 .1, PG II
UN1748, Calcium hypochlom e, dry. 5.1. PG 111 UN2880, Calci u m hypochlorite, hydrated mixture, 5.1, PG II
UN2208, Calcium hypochlorite, 5 1, PG Ill
UN2208, Ca lcium hyp oc hlori te m i xtures, dry, 5.1, PG Ill
UN1471, Lithium hypochlor1t e. dry. 5.1. PG II
UN147I , Lithium hypochlonte m i xture. 5. 1, PG II
Chapter 11 Chemi stry of Some Oxidizers 435 I I j The s hippwg de~npuons of :1 11 01hC’r metallic hypochl orJt l’S :1nd th eir so l 1 inorgJmc, n.o.s .• 8. PG 11 .- “Ui’: 179 1. H ypochlontc: solut ions (cont:1 1n s sodi urn ~rn’\ Sod,”m 11 .7 D I· A ND TR ICHLORO ISOCYANURIC 436
Although C;J.lcium hypochlonte conti nues to be a popular component ~f industrial saruulloit 1-1 Cl N N o – C C – 0 O = C C – 0 CI – N N – Cl CI – N N – CI II 1)1 We sru d y the natu re o f th e bondmg m th ese compou nd s more hi ll y in Chap ter 12. chlo ri ne va lue cha1 ran ges from 90 % to 99%. They are a lso ava ilable co mmercially u 11 .7-A COMMERCIAL USES OF 0 1· AND TRICHLOROISO CYANURIC The major use o( th e d s· and m chloro1soc y:mun c aci d pro ducts is t o chl o rin:u e the watrr11 Di· and tr ic hJoroisocyanunc :icids are a lso co m po nents of dry laundry bl eaches, dcur- 11 .7 -B TRANSPORTING DI· AND TRI CHLORO ISOCYAN URIC When shipper s offe, r d1ch loroisocya nun c ac id , tn chloroi socpnuric 3 ci d, o r th e sa lts of ;~;~e schoo7no~~ ds for tra ns portation, DOT requi res them to provide t he ship ping dCSCtlP- Chapter 11 Chemi stry of Some Ox id izer s
— Shipping O@Scr1 pt1on ,;. o f t h e O,lo n n a t ~d l,;.ocy-1 nun c Aci d ,;. cttLORINATE D 1so~ NURIC ACID l),,hl or o• iocyanuncac id SHIPPING DESCRIPTION UN246s. ~ a n~ c aci d, dry, 5.1. PG II o, ,tiip pt rs nd c:irricrs to compl y wu h a ll applicabl e labe lin g, ma rking, a nd placa rdin g
rr.:iiu rtinents.
11.8 CHLORINE DIOXIDE Chlonn(“d10 , 1tk
Chlo ri ne dioxide is routinel y produc ed nea r 1he pomt of i1 s imended u se. In the si m- N,1CI O(mJ) – ~H C l(dq ) – • NJCl(aq l • 1-1 ~0 (/) + Cl~(gl In 1hesc-cond step, the c hl orine 1s rea cted with a sodi um chlorite so lution, whic h re s ulc s in :: -.:.1CI01(aq) + Cl 1t 8) – X10 ~1g) – ‘.!NaC lf w/l \’!;’ hen chlorine dioxi d e is di ssolved in water, an aqueous so lur ion is produced known Chlorine- ~GURE 11 .5 Cnlorme dio xide usua ll y Is generated at 1111:• locat,onwl’Lere it ,s to be used 1n tn ,s ~1mp\•f1ed ” tctareascontam ,natedw1thmold,bacteria. and v1ru ses
Chlorin• Chapter 11 Chemistry ot Some Oxidi zers 437 ‘1
I I I
I Consum .,
Fir•works and
Special Flr• works
firewo rks • Pyrote ch – r;~~l~ ~fe:~1t~;!::sl;:\t ~:h;e”c1:;~~~-t he aqueou s solu ti o n surv ives for 3 long hlTlc, Illa 1s mhala 1to n toxici t y. Ex pos ure 10 chlo rin e d1ox1de a lso caus es severe respirato 10~ 1 1 .8 -A COMMERCIAL USES OF CHLORINE DIOXIDE C hl o rine d ioxide 1s somet imes al so use d as a microbicide. For example it · Ustd In 2002, when anthrax-laden ma il was di sco vered in postal areas and in 1hc Han Stq In 2 0 05, fo ll o w ing th e Hurr icane Kat ri na di sas ter alo ng the Gu lf coas t, chlorine ~ox- 11 .8-B TRANSPORTING CHLORINE DIOXIDE NA9191 , C hl orinc d iox.idc, hydra1 c, frozen, 5. 1, (6.1 ), PC II (Poison)
DOT a lso requi res s hippers and ca rr ier s to comply wit h a ll applicable labeling, mJtkmg, 11 .9 OXIDIZERS IN FIREWORKS AND Fireworks ~re ite ms des igned primanl )’ for entertai nm ent purposes wi th 1he inte lll of pro- firewor ks. Two cl asses are espec i:-. ll y imporlant: Fi reworks 1.3G and Fireworks !.4G(for; 438 Chapter 11 Chemistry of Some Oxidizers
h oOT d1 v1s1on num bers o f the rel evant haz.ard class and its compatibility gro up oduce audible effects. In addit ion, ch1\d -protecuon laws ha,•c b:mned the possession , crsC al so compels manufacturers 10 pr ov ide special labeling mformauon on the con – rl rew ork s 1.3G (spe ci 11 I fi re w orks 1 .4 G {comm on Although sta le and loca l laws attempt to prevent 1hc widespr ead sa le of firewo rk s to 10 a pcrnut 1s all owed to sell fi rewo rks 10 the public. To further reduce o r climm:nc 1hc risk of Onr co mponent of all pyro1echnics is a pyrotechnic m ixture of a n ox idi zing agent Sodium chloritc. sodium chl ora 1e, a nd sodiu m pe rch lo ra te deco mpose 10 produce N:1C102(s) – · N aC1(s ) …, 0 2(g) So NaC\0.i{() – N:iCl(s) + 20 ::_lg) .-\ltho ngh th e o xn;cn produced by these reactions aids in actuating the display, mo re complex The uniqu e co lo rs obse r ved during the display o f fi reworks re s ult a s ce r1ain co m- Chapter 11 Chemistry of So me O xidize rs 4 3 9 I Ahi%11 Examples of the Chemical Phenomena Associated with the Actuation of Ft~works Sod1umch!onte
Sodium ch lorate
Sodium REDUCING Charco.il
Sulfur Magnesium
A h,1m,num
Charcoa l
Su lfur
M.Jgnes ium
Alum inum
Ch omoa l
Sulfur I Magn e1ium EQ UATIO N REP RES ENTI NG THE REDOX REACTioN
– ,(JC) • NaCI01{S) ___, Na (l{s~ Ss(s) • 8″-:.aCI01M – 8NaCl(s) • as o2(g) 2Mg(.l) • NaCI01(l) 2″”g0 (s) • NaO(I) 4Al(l) 3Na(101(s) – 2Al103 (.I) + 3N•O(JJ K b) , lNaCI01(!) – lNa Cl[l:) 3COJ(g) 35 8(1) 16NaCI0 1{s) – 16NaCl (s) -t 24 SOi(9) JMg (s) • NaCI01{s) – JMg O(s) – NaC!(J) 2Al{s) NaCI 0 1(s) – Al201(s) • NiiO(s) 2C(s) • N•C10~(s) – • NaCl(s) • 2C0 1(g) 58(s ) • 4NaCl04(S) __, 4NaCl(s) – 8501(91 4/v’g(s ) NaCI04(s) – 4Mg0 (s) • NaQ(I) 8A l(s) • 3Na(l04(S) – 4A l201(s) .,. JNaO(I) chlo ride s, whic h fl uoresce strongly in the visible wave length s. Some examples and tM Ba rium chlor ide ydlow-grcen Cupr ic chlorid e blue-gmn Firework s have also bern usrd as wea pons of mass des truction. The mixture of~ 11.9-A TRANSPORTI NG FI REWORKS 440 Ch a pter 11 Chem istry of Some Oxi d izers
Shipping Descriptio ns o f Fireworks”‘
REWOR KS — _ ~ PINGDESC l!.I PT!O N 1 ~rk1. d,v islon 1 3 UN OB S, Fir ew or ks, 1 ) G, PG II (EX-)(.l(U)() UNOJJ7, Fi reworks, 1 4S, PG II {[X •)()()(lUI)
~1,r,esforShPl)(l9¥idTrM61)0n”‘9Fi~M’Wl,ngtan. OC: U5. ~mtmofTransport~h01’\ lOl l)
DOD ) nauonal stoc k number, product code, or otht’ r idenn fyi ng information in th e sh1ppmg tSCl”rior requ ires shippers and car rie rs 10 compl y with all ap plicable labeli ng, markmg, ::im~g fire wor ks to restrict mo \’e ment m a transport ve hicle and protect them a g:H ns l Wh en eme rgency responders encountr r fi rewo rks durin g a 1ransponat1o n mishap, 11.9-B DI SPLAYING FIREWORKS NFPA h:is also bee n concr rned wit h the trai ning of indi vi dua ls who di spla y fir eworks. doors only b)’ adh r ri ng !O specified minimum sepa ration distances between the :1.ct ua- EXApprova l Numbet(onoackag e E~2016
Haia rdlabol. 49C ,F.R § 172 .4 11, PVRO FOUNTAIN
“”'”””‘°’ ~ !FIR~~:i~: ~9 4 ~odr (or fo ni-ork.lDuplay (Quinc-y,Mawdt=: Nlt•=I Flre r ro1«tion,\gfflq ), 2010.
FI GU RE 11 .6 Th1spack- Chapt t t 11 Che mistry of Som e Oxi dize rs 44 1 442
ifriiiiifi Shipping Descriptions of Some Representative Metallic Chlontes, Chlorates, and Perchlorate s UN1 445,Bariumch lo1ate. s 1.(6 1). p~ UN14S3. Ca lclum chlo r1t e, S 1, PG 11 — Barium chlorate –~UN271J, Magnes,um ch lor~ ….. UN~otass ium chlorate, 5. 1, PG 11 11.9-C TRANSPORTING METALLIC CHLORITES, T he oxidize r s used in fi rewo rks a re avaibb/e as com me rci al c he nuc al products, Whn, 11.9-D ILL EFFECTS CAUSED BY EXPOSURE TO Considerab le co ncern abo ut th e hea lth effoct s lik ely co r es ult fro m expos ure to ptrdtlo, Does h uman exposu re to pe rchl o ra tes p ose a h ea lth ris k? S1udies rr 1•e:1 l a link bc~ttn JNJ11onJJ Rewcar,h Coun” I of rhe NmonJ J AcJJemy ol Sc, r 11, r~. /fra//h /mJ,l1wt10I/S o/ Per.blo•.1lr l•!d1.,. Chapt er 11 Chem istry o f Som e Oxi d ize rs
t n• of null1on s of Amenc.1 11 women and 1he ch ild ren tht·y conce ,1•e , especiall y bt·cause ~- ~crchlor,H e con r:a m rn a u on 1s a ho tl y co nt este d po l1u cal m ue in Ca l 1forn1;1 and 11.10 OXIDIZERS IN FLARES, SIGNALING Flarts, signaling smokes, and smoke bombs a rr d ev ices th a t co nta in :i p yro r«h n ic m1x- r; ro 1dr nr ify a nd o bsc ure scenes o f interest, cordo n off acc ide nt sites, a nd coo rdinat e In 1he cw1han wor ld, roadsi dr fl a res arc used to com mum ca te d1su ess, ident ify a tra ns• ,•1.”,01m!rJI~ ~ulf~r l\llJ\\I Ulll [‘.”n.hl.:,r.nc
fl .:, re • Any art,cl e s,gn • lin gsm oke • Any I!
smo ke bomb • Any ~111.>nt.0 11 1 o”J~ ‘- ultur J,,,,1Je p,,u,,1u111 ,hJ,,n,k ‘i tn•;:c·n J 11,.,J,· O•)i~n operat ions
.\l rl rtJ f}’ an d c ivi lia n aviato rs an d sa ilo r s use fl ares or fl a re/sig na lin g s mo ke co mbin a- 11.10-A CHEMICAL ACTUATI ON OF FLARES, ln add tt1on to a n oxid i:u ng a gent and rc.-d ucin g agent , flares , si gnaling smokes , and smo ke When rh e ch e111 1ea l mix tu re in fl a res , signa lr ng smo krs , a nd smo ke bo mb s is a ctivated JOKC/O~!l) + J ~ ~( q – • 16 KC l( sl .,. :!4S0,: IC’) Ch apter 11 Ch em istry o f Som e Oxid izers 443 ‘ I
/I 444
r he th (‘ rm.11 d t·com pos 11 mn of sodrnm b1carbon.H t’
~N.1 HC0 ,11l -• N,1: C0 1t 1 l -+ CO:(cl .. H:Oi,~J As c.irbo n di o xide ,in d s ul fur d 1ox1de evo hc 1n 10 the :m, th q · d1 <: pcrsr lhC' dr .
1mmed1.1tt." area . e l!llf.:
Th e usr of smo ke bombs an d orh u py rorcc hmc s as r spe c1all y 1•1rn l to the succ~ 1/
use as d1s 1r~s srg nal s 1f thei r a irc raft foi\ Fbr(‘S are al so used by military ~v:,1~bi Smo ke bo mbs a rc- usl!’ d by th e 1111l 11 ary to vis uall y ma sk the movl!’ ment of treo~a 2A](q – CCli – CCh(j) – JZnO{1J __. 3ZnCl:/ n + Al1O3(s) + 2C(iJ The zi nc chl o rid e attract ed atm osph e ric mo istur e ro form a fog . rhr alumin um oltdt: 11 . 10-B TRANSPORTING FLARES, SIGNALING SMOKES, Wh e n s hippe rs offer fJarC’s , signal ing smokes, and smoke bo mb s fo r 1ra nspo rt:1tion, DOT 11 . 11 THE THERMAL STABILITY OF Ammo nium compo und s are substan ces whose unm co ntai n an ammon ium ion (t-.li/J Ammonium compounds ma y decompose imo the compou nd s from which they war /’. H~CI({) – • NH i(g J ., /ICl (g) Th e a mm o nium compo und s that deco mpo se III this simp le manner ge nerall y are~ Chapter 11 Chem ist ry of Some Ox id izers
Sh1ppmg Descnpt1ons of A-ires, S1gn•hng Smokes, SHIP,INGOESCRIPTION
UN009l, f lares, aerial. l J G, PG II (EX •u ~u )
UN0403 , Flare s, aerial, I 4G. ?G II (fX •x.uu)
” UN0404. f l;i•e~. aerial, 14S, PG II (EX ·lX.UX) ” ___ __:Ucc.:N04 21 , Flare1. aer ial. I 2G . PG II (EX •x~ ~;:d ;in~ 1t ia t m g d e~1c@ ___ .._ __
s,:;;e 1,gna ls I ~:0196, Signa ls, smoke, 1 1G, PG u (EX · XJOllOll
~ tllMeS
: UN019 7, s,gna ls, smok e, 1 4G. PG II (EX· XJOllOI )
I ~~0113, s,gna ls, smoke, 1.2G, PG II (EX ·unx) UN0487, Signals, smoke~ G. P~ · XJOllOl….2_
UN009 2, f lares, surface. 1 JG, PG U (EX·lOUlXX )
UN0418, Flares, surface, 11G. PG II (EX-uxxx)
UN0419, f \;i res, surface, 1 2G, PG II (EX·)()IUX)
ammomu m com po und s are ammonium azidc, ammonium bro mare, ammonium c hl o- 11.11-A COMMERCIAL USES OF AMMONIUM COMPOUNDS Ammomum perc hlorate is 1he only o th er ammoni um co mpound use d m sig nifi ca nt \ lum ,n~ ni o\l..k ,\l ununum chl,,n,k \\’ J t~I
11.11 -B TRANSPORTING AMMONIUM COMPOU N DS Chapter 11 Chemlrtry of Some Oxid ize rs
I 445 r ii-‘=i1iiiii Ex,i11mpl~ of Ammo ni um Compounds Th a t Are Hazo1rd o us Mate n al s Ammon ium az1de1 N H,N 1(s) – 2 Ni{g) 2 H!(g) —-
Ammonium brom•ll!• 1 lNH1 8 r0 1(.1) – lNH,Br(!) 301(9) Ammonium chlorate• lNH1 CI0 1(s) – 2NH,CI • 30 i(g) Ammon ium d,chromate —(NH.J2Cr10 1M – · (•101(1) N~4H10(g~ Ammonium fu lminate• lCO(g)—-
Ammon,umn1tnte1
l\uogen
Ammonrum perchlorate -2NH~CI04(s) – Ni(g) • Cl2(g) • 201 (9) • 4H20 (g) Ammoo,.,m perc~loraU N ffogen ( hlor,ne 0,yge n Yl•ter Am.,,on,u.., ~1m•n91r,1•e Mdngane1e(11)0 1·de N1!ro9en Ory gen Wi’lt1
~–m-.-~—~-,-~-d-.-~-~-~—–,-~-~-b-½-~—– – – –•-•~ 0D0Tprohibitsthe 1r1mponat,011of 1htsema1er l•’1 1Fi1iikti Shipping Descnpt1ons of Som@ Representative Ammonium Comp ounds Ammomum dichromate
Ammon iu m n itrate fertilizer
, SHIPPJNG DESCRIPTION
UN143 9, Ammon ium dlc hromate, S 1, PG II
UN2067, Ammon ium nitrate ba1ed fertiliur, 5 I, PG II ., Ammonium nittal! emulsion UN 3175, Ammonium nitrate emulsion, 5.1, PG U Ammon ium nitrate/fuel oil minures (conta ins pr, lled ammon ium NA0JJI, Ammon ium nitrate-fue l oil mfxtures, 1.SD Ammonium ni trate, liqu id (hot concentrated solution) UN2426, Amm on ium nitrate, liquid, 5.1 Ammonlumpersu lfate
446 Chapter 11 Chemistry of Some Ox idize rs
UN 1442, Ammonium perchlorate, 5.1. PG U — f Jl su rrq u1res sluppt’rS and GJ rnrrs 10 comply with :ill app l1c:1ble labding, m.ukmg, 11_12 AMMONIUM NITRATE 61 IJ;, 311 rn 10 111 um 1011 . its ch r mica l form ula is :\’H-1;,.”0 ;. s~’ \’eral gradrs arr :1vai la ble fauli ir r-gr..1dr a mrnoruurn mtr:1t r JS commonl y encount ered a l forms and fo rm d is• Nll .iNO i! sl – N~0 (11l + 211 20/d I Techmc.i l-grnde :a mmon iu m mirate 1s producrd for a \’anety of uses. For rxa mpl r, 1t 11 .1 2-A AMMONIUM NITRATE AT FIRE SCENES \ mrr1<:m1ummtr:11c N11roiicn Nitrug,:nd,o\lJe \\ ,,J cr
lhest decompomi on products are gaseo us. t irr, wh en the deco mposition produces are confined or ca nnot be \’ented from the storage
Ammoolum 0initrog,o Ch1pter 11 Chem istry of Some Oxidiz ers 447 I s,um addod ‘””” “”‘H;'””” ammon ,um nr:rl’le \ ..,
15001onso1 ~•i”~R!i~d °;,e~~”G?;;;~,1 :’F:~:~~c~: ~~;t..,’?~ ❗ 1: ~:~;ra~~:,~ 01J•l a1Joof 1rt,er’lal or~rewtn.n uiehoc-;tna!Y,1i1sreevtooru~ v. nenu,ecargo’lh,ps!JOSlol.leUI),~ area. a ma 1or explo~1on rs hkdy co occuL This was th e fau of the Fr(‘nch cargo ship s_s In 1947, the Grandcamp ,..,as docked :it rhe harbor in Texas City, Texas, wbeu Altho ugh fi re s m 1olnng ox1dmng agenr s can effec11l’el)’ be ex t ing uis hed throap. Tht” explosion of th e Grandcamp is now rega rded as t he worst ma ri ume 111C1dal fn contempora ry tlllles, the worsr industrial accident fo r emergency responders inl”(ihrd 11 .12-B WORKPLACE REGULATIONS INVOLVING THE OSHA has pro mulga red regula tions rel aring to the sto rage of bu lk quanmies of J(TIQ)’ ‘Gl,nn HCi~. ·frmluer B!nt lgnue, Concerns.• Chr,,r. £rig . . Vru,s. Vo l. 91 (! 0 J J ), p. jj_
448 Cha pt er 11 Ch e m istry of Some Oxid ize rs
fhe OSHA rt”gulau~n s J>t”.n a m 10 thrt”e sub1ect areas: 1he nature of the building m \\ or piles wirh,n an a pproved butldmg; and the sto ragr of ammonium nimue w ith fll, ~ .,rure of t he Build ing in Wh ich A mmon ium Ni rra tt’ Is Sror ed
1 • All floo nng m storage a nd ha n dling a reas within an ammonium nit rate sto ra ge budd – 1 The ammonium n it r at e stora ge build ing a nd 1cs struct urrs must be dry and free from 1 Unlt”Ss consrrucred of nonco mb usn ble ma te n al, or unless adequa t e facilit irs for fight – • Sui1.1blt” fi re-com rol d e1·icrs, suc h a s small -hosc or pan.abl e fi re exrmguLSher. . mus, 1 \rater supplies a nd fi re h ydrants m U5t be located nC'”3.rby an ammonium nitrate sw r- The Storage of Ammo ni um Nitr a t e in Con t a in ers nm of rh t” prod ucr C’XCC’C'”d s 130°F (54″C). panmons of the J ntmo nium nitra te storage bu ildin g. ammonium n ic r;1 ce sto rage bu ild ing ch a t is not cquippc-d wit h an automa u c spri nkle r Th , Storag e of Amm oniu m Nitra t e in Piles the product rxceeds ! 30° F (54°C). 16 m) m w1 drh , :1n d 50 feet ( 15 m ) m lengt h. When the pi lts a re sto red wi t h in a b u il d – 1 A1s!t-s mus r be pro l’id ed ro sepa ra te am mo n iu m n itrate piles by a clcn space of nor 1 Bm s must bt” kept clea n an d frre of ma tena ls that ,a n contaminate ammonium nm.He.
Ch il ple r 11 Ch e mistry of Some Oll idlzers 449
11 FIGURE 11 .8 Al 29 C FR §1910 109, OS t’A reQ u me ‘Tl ployer1tostoreby lk Q~nti l.eS [>1000 P01Jnd:1 • O wi ng to rhe corro s1\’e and reacri ve p roperties of ammonium nitrate and to ar~ I AMMONIUM NITRATE I • The height or depth of th e a mmonium nnrare piles is limited by th e pressure-srnhnc Th e St o ra ge o f Am m onium Nitrat e w ith Other Su b sta nc es firewa ll s of no t lrss than I -hour fire-resis tance r aling, or sepa rat ed by a spa« rt 450 Chapt er 11 Chem istry of Some Oxidizers
,on i:1nun:111 ng sub srnncc s, mcludmg but 1101 l1mJt cd to anm1Jl fat s, bJled co 11 on, 1 11.12-C HOMELAND SECURITY ME ASU RE S INVO LVIN G $1J1ce 9-11. la w enforcement agencie s h:i,·e taken measures to reduce the potemfa l for the 11-1ihm iheir junsd ic rions. Because ammonium nit ra te ca n be used hr te rrorists, feruhze r DHS and the U.S. Coast Guard (USCG ) have been especially sensi t iv e to the entry of SOLVED EXERCISE 11 .3
-. , os~ ~ regu1a1011 at 29 CF R §1 910 109 st1ou lates th;it ammonium rwate fen:1h1er cannot Ofdnar,ly be S.5, • 32 •11–1~ …. oj’.S\ – eSO;g, • c·~0:9′ CJ’1,0,9 ]P,.!] Ci~.! “‘~1t lkely requires t/’le seg re ga tion oi am mon um nitrate from sulfur and foie ly drded me:a’s to 1ec..1::e Chapter 11 Chem istry of Some Oxi d izer s 45 1 r htuva!e nt chrom ium compoundconta in1n9 At J.3 C. F. R. S 126 .l S, DHS h.1s prnmulgarcd rrguL111ons rrl.111ng 10 thr • L~; 1 • ~;;:: 3 • ~~:~r;:;::, :!~,:t:~~1i;1:,~;t~~~re~~:~ 1:;u;::1i:~;s~·,.d1~w1ce from rl~rric ~1nnL 11 . 13 OXIDIZING CH ROM IUM COMPOUNDS The metallic chrom::ites an d met::illic dich romace s :ire compounds composed of aJIOSI· Th e o xidizing chromium compounds a re manufactured for comme rcia l use from -H l( r~04(11 – KK2C01(il + 70 .:f~J ———-. 8K,C r0,11) .,.. 2Fc , 0 1(s) + SCOi(tl Pora srnun d1chroma te 1s dll’n produced by rhc r<.' JCtio n of sulfu rJC :icid with porass1Ulll
ch rom;1te.
2K:l rO ,/llql 11 2so 1raqJ 452 Chapte r 11 Chemistry of Some Ox id ize rs
p,) tJssnun chrom ate m;1y be produc ed from po1::i ss1 um di chromJte, and 1•1cc vers:1 . by K: Cr20;(aq) • 2KU ll !aq/ • 2K: Cr0~1 01/J 11 _: 0 (/l
2 p,.,,: ,n, _im,,,~1,c 1/ “JrO The mcra ll1 c chroma tcs and metallic d1chromJt es are sohd yellow .1nd or,mge com- 11 sciluuons. trratmen r agents to pre1·en t the formation of a minera l sca le that oth erw ise would form m loca ted at petro eum re menes, power plants, chem ical plants, 1 Jnd elsewhere, where 1he y :ire used ro cool water by evaporar.ion. In 1he past, the waste ge nerated in connection with us ing Ilic :ibsorption of a hex:ivalrnc chromium compound into the Erm Brocko\’ic h, 1he heroine in the blockbuster mo\’ie of 1hc FIGURE 11 .9 Cool,ng 1owers ofte n are mass,~e wate,- :i~•r of En, 1ronmcn 1a! Heal th HH ,lrd A;sc11mcn 1, E, 1dr”ct 011 th , Drvtlopmtn lJ/ a•rd R ,produc/,0 11 Tu r ic- Chapter 1′ Ch emirt ry of Some Oxid ize rs 4 53 I //’/ 1 I / f!/ 454
Pot•»•um 11 ;m •r. EPA h.1 s al~ o used the.’ :iurhora y of 1hr To'(JC Subsr,mces Co ntrol A,:~: 1; 1 d~ A1 40 C.F.R. 5749.68, FPr\ rcquirC’s d1 s1r1burors to labe l contamrr s of h 1 This product contains hexava/ent chromium . Inhalation of lung cancer. Federal law prohibits use of this substance in sively to, and are an integral part of, heating, ventilation EPA req ui res th is label 10 I,(‘ J ffix ed ro the conramrrs wit h such cons pi cuous ness tha dit 1 condHJons of purcha se ;rnd use. llUry
11 .13 -A POTASS IU M OICHROMATE Bec:iuse ir 1s a s1rong oxid izer, potass ru m dic hromare is che rrn ca l/ y rnco mpauble 1orli K:Cr20 · laqJ – l -lH Cl (aq) —,. 2CrC l 3( {1{f) .. 2KCUaqJ t 7H20 (/) + 3Cl~) The eme rgency inciden ts 111\’0 h·ing 1h1s ha za rdous ma teria l genc- r.:tll y are assocfa tc-d 111th 11 .1 3-8 CHROMIUM TRIOXIDE nc aci d to a s.irur.ircd sohmon of potass ium dic hrom:it e.
-. 2K I/S0 Jraq! + 11~0 ({) + 2Cr0j.(J) Ch ap t er 11 Chem istry of Some Ox id ize rs
Ch r<'r11uin1 moxidc ,s usrd for mrIJI 1re,1t mrm procesr.es such as ch rome pla1mg, copper
,inppuig, alt1m1nu111 a nodlllng. and corrosion prt\'tntion.
11.13.C CHROMIUM OXYCHLORIDE ~:,. hl ortc aci d and sulfuric ac id IS added IO a SJtu ra1rd solun on o f pota ss ium dic hro – Chromium ox}chlondt 1s no r onl y an ox1d1ztr. It also reacts 1ery violrnt ly 11 1, h w.i rer, (,(r0:Cl2/// ,.. ·Ul .? 0 (/l _,. 2CrClt ((1ql -+- 4 1-1 :C rOJ(uql 3Cl:1 1;) ln ,his 1ns1;1ncl’, the chro mrc ,wd is the Mtru rM chromic aci d (nor ch romium tnox1de ), hic h t XJ>IS onl}’ m solm1on.
11 ,13-D AMMONIUM DICHROMATE 11 .13-E WORKPLACE REGULATIONS INVOLVING THE OXIDIZING 11.13-F TRANSPORTING THE OXIDIZING CHROMIUM CO MPOUN DS ifriiilifi Chromi c acid
Shipping Desrn pt1ons o f the 0 1ud1Z1ng Chro mium I SHIPPING DESCRIPTION
UN1755, Chromic ad d solution, 8, PG ll ~um~e UN2720, Chromium nitrate, 5 1, PG Ill Ch1om,umtriox1d _ _:, ___ -i-=-UN’-l –”6″-3, -‘-Ch—‘,o-m_i, _m _u l_o,_id_, . _ao~hy_d,_o,_••-‘ ·-‘• -” -‘• ‘- G_II __ _ Chromiu m Chapter 11 Chemistry of Som e Oxid iz ers 4 5 5 ill ., I I i, / 11 ,
I I ‘ I Ammonium Potns ium
11 .14 SODIUM PERMANGANATE AND Meta/l,c permang<111a1es arc compounds in which m,111 g.111 cse assumes the +? OJC •
sta r~· - Tht"r art" gl·nrral!y encountrr('d as dar k \Wier. mdcsccnt crys r,1 !s. There ar{' t¥.·1d.i.~
mercially 1mporrant mrmbe rs of th ts class of comp~unds: sod ium, pe rmangJna ie ando ~
sium permang.mJte. Their chr micJI formulas are -...: .1 \ l n0 -1 a nd K\l n0 4 , resP«'tn el}~
11 .14-A PRODUCTION AND COMM ERC IAL USES 2,\ l nO, r~J + ~KO H f/) ,- 0 :IC?J – · 2K~ ~fo0-1(l ) – 2Hi 0 /g ) solut ion of the porassium mang:rnare is th en ox1di u d dcctro lytica l/ y to prod uce pota~ 2K 21\ l nU-1( oq) – 2Hz0 I/J – • 2K,\l n0 -1( aq) + 2KO H (t1q) + lli(f) The potassium permang.ma1e is tht’n se paraied from t he po tassiu m hydroxi de br You ma y be familia r wi th dilute so lution s of sod ium pc-r manga nate an d pormWII Porassmm permanga nate ha s al so been used ro co ntrol the infestation of the qwgp 11.14-B TRANSPORTING METALLIC PE RMANGANATES 11 .15 METALLIC NITRITES AND METALLIC NITRATES 3 rrs jtl:lliilfl a,r,.-m perm.i~anate
Clc,umPerman~nate
~ ermangana t e
SC{lumPe~a nganate
z,r,cperm anganate
Shipping Descn pt1ons o f the Meta lli c P@rmanganates
SHIPPIN G DESCRIPTION
~ N1 448, Bar, um permanganatt’, S 1, (6 1). PG II (Po,son)
UN1456, Ca1< 1um p,rmangana1e, 5 1, PG II
UN1 490. Pot,m1u m pe rm anga na tt’, 5 1, PG II
t uN1So1 Sod ,um pt’fmanganatt’, 5 1, PG II Jre ,spcci,1ll }’ commo n ox id ize rs; for exam pl e, sod ium nitrate and potass mm mtrate are For decades, sodium mrrite and sodium mtrat e have bet”n ad ded 10 mw meat (bacon . When ind 1l’idua ls ingrst or inh ale sodi um nimt e or sodi um nim1t e in excess, 1hey arc 11.1S·A SOME PROPERTIES OF METALLIC NITRITES :-l-1.’-:0 ~1mn — Na20 2(aq) + H20 U1 – N .1i\’0 1(aq \ + 2N :iO H (oq) I >J,”rn n,u ,•~ ~o.h u1 11 \u lli1 r ll _,d rod1 lonc~ ,J ‘;o ,h uu11u lfru c \,,J1um ch lon,lc \ nm:n., de \1 ,!tcr
Although me talli c nitn tes ge nera ll y are sr:ible to he:i r, they decompose :It r le \’ ared 2N.iN0 1( 1) – • Na10 ( 1) + N0~11:) NO(.~ l ll, 15,B SOME PROPERTIES OF META LLIC NI TR ATES Sod ium Sodium Chapter 11 Chemistry of Some Oxid izers 457 r I’ I I I I \\” hen hl’,irt:d , mc1.1.ll1c mrr.w:s decompo:.t· m the fo llo wmg wa >·s:
Thr albl 1 mer:d m trates decompose ro form !he respC’ct1vt• alkali metal nitrne 2,,; .:i:-: 0 1rq _. 2;,J,1NO:r11 + 0 ~(.111
:\11r.1tes of the no ble me tals decompme to produce th e metal, nit rogen dio -d 1 d1ox 1de, and oxygen.
::!Ag\ ‘ 01(1) __. :!Ag(‘) … ~N0 2f1) – 0 2ft; ) .\!era! mrr:1 tes other than the alkali metal nitrates and the noble metal nitrates d«ornflOlt ::! PhlN0 1)z( 11 – • ::! Ph0 /f ) “1” + 0 2(1n
11 .1S-C FDA REGULATIONS INVOLVING SODIUM NITRITE At 21 C.F.R. §§ 172. l iO and 172.175, FDA publi shes maximum permissible concentra. As a color fixative in smoked, cured tuna fi sh products so that the level of sodium FDA also req ui res the finished product to be labeled with the name of the addi1we, 11S 11 .1 S-D TRANSPORT ING METALLIC NITRITES AND NITRATES 1hen shippers offer ro transport :l meta llic nitrate or metallic nitrite that is not lisrtdal When carr iers transport a pota ss ium nitrate and sodium nitrate mixtu re by hi ghway POTASSIUM NITRATE AND SOD IUM NITRATE MIXTURE
458 Chapter 11 Chemistry of Some Ox idizers
– Sh1pp1n9 Descnpt,on s of Some Re p~se nta tJve Meta lh c Nltntu a nd N1tro11 t H ,-4ETALUCNITRITEOR~ TE SHIPPING DES CRIPTION Alurmnum~•~ c~:(,~m nitrate
tudn1trate
N·C~e –
——-r-UN1438, Aluminu m nitr~ S 1, UN\ 438, PG I~
, UN1446, B,m um nitr ate, S 1. (6 1), PG ll (Po i~onl
~ ~ 1454, Calclum M rate, 51,PG II~
_!. UN146~ Lead nitr at~. 5 1, (6 1), PG II (Po!sonl Po~ n1tra1_, ___ I UN1486, Potass ium nitrat0 1,_PG_ I_II _
Potm~ rlte UN1488, Pota111um nitr,te, S 1, PG n 1 z,ncnitrate UN1514, Zlncnitratt, 5 \, PG l1
11.16 METALLIC PEROX IDES AND SUPEROXIDES 11.1 6-A PROPERTIES OF METALL IC PEROXIDES 2Na20 2(1l _____, 21\’,110 ( ,) + 0 2! g) 2(3301(5) – • ::!ll.10(l l 1 · 0 ~(t; J They also ox1d1ze finely divided combustible metals like- powdered aluminum.
~Al{1 ) T JN;1102(fl -+- 3Hz0 (/ J – Al ~OJ< ,) + 6N ~10H11)
\l" 111 mum "W, um l)(f011J~ \ \mu Alu1111num n\1d<' So.hum h)dro\l J,
The metalli c pero xides are also wate r-reacti ve substances. S0 To pre\’ent metal lic peroxides from ab~orbing atmospheric m01s1ure, they should be ll .16-B PROPERTIES OF METALLIC SUPEROXID ES Sodium t p1roxld1
Pot11sium Chapter 11 Chem lrtry of Some Oxidizers
I 4 59 r 460
Sod ium ffrjifMI Bar 1umperox1de
Ca lciu m peroude
l •t’1 iumperox 1de
Magnes,umperox,d e
Potass ,u m pero .,de
Potau1um sup1uo x1de
Sod1 um perox 1de
Sod ium superox1de
Shipping Descnpt1ons of Some Represe ntative SHIPPING DESCRIPTION UN1449, Ba rium perox ,de, 51,(61), PG U(P~
UN1 457, Ca!c,um pe roxide, 5 1, PG II —–
UN1472, Lith+umperOl1de, S 1, PGII —-
UN1476, Magnesium pe roxide, 5 1, PG 11 —- UN 2466, Potan1um superoxide, S
UN1504. Sod iu m peroxide, 51, PGI —- its u~ r for .:i period ranging from 51111nuti.’S to SC\’era l hours. The moistu re andcarbon d10t· !2 K0;(1) -1- 6H~O(g) – , 12KOH(sl -r- 90~(g) l\11J”IUIIIO\!JC Cdrhnnth \)\IJC f’c>ld,\IUnl<.~1 1'<.lll,IIC
11 .16-C TRANSPORTING METALLIC PEROXIDES AND SUPEROXIDES 11 .17 POTASSIUM PERSULFATE AND ,\oletall1c pcrsulfotes arc compo und s co mposed of a merallic ion and the persu lfa 1e till. r o a ‘ Tw o cx:imp!cs of met::illi c pe rs ulfa 1es are potassi um persulfot e ;ind sodi um persu!falt, Chapter 11 Chemistry of Some Ox idizers Shipping Otou np tions o f M@talltc Pt>”‘ullat H
“4{TAlliCPERSULFATE soourn Persu lfc1te
SHIPPING DESCRIPTION + N1491 , Pota11 ,um per1u lfate, s~u 11_17-A PROPERTIES AND COMMERCIAL USES .Hi.:SOJ(/) + H.: O!(ll – H.: S.: 0 8(/J + 21-110 (/ ) Thi s highl y co rr os iv e solution is popular for seve r.ii tec hn ical a pplica tio ns. Most nora – The metallic persulfotes .ire thermall y unstabl e. For exa mpl e, oxygen and sulfur ~Na ,: S~O~(,) – 2N:l~0( JJ + -lS01(g l – 30~(g ) 11.17•8 TRANSPORTING METALLIC PERSULFATES When shipp.:- rs offr r metallic persulfates oth er than potassi um persulfate or sodium 11.18 MATCHES The rwo types of matches shown in Fi gure 11 .10 are commercially popular. They are l1.1 B-A STRIKE-AN YWHERE MATCHES 11 n11 xt ure is mou nt ed on :i small stick of wood and covered with paraffin wax.
strike-a nyw here s,:ifety m,:,tch • A Chapt er 11 Chemistry of Some Oxi d izers 461 FICiU RE 11 .1 0 Th, / P•S:i- powdere d gins, gl11e
~S, PbO1, glue
-r- Paralfinw u Red phosphorus
‘”‘~~
Af’\ KCI03, SbiS :i, glut P1raffl nw 1• Cardboard
1,1
ibl
I + friction
Tetraphosph oru s tr isu lfide ignites as the match head is struck against a hard surface. Tbt P4S~(s) – 802(e) – • P40 10(s) + 3S0z(g ) 11 .18-B SAFETY MATCHES l6KC!Od1) .,. )~,(1) – · HlKCII J l + ~.tS01(g) Th en, th e energy evoh·ed from th e ox idation of 1hc sulfur ignit es th e antimony trisu.1 6dt.
1.’.\ b!S ,f} ) + 90 !(0 – • 2Sh;U 1tg l t 65 0 118) 462 Chapte r 11 Chem ist ry of Some Ox idizers
iilhilE·I Sh1pp1ng D~u npt1ons of M.itch~s 11 , 18·C TRANSPORTING MATCHES 11 .19 RESPONDING TO INCIDENTS INVOLVING fu·s t•on-1h n cc ne respo nders generally can identify rhe prt”S(“nce of a metallic oxidize r at 1 Th~ number 5. 1 as a component of a sh ipping description of a haz.ardo us matenal The rcrommended method of r xtinguishing fi res supponed by mos t liquid or solid ox1 · Although water effec1ivdy extin gui shes most fires supportrd b)’ meta llic oxidizers, SOLVED EXERCISE 11 .4
l’.’ny i11! e11en t,al lo dam or d,l,;,e the water runoff grf’lerated during , response aruon ITTYOlvlng a wltd OX!.d1ler1
S!il~tlon : 1/Jhen watl’I ,s used during a re1p011se Ktloo 1n.o\1m9 a solid ox.d zer l”.S pnmar, function IS to d,lut, Chapt er 11 Chem istry of Some 0 1d d1zers 463
I
1n tr’lt’ on ,c eau.!lt on, we rt.:id· /y observe thai the ,ron(II} 1cm beco
cNo~-:~,~~~r:!~~1~~~~1:6 ;~ a~ _,~n:, be:~ohrnc~~~~;~u:~l l~~o~: ,;r:: :~:r~: rMJmb!f c(
dKrN2 ,n QJ()dat en number ,s .!ISSOC•.!lt!’d with reduct,on, th e d,chroma te rons are reduced Thus, sooru~’
mate ,s the oxrd.z,ng agenr “”‘
Oxidize r s generalJy are perce ived ~s rclari vel y_ powerful chemica l sub stances, becaUSttbry
o fren react rapidl y, e ven a t e xplo sive ra 1es, with other s ub stan ces . These latter subsca
include fuel s, lubri cants , grea se~, o ils, cotton , animal and ve~etable fa1s, paper, coal,~
straw, sawdu st, and wood sha\’mgs. Becau se the y a rc porent1llly powerful, oxidizers hart
been chosen by te rrorists ro inre niio~all y c~use ma ss d~s1ru_ction and chaos. ln 1995,an
A m e rican terrorist used an ammonium mtrar e/fuel oil mixture a s a weapon o( mau
des truct ion. Ignition of the mixture des tro yed the Murra h Federal Building in Oklahomi:
Ciry, sho wn in Figure I 1. I. The incident killed 168 people and injured 850.
indi vidua l oxidizers can be approximat ed by examin ing the li sting in Table 11.3. In ,bu
series, o x idi zing agents a rc arranged accordin g ro their decreasing oxidizing power. Any
s ub stance w h ose name app ear s on thi s li st is a stronger oxidizing agent than the sub-
s tanc es who se names are lis ted below it. Ir is not e wo nh y that many substa nces are s1ro11-
ger oxidizing a gents than ox ygen itself.
Ozone
Hydrogen perox ide
Hypoch lorous acid
Metall icch1oratesb
Lead diox ide
Metallicpermanganatesb
Met.!lll icd ichromatesb
Nitric ac id (concentrated)
Chlorine
Su lfur ic ad d (concentrated)
Metall ic iodates
Bromine
lron(U I) (Fe 1 · 1 compounds
Iod ine
Sutfur
Tin(IV) (Sn4 · ) compounds
b1~ an,md ,c envlron men1.
cJ n increase t he rate of combustion of Olher materials with whic h it contacts, NFPA dis –
cmg ms he s the degree of haza rd posed by specific oxidizers by assigning them co classes of
oxidizers as fo ll ows: 1
of combustible materia ls wit h which it comes in co ntact.
Cla ss 2 oxidizer. T hi s is a substance that causes a moderate increase in the burning
rai e of combustible materia ls with whic h it comes in contact.
Clas s 3 o xid izer. T his is a substa nc e that causes a severe inc rease in the burning rate
of combustible materials with which it comes in contact.
contamination or exposure to thermal or physical s hock , and that causes a severe
increa se in the burning rare of combustible materia ls wi1h which it comes in contact.
Hrdrogen peroxide is an important substance having the che mical formula and molecul a r
11ructure l 110! and H- 0 – 0 – 1–1, respectively. Specific conce ntration s o f h ydrogen perox-
id~ so lution s are designated b)’ NFPA as me mbers of each class of o x idize r. They arc used
Prrmarily for the fo ll owing purposes:
anri scp rics on minor cues and wounds, as well as sterilizing a nd di s infecting a ge nt s . Th er
used in NFPA’s stan-
dards and codes, any
substance that can
increase the rate of
combustion of other
material and, under
some ci rcumstances,
can undergo vigorous
self-susta ined decom-
position due to con –
tamination or heat
exposure
As used in NFPA’s
standards and codes,
any of four classes in to
which in d ividua l oxidiz –
ers are ass igned based
on their ab ility to attect
the burning rate of
combustib le materials
or to undergo self-sus-
tained decompos ition
35.,,o solution
All 1norgar11c nrtrates (un less otherw,se (lass,f,W)
All lnorgamc n rtrm~s (unless otherw ,se d,11slfred )
Ammon i um pef}u lfate
B<1 num pero:iude
U lc,um pero•1de
Pota ssiu m d,chromate
Potass1umpercarbonate
Potass1umpersulfate
Sod ium carbonate pero,ode
Sodium d•chlo1o+tr1a zi ne tr 1one di hydrate
Sod1umd,chromate
Sodium perborate (anhydrous)b
Sod ium perborate monohydrate
Sodium perborate tetrahydrate
Sod,umpercarbona te
Hydrogen peroxide so lut,or,s (greater than 8% up to 17 5%)
Leadd ,oxide
t1th1um hypoch lori te (39 % or less ava d.,ble chlor,ne)
Lith ,umpero:llde
Magn~n.,m pero.1ude
Manganesed10:ude
Ni tric .tc, d (40 % concentrat,on or less)
Perch loric <1c 1d solutions (h,m th
Barium chlorate
Baruam hypoch lorite
Barium perc;hlorate
Bar ium permanganate
1-Bromo-3-ch/oro-5,5-d ,methylhydantoin (B COMH)
Calcium chlorate
Ca!oumchtome
Calcium hypochlonte (less than SO% by mass)
Calcium permanganate
Chrom ium tr10,11de (chromic ac rd )
Halane (t.J -d1chtoro-S,S -dimethyl hydantoin)
S1font1um peroxide
Trichloro -s-tr1az1netr1one
z ,nc pero:1Ude
Pe~~~~;” ac id solutions (more than SO% but less th,ri 60″ ti,,
Potass ium pe rchlorate
Potass i um permanganate
Potass1um perox1de
Potass ium superoxide
Slive r perox ide
Sodium chlome (40% or le ss by mass)
Sod ium perchlorate
Sod ium perchlorate monohydrate
Sod ium permanganate
le~perchlor,ue
Strontium chlor ate
lithium hypochlorite (more t h an 39 % available ch lorine)
Lrth1um perch lorate
Magnesi um bromate
Magnes,umchlorate
Magnesium perch /orate
Mercurouschlorate
Caluum hypochlorite (over 50 % by mass)
Chlor,c ac id {10% max,mum concentrat 1on)
Hyd ro gen perox ide solutions (grea te r than 52 ~0 up 10
Mono- {tr1 chloro)-tetra -(monopotaui um dochloro)-pent,H –
Th allium chlorate
Urea hydrogen perox ide
Zmcbromate
Zl ncchlorate
Zinc permangan ate
Potass ium chlorate
Potass ium d 1chloro+triaz lnetrione
Sodium bromate
Sod ium chlorate
Sod ium chlome (over 40 % by mass)
Sod ium d 1chloro-s-tr1az1netr1one anhydrous
15 m icrons) Hydrogen pero ~ide solutions (more than 91 % by man)
“pnmPd m.J1Pr’-‘/ a no1 the romplete o ffic, ar posrt,on oft~ NF PA on thP refe ,enad subi m wt, 1cn Is ,epresent e-d only by the ~•rd 111 iarntiflY.
‘1od ,uM perborJtP ii thP rommon namP fo, the sub1tan ce whole p1ope , chpm lcal namp 111od ,um pero• obo••te (Sect ,on 11 ~-El
Jrrc0 h sp ira ls a nd medica l clinics 10 desfroy ge rm s lik e Escher, clna coli, botulism,
u,eJ 111 II
;:1nd o th er mfect iou s microorsani sms that cause dr sease.
rocrss . hy dr ogen perox ide oxrd1zes the dark -colored pi gment called melarun to co lorless
•d
cJI in _u~r : o bleach co tt o n, tlour. woo l, straw, leather, gelar m, and papt’r. T he- JO% so l u-
JISO u>r I O be used instead of ch lorine for treati ng dnnkmg wa ter. Contempora neously,
uon
:~~t1::1 has a lso ac hieved nmorir1y in con nection w ith rr s mi suse by terrorists for the th:iucuon of rhc- explos ive criaceto~e rr iperoxide (Secuon 13.9-C) . . _
try to cxrc ut e oxida rio n-reduct1on react ion s. They a re o flen dil ut ed befor e- u se and sto red
nd usrr)’ as rocket-g rade so lu tion s. T hey have been used 10 o ~i di ze fuel s s uch_ as h ydra –
1 •hJCh lau nched the Apoffo roc kets a nd orhcr pa yload s mw space. Ru ss ia u ses the
:;:;i:n 10 launc h Soyuz roc kets into s pace. T he 90 % so lu tio n ha s a lso been use d by the
U.S. rml1rarr.
Th ;e so lut io n s vis ibl )’ re se mbl e wate r in p h ys ica l appea rance, alrh_oug h th ey may
hJitt slightl y pungent, irrit atin g o dor s. Some o ther phys ica l properties of hydro ~e n
nol ~~!r~·orld”s s uppl y of hydrogen perox ide is manufactured by a number of method s.
Onr i,wok es rh e oxidation of 1sopropr l alcoho l, during which ace1one is coprod uced.
I
I
l,or ror ; J .,kuh” I
p(‘to:.:1 dl’ sol 1111on may then be diluted to produce the d es ir ed concentration fo r co m –
memal salc.
Melt,rigpo.nt
Vipo1d ens1ty(drr: l )
lo’~b,1tty1nwa1e,
~H,O ,(nq) __. 2H 20({) … O ~(g)
most notabl y, iron, coppe r, chr omium, a nd sil ve r. An aqu eo us so luuon of 8% hydr 1,
pe roxide LS comp letely deco mposed following a I 0 -mo n_th ex pos~ re to light, wh er:tn
si milar soluti on kept in darkness fo r the s:m1e length of ume r~~1ams virtuall y unal ter~
In solutions of co nce nt rati ons of less than 30%, the dec’:’~po ~mon °~ hydrogen ~ roxidt
occu rs so s lowl y wh en sto red in dark gla ss bot~les tha~ It ~s virtually 1mp_erc eptible.
when rh cr decompose. These hot solutions th en va porize. ,:-o preve nt th eir decom~i-
rion from posing a haiard before th e intended u_s~ o f ch e oxidant, a ll commercial for111.1
of hydrogen peroxi de arc s ta bili zed by ad d1t1 o n of a s ubstanc e 1har retards Jts
evolved 10 cause th e spo ntan eo us ignition of nearby combusuble materials.
Hydrogen peroxide so lutions having a concentrat!o,_, in _excess of 20% are highly cor-
rosive. \'(/ hen exposed to skin, they ca use seve re 1rntat1on; and w hen exposed to the
e)·es, th ey ca n cause blindness.
shipper affixes OXIOtZER and (OilROSfVE labels to 1h,s
1n1ermed1atebu lkconta1nerhold1ngahydrogenperox-
1de solutwn cons1s11ng of 30% to 32°,o hydrogen perox-
ide The shipper also poru OXIO!ZER placards tha t
display the DOT 1den1,f,ca1J o,, number 20 1~ across their
center areas (CourresyofA-.mrorPerirxrndn
H ydrogen peroxid e has been linked wi th the na val disam,
onboard the Ru ssia n s ubmarin e Kursk. In 2000, the Kurd
exploded and sank in the Barents Sea. Aboard were a numb(r 0f
torpedoes, each of wh ose fuel system s consisted in part of highly
co ncentrated h ydroge n p eroxid e. Inves tigators proposed tba1
the di sas ter was linked to a lea k of h ydrogen peroxide from a
single torpedo. The oxidizer interact ed wit h the torpedo’s stain•
less steel casin g, which catalyzed the decomposition of tlu:
hyd rog en peroxide. The subsequent buildup of oxygen rcsultrd
in ovc rpress ur iza ti o n of th e torpedo and its sub sequent explo-
sio n. Thi s first ex p lo sion th en ini t ia ted the det o nation of othtr
torp edoe s wi thin the storag e compartmen t. The hull of the sub-
ma rine burst, and the Ku rs k foundered and sank . There were no
sur vivors.
HYOROGEN PEROXIDE
employers to limit empl oyee ex pos ur e to an inhalation concentr.1·
tion of I part per milli on , averaged over an 8-hou r workday.
Hydrogen peroxide solu t io ns may be tran spo rted by means of
m?to r van s on public hi ghways or by rai l in boxca rs, u~uall y~:
t.:uned in nonb ulk darkened glass or plastic bottles or inter~.
ate bulk co nta iners like the type s hown in Fig ur e 11 .2. In 3 ddikOO.
hydrogen peroxide may be transport ed in bu lk in a tank [fl.IC Of
rai l tankca r.
Peroxide Solut10ns
(co ntains 8 •/o – 20 % hydrogen pero)( ide). 5.1. PG Ill
(conta ins 20%-40 % hydrogen perox i de), 5.1. (8). PG II
(conta ins40% -6Q 0;. hydrogen perox ide). S 1, (8), PG 11
(co ntains >60% hydrogen perox i de), 5.1, (8). PG I
h w provide the rel evant s hipp ing description s hown in Table l 1.6 on an accompany-
;~iling, marking, and placarding requirements. \'(‘ hen the solution co nrains more t han
JO% hyd rogen peroxide, carriers must comply with a special marking requirement. DOT
rrquirrs th em co mark each s ide a nd each end o f th e tank HYDROGE N PEROXIDE,
AQUEO US SO LUTIO N o, HYDROGEN PEROXIDE, STAB ILI ZED.
pero,;;de for transponat, on In a ca,go tan k by h,ghw4Y
(bl Wh ,ch DOT plac ards and markings does DOT reQ u•r e to be dis played on the cargo tank ?
(, ) DOT 1eQuIres the shi ppe r to provi de the foll owing shipping des.cnpt1on of an aQueous so!ut1on contain•
I
PRIMARY HAZARD CLASS OR DIVISION, SUBSIDIARY
1
~•/o to 32
/4 hydrogen
(lb)
!
~r d~ e tank DOT proh ibits the d,splay of the 1dent1f1cat ,on number on th e subs1d1ary CORROSNE p lac•
Chapter 11 Chem istry of Some O xi d izers 431
I
Any nonchl orine
substance used as a
b leach ing agen t durm g
the la undering of
fabr ics
A REL EASE OF HYDROGEN PERO XIDE
scenes, they should :mem pc no r onl y to extmgmsh o ngoing fires but 10 dam 1dci.;
wa te r r unoff ge ner.11 ed w hil e com b:mng th em . When :1 fir e has no t occ urredor ~ike tlit
t1o ns sho uld be seg rega ted fro m co mbustibl e materials. ‘ 1 e 50!11.
A nu mber of pro duces are available commerc iall y that remo ve und es irable srai d
the la un de ring of ga rme nt s :ind other fabrics. Those that d1 ssoke in water tons lltuJc
hyd roge n peroxid e are called nonchlorine bleaches. Their use during launderin Prodllct
tio ns provi des ch e ad vant age th a t th ey do not destroy most fabrics or harm th/ ~
ance of the ir colors. whic h ca n occur wh e~ chlo_rin e bleaches _(Section I 1.6 ) arc us~:31·
o f sodium carbonate and hydrogen perox ide whose chemical formula is 2N az CO .3~ ;
It 1s al so known as sodium ct rbo na te peroxyhydrate and sodium percarbona:c. 1/ !
whit e ~owder th:it dissociates into sodium carbonate and hydrogen peroxide wh~n ::
solved in wa rm or hot water.
Sod 1umc.1!bo nJ!c~ ru \)h)dr’JIC
SoJ1umcMbon.11c M)J ruge npc ru\l(k
severa l clean ing agenrs and laundry detergents manufocrured by Arm & Hammer. Anotbtr
exampl e is Clo rox 2, a liquid product whose act ive ingredi ent is hydrated sodium p(roxo.
bo r:1 te, co mm onl y called sodium pcrbor:1te.
\! \/
– / \ I\
Sodmmp..·ru~o borl k’
{S,>J1ump,;:rbura1.· 1
peroxi de.
Sod,u,n pcnJ\ o borme S .. hum m,.IJl>urJtc H)ll •o~,-o J’O:nl\ ld~ IIJ1cr
(‘ioJ1um~rbor31c 1
to wa 1cr and oxygen. Table 11. 3 illu strates rh at hydrogen peroxide is :1 mongrr ox~•
age nt than oxygen; hence, a gre ater bleachin g act io n is accomplished when fabncs arc
laund ered wirh Clorox 2 in cold wa rer.
1\lleta llic hr pochlorires are co mpounds compo sed of a metallic ion :ind 3 hyp~hlont~
ion (ClO – ). The mos t co mmon con~mercial examp les are sodium hypochlorire a~
ca lcium hypoc hlo ri te, each of whi ch ts encount ered a s th e acri,,e componcni of seH 1
h ouse hold a nd comm ercial bleaching and sanitation product s. Their chemica
fo :1
~1> – th ese substan ces :1 re d1 strngu1 shcd fr om metall ic perox id e bleaches by cal l mg
ihe n~~iring launder ing, bleaching_ age nt s ar ~ mixed with detcrgems 10 remo ve unde sira _ble
fro J!l fa brics and o.th cr textil es. Chlorrn ~ bl eache s can be used saf~ly onl y on tex ul es
niJ ~ ch ;H th e bleaching ~ct’.on 1s accomplished by chlor ine, bu1 1t 1s actua ll y the ox1d 1zrng
c,n , f th e hypoc hlonte 1011 . _
1’°11~:en chlorine bl e:1 ches can be used safel y during rh c laundering of fabric s, Am erican
cex\e ~cfi . Wh en the use of chlorine bleaches should be entirely avoided, th ey post the
0~J1dl: srrnbol ; :ind wh en neither a ch lorine bl each nor a nonchlorine bleach can be used ~,,~.~”·E·A· •
heir available chlorlne. This term is used to compare th e effectiveness of bleaching ~gents
:itch elemental chlorine, which has 100% a\·aibb le chlorine. A bleaching agent hav1~g_an
JiJilable ch lorine value of 99.2 % has th e same bleaching power as a solution contammg
99.2% chlorine by mass. .
be twe en its :1ctive ingredi ent and an acid; for instance, th e a\’ailable chlorine in a bleaching
ai;e nt containing calcium hypochlorite is determin ed by subjecting the agent to a reaction
111th hrdrochlori c :icid. Chlorine is produced as follo ws:
fJIClu lll h}[XXhl Onle ll }droc hlonc 11rnl C11lc1u1n chlumk Ch lon ne
then determin ed.
a1a11J ble co mmercia ll y as aqu eous solu tions. When they arc. he:1tcd, metallic hr pochlo-
mes decompose to produce oxygen. For instance, th e thermal decomposition of calcium
h)poch lornc is represented as follow s:
reactio ns and co ntributes to the degree of fire hazard.
So lid sodium hypochlorire is an uns1able compo und, but its aqueous so lutions are suffi –
cient! )· stable when their contact with light is averted. Even 1he solutions of 1he metall ic
h) pochlori tes decompose when exposed IO th e ultrav iolet radiation in sunlight.
and a, components of other household laundry products. A well-known example is th e
hou sehold bleaching ag ent known as Clorox. an aqueous solution of sodium hyp ochlorite
hJi’ing 5. 7% avai lab le chlorine.
commerciall y. The solution kn own commercia ll y as Multi-cbfor is a sodium hypoc hl o ri te
Any metallic hypochlo•
rite or other ch lori ne –
conta ining substa nce
used as a bleaching
agent during the
laundering offabrKs
• The amount of free
chlor ine that a sub-
stance yields when
treated w ith an acid
1
I
wate r
Water
Brine
tank
water
FIG URE 1 1 .3 Tht’ process by w h,ch sodium hypochlor,te m ay be electro lyt,call y proc:!uced on-s,te from a bnrie {sodium chlonde) soll/llQrl
The Cllld,zer ,s I.ISed by hO”lP•tal pe~onn l.’I to d s,n fect su rfaces and equ•pm ent contam ,nated w ,tri m1crob ,al pathogens It may alsobtl.l5ed lll
co ntrol a!gae grOW-J1 1n ldrge bcd,es ol stand ing water
hypochJorite
{ HTH) • A commernal
oxidizer composed of a
meta lli c hypoch lorite
rreatme nt of water s upplies, sewage effluents, and the wate r in swi mming pools, spas,an,S
hot mb s. It is al so used to sanitize equipme nt and surfaces on dairy forms and P<>Wtrf
planes , food-processing planes, breweries, and beverage planes.
eous chlo rine mro an aqueous solu tion of sodium hydroxide. A mixture of sodium hrpo-
chlorite and sod rum chloride was produced.
wuh water ro produce its household product. The new process eliminates the risks mori·
ated with stori ng, transporting, and using elemental chlorine (Section 7.3 ).
in Figure 11.3, for example, it is prepared by electrolyzing a portable brine so lu tion.
S<.1J1umchlunJ.: So.:! 11nnh~po.. hlon tc· l l)dn:•gcn
Calci um hypochlome is commonly us ed for ];arge-sca le bleaching o perations, sanicizir4
municipal drinking water, disinfecting domestic and municipal swimming pools, and SC\11′
tre-atmenr. The commercial gra des of calciu m hypochlorite are avaibble a s unique subscJnr;l5,
solutions, and other mixtures with drying agenis and o th er additi\’es. It is frcquentlycnciut’
tered in products known commercia ll y by che rrade name high-test hypochlorite, or HTl’l,
rure of calcium hypochlorire and calcium ch loride is produced.
Cat.1um h) J ro”Je Clilonnc CJluurn l!)pv..hk•nl( C.1l,111m ,hlorulc \\’lier
precipitate as th e solid.
ihrin to burn with an increased intensity a nd to generate a signifi cant \’o lu me of gaseous
products. This is 1llu sirated by rhe test result ~hown in Figure 1 1.4.
\’fhrn shippe rs offer a metallic hypoch lorite for transportation, DOT requires them to iden-
ri~· thr appropriate !’tubs tance as shown in Table 11.7 on an accompanymg shipping paper.
DOT also requires shi ppe rs and carriers to co mply wit h a!\ applicable la beli ng, marking, and
pbcJrd ing reqtnremenrs.
,\l usIraIes I he enhance d
rate at v,h ,ct> cellulose
powderburnswrien ,I ,s
m,xedw1thh1gh-strer1gtt”I
ca lc,um hypochlori te
{7 26%ava ,l ablect11orine
and56%wate1) l 81fJN·
m,won, fhf;i/>elh8
F,n.i , Rt’DO’t. o~>d•ll!·’ C1Jssd,-
r,111on Rese.irr:.n Pro~r resu
;indCr,rer,.i. Fo1e ProleCTO’I
;i~,r;r,F-oundilt/Ofl Qv,rcy,
MA No~ber 7009 )
METALLIC HYP.:.OC.:.H::.LO:cR.:.IT.:.E ___ _ _ _____ I :_:SH:::._IPPING DESCRIPTION
81111.1m liypochlorl te (con ta ins more than 22% avail able (hlorine) UN2741, Barium hypochlori t e, 5. 1, (6 .1), PG U (Po lson)
lcontaim more than 39 ~1 availab le chlorine (8.8% ava,lable
oxygen))
hydfite
more than 39 % ava il abl e chlori ne)
U lci1.im hypoc h lorite mixtur es dry (contains more than 10% but
not more tha n 39% avai lable~hlor1ne)
UN2880. Ca lci um hypochlori te, hydrated, 5 .1, PG II
• ._
,d,::-niified gene n cJll }’ m i hc Ha z.irdo us l\hr en.ll s Table 3S ” UN 179 1. H)’~
~fnsl!,
chlome ), 8 , PG 11. – or -uN I 79 1. t-l ypochlorHc so lut ions _(con r:1i ns sod nun hyP<>c fPr>.
nrc ). 8, PG Ill . – Shippers mu sr include th e n:1me of th e sp ec1f1 c compou nd s pa remh bJo.
m tht’ proper shipping nam e. Fo r exampl e, \_,-hl:·_n s h1pp t’rs ~ffc r zmc hypochJo~
1rJnsportJt1on, th ey enter th e followmg s h1 pp1~g d_escnp11o n o n_ a s hi pping p~ or
-u:-.J 179 1. J-l ypoc hl o rnes, inorg:1 n1c, n.o. s. (con ta in s zin c h ypoc hl ori tc ), 8, PG u.~ Pf!”
ACIDS A ND TH EIR SALTS
products. 1r h:1s been largely repl3cl”d Ill mod em prod~cts w1~h certa m _ch lorina ted dem,.
t1ves of isocyanunc acid . T hese compo und s mclude d1chl o ro1socya nunc :icid :ind tnchb.
ro1socyanunc acid . The molecul.1r srructures of the se compounds are relatively complex,
I
I \ I \
I
\ I \ I
C C
O 0
Di- :1nd mchloro1 socy anu n c acid s are w hi1e tabl e1s or powders havi ng an ava!Ublt
their sodium :1n d potassi um sa l1 s. These compo und s a rc typical ly encountered in 50-poun.:I
(ll.7 -kg ) pai ls o r buc kets.
A CID S AND THE IR SA LTS
sw immin g pools. Fo r thi s purpose, th ese compound s arc usually rcforred to as d,cl,/o,ind
trichlor, respectivel y. 0 1- and rr ichloro1 socyan11n c acid s a nd th eir sa h s rel ease their chlorut
slm, Ir in to swimnung poo l wa tl:’ r. They have much longe r li fes pans when dissolved in water
1han either free chlorine or th e metalli c hypoc hloriies, a ll of w hich rapidl y dccompose 1\.-hrn
exposed ro rh e ultr:iviolct rad ia u on in s unlig ht. Thus, di – and tri chloroi socya nuric aodsand
th ei r salr s a rc considered more desirable fo r th e purpo se of c hlorination, es prci.illy in areas
\\he re sw imming poo ls are exposed to inie nse s unli g ht fo r t’X lended periods.
genrs :ind ~ther di sh washing compo un ds, scouring p O\\ ders, and bactericides. They 1\3\·calso
been med tor rh e punficanon of drm king water a nd rhe non shrink ing trea tment of wool
ACIDS AND THEIR SA LTS
Ta bl e 11 .8 on an :iccompanr in g s hippin g paper. DOT .:dso requil’d
UN2465, Oichloro,iocyaf’lur ic ad d ~alts, dry. 5 1, PG II
3
Al hou gh chemists recogn ize rhr ee oxides of chlorine, on lr one is commercia ll y ~mpor-
• 1 • chlorin e dioxide. At room 1cm perature, thi s sub srance is a red -ye llow gas h a \’lllS th e
~~1;::U,:11 fo rmu la Cl01 • h is a h ig hl y unstab le s ub stance , dec ompos ing inro its elements at
3n ex pl osi\’ t rJ. te.
rhfied ge nerator in Figu re 11 .5, it is produced in a two -step process, each of w h ich is
ron duc ied under vacuum conditi o ns. In 1he fi rst step, so dium hypoc h\orit e is reacted with
h) drochlork acid to genera te ch lo rine.
<;o<1,11mclll;m..k
the gtnera tion of th e chlorine d iox id e.
w,J, 11 111, hh•nl c Chlonn,· Chl,,nncd”‘ ‘”k <;,...,1,umchlt>nJ.:
JS rl,/o r111e d1ox1de h ydrate. In commerce, this so lution is froze n before II is shipped 10 a
dio1<.i de
;c ;,r-ia~c. two ,n dependeni chem ical 1eactIom work In 1.m,son to genera te the gas Although ,ts p nm ary use ,s
,
1
~~a oa~r Pul p, m mo::1ern tim es . ch lorine d,o;,;.,d e freque nt ly nas been selected over otner m ,c100LOOes to
dio• lde
I
nic dev ices in tentiona lly
des igned for th e pur –
pO!>e of pro duci ng a vis-
ib le or audtble eff ect by
me ans o f combu n ion,
ex p lo si on, deftagra t 1o n.
or deto nat ion react ions
As wic h chlo_nnc it sel f, the prin cipal risk associated w11h expo sure to chlorine d
d :11na se. ry and ‘Tt
C h lo rine d1ox1de a nd cle-mem a l c hl o nn e gtncrall y are used for the same p
co mpari son, how~ v: r~ chlo nne dm x1d~ is approx im:uely 2 ~2 11_mes more po~~::s. By
chlo rin e as a n ox1dmn g agent. For thi s rea son, chlonne d1ox1dc is sometim I 1~
o ver ~hl o ~i nc_ fo~ blt·achin g pape r pulp and producin g white wh i:- a t flou r, cv:~ ~h’Cttd
chlorine d1ox1dc 1s mor e cos tl y. OIICh
di sinfe~ I wat ~r in th e dair y. be ve rage , and oth er food i~dus1r ies. At wa:,r. ;:,a t IO
pl a nts, n s use 1s g~ ni:-rall y s upplem em_ary to the use of chlo ri ne fo r killing bacteria Bttall\tJtt
11 is capable of killing Cryptosporu/mm partm m, the use of chlorim· dioxide to ,disin::
dr in ki ng water compares favorabl y w uh o zone.
at e Office Building, EPA contractors chose chlonne diox ide to ~cstroy the anthra x. n.;
m.:111 pac k:t ges and Sena1e offices were decontaminated by discharging th e gas into lhca
sphere of seale~ -o ~f area s, where i_t ~emamed f?~ seve ra l h~urs _be~ore ncu1ralization.~
ha rd surfaces wnhm the Senate bu1ldmg were d1smfected using l1qu1d chlorine dioxick
id c w as also used to erad1 ca1 c the mold that gr ew in homes that had been inu ndJtcd 11,tlt
war er. It ha s al so been used rn control the infcs ra1ion of the pipe-clogging, 1h um bna~-
sized quagga mussel in wa terwa ys .
DOT a ll o ws chlorine d io xide to be mm s po n ed onl y w hen i1 is fro ze n as its h>drair.
When shippe rs offer the fro zen hyd ra te for tran s portatio n, DOT require s them to nmn•
tai n th e gas in 1he so lid scare using dry ic e or other mea ns and to ide nt ify th e gas 0111n
acco mpan yi ng shipping paper as follo ws:
and p lacarding requi rem ent s.
OTHER PYROTECHNICS
du ci ng aud ibl e and vi si b le pyr0technic effect s by co mbustion, explosion, deflagra tion,01′
deionauon reactio ns. Some famil iar examp les include fi recrac ke rs, Roman candles, pill”
w hee ls, fla res. serpent s, s par kl ers, skyroc kets, and to y tor pedoes. Spccia l- effee1s firc” orks
include com ets, fou nt a ins, strobe s, and kaleidoscope she ll s. To ch o reogra ph an aerial fut-
wo rk s prog ram, modern profess ionals use compu1e rs, flame generators, and firing s)1·
te~ s ihat. actuat e a set o f redox reactions , each of w h ic h is precisely tim ed to prornlt
lav is h ae nal sc ene s s uch a s chrysant hem um s hell s. In a modern program, li ghting consoles
sy nc hron ized ~vith th e act ivation of the se reaction s are int egra ted inr o 1he pcrfo rm:i_ncr,
. In th e Unued Sta tes, the GI-IS sys tem (Sec 1ion 1.9 ) is u se d for th e classificauon ol
merly call ed s pec ia l firc\v o rk s and com mon fireworks, re s pectivel y) . ·· I.JG” and “1.4G
JfC’ :,;n 15.4 – B). Fireworks 1 .3G,_ or specla_l fireworks , a_re rclati~·cly la rge fir ework
15~ de-signed for use b y profcss1onall y tramed expert s. Fireworks 1.4G, or consumer
dc11’es ks are relauvcly sma ll firework dev ice s designed prim ari ly as cons um er products
fifew or b}: th e ge nera l public. The GHS sy mbo ls pertaining 10 fi reworks in both h:nard
fo r use are provid ed in the marginal a rt, but 1hc hazard diamond mforma1 ion is noc noted
c\J•;e:hey va ry according to their chemica l com po sit ion .
,ince,\I l6 C.F.R. S 1500.1 7, CPSC -~as ban~cd 1he use of cer1ain firework s devices intcn ~cd
::~~fociure, and sal e of cherry bombs, a rype of fi reworks physica ll y resembling red chc r-
ot5 with green stems. _Cherry bombs were_ acti vated by ,gmting fuses t1hc gree n ste ms) ch~t
co ntacted a pyrotechnic mixture of potassium perc hlorate and metallic alumin um . The ac n –
iau on of this mixture caused i_he loss of hundreds of eyes and fingers each year; hence, C PSC
,nsumted an outright ban agamst the sa le and~ of ch~rry bombs i_n the Uni_tcd States.
tai ners of ccrrnin consu mer fireworks. Although th ere are far 100 man y t)’ pC$ a nd s1a 1e-
rnent> t0 list here. they may be accessed at 16 C.F.R. S \ S00._14 (b )l 7) .
fir eworks , displ il Y f i r e-
works) • Relat ively
largef1rewo r k dev i ces
desi gned pr i marily for
d i splay by professi onal
uperts
firewori<.s. cons um er
fi reworks)• Relatively
small firework devices
d~igned primarily for
use as consumer prod -
uru by the general
public
unau ihonzed individuals, incidents involving 1he misuse of fireworks annuall y ca use num er-
ous $CCOndaT)’ fi res, bli ndness, deafness, the mutilation of fi ngers, and death. In most sta tes,
reduce or eliminate the likel ihood of 1hesc incidents, only a licensed re1ail ou tl et that posts
ino den1s caused by th ei r mi suse, state and loca l laws rigidly require 1hat common fi rewo rks
\'( actua ted on ly tn acco rdance wit h the manufacrurer’s wa rn ings and instruc1ions. Display
fi rc-11o rks must be actuated by trained experts only. Even und er 1he best of cond it ion s, the
3cruauon of all fireworks ofte n consti tut es a risk of fi re and explosion.
3nd a reducing agent, The most co mmonl y encountered oxi dizers arc sodi um chl ori te ,
sodium chlorate, and sod ium perch lo ra1e, all of which arc a lso co mpon ent s of veh ic ular
m bai;s, solid rocke t fue ls, and certain fenilizer s. Sodi um perchlorate is the oxid izing
Jge m of cho ice fo r most p yrotech nic displays, and charcoal, sulfu r, pulverized magne-
sium, and aluminum flakes arc t he reduci ng agen1s. To pro\’ide co lo r w h en fireworks are
actu:i trd, one o r more meta llic com po unds a rc added 10 firewo rk s formu\a1ion s.
ox}gcn when th ey arc h eated.
So
‘ioJ 1um 1i.:rchl or:11c ‘il)lhumchl onJc O,;grn
rtdox rcarnons arc responsible for the brilliant lighting and sound effects associa ted with f1 re-
11 0rks displa ys . Whe n 1hc mixture of an oxidizer, charcoal , sulfur. and finely divided magne –
iium or alu rmnum is acti va ted, th e resulting redox reactions occur at explosiv e rat es. The
P~est nc e o f m;i_gnes ium powder enhances the brilliance of a fireworks di splay, wherea.s the
1 diuon of CO.’\rsc aluminum flakes produces lum inous ta.ils. The sc1s of equati o ns in Ta hle
11 ·9 illustrate some of lhe redox reactions associated with 1he actuation of 1he rcacti\’e m ixt ure .
pound s vapori ze or decompose. T h ese compounds are almos t exclusivel y m eta llic
I I
OXIDI ZING
AGENT
pe rch lorate
AGENT
1 Aluminum
Caroon Sod um{hlor If Soa-1,mchlor,de C••bond’°l.Of
Su•fur Sodlum(hlor,te SOd,um
Md<)n p11vm $()(1,um 1h'or,1e r.Ja.ine11um o.,d, Sod~,, Olb-di
Alum,m,m Sodumchlo,.!e Alumlf\u’TlOl idf S
ca1bM SOClumchlorate Sod -umchlo,,de C•rbond>Ollat
Sulfur Sod,umch lor.itt SOd,umchlono, S!l’furdOMld!
M•gr,t\,um Sod,um u,iorite M.ign,1,um o• lde So.:lnifl’Hl’tlor,d!
Alum,num Sod,umchlora te Alum,oumo •1de l,odiull’ltl’IQ
Carbon Sod1um~,chlo,a1, Sod umchlor11:lt Orbon(l,01Jdt
Sulfur >odumpe,ct,lorau Sod•umchlo11(1e Sulh.rrd,olldt
Magne1•um SOC11um p,rchlo •.ite M agne1,um o• •de So(l,u'” clllordt
Aluminum Sod,~m ~rthlorate Atum,f\1/m o, lde Sodl
colo rs they exhibi t on va porizati on are noted here:
Li th iu m chlo ride crimson red Ca lci um chloride orange red
Potassiu m chl oride lavender Sodium chloride go lden yell ow
Str onti um chloride ca rm ine red
uve substances in fi rewo rks was the active 1:x plosive in the pr1:ssure-cooker bombs u.td
dunng the 2013 Bos ton Marath on cerror is t :mac k.
When sh1pp ~rs offer fi reworks for transpomitio n, DOT requi res th em to d1:scribe cht firt”
;•orks genmcally as shown in Table 11.1 0 on a shipp ing pap rr. DOT re quires shippers!O
incl ude the app licable EX •num br r (d1:sign:i 1cd here as EX-xxxx.x), Department of~
~ ~isi on .!..:_1 _ I UN03B, Fireworks, 1 I G, PG II (EX-,c.~ _
f!!.
~ d ivisio n \ 2~ _____ U_ N_OB4. Firewo rks, I 2G. PG II (EX •xl()()O() __
::woru. d,v1s, on 1 4 ~;0336. Firework s, 1 4G , PG II (EX.-x)()()(x)
· don. The naiu re of these latter req uirt’mems 1s di sc ussrd in Sect1on 15.4-C. .
d )Jcarding requ irem1: nr s. h al so req uires carrir rs m bloc k and brace packa ging con·
rxpasu re to ignition sources. . .
ihw pacbgin g mu st iden tify th e app ropri ate EX -number, EXPLOS IVE labe~, pr? per
shi pping nam1:, UN idr nrification number, and UN pac kaging specifica uon ma rk in g. Eac h
of ,he)( DOT req uirements is illustrated in the exa mplt: shown in Fig ure 11 .6.
1.oc3! or dina nct’s reg ulatr how fireworks are dis pl ay1:d. Rega rdl ess of their natu re, fi re·
11 orks shou ld never be actuated when climatic cond itions are dangerously dry or when
the 1nnd spt t:d exceeds 30 mi/hr (48 km/h r).
1t requi res the m !O co mpl y wit h al least 1he fo ll owing/
• Professionals who pubhcly display fi reworks must be experienced, res ponsible, and bonded.
1 fo r bo th land and watr r di spl ays, professionals ma)’ act uat e aeri al shell dis pla ys out –
11on pom t an d th e spectators.
or shipping paper )
49C .F.R. \172 .320
49C .FR §172406
General Mark ing UN Pack;igmg Speci fica1, on
Require ments172 .J0 1, Ma rk, no 173.22 l al & 178 .503
1
; ·; .~! ~ll7i.J 0
, UN ID. Numbe r 49 C. 1′” R. § 172 30 Ha )
a91ngfo r t1anipon ,ng
fireworks 1s a f ,berboard
OOJ;thathasbeenprop-
erlyma rke da ndlabe led
fortransportallon Due to
space constramts the
nam es o f the shipper and
receiver are not noted
IR.>QularcwyGulOo.”bneslor
511.pp,ngM!dlta,uponmg
frre,.,,o’l:S l’,’45/’lxlgrM , DC
USDtp,l r1 mentofTr,;;nspo1-
ra1,onJ,JOIJI
METALLI C CHlORITE , CHLORATE ,
OR PERCHLORATE SH IPPI NG DESCRIPTI ON
UN1447,B ariumperchlo rate, 5 1,(6 1). ~
UN1452, Calc lumch(~l. PG~
UN14S5, Calc1umperchlorate, S l ~
Ban umperchlorate
Ca lc1umchlorate
Ca lcium ch lor ,te
Ca /ciump@rc hl ora t e
Magnes,umchlorate
Magnesium perchlorate
Potarnumchlorate
Potu11 um perch lorate
Sod ,um cnlorate
Sod1umchlor1 t e
Sod iumperchlora~
Z,ncch lorate
~ 75. Magnesiu m pe rchlo rat ~
UN1489, Po tas s,umperchlor ate, so lid, S. 1, PG u
UN1 495, Sod ,um chl orat e,_ s_. l,_PG_ 1_1 __ _
UN1 4915, Sod ium ch!or 1t e, S 1, PG 11
UNISOl , Sodium pe rchlorat l!’, S~l ,_PG_ I_I __ _
UN1513. z,ncchlora t e, S 1, PG /I
CHLORATES, AND PERCHLORATES
sh ip p e rs offe r th ese in d ivid ua l co m p o u n ds fo r tra nsp o rt a u o n, DOT requ ires tht m ro
provi d e th e r cleva m s h ipp ing desrnp tion o n a n acco mpan yi ng sh ipp ing paper. Somt
exa m ples for severa l represent at ive m etal lic ch lo rn cs, c hl o rar es , a nd perch/orates arr
Ii seed in Tab le 11 . 11 . Wh en me ta ll ic ch lornes. chlo rac es , a nd pe rch lora tes a re not sp«ifi•
ca ll y lis ced a t 4 9 C.F. R. SI 72 . 10 1, DOT requires rh ei r sh ipp er s to prov ide a generic s/up,
p ing desc r ip tio n o n sh ipping p ;1 per s a nd n ame rh e speci fic co mpo u nd pa rentheriaUy. 11
a lso requ ires shippe rs ;1nd ca rrier s to com pl y wit h all a pphcabl e la bel ing , ma rk ing,JnJ
p lacard in g requir ements.
METALLIC PERCHLORATES
r are ions has bee n p u blicly \’Oice d, p J rt1cu!arly because perc hlo ra te ha s been idenci/itdlll
the wa te r su ppl ies o f 35 sta res. This wi desprea d g ro und wate r co n c:i min a tion isassociJtd
wi rh th e fo r me r mi lita ry use of me ta lli c pe rc hl ora ce s as roc ke r fu els. Today, rh est COOi’
pounds have been r epl aced in fi rewo r ks a nd roa ds ide fl a r rs w ith compo u nd s rhar ~ft’
fr iend ly ro pu blic hea lrh an d rhe enviro nm ent .
the consumpt io n o f p r rchlo rare-co m a min ;11cd wat e r and dama ge ro th e thyroid gbod.
neu ro logica l p roblem s, and th e in ability of hum a ns to p rope r ly p ro duce gro wth ·
fe cal-d eve lopmen ta l hormones. 3 Perc hlo ra te polluti o n pOf e n ria ll y affects 1he heahho
1WJ~hmg1on, DC: Nmon~I Audem,ell Press, 1005 ).
t hlorate pre1•c n ts 1hc propc.- r p rodu ct io n of 1hr hormones nee d ed fo r d c1•clop in g
~~’56 In 1005, EPA set a d a rl~• dose o f pc rc hlowe rh a1 pt.”op!r ca n s;ifc ly ingest a t 0.7
i;l1 of body werg h t.
‘\eiJdJ , tll’O r.t.1tes m wh ic h perch~o ra te pollu t 10 11 rs es peciall y p ronounced. O w mg to
· ubhc pressu re, a ddmon a l i’.1forma t1 o n on rh r hea lth eff« ts rcl J n ng to perchlora te e xpo ·
:ute ,s iikel)’ ro he fo rthco ming .
SMOKES, AND SMOKE BOMBS
mreof an oxi J1 zi ng age nt a nd rr duc1ng ?ge nt . Th ry a rc usrd by ci\’il i.1n poli ce an d the .m 1l1 –
:u,iti rs dur ing local assa ult opr ra t1 on s. Wh en thrr arr used by the m1 l1rary, th ese d evices
;i re he lpful in locat ing frir ndl y unit s as well as e nem y ta rge1s :i nd cont ro ll ing the la yi ng a nd
bhingofJ rt1lle ry.
ronJt10 rl ,1cci d r nt or mec han ica l fa ilure, a nd cont ro l traffic du r in g n ig httime ho u rs. Fo r
th~ purposes, 1he flares a re composrd of a mi xture of stront ium nit r;ltt’ , sulfu r, pota ssi um
p(rch/orJtC, a nd s:i wdu st, the co mbma t10 11 o f w hic h 1s tn ‘.>C’rted in to cardboJrd tu bes. Whe n
rht)’ art· ign11 ed , the sa wdu st burn s a t th e approxi mJt e ra ce of I in J mi11 . Th e red ox reaction
prod uces an 111 1e nscly ca rmme-red glo w. Th e chenuca l rra rn o n is re prcsc.-nr ed as fo llows:
co ntal ningapyrot ec h-
mc su bstan ced l!’s•gnl!d
t o lllum,na tl!, /d@n t 1fy,
sign al, or wa rn
typ, of smo ke bomb
w hose actuat ion co m –
mun icates p rearranged
,nfor matlon to troops
orothe rs whos ubse-
quent!yobserv@t he
sig nal from a dlsta n<
de vice conta in ing sub ·
stances that produce
smoke wh en actuated ,
g,ner all yforus, ln
concea ling m ili tary
oo ns ro com m u ni ca te di st ress wh en a m m a mes. The U.S. Coas t Guard regul a t es the
feJturcs of se1·era l ty pes, including the handh eld, rt’d fl a re: fl o a ti ng o r:ingc-s rn o kc fl a re,
rmul -prowc red pa rac h u te red fla rr; se lf-con tai ned , roc ket•pro pcllrd para c hut e, red fla re :
handhrl d o ra nge sign ali ng smo ke; fl o ating oran ge signalin g s mo ke, ;1nd red a erial p yro·
1echn1c fl are. 1\ desc rip tion of r ac h d e\•ice is p ro vi d ed ar 46 C. F.R . Pa rr 160. Each is c om –
posed of a urnqu e mi x tu r e of subst ance s.
SIGNALING SMOKE S, AND SMOKE BOMBS
bombs ofte n co nt3in so di u m b ica rbon ,u e a nd a n o rgan ic d )’e. M ose co mm o n ly, 1he o xi-
dlllng an d redu ci ng agents are potass ium chlora te and ele me nt a l su lfu r, respectiv el y. The
mJxture of co mpo nent s is comp ressed into ca rtrid ges, ha nd gr enades , a nd cani ster s.
by ignmon, at !eas t t wo ch e mic a l reacuons occ ur:
1 The oxidat 1o n- rcd uct10 11 react ion betwee n po ta smim chl o ra te a nd s u lfur
Pu1J,”umrhk,rn1,· Sul fur l’o!J-.,u m,h k•nJ~ SuUurd,u , 11!.
-;,..,J,Jm t,a.ut,,.,n.11~ ~. ,J,u111 ,JrNJ!lJ!( Curto,,n J1>•\IJ~ 11 31_,
rrnl1t:1ry oprr:m ons. An ;ators rouu nd y c;irry flares m th eir fli ght SUHS or 011 I f 11.
deco ys ro thwa rr he:11 -seck ing mi ssi le s. \'( hen they an· :1eruatcd, th ese flares emit I.I
infrared signal that mimics the heat d1 sc h.1rged by a n :urcraft rngin c. When it fl.a
e1rcted from th e :urcr::ift, 1hc nms de rravd s towards 11 rather than t he ai rcra ft. rt 11
, chi cles dur ing combJ 1 ac t1 v1t1es. A po pular smo ke bomb USt’d by tht’ U.S. Arm d nd
t he Ko rea n co nflic t wa s a pyro tec hni c m ix ture co mam ing 6.7% g ranula tl!’d al : rni:~
4 6.7 % zmc oxi de, and 46.7% (C~ H~, o r CCl3-CCl 1) hexach lor~ thane by rnau.
rh e co mponC’ nts of thi s nmo urc werC’ acru at r d with 3 fu se , th e products th.1t appearr,J
ih e s moke were a lu min um ox ide, zinc c hl o ndC”, and ca rbon (soo t) . 11
,\lummu,n HcuchloJroclhJac lonco,,J,• 7Jnc , hl,mdc A/ u11u numo,..i., Carbal
refl ectC”d light , and th e carbon co lored th e smok e cl oud gray.
AND SMOKE BOMBS
requires them ro idenrify rhe appropnatr it em generica ll y as show n m Tab le I l.l l . DOT
al so rr qu in: s shippe rs and carri e rs to comp ly with alt applicab le labelmg, mar king, and
pl aca rding reqmrr ment s.
AMMONIUM COMPOUNDS
an d a negativ e io n . . \fosr :1re th e rmall y unstabl e. When rher a rc heated, :i mmonium com·
pounds decom pose m eith er of the foll o wing ways:
inirfa ll y ma de. For instance, when ammo nium chl o ride is heat ed, it the rmally dmim-
poses to fo rm ammon ia and hyd rogen ch lo r ide .
Arnrnomu111chlonJc Ammo n,J l l ) Jn;,i;,·nc hl on Je
regard ed as ha zard o us nwe ria ls. of
Am mo nium compo und s ma r a lso decompose by o x idati o n-redu ct io n, Examples
a m mon ium co mpounds that decompose m this manner are illu strated by the eqlll·
1ions in Ta ble 11. 13. T he rna1ority o ( them decompose at ex pl os ive rares when hea rrd.
For th is reaso n, DOT proh ibns the ir tran sporra11on by an y mode. Exarnplrs of 1hesr
and Smoke Bombs
UN0420. Flar es. aen al , 1 lG. PG II
~ none,p los1ve), w ,thcorros,ve ‘ UN2028, Bomb1, 1moke. nonup/01ive. 8, PG 11
1 ”
ra te, ammonium fulminate, ammonium mtr i1e, and ammon ium permanganate.
S«Juse few compound s conta ining the ammonium ion arr th e rm a ll y st:i ble, th e indu s-
tnJI um of the se co mpound s are foi rl y limn ed. Ammonium rmra t e is by for th e mo st
imponam compo und co n1a111ing the ammonium ion. In Sectio n 11 , 12, we obsen’e 1ha1 it
112n important commr rcia l femhu r a nd explosive component.
•mo unts m th e Un ited States. 11 accou nts for 70 % of th e sol id propellants used by the
mospacc mdu s1ry 10 propel space sh uul es. T he ammon ium perc hlo ra te is mix ed with a
fud lrkc powdered a lum in um and a binder. When igm ted, a n oxida tion-rcducuon rt”ac •
hon occurs t hat ge nerates sufficie nt ga s 10 propel the shun le imo o ut er sp:1ce.
\t1hen amm o ni um co mpou nd s are 1ra nspo md , DOT req uires shippers 10 provid e th e rel –
ri·ant 1h1pp ing de scr ip t ion shown in Tabl e 11. 14 on a n accompanying shipping paper.
AMMON IU M COMPOUND EQUATION llLUSTRATIN G THERMAL DECOMPOSITION
Am ,., on um b•O'”‘alt ,,. ..,,.,0<1,um t;i,om ,clt O')' g en
Ar-mon ,um tnl011te Arimo~””‘ c~Jor.de Orygeri
~..,on,um cHt,rorr>•t e (hrom 1,m ( I/ o•,cle I\ 1,09en Wn,,
– – —– —– — —–
Ammon ium permanganat e• lNH,MnO.Cs) – 2Mn0 {1) N;(g) • 01(9) 4H10(g)
A.'”lmon,~'”l Pt”O•~a ,su tl~T~ Ammo.,,a N,trogen Ox;g en Sulfuri:t.o…oe W,re,-
“Also ri,mt-d ammon iym perJu lfate
AMMONIUM COMPOUND
____ uN_10_71, Ammon ium nhra te based fertlliztr, 9, PG III
Ammon ium nitrat e su1pens ion , UNJ375, Ammon iu m nit rate suspension. 5.1, PG N
Ammonium nitrat e gel (int ermed iate for blast ing eJrplos 1ves) UN3375, Ammonium nitrate gel, 5. 1, PG II
nitraieandfvel o il) (fX-.1ooooc:)
Ammon ium nitrate (conta ins more I.Man o.i •i. combustible substances ) UN0222, Ammonium nitrate, 1 1 D, PG II (EX·~
Ammoniu m perchlorate UN0402, Ammon ium perchlorate, 1 ID, PG U (EX·xo:o.1
UN1444, Ammonium persulfate, 5.1, PG Ill
~ p].K.irdingreq u1rcm r n1 s.
. :unrno111um nHrJte 1s the most co mm r rc1a tl y 1m por1:1 nr chrm1c:1 I prod uct co nta in ·
in!r~J~ns a fert1l1zu, dy11ami1r, nitro us oxide, and techn ica l grade, all o( which a re av~ il –
1;1tconune rc1,1!l y as cr)’stals, tl akes,gram s, and pn ll s (s mall, bead-like pe-llrts ). Thr ch.1r•
;,rwsocs of th ese gradrs :are bridl y noted next.
mbunon centr rs. fr ml1 ze r-gr:1de ammo ni um nmat r is a formulation of ammonium
mtrJ ft” with ammoni um sulfat e or ca lcium ca rbonau, l’ach of which reduces the
portn nal risk of m self-drcomposition. As its na me imphrs, it 1s imrnded fo r use as
Jn Jgricu ltur.il fertilizer. It is co mmon ly so ld m 50-pound (23•kg ) bags.
O)n ami te-gradr ammonium nitrate is wide ly used during road construction a.nd
b!Jstms opera nons 111 rnmes and quarries, wherl’ it is th e ncrive componl’nt of blasnng
Jgtnrs. his also a compontnt of uniqur ex plosivl”s hk r am mona l, a mixture o( am mo·
mum mtra lt’ :1.n d powdered a lum in um . Ammonium nitrat e ha s also bren co mbmed
wuh n.rr ma bursting charge use d in demo lition bombs. Ir is also 3\’a1/abl r com·
mcw all )’ mixed with d il”sel fuel, ca ltr d :ammonium mt ra tdfuel o il mixture, o r AN FO .
Th e prcsencr o( th e die sel ml mak es AN FO easier to deto na te th:1 n a mmomum mtrate
Jlone. Although H ca n br safely handl td and transponrd, ANFO dr tonat rs wit h a
powerful force whr n it is ig nite d. A!\’ FO ha s been mis use d m acts of trrroris m to
ausr c.11 :1stroph1 c dnmage ro human health, safr ry, and nat io nal sec urit )’.
\ “1 rrous ox id e-g rade arnmomum nitrat e is ustd to prod uce drn itrogrn ox1d r, or
rn rrou s oxr dc, by gen llr hea ring. It 1s know n commonl y as laugh mg gas. an anes thet ic
used n1J1nl y by dent ists 10 lessen th e anxiety rx perie ncr d by some patients.
,\mmom11m111ia1r \\ Jt~ •
l:i a component of cold packs used for 1reatmg minor athl r tic in1ur1 rs. Beca use the
d1sso ll’lllg of ammo nium nitrate in wate r is an endmht rm 1c procrss, the solution is
co ld wh en fim produced a nd pro vides reli c( fro m pain wh en a pplied to bruises.
Ammoni um nitrat e melts at 337°F (l 70 °C) and decomposes brtween 350 and 4 l0°F ( 177
~nd 210°C). Whrn a bulk quant ity of ammoni um nitrate is presrn t at a fi re scr nr, it may
undergo tht’rn1al decomposi ti o n ar :111 rx:p!osh·e rate. The dec om po si tion producrs an
Jrra)’ uf products includin g thosr illusrratrd by thr followmg two eq uat io ns:
f When rhe ga ses produced by 1he dccompostt ion of ammonium nitrate a re venrrd
rorn the fire scene, rh e threat of explosi ve dl”com posirion is redu crd o r ehminarrd. How-
oitrat•
oxide
1
I!
2200ronsof I ..
fue l oil
tre h~c,’1~ to tne ‘lO-C’I anc: 3PO ‘I ste.tm t/’1e ‘re co,triwtd to ::M’n. trie ammomut”I rma-” o«xr~ rl:t
rto” m.x,,_re o• nrtrogen. n,irogen d ox;ce or19tt1. ana wa:tr vaoor Tr s oroduct1on of 9_a1.ts a.
$J1hunared oec,:ievlt”!( lf’daroano:–tr 35 00 •.-.ere -i,¥red ihepro;?fftyc:,imagewascomparQ !tJh:
e.Qe r eri~ea Cur ng a rra,or wart -re bQ..-blng ‘1CJcw1t i’lt total orootrty oss was t”S”…ma:ed as S33 f”‘.lo,
c.:lseaon19,<:7costs
Grandcamp, a pomon of whoSt” features a re illustrated in Figure 1 1. 7.
c:iughc fire ” ‘Hh nea rly 2280 rons (2070 [) of fcnilizcr-gr;1de ammo n ium nitmeonhoanl
s rored w1thm PA·o hol ds. The he;1c generated by the fire caused 1he ammonium wtrut 11
mdc and decompo~.
;1pplicat1on of warer. this attempt was nel’er made onboa rd rhe Grandcamp. lnste:ad,
orders were issu ed ro seal the hatches to rhe holds to eliminare rhe air suppl y to thtfin
and pre1·ent damJ ge co the cargo by water. Supporred by oxid izi ng agents, howe,ce:r,~
fire conunut”d m burn m the abst”nce of air. Internal press ur e withm the holds incrcutd
until .i major explosion rdeast”d the confined g.a ~s.
in rn lvmg a chemic.ii subru.n ce. Ir caused the dC’;Jth s of nearl)’ 600 people, including l id
Galves1on’s 28 firefighcers. h sen·es to 11lumate dramaucally t h e potenril ll)’ h.1urdous
nature of oxidizers in gene ral and ammonium niuate in pa rt icu la r.
th e explosion of ammonium niuate ac a fi re scene. In ZOU, 28 w 34 tons (25 103 1 t d
ammonium ruttatt’ exploded at a feniliu r storage and distr ib ution cent er tn West, _TCUS;
Ftfrecn people, including 11 fi refighters, lost their li1·es and Ol’C’r 200 res idents ” ‘ere UJrurtd.
BULK STORAGE OF AMMONIUM NITRATE
mum nitrate ar 29 C.F. R. § 1910.1~9. T~ese regulations a ppl r to fa r mers a~d at~
e mployers w ho ~to.re and use ammonium nitrate m workp laces , as well ~s cht _o11 n~ in
lessee of any bu1ldmg, p remise, or sc rucrure in which th e ammo n ium mtratt 1s sro
q uanrnies of 1000 poun ds (454 kg ) or more.
bJch storage of ammonium nmare 1s in tend ed; the storagt of .i mmonium nnrare m ,on-
u;,:~ul,,ra nce5. \X’e note rach su b1ect arC’;J st-pa ra1el y to appreciate 1he exten t of the pre •
:unon.i th,.u muse be undertaken w pre1·ent mi shaps.
A building ust-d to store ammonium nmate may h..1 \ea basemenr on ly when th e base-
men! has b«n cons tructed so IT 1; ope n on at fa ~t one side.
n,, buil ding used to store amm oni um nmate ts hmHed 10 one story m height.
n,e building u,;ed for the Storage of am monium mt rare must be adequately \C’ntilacrd
or~ of a co nstruct10n that allows self•venula1mg m the e1ent of 3 fire.
n,e “all on the exposed side of an ammomum nmate sto rage bu , ldmg that is wirhm
50 {et” ! (15 m ) of a combmtible building, fo rrst , p iles of combusuble materia ls ,md
sim ilJr exposure haz.uds must be of fire- res1 sm ·e construcn on. In lieu of a fi r r-
resist1\e wall, ot her suuable means of exposure protC”Ct.ion, such ;1s a frtts t and1ng
.,,, 3 JI, ml} be u~d.
,ni; must be of nonco m bus u ble material or p ro1ccted agam st 1mpr egnanon of ammo-
ni um niua1e, and m ust be “ithoU! open d rams , craps. runnels, pllS, or pockets in ro
.,,,h1ch anr mohen ammo nium ni tra te could flow and be confined in the e vent of fir e.
wlrer ‘>C’t”pJge th rough th e roo f, wa lls, a nd floon .
mg a roof fi re are ;n •ai la b le, b ulk sto ra ge suucrures w n hm an ammon iu m nit r ;1 1e stor-
3i;e build mg cann ot exceed a he igh t of 40 feet ( 12 m).
be pr011ded th rou g ho ut J n a mmonium m tra t e sto rage bui lding and in che load in g
~nd unlo.idmg a reJs.
agt bu1ldmg m acco rda nce wi th recog nizt”d good pramces.
• C.Omainers of ammo ni um m trar e can not be accep red fo r sto rage w hen che temper a –
I Bags of ammoni um n m att”ca nnoc be stored wi1hm 30 inches (76 cm ) of , he wall s and
1 ‘.\o more than 2500 ions (21 70 r) o f bagged a mm o mu m ni trate ma y be st ored m an
system .
1 Ammonium nm are ca n no t be accept ed fo r storage in pi les when th e te m pe r:1 m rr of
1 Pi les of ammoniu m n m are o rdin ari ly ca nno t rx,eed 20 fee t (6 m ) in h eigh t, 20 fC’t”t
ing of noncombustible constr uction o r p ro tect ed wit h ::auro ma ri c sprin kle r s, 1hr lengt h
of the pil es is unl imi1ed . Ammon ium n i1r::1te piles c:1 nn ot be stacked cl ose r th an 36
inch es (91 cm ) be low t he roof o r s uppor ting an d sp reader beams.
lm than 3 ferc (0.9 m ) in wi d t h. At le::ast one ser”ice or ma in ai sle m the sto rage ;irca
tlut is no r less tha n 4 fee t (1.2 m ) m width a lso must be pro,·1ded.
(454 kglJ of amnonivm Mme W1th1n a blfl tha t IS dean ard free ol coma m,na’ll5 ‘Nhtn the a’l’l”lOl\.vfl~
1s stored as a p le, ,t mus! be sized 1n a manner th al a’/ ma teri al w1h1n the pil e may be pe nod,ca:t, Mer~ i;
b 1ri must be separated by fa” wdlls from tla mMable and combustible matenais, COHOS/Ve mat@N:s. other ix:fi9t
and substances l’llth wh ,ch th e ammonium cO\Jl d react Employers ma~ no1 store e~plos1Vf’! or blasting ‘9flll3
wn/’l ,n th es.ame bu1ld111 g
comam inauon , ga lvanized iro n, copper, lead, an d zi nc can not be ust’d in the eonsrnr,
tion of a bin unle ss the y are sui tab ly protected . Although a lum inum and woodrn }q
protect ed against im pr egna tion by amm onium mmue are permi ssible, 1he putitiocll
di vi din g the ammonium mt rate storage area from t he s torage of other prod uru dw
could contaminate the ammonium nitrate mu st be o f “tig ht~ co nstructio n, as illus-
tr a ted in Fig ure 11 .8.
Ammonium ni1rate storage b ins and piles must be clearl y marked wnh signs mding
a s fo llows:
The piles of ammomum nitrate mu st be sized and arranged so that all material in the piles
is mm·ed periodically to min irruze caking of rhe ammoni um nitrate during its storagt.
ren den q of rhe pr od uc1; howeve r, in no case can rhe ammonium nitrate bt- piled
high er at any point than 36 inches {91 cm ) be low the roof o r th e suppo rting anil
spr eade r beams overhead.
Dynamite, Ol hr r ex plo sives, a nd bla sti ng agents are prohibited for loosening amroo-
mum nitrare that ha s ca ked.
• ~mmoniu m nitrat r mu st be sto red in a se parat e bu ilding, sepa rated b)’ approred~1~
!e:ast 30 fet’t (9 rn ) from the storage of organic chemicals, acids, or 01her _corroil
m:iterials; mat e rial s 1h :1 t ma y requ ire bla sting dur ing proce ssi ng or ha ndling; ‘°;
p r essed flammable g a ses; and flamm a ble and combustible mater ia ls or 01 ir
bJ kd rags, baled sc rap pape r, bleaching powder, burlap o r cotton b.ig.s, ca usnc w da ,
,o.il, coke.”, charcoal, cork, ca mpho r, exce lsior, fibrrs o f a ny kmd , fis h OLIS, fis h mea l,
foJm rubber, hay, lubricating oil , lmseed oil, o r o ther ox1d1uble or dryin g oi ls, nap h·
thJk ne, oa kum, oiled cl?1h ing, oilrd pJper, mle d textil es. pamr, maw, sawdus t, wood
shJv ings. o r ,•egr1.1ble mis.
Flammable liquid s (s uch as gasoline, krrosenr, so h·rnts. and light fuels ), liquefied
pt’rroleum gJs, sulfur, and fine l)’ di vided metals cannot be sro red o n the sa me prcm •
isrs whne bulk :immonium nitrate 1s stored .
AMMONIUM NIT RAT E FERTILI ZER
,nmi nal mi suse of ammon ium nitrate fe r11h zer that 1s sto red, handled , o r tra nspo r1ed
v,uhin their jurisdictions. Given th e uno rth odox wa ys m whJCh terrorists ma y ob tain a nd
u>(‘ rhe ferti lizer. l.iw enforceme nt :igencies mu s1 be provided with su fficirm info rmat io n
to 3ccou nt for bulk quantities of ammonium nitrate potrnt iallr av:ii lablc to terrori s ts
com panies must notify the Depanmem of Homeland Security when 1hey possess I ton
1o. 91 1) or mor e of agricu ltural material.
bulk quanllllt’S of ammonium nitrate fertilize r at the nation’s pom. At 49 C.F.R. S 176.415
Jnd 33 C.F. R. § 126.28, respecti\’ely, DHS .ind USCG require the owne r o r oper.uor of a
11 :1trrcraf1 loJded with hulk quan1ities of ammonium nitr:it r, o r a watercraft on which
bul k quant ities a re imended to be loaded, to recdve w rin en permissi on from th e Cap tain
of the Po rt before the load ing o r unloading operations occur. The permit stipulates that
iheowne r or operJtor must load or unload the ammonium nit rat e at a facility r emoved
fro m congemd areas or high -v a lu e or high -ha za rd ind ustria l fac1h1i es and at whJCh an
Jbunda nce of water for fi refighting purposes is available . DHS a lso req u ires the water-
mft to be moored bow to seawa rd and ma imamed m a mobile statu s hr the presrnce of
rngs and th e re.idmess of its engines so it may pas s unres tri ct ed to oprn wa t er in th e evem
of3neme rge11q·.
r.nd 1n the Scll’1e lx,- ld ng with either sulfur or finely dM ded metal’S What 1s the mO\t hke!/ rea~o’l OSHA
‘~-·~ammon um fll!rate to be segregated from these substa nces?
»lution: Ammon ,um nitrate 1s cnem ,call y 1nco mpatio’e wnh both elemental su lfur and finely d,·11ded !’!’eta’s
‘.’,”hf1e , oom!toan1gr1otonso,me , the resu lt1 ngcombust1onreact,ons arev1olemand0
~,tal
f,’T’mcn,u~ r ‘JJ\~ Su”•’ a d •, :-C•(lNl ~-o•
Oit ‘1”\dle the 111~ of f, re and e,pios,on
Any
thr om1um1nthe+6
ox idation state
~1ur.1ge. sto wrng, loJdmg, unlo.idmg, d1schJrgmg, and tran spon.mon of bulk hJndJlllg,
of ammonium mrr a rc- a t J w:nafront f.1c1 l11 y. Thesr n·g11Li11om are ar qu.i.nllllts
fo llo,, s: p, aphra~d~
3
~:o:r:l~~~ii;
~;r:~1e of thC’ a rnm omum n11r,11r mus t br mJrhd on the OUflldt
5
1i1~:ts/s: 3
:~~:{[::~t ;~:~tte~~J~c~~~’.hr stor.1ge of ammonium nitrate~
The am monium nurare musr be S(‘ paraced b)’ a fire -n•s1s111•r wall orb dis
JC lease 30 fee t (9 m ) from organic ma1.cr1als or o rh c-r subst:inces ch!/coul~ nct ~
conrammau on, suc h a~ fla mmable liquids, _combus11ble liquids, corrosi\’e Ii C11at
me1all1c chloraces. me ral!JC permanganaces. finely dJ\’lded metal s, caus ric soda quid.I,
co.i i. sulfur, con on, coal, fats, fis h otls, or 1•egrr:ible o il s. , chu.
Ammonium nit rate ~ usr bt’ srorr1 on a clean wooden or concrete floor or on lkn
01•<.'r a clean floor. When :immonium nitrat e 1s stored on a concrrte floor. :
mus t first be co11errd 111t h a moisture barr ir r suc h as a polyet hylen(.' sher t 0 ; a: Ju~
l.i mmared paper. P tic
Any spilled ammo111 um mt rate mu st br promp_rl y and thoroughly deaned up and
removed from t.he waterfront facility. If ammomurn nmare ha s remained in
11 i1h a wooden floo r for an y leng ch of time, the floor mu se be sc rubbed wirh~:
and all spilled m:11 wa l muse be thoroug hl y di sso lved and flu shed away.
An abundance of wat er for fi re f,gh cmg must be readily a11:1ibb le .
Open drams, trap s, pm . or pockr cs that co uld be filled with molttn ammonaua
nitrate in rhe e1·ent of a fire must be eliminated or plu gg<.' d.
Chrom1u m-co nra 1n1ng com pound ~ m which the chromium assumes the+6 oxid:mon stair
are call ed oxidizing chromium compound s. The +6 oxidation s1::ite of ch romi um is W
hex::ival enr chromi um ion. The oxidizing chromium compounds :ire also callrd he.ovalent
chromium compounds. The y are metallic chromates, m<.'tal11c dichromates chrorruum
trioxide, and chromi um oxychlonde. '
ti_,e aon and th e chromate .aon (CrOi ·) and di chromate ion (Cr1O~- ). re~pecrivel y. Pow-
sJUm chromate :ind po1:1ss111m dichrom:1.te are spt·cific examples. Their chemical formUW
Jre K2Cr04 an d K2Cr20·, res pectivel}’.
ch ro mite ore. whic~ we represen t here as FcCr1 0 4 • For ex ample, co produce potassium
dtchromate the ore 1s first 11(.’at rd at kiln rcmper:irures with pot:iss ium c:irbona rc 10 pro-
duce po1Jss1 um chroma te as follows:
1 lmn le 1′ .. 1,,,,umca,t,,,n,1~ (1,H,·n 1′.-i.1,,:un1,hrnmJI(” 1n,n1 l;l1 0,1dc c.t,,,11 …
l’,,1J OUPllch, ra,t, \uUunc.1,11 l’,,1.”,1u111J,chrwnJlc
;tieri ng rh e pH cond1uon s as follo\1 s:
K,Cr0Jfilql + .:’ ll Cl(aq) — K:Cr ,O·lmf) – 1-f , 0 (/l
roun ds, re spec ti vel y. Co nsl•quemly, compounds such :is lea d chr o mat<.', s1romiurn
,hrorna te, and w 1c chromate hJre been use fu l as pigments m 1ndusm al p.:imt s. The o:,a -
dizi ngchron11urn compounds ha1·e also been us<.'d to mJnufacture tcxule dres and presenc
ood an d lc.nh er. Th ey are also th e ma1or compon r nr s of chrome electroplating ba 1h
!kfore the i 990s. he xavalem chromium compounds commonl y were used as water-
ihe ,irc ulaung waters use d m air cond1t1oners and mdusmal cooling 1owers. The produc-
uo n of this sca le reduced the efficiency by which heat was trans·
ferrtd ro ch e wa
ter. Cof~ J;ng wwm often m h,g, “‘””””‘ [ J I
The rnosc readil y recogmz.able t)’pe of cooling tower is prob::ibl y ,,,.~ _,,,. .. , .. -~” .•. , ~” ….. :
cooling rower s :ire also loc::it ed wherever large heating, venti la – –
110n, ,m d.a1r-cond 1taomng or refrigeration systems a rc needed. I
The coolmg rower shown m Figure I 1.9 is a component of :in 31 r-
cond1t1omng and venti lat ion system 1har cools a major hot el.
hexa1·Jltnt chro mium -ba sed water-tre;nment agents at petroleum :=-
refinwes, powe r plants, and chemical plants w::is of1en discharged D
1n10 ons1 te unlined surface impoundments. Rainwater caused rhe
hexJ1alc m chromium compound ro see p inro ch e subsurface and
co ntJrnmate the underl ying groundwater aquifer.
boor cJn cau se a number of hea lth ailments. In particular, ch e
mhalJri on of th e dust or fin es of hex::ivalent chromium com-
pounds has bee n linked with th e onset of lung cancer in humam.
Thus, th es e co mpounds :ire ranked as human carcinogens br the
mhJla1ion route of exposure.
same name, alleged in th e film that the long-term consumption
of wate r contaminated with elevated le ve ls of hexavalcnr chro-
mium causes cancer :ind other health ailments. Ar the time of th<.'
mo ~ic 's rcleJse m 2000, there was scant evidence to definitively
link th ese hralth problems with the consumption of hexaval<.'tH
chromm m-contaminated w::i 1er. Toda y, howe ver, scientiscs ha1·(.'
dw e1·idence 1har ingestion of chis contaminant nor only causes
the onset of stomach ulcers and sto mach :ind in1 cs tinal cancers
bu r rnJ.)' also damage the kidneys :ind liver.5
rewculat,on ruucturei. used to 1emove heat fro m me
water by contact.ng th e flu,d with <1
f Ch, o,,,11m, / l/r,;J1.•J/t111 Com/io ,mds} 1Ca lifo rmJ EnrnonmcniJ I Pro r.-.:t ,o n Agrnn\ 2009).
1
I I. I
dlthromat• EPA hJ s Set J m n:irnum rnm.umn .rnr k1t·I o t JOO µg/L of fot:il chrom
US(‘ of “-ll c.’r-trC’:Hmrnr .1g t”nls conr.u mng hrx;11•alcn c chromium m hearing l 0 lub11 ~
and ;ur-conJmonmg ;1nd rdriger.Hion S} )tcms. This ban .11ms ro rrducr 0;n(‘ 11 ;’C’1Jtil.i¾I po rr nr1.d of l’ .-..:posmg md 1v1du:.1/s IO their :ur enms1ons. ninafttbe
~::~:~.~;~ :~’:l;;~-~:~;:rmenr agenrs d1~1nbwc-d rn comm C’ rce and mtrndrd fo r u;~
::
hexavalent chromium air emissions increases the ri sk of
comfort cooling towers, which are towers that are open
water•recirculation devices and that are dedicated exclu-
air conditioning, or refrigeration systems. ·
warnrng stJtemenr is read and understood by thC’ ordinJr)’ rndi vidua l under custo
Pora ssrum dichromJ le 1s frequently used commercially as :1 strong ox1d1ze r; fo r enmpk,
1c 1s a component of rhe bJ rh solutions usC’d for ch romrum p lating. Whc- n hc-a ted, potas-
st um dichromate decomposes to gene-rare ox ygc- n as follows :
man y orhc-r substa nces. For example-, po1asmun Jrc hro ma tC’ an d hydrochloric acrd rm
ro produce chlorine.
Pou,, ,umd ,rltrom.ire lhd nx hl onc .lm! ChmmKr hJvnde POIJ,”um , h/,;,n
ir s tendency to oxidize the substances with whic h it ma kes co nr:i ct.
The acids associa ted wuh the meia Hic chroma res a nd morgan ic dic hroma tcs cXJJI
only in aqueous sol urrn ns, but when the wa ter is eva po ra ted fr o m rh em, a compound
formally called chromium / VI) oxide remarns . This :1 nh )’ drou s co mpoun d is ~lso
known as chromium trioxide, chromium a nhydri de , a nd chro mi c acid . Je s chemtCJl
formulJ is C rO, .
. Chromium moxrde is ;1 red so/rd preparc-d indus rri:1H y by .i dd ing co nctn rraied su!fu.
PotJ, , 1~tl\ h1,ulfJI~
(hronuu!II U’)Ol#
CJ, 1,1111111 oxychforidr ts a da rk red !1qu1d 1h:1.t fo rm s \ 1 hen a nuxtu rt of conct·nrra ctd
~;J[r. It 1s also CJIIC’d chromyl chl orrd C’, and its chrm1ca l formu la 1s CrO! CI :,
forn 11 ng chrormum( JI /) ch londl’, chrom ic :1.ci d, ,m d chlorine.
C~rom1ulTL( llllchl onJo ChrotnfflM.ld
11
Ammonium d1chromat ~ is an orange so li d used as a compo nent of cert ai n pyro tec hm cs. Ir
is ~/so u;cd ro dye fabri cs a nd ro :i her th t tex1ure of animal hides du rmg rhe produw on
of /el thtr. hs chemical formula 1s (l\l-l.;)2Cr 20 -. Wh r n hea ted, amm omu m d1chr oma1 c
drcomposesio fo rm nitroge n.
CHROMIUM CO MPOUNDS
Whtn used in the work pla ce, OSHA rl’qulfts tmploytrs to limi r l’ mpl oyec expo5ure to a
hm1·ale nt chrom ium inh.i bt ion conce ntration of 5 µg/ml, :wer.1.gc-d over :m 8-hour wo rkd.J }’,
\ihen shippe rs offrr au oxid izi ng chro miu m co mpound fo r transportation. DOT rcq uirC’s
rhtm to dc-scnbe it as show n in Tabl e 11. 15 o n an acco mpan ying shippi ng pape r. DOT
1/w req uires ship pers .i nd ca rric-rs ro compl y wirh a ll appli c.iblc !a bd mg, mark ing, :md
p/Jcard1ng rrqu ire mc-nts.
OXIOIZING CH ROMIU M
COMPOUND
Co mpo und s
o,
UN17SS, Chromic add solution, 8, PG Ill
~ th lo-rid- ,–+-U-Nl_75_a—‘C-h,o- m- ,,-m-o~- ,-hl-~ ~ld-,, ~a ~PG~,——
Chromoiulfur ic acrd UN2240, Chromosulfu ric ac id, 8, PG I
oxychtor ldt
I I
I 1
”I
1/
dkh,om•lf
POTASSIUM PERMANGANATE
The metallic perman ganates arc ma nufoccurcd from ma nganese ore contain ·
70 % manganese dioxide. As th e ore 1s heated wuh either sodium hydroxide or mg about
hydro xide, th e mangan c-se und ergoes ox1da1ton to produce the co rrespon ding alk~a»i taai
mang.1~.He. For examp lr, potass 111m manga nate 1s formed from the ore and poi~s~
hydroxid e. 11.tri
\ t111i;.1~\eJ1011Jc l’uu”1urnh)Jnl\1ck (h ~e•n f’,1u,-1u mnu opn;uc Watrr
s1umpc-rmangan arc .
P,,1J1,1urn IIIJfl,JflJ[l” \~ J r,, l ‘,,tJ”IUlll r•:nuJfl~Jn.11,· !’01 .1–,u m h),lro .. ,k H) lh’fQ
crystal lization.
permanganatc thac are used pharmaceutically to cure derma titis having a bacterial or fu 12-
gal origin (~athlete’s foor” ), Th ese sa me so lu uons are used to trea t fis h dise ases. Jbr
concentratcd solutions are usc-d !O remo1·e objectio nable matte r from chemica l and bto,
log ical process wa ste s by oxidation. The effluen t gases fro m ma ny in dustrial sources an
also often elim inared or reduced in concentration throug h red ox rea ctions im·ol11ng tbt
use of sodium permanganate or pot;1ss iu m pe rm:rngana rc.-.
mussel (Section 11.8-A) in warerw:i ys. Po tas sium perma ngana te solutio ns are inj ecredmro
pipes where the mus sels congrega te and th t’rt” by di sturl> 1he now of warcr in the intakeJnJ
discharge sys tems. The oxidizing agent kills 1he pesky mu sse ls.
Wht’n shippe rs offer a me1al/ic permanga nat e for trnnspo rt ario n, DOT requ ires them ro
id entify it as show n in Table 11.1 6 on an :iccompa nying shippi ng paper. When shippm
offer a metallic permangana te no r li sted in Tab le J l .1 6 fo r trans portat ion, DOT requires
th em t~ id ent1~ rhecompound gene rically on 1hc.- shipping pape r as “UN 1482, Pu mang.,·
nates, morgamc, n.o.s., 5.1 , PG II ,” “UN l 482, Permanga nates, inorga nic, n. o. s., S.I ,
PG Ill,” or ~uNJ 2 l 4, Pr rmanganates, inorganic, aqueous solution, n.o.s., 5.1 , PGII.’
DOT ?]so requires s~ippers to enter 1he name of rhe specific co mpo und parent he ticall pn
ihc sht ppmg descn ptJOn. It also req111re s shippe rs and carrie rs ro co mply wirh all labeflllg,
markmg, and placard ing req uirements.
.\1 ctalli_c nitrites and mt’~allic nir r,Hes arc co mpound s co mposed of metallic ions ~nd tbr
nitrtte ion {NO~) and nir ratc 10 11 :\O i ). res pcc ti1·ely. In th ese co mp oun ds, the nirrogtll
atom ass umes ox ida tion numbe rs of +3 and +5, respt”c rivcl y. 1\,lerallrc nit r
456 Chapter 11 Chem istry of Some Ox idize rs
~lfl-“LUC PE MA NGANATE
UN151S, Zincpt>rmanganat,, 51 , PGII
rornmon compo nent s of blas ting age nts and ot her explosives. Sel’c- ral me1a lh c nit rates arc
Jlso used to prod uce color in act iv ated signali ng Oa rcs.
hot dogs, and luncheo n mea ts), poultry, and fis h to fix thei r color and inh 1b1c th e growt h
of Clos trrdmm bo1ulm11m, the bac1erial spo res thar cause bo1u hsm. This use was limited
bi ih e U.S . FooJ and Drug Adm imstrat ion when scic-nris ts demons tra ted rh:u nu.r ites ca n
rroduce carcinogenic N-mt rosa mm es in the stomac h. The nimr cs r(‘aCt wi1h stomac h acid
ro fo rm mtrou s aci d, which in rum re.:icts wi th the pro1ei ns in meat 10 form N-mtrosa –
rnmcs {Sectio n 13.8- 8 ), organic compo un ds containi ng the gro up of atom s – N- N= O.
Loll’ co ncentr:iuons of N-ni1ro s:1n 11 nes have been iden tJ fied in smoked fis h, cured mea t,
~m. and chee se. Beca use res1 an imal s exposed to N- nitrosami nes deve lop ca nce r,
.\’• mtro samme s arc rcg;1rded as probable hum:m ca rci noge ns.
l,kd)· to suffer fro m methcmoglobinemia (St”C tio n 10. 14 -8 ). In ra re mstance s, rh1 s a 1l111 r m
c~n also be comracted by abso rpt 10n through the skm , e.g., from ex posure to molt en
sodiu m nnrite or sodium niir are.
.\l (tJ lhc nitri tes can ac t as ei th er oxidizing age nt s or reducing agents. They are oxidized
10 metallic nitrntes and rc- du ced to ni tric oxide (NO) as fo ll ows:
SJ,uu11>1trn , ~(‘
2N .1C l(oq) + 2NO(g l + H; U (/J
tem per:nures, For example, sodium nit rite decomposes as fo ll ows:
~oJ tu m mini ~
.\letall 1c n11 ra tes rrac t on ly as oxidiz in g age nt s. In rhe presence of acids, th ey arc conve n ed
to nir ric oxi de, nitrogen dioxide, or ammo nia . This chc-mical bcha vio r is exe mpl ific-d by tht’
chemi c~I rcactJon~ of zinc with concenira ted nitric aci d noted in SeC1 io n 8.8-A.
nitrit e
I
I I
ox) grn . For ex:.1mple. sodmm rn r rJ tl’ therm.1.ll y decompo ses to form oxygen.
oxy~en. For ex:imple, silve r ni trate thermally deco mposes to produce sd vet~
~ ar.1
<;,her
m fo rm th e respecme metallic o,udc-, mtrogen dioxide, and oxrgrn: For rxamplc,lcadl!Jl
nitntc- thrrmall r deco mposes to produce lrad ox ide, rutrogrn dioXJde, and oxygen.
AND SODIUM NITRATE
tions of sodium nimt C’ and/or sodium m1rat e in arrain foods intended fo r ust as fol10’A1:
nitnte does not exceed 10 pans pe r million in th e finished product
As a preservarivr and color fixati ve , with or without sodium nitrate, in smoked, CtJnd
sa bl efis h, smoked. cured salmon, and smoked, cured shad so rh :ic the level of sodi1111
nitr ite does not exceed 200 parts per million and rh e level of sodium nitrate docs oor
exceed 500 pamper million in the fini shed product
As a preservarh·e and color fix :ni ve, with sodium nitra1e, in meat-curing prepam1om
for the home-c uring of meat and meat produc1s (including poultry and wild gamti
with directions for use that limit rhe amount of sodi um nitrite to not more 1h.1.n200
parts per milli on in th e finished meat product, and the amount of sodium nimucto
nor more than 500 part s per million in !he finished meat product
concentration, direcuons for use, and th e statement “Keep Out of 1he Rrach of Childun.·
When shippers offer :1 metallic nitritr or met;1ll 1c nitrate for transportation, DOT rNjUll’tS
them ro describe th e appropnare substan ce on an accompanying shipping pa prr. Somt
exampl es for several represe nrar ive metallic nirrim and nitrates are listed in Ta ble I 1.17,
\'(
49 C.F.R. Sl72.l01 , DOT requires them ro identify 1he co mpound generi c;1ll y and to
rn trr the name of th e spmfic compo und parenthetica lly 1n the shipping description. DOT
also requires shippers and ea rn ers ro complr wi1h all applicablr labe lin g, ma rking,aM
pbcarding requirem en ts.
or rail, DOT requ ires th em to d1sp la r the n;Hne on rwo opposing sides of the pac kaging.
s,numn1tr ate
UN2726, Nickel nitrite, 5 1, PG 1(1
5
1v, rn ltrate _ j UN1493, 511vern ,tratt, 51 ~
~Ill~ ——~ UN \ 498, Sod ium nitrate, 5.1 , PG III
So(lu~ ____ UN1~00.Sod,umn,tr1te,Sl,PGII
The compounds composed of metallic ions and p<:rox1de ions [0 ~- or t--0- 0 - 1> 1 are
CJl lrd mera/1,c peroxides, and th e compounds composc-d of metallic io ns and superox1de
ion> [0 .: or (-0 – 0 – r] are called meta/be rnperox1des. The commercially important
meiJlhc peroxides are co mpounds that contain an alkali metal 1011 or an alkaline earth
111ml 1011 . Ex;im pl es are sodium p<:rox1de ;ind banum p<:roxide, whose chemical fo rmula s
are \' J20 2 and ll.10 2, respectively. There is onlr one commerci:1\ly impor1ant mrtallic
supe rox1de: pot::issium sup<:ro xide . hs chc-mic::i l formu la 1s K0 2•
The metallic peroxides are therma ll y unmble, highl y reactive compounds. When heated,
the y decompose to the corresponding metallic oxidr and oxygen.
So<11u m 1x:ro " Jc SoJ1 um o11
B;mum(,(rm 1Jc l! Jn umo ,,Jc l h: gc n
2N,120 2(s / + 2H20 U) __. •\NaO H(,uf) – 0 2(1.”l
stored in right!)’ closed, mois1ure-proof contamers.
lhr meta llic superoxides arc rhermaUy unstable, warer-re’Jctive. compounds. Their water reac-
111·1ry is put to use in a type of chemical oxygen ge nerator that provides breathable oxyge n to
peroxld1
Barium
s up1roxld1
persulfate
METALLIC PEROXIDE OR
METALLIC SUPEROXIDE
Met.i lhc Peroxides and Supe rox,des
_. UN1 491 , Potarn um perox1de, 5 1, P~
UN2547, Sod ium supero11.1de, 5 1, PG 111
idc m rhe user’s breath are :1bsorlx-d by potassium superoxidc containrd in a canistet Tut
chemica l acuon of the moisture :md the suJ)(‘roxidc generat es oxygen. The oxygen rntm,
breathmg bag for subsequent inh.1bt10n , :rnd the exhaled breath repeals the cycle.
l’nra,,,um ,uf
DOT requ ir es shippers who offer a met.il lic peroxide or supero xi de for tra nspon.i tionto
rdent 1fy the rele\’3nt submnce on an .iccomp.in)’ing shipping pape r. Some examplaflX
sever.ii rep rese ntar ive nmaltic pero xides and sup eroxides are listed in T.ible 11.1 8. Whtn
shi ppers offer a metallic peroxide or its so lutions rha! are 1101 l1 sred at 49 C.F.R. 172. 101,
DOT rrqu ires them to id.:- nt 1fy the compounds or solutions generically and to list thtu
sprof1c names parenthetica ll y. DOT requ ires shippers and ca rrie rs ro comply with all
appl 1c.:a ble labeling, ma rking, and placardi ng requirernems.
SODIUM PERSULFATE
also ~ailed t~e peroxyd 1sulfo1c ion (S~ O~ ). T he pt”rsulfot e ion is :il so known as rhtpcr·
oxyd1su/fa1e 1011. It ha s the followmg Lewis stru cture:
l” o-o i uj
whose clwrn1c,1I formul:l s :ire K.:5!0 g and ,’\,1/ )~0 ~, res pectively. They arr white sofid;.
rot~iilurn persulfa te
UN 1505. Sod ,umpersulfate, S 1, PG Ill
The rllt’tallic persulfates are th_e s.:i hs of peroxyd1sulfuric ac id, whose chemica l formukl 1s
11 ,s,O~. The latte r sub srnn ce is a liquid prep ared by mixing 30% hydroge n peroxide and
9sr; sulfunc acid 111 a 1:3 rati o by ,olume.
‘\ullum;,,,.,.J ll ) J’<'bc n1"- n.>“J.: l’>.’nl\).Jisu1fun, ‘1<,J \\ ao,·r
hil 111 the computer-chip mduStr}’, whf’re it is known as piranha, perox yd isulfuri c acid
15 ·~sed co cl.:-an 1he wafe rs th at are processed into chips.
diox ide arr gl’ nerat cd whe n sodium pl’rsulfate is he.1 1ed.
“W iumo ,,Jt Su ltur ,1, ,:, .,,Jc O, H-,:”
\ihm shippers offer pota ssi um persulfote or sodi um pt”rsulfare for transportation, DOT
crqu 1rcs them to provide the relevant shipp ing description shown in T::ib le I 1.19 on an
Jccompanying shipping p::iprr.
pm ulfa1e and thm solutions for 1ranspona1ion, DOT requires th em 10 identify the sub-
sunccs generical ly as ~uNJll 5, Persulfat es, inorganic, n.o. s., 5. I, PG Ill ” or “UN32 I 6,
Pmulfa1cs, inorg.inic, aqu eous so lution, n.o .s. , 5.1, PG 111 .” DOT also requires shippers
to enter th.:- n:iml’s of the specific compounds parenthetically in the shipping description,
Jnd to affix an OXIDIZER label to their packaging. DOT also requires shi ppl’rs and car-
nm to complr with all applicabl e labeling, marking, and placarding requiremen ts.
M:udm are 1m ns usl’d to intentionally initiate fire when 1he mixture of substances con-
tJinc d 111 their heads is rubbed against ::i hard surface. They have long served as one of the
whcs t comm.:- rcia l products in which redo x react io ns were used to pro vide fire on
drmand. hen today, th ey .ire th e most common items used to int entionally initiate fires.
c•llcd strike-anywhere matches and safety matches. It is app rop ri:ue ro examine rhe
chtrnistrr associa ted with their burning, especia ll y insofa r as th ese processes invol ve the
u5r of oxidizers.
~c head of a srr ike-a n)’\Vhl’re m:itch co nsis ts of a mixtu re of 1e1raphosphorus trisulf1de i\’0 ca_lli:d phosphoru s sesquisulfidt) , sulfur, lead(IV ) oxide, powdered glass, and glue.
mat ch • A ma tch
with a bu ll s-eye head
con sisting ofawh1te
tip containing t@tra-
phosphoru s trisu lfide
that Is actuat@d by
rubb ing it aga inst an
abrasive strip
match desig ned to
ign ite only when iu
head is rub bed on a
prepa red surface con –
sisting of red phospho-
rus and powder ed g lass
wlr.,-•nr,-,,he!’fr-1•tch ,f’I
{a)ign1~whentnl!Sur·
faceof1t1,ma1chhud ,s
ruobedaga.t’l:stahard
surface Thes,i,tymatcn
n (bl gnt~,,.,henthe
surfaefof a matcnh,ad
s W\lck aga,nsta surfa”
cont.an1ng red ohospho-
rus and POY.rdered gl,m
Th,f1f’!tnangles tothe
ri ghtofP
– Wood
Rtdpho19horu1+ KCIO,
evolve d hear of combustion miwn es the comb ustion of the sulfur and wood.
T e1r:tpho:,pllofu 1 ln111ll1dc U\ )f<'n r ~ndpho,rh<)f\l, ,.k,,m.k- S111iur dlO~Kk
The acme compon r ms of a safe ty match com1st of a mixturr of antimony irisulfide, sul·
fur, and pota ss ium chlorate, glued to a pi ece of ca rdboard. A safety ma rch ignit~ br
mea ns of friction agains t a prepared su rface con sistin g of red phosphorus and powdmd
gl:m. Th is surface is usuall )’ on th e box, book, or ca rd . When the match head is ru bld
on rhi s sur facr, th e hea t initia1es a redox rea ction as follows:
1•,~.u\1UIII chlorJIC Sulfu1 l’<>l.1>,mmc hlvnde S v!fu1J10 >1Jc
,\n11n11H1) 1mulfi,k l)\) f
MATC_HE_S-:–=-:—-t-,’,–“,–“‘,–IN:.:G.:.OE:cSC:::R::_>n:::10:::N __
S.,fl’IY boo k mltchu UN\ 944, Mltches, safety boolr., 4 1, PG Ill
5u, ke-anywhffe m,tches UN13]1 , Mltchet strikt anywhere, 4 \ , PCi Ill
\\”htn shippers offe r matches for tran spo rtation, DOT req uires them 1o provide the rel e-
11ni shipping d_escripuon as shown i~ Table 11 .20 on the accompanying ~hipping paper.
!)OT ~lso requires s~1ppers and ea rners to comply with all applicable labthng, marking,
JnJpbca rd1n g reqm rem ent s.
A RELEASE OF A METALLIC OXIDIZER
J trJnS pi.lrl:lt1on mi shap by obse rving at least one of the following:
hmd on a shipping paper
Tii t word OXID IZER an d the number 5. I printed on yellow labels a.ffuced to pa cka g,mg
The word OXID IZE R and the number 5. 1 printed on yellow placa rd s pos1ed on
tJch sid e and eac h end of a rr.rn sport vehicle conta imng 1001 pounds (454 kg ) or
mortof an oxidizer
J1m-s 1~ 10 deluge them with water. Metallic oxidizers generally are soluble in wate r. \Vh r n
tht)’ arc dilut ed with water, their chemical react i,·ity is sharply reduced or eliminated.
emcrgr nC)’ rt”sponders need to exercise cauiion when applying the wa ter. Many solid ox1•
dizm melt befo re 1hey decompose. These hot molten mat eria ls flow to adjoining arra s,
11 hm th r r ma r mix with combusrible materia ls and support their ignition . Although
IIJ ttr mar be :ipplie”d to fires supported by oxi di zers, it should be app lied onl )’ to bulk
quanti ti es of mol ten oxidizers as a fog to avoi d 1he rapid generation of steam th:it ma y
c;1 u1r th e molten material to splauer. Experts al so reco mmend the use of sand on fire s
in1oh•mg bulk quamit irs of mol ten oxidizers.
tr,o1 dwa ppreoably1o thattherateofano.adauon-reduaionre.Ktionkl.reducedV-Jhen1h,runoff -ste’t
‘-~ “ended ho·,, e, er , the waterevap01ates and lea~t$ the ox,d1zer 1n a dr, state wheteupon 11 19a.nsvscec11-
bi to SIJPP0!11ng the com bustion of manr1 For this realOn the wa~r runoff genera1ed dul’1ng a re:s.oorue acoon
·o!l i ng a 101 d o, 1d,z, r should always bt damm,d 01 d, ~ed so tnat tne oxd1:er may bl’ rieutra ‘ ZM Delore JU
•·~a:e d,socwt,on So dumsu\f1te1sal)p,calneulfal,z n9agff’lt
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