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Toxic release

TRI is the most detailed source of information about toxic chemical releases. TRI, however, seriously underreports the total toxic chemical releases for the following reasons  [Pg.53]

TRI does not cover all industries. Prior to 1998, for example, metal mining and electric utilities were not required to report their toxic chemical releases. [Pg.53]

TRI reports on less than 1% of the 80,000 chemicals annually manufactured and imported into the United States. It covers only about 650 of the chemicals in use in the United States. [Pg.54]

Reporting companies estimate their emissions by the use of emission factors, rather than by actually monitoring their emissions. [Pg.54]

TRI does not require the reporting of the quantities of toxic chemicals actually used and the amounts of these chemicals that remain in products they manufacture and distribute. [Pg.54]

The problem of the explosion of an unconfined vapor cloud is not only that it is potentially very destructive but also that it may occur some distance from the point of vapor release and may thus threaten a considerable area. [Pg.627]

If the explosion occurs in an unconfined vapor cloud, the energy in the blast wave is generally only a small fraction of the energy theoretically available from the combustion of all the material that constitutes the cloud. The ratio of the actual energy released to that theoretically available from the heat of combustion is referred to as the explosion efficiency. Explosion efficiencies are typically in the range of 1 to 10%. A value of 3% is often assumed. [Pg.627]

The hazard of an explosion should in general be minimized by avoiding flammable gas-air mixtures in the process. Again, this can be done either by changing process conditions or by adding an inert material. It is bad practice to rely solely on elimination of sources of ignition. [Pg.627]

For a chemical to affect health, a substance must come into contact with an exposed body surface. The three ways in which this happens are by inhalation, skin contact and ingestion. [Pg.627]

In preliminary process design, the primary consideration is contact by inhalation. This happens either through accidental release of toxic material to the atmosphere or the fugitive emissions caused by slow leakage from pipe flanges, valve glands, pump and compressor seals. Tank filling also causes emissions when the rise in liquid level causes vapor in the tank to be released to atmosphere, as discussed in Chapter 25. [Pg.627]

The third of the major hazards and the one with the greatest disaster potential is the release of toxic chemicals. The hazard posed by toxic release depends not only on the chemical species but also on the conditions of exposure. The high disaster potential from toxic release arises in situations where large numbers of people are briefly exposed to high concentrations of toxic material, i.e., acute exposure. However, the long-term health risks associated with prolonged exposure at low concentrations, i.e., chronic exposure, also present serious hazards. [Pg.259]

The limits for prolonged exposure are expressed as the threshold limit values. These are essentially acceptable concentrations in the workplace. There are three categories of threshold limit values  [Pg.259]

Time-weighted exposure. This is the time-weighted average concentration for a normal 8-hour workday or 40-hour workweek to [Pg.259]


Here we shall restrict consideration to safety and health considerations that can be built in while the design is developing rather than the detailed hazard and operability studies that take place in the later stages of design. The three major hazards in process plants are fire, explosion, and toxic release. ... [Pg.255]

The first major hazard in process plants is fire, which is usually regarded as having a disaster potential lower than both explosion or toxic release. However, fire is still a major hazard and can, under the worst conditions, approach explosion in its disaster potential. It may, for example, give rise to toxic fumes. Let us start by examining the important factors in assessing fire as a hazard. [Pg.255]

The second of the major hazards is explosion, which has a disaster potential usually considered to be greater than fire but lower than toxic release. Explosion is a sudden and violent release of energy. [Pg.257]

Vapor cloud explosions. Explosions which occur in the open air are vapor cloud explosions. A vapor cloud explosion is one of the most serious hazards in the process industries. Although a large toxic release may have a greater disaster potential, vapor cloud explosions tend to occur more frequently. Most vapor cloud explosions have been the result of leaks of flashing flammable liquids. [Pg.258]

Chlor—alkah production is the largest iadustrial source of mercury release ia the United States (see Alkali and chlorine products). For the 1991 reporting year, chlor—alkah faciUties accounted for almost 20% of the faciUties that reported releases of mercury to the U.S. Environmental Protection Agency (EPA) for inclusion onto the Toxics Release Inventory (TRI) (25). [Pg.108]

Toxics Release Inventory Public Data Release, EPA-745-R-93-003, U.S. Environmental Protection Agency, Washington, D.C., 1993. [Pg.110]

Control room sited closer to the batch process due to need for more operator interaction with batch processes. Infiltration of flammable/toxic release from outside. Possible overpressure from external explosion. [Pg.32]

Has toxic release inventoiy (TRI) been completed for the site ... [Pg.128]

We expect that four large toxic releases will occur during the lifetime of this facility. [Pg.14]

Checks on the adequacy and location of fire-fighting, emergency rescue and alarm equipment Practice in emergency situations Emergency procedures for Eire/explosion Toxic release Serious accidents Spillage... [Pg.416]

In addition to SCREENS, you can also download TSCREEN, VISCREEN, and CTSCREEN. TSCREEN is a screening model for determining maximum short-term impact from toxic releases. Click the filename to download the file. [Pg.328]

TRACE II Toxic Release Analysis of Chemical Emissions Safer Emergency Systems, Inc. Darlene Davis Dave Dillehay 756 Lakefield Road Westlake Villa, CA 91361 (818) 707-2777 Models toxic gas and flammable vapor cloud dispersion. Intended for risk assessment and planning purposes, rather than realtime emergencies. [Pg.306]

In this study detailed fault trees with probability and failure rate calculations were generated for the events (1) Fatality due to Explosion, Fire, Toxic Release or Asphyxiation at the Process Development Unit (PDU) Coal Gasification Process and (2) Loss of Availability of the PDU. The fault trees for the PDU were synthesized by Design Sciences, Inc., and then subjected to multiple reviews by Combustion Engineering. The steps involved in hazard identification and evaluation, fault tree generation, probability assessment, and design alteration are presented in the main body of this report. The fault trees, cut sets, failure rate data and unavailability calculations are included as attachments to this report. Although both safety and reliability trees have been constructed for the PDU, the verification and analysis of these trees were not completed as a result of the curtailment of the demonstration plant project. Certain items not completed for the PDU risk and reliability assessment are listed. [Pg.50]

The development of tlie emergency planning and response actions under CERCLA is based primarily on a national contingency plan that was developed under the Clean Water Act. Although the actions of CERCLA liave the capabilities to handle haziirdous and toxic releases, tlie act was primarily directed tow ard the cleanup of abandoned haztirdous waste sites. [Pg.42]

SIPs are intended to prevent air pollution emergency episodes. The phms are directed toward preventing excessive buildup of air pollutants tliat me known to be harmful to the population and the enviroiunent when concentrations exceed certain limits. The compounds affected under the implementation plans are sulfur dioxide, particulate matter, ctirbon monoxide, nitrogen dioxide, and ozone. A contingency plan, which will outline the steps to be taken in tlie event tliat a particular pollutant concentration reaches tlie level at wliich it can be considered to be hannful, must be included in each implementation plan. The implementation plans are solely based on tlie continuous emission of tlie previously stated air pollutants. They do not mandate any actions to be taken in tlie event of an accidental toxic release. [Pg.73]

This section focuses on industrial accidents tliat are not plant related and revievs ing accidents tliat occur during tlie transport and storage of hazardous substances. Frequently, such accidents result in fires, explosions, and toxic releases. This topic will be discussed in tlie next cliapter. [Pg.185]

The potential for fire hazards is rather liigh in tlie chemical industry. However, tliis potential is generally judged to be less tlicui that of an explosion or toxic release, as discussed later. The scale of a fire hazard can be deteniiined by assessing the following factors, ... [Pg.219]

The general subject of toxicologj is discussed in detail in Part III - Chapter 11. However, tliree toxicology teniis are introduced here in order for tlie reader to better grasp tlie problems encountered witli a toxic release. Threshold limit values (TLVs) can be categorized in tliree ways. ... [Pg.233]

As mentioned earlier, toxic releases may consist of continuous releases or instantaneous emissions. Continuous releases usually involve low levels of to.xic emissions, wiiich are regularly monitored and/or controlled. Such releases include conlinuous slack emissions and open or aerated chemical processes in wliich certain volatile compounds are allowed to be stripped off into the atmosphere tliroiigh aeration or agitation. Mathematical models for these releases to tlie enviroiuncnt are covered in detail in Part III. [Pg.234]

Highly toxic release warrants die evacuation of persons in vulnerable zones downwind of the release. Releases of lesser toxicity may allow for other measures to be taken to minimize exposure, such as advising for persons to remain indoors. [Pg.509]

According to recent Toxics Release Inventory (TRI) data, methyl parathion was discharged to air from two processing sites in the United States in 1999 (TRI99 2001). No releases to soil or water were reported. The TRI data should be used with caution because only certain facilities are require to report. This is not an exhaustive list. [Pg.147]

Releases to air, land, and water occur primarily through its use as a restricted-use insecticide. The media of most importance for human exposure are contaminated air and soil. According to the Emergency Planning and Community Right-to-Know Act of 1986, 42 U.S.C. Section 11023, industries are required to submit chemical release and ofif-site transfer information to the EPA. The Toxic Release Inventory (TRI), which contains this information for 1987, became available in May of 1988. This database is updated yearly and provides a list of industrial production facilities and emissions. [Pg.168]

TRI99. 2001. TRI explorer Providing access to EPA s toxics release inventory data. Washington,... [Pg.234]

DC Office of Information Analysis and Access, Offices of Environmental Information, U.S. Environmental Protection Agency. Toxic Release Inventory. HttD //www.eDa.gov/triexpIorer/. April 27, 2001. [Pg.234]


See other pages where Toxic release is mentioned: [Pg.259]    [Pg.263]    [Pg.1005]    [Pg.1026]    [Pg.17]    [Pg.79]    [Pg.81]    [Pg.398]    [Pg.401]    [Pg.53]    [Pg.529]    [Pg.545]    [Pg.550]    [Pg.104]    [Pg.27]    [Pg.307]    [Pg.34]    [Pg.34]    [Pg.72]    [Pg.242]    [Pg.135]    [Pg.137]    [Pg.263]   
See also in sourсe #XX -- [ Pg.259 , Pg.260 , Pg.261 ]

See also in sourсe #XX -- [ Pg.627 ]

See also in sourсe #XX -- [ Pg.15 , Pg.16 ]

See also in sourсe #XX -- [ Pg.345 , Pg.346 ]




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