FLAMMABLE.GASES AND LIQUIDS AND THEIR HAZARDS.EPA 744-R-94-002 PDF

the flammable vapour in the cloud is 90 tonnes (U.S. EPA, b). The threshold is estimated by modeling with Process Hazard Analysis Software The equation for estimating the evaporation rate of a liquid from a pool is . Flammable Gases and Office of Prevention and Toxic Substance (). EPA R KEY WORDS: Acute hazards; environmental equity; GIS; worst-case exposure. 1. Flammable gases and liquids and their hazards (EPA R-. ). Background: Section (r) of the Clean Air Act (CAA) requires facilities that have threshold installation: a hazard assessment, a management program, . Agency (EPA) an RMP that summarizes their Risk Management Program Gases handled as refrigerated liquids at EPA R

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Once the expansion energy, E, has been determined, the expression for the turbulent coefficient is: Information specifically related to consequence analysis includes quantity released, temperature liquidx pressure of chemical released, overpressures created by an explosion, projectile distances, vapor cloud size, flashback distances, and property damage. The database does not distinguish between on-site and off-site injuries and fatalities.

For liquids, the entire quantity released is assumed to be in the pool. Explosions anf flammable substances accounted for accidents, and fires excluding fires involving explosives accounted for accidents in the database. Releases as great as 1, metric tons have been identified, but they have usually produced fires or firestorms.

According to Pineau et al.

Basic Prediction Procedures for Environmental Fate

Oil on the surface of the water reportedly travelled through culverts under a highway and railroad and collected on a stock pond located 1, feet from the point of the rupture. The release rate to air is flammable.gaes as the rate of evaporation from the pool. Vapor cloud fire results for a 10, pound release of ethylene, based on dispersion to a concentration equal to 50 percent of the LFL, indicated a downwind distance of meters, which is greater than the vapor cloud explosion distance of meters for flammable.gaees.

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Distances are clearly not linearly related to the quantity released; i.

BLEVEs also generally result in ignition of the vapor cloud when the substance is flammable, and a large rising fireball may form, the size of which will vary with the accident conditions and the type and amount of hazardous material present. The procedures and examples in this module have illustrated various modeling techniques that can be used to predict areas of possible impact associated with hazardous material accidents. Exhibit C, in Section C.

Yellow Book, Chapter 5, “Evaporation,” Pp.

The calculations in this section model the consequence distance in a vapor cloud fire when the material evaporates from a pool on the ground rather than flashing into a vapor state after an instantaneous release.

Section r of the Clean Air Act CAA requires EPA to develop a list of at least regulated substances that, when released, can cause death, injury, or serious adverse effects to human health or the environment. This amount develops as the dispersion flxmmable.gases. Peak overpressure is most commonly used. From Equation 1, the maximum area of the pool would be 50, lbs times 0. The five vapor cloud explosions are described further following Exhibit Identify the appropriate flammable substance and quantityreleased.

The database contains reported accidents which occurred during industrial production, storage, handling and transportation of hazardous materials.

Effect of Varying Concentration. Spills involving more than one type of chemical are possible during some transportation accidents, especially when the accidents involve railroads.

The specific substances reported most frequently in the database were gasoline and LPG propaneboth flammables. To fllammable.gases jet dispersion, the envelope within which the concentration of a turbulent jet is above a specified level, jc, is represented by a major axis of length: The gas discharging or venting from the hole will form a gas jet that “blows” into the atmosphere in the direction the hole is facing, all the while entraining and mixing with air.

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Sonic boom glass failure Breakage of windows, small, under strain Typical pressure for glass failure “Safe distance” probability 0. Liquid factors are provided for two different wind speeds since the wind speed affects the rate of evaporation. The indicative criteria related to flammability are discussed in Appendix A. The two largest spheres, full to theirgallon capacity were saved from BLEVE by water from rail tank cars.

Section 6 discusses the different types of flammabld.gases chemical fires and explosions. The duration of the fire and the length of time it might take an exposed person to escape or take shelter from the fire would be important considerations.

An extensive variety of combinations are possible when considering the reactions of broad groups of chemicals. Successive approximations of the calculations for the value of Fx are then calculated using the new values for the distance until one value is approached. The University Transportation Center for Alabama. Lewis reports that “significant” blast effects have occurred under semi-confined conditions for quantities as low as kg pounds ; Lewis does not further describe the blast effects.

Instead, the associated hazard is a rapidly moving flame front.

Brief Records : EPA National Library Catalog

For this analysis, the linked model for instantaneous and prolon ed releases was used. The Agency agreed and noted its intent to evaluate hazards other than toxicity in the future.

There does exist one concentration at which hazards.pa composition of the solution does not change as evaporation occurs. Vapor cloud explosions have occurred at quantities as low as 20 kg, but the damage they have produced has been very localized and of little concern regarding injuries and losses Lewis The vapor pressure and evaporation rate of a substance in a solution depends on its concentration in 744-r-994-002 solution.