Document 6N2nLNoJo2D3d37LprdeqjE9

CHAPTER 8 1954 Guide 160 apply a reasonable safety factor to the ventilation estimate without con sideration of the concentrations of gases or vapors that approach the danger point. Safety engineers prefer to' limit the concentration to j or of the plliioonnowwggineetttrr.hleexpc'loasp'iavecicl,t;iyum-gautitun,tduainoddesthi_g_i_sn___ffaaovcf.tt. vssehhonouutilllddatbbineegggiievveqenunifpfumllewnte.igh~R_t_ai_nr_e_d'lyetes1hrmouin1ldJ consideration be given to operation above the upper explosive limit in the coopnesnidaereraatsioonf bbeu'igl'di'vi'ne-g-n-s--t-oo--rroorpooeomrmasst--i--oneevuveuenunutchthoouugghhuunnoocccuuppieiedd----bbeeccaauusseeththee danger of temporary drop of gas concentrat'ion t-o a p- o- -i_ni.t within the ex ploAsibvielitryanogfeaisfltaomomgraebalet. liquid to form explosive mixtures is determined largely by its vapor pressure, volatility, or rate of evaporation. Flash Table 4. Limits fob Toxic Dusts, Fumes and Mists SUBSTANCE A S.A. Standards, M.A.C. mg/cu m Threshold Limit Values, A.C.G.l.H. 1953 mg/cu eg Antimony. Arsenic -- Barium-- Cadmium............................................... Chlorodiphenyl..................................... Chromic acid & chromates as CrO*. Cyanide as CN.... Dmitrotoluene........ . O-Dinitrocresol___ Fluorides............... Iron Oxide fume.. Lead............... . Magnesium oxide fume. Manganese.. Mercury.... Parathion {0,0-diethyl-0-p- nitrophenyl thiophosphate). .j Pentachloroanphthalene......................................................... j Pentachlorophnnol........... ......... I Phosphorus (yellow)........... Phosphorus pentachloride. Phosphorus pentsaulfide.. Selenium as Se. Sulfuric acid.. Tellurium. . Tetryl......... Trichloronaphthalene.................... Trinitrotoluene................................. Uranium (soluble compounds) -- Uranium (insoluble compounds).. Zinc oxide fumes......................... .. Q.l (W) 0.1 0.15 point is a convenient method of expressing this property in terms of the.; temperature scale. It may be defined as the temperature to which a com- J. bustible liquid must be heated to produce a flash when a small flame is-;, passed across the surface of the liquid. The higher the-flash point, the v more safely can the liquid be handled. Liquids with flash points underi; 70 F should be regarded as highly flammable. y Upper and lower limits of flammability of gases and vapors, and the flash - points of the corresponding liquids are given in Table 6. Methods for estimating the flammable limits of mixtures of gases or;; vapors must be applied with caution; the reader is referred to other publi catDioenssigfnorotfheisquinipfomrmenattifoonr.1th2'e13 control of combustible anesthetics is out.* lined in Chapter 7. Construction of equipment for handling air contain- . Air Contaminants 161 ing flammable substances, or operating in atmospheres so contaminated, is discussed in Chapter 46. ' It is customary to report the concentrations of flammable gases or vapors in percent by volume, or volume percent. Comparison with concentra tions on the part per million scale used in chemical, medical or industrial hygiene literature is readily made by the conversion: 1 percent = 10,000 ppm (parts of contaminant per million parts of air, by volume, or in other words, cubic feet of contaminant per million cubic feet of air). It will be noted in Table 6 that nearly all of the substances listed have lower explosive limits above 1.0 percent, while the maximum allowable concentrations for gases and vapors in Table 3 are below 1000 ppm or 0.1 percent in most cases. Therefore, control of toxic or injurious vapors to levels below their maximum allowable concentrations for health usually requires much more effective ventilation than for the prevention of a fire hazard. COMBUSTIBLE DUSTS A dust explosion is essentially a sudden pressure rise caused by the very rapid burning of airborne dust. The primary explosion often originates Table 5. Limits fob Mineral Dusts Substance Threshold Limit Values A.C.G.l.H. 1952 mppcf* -. Alundum.................................... Asbestos...................................... Carborundum................... /. Dust (nuisance, no free silica)'. Mica (below 5% free silica) -- Portland cement.................... . Silica--high (above 50% free SiO). Silica--medium (6 to 50% free SiO). Silica--low (below 5% free SiOi) Slate (below 5% free SiOi)................. Soapstone (below 5% free SiOi)____ laic. Total dust (below 5% free SiOi). * mppcf--million particles per cubic foot of air, standard light field count. 5 50 50 20 50 5 20 50 50 20 20 50 from a small amount of dust in suspension exposed to a source of ignition and the pressure and vibration it creates may be sufficient to dislodge large accumulations of dust on horizontal ledges or surfaces of the building and equipment, thereby creating a secondary explosion of great force. Inus the air conditioning engineer is involved for two reasons: (1) to obtain a movement of dust-laden air into exhaust hoods or openings, and through ventilating or pneumatic conveying ducts, in a manner that will prevent accumulation of highly flammable dust at points where it could ignite inside the equipment; and (2) to so design process ventilation as to prevent the escape of dust which might settle on horizontal surfaces and become a potential source of disaster at some distance from the dusty operation. (See Chapter 46). Intensity of a dust explosion depends upon: chemical and thermal Properties of the dust; particle size and shape; concentration in air; proporwon 0f inerf dust in the air; moisture content and composition of the air; size and temperature of the ignition source; and degree of dispersion of the ust cloud. Investigations on the explosibility of dusts require determina*on of the maximum pressure developed during explosion of a known air ncentration, as well as determination of the rate of pressure rise. In-