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Ignition Points

Gaseous Hydrogen Chloride. Cast Hon (qv), mild steel, and steel alloys are resistant to attack by dry, pure HCl at ambient conditions and can be used at temperatures up to the dissociation temperature of HCl. The corrosion rate at 300°C is reported to be 0.25 cm/yr and no ignition point has been found for mild steel at 760°C, at which temperature HCl is dissociated to the extent of 0.2%. [Pg.446]

Other early match-like devices were based on the property of various combustible substances mixed with potassium chlorate to ignite when moistened with strong acid. More important was the property of chlorates to form mixtures with combustibles of low ignition point which were ignited by friction (John Walker, 1827). However, such matches containing essentially potassium chlorate, antimony sulfide, and later sulfur (lucifers), mbbed within a fold of glass powder-coated paper, were hard to initiate and unreHable. [Pg.1]

The point at which enough heat has been added to start combustion is known as the ignition point. Once initiated, external heating sources are typically not required to maintain the combustion process, because most fuels release sufficient heat during the combustion process. [Pg.3]

According to the National Board of Fire Underwriters, activated carbons normally used for water treatment pose no dust explosion ha2ard and are not subject to spontaneous combustion when confined to bags, dmms, or storage bins (64). However, activated carbon bums when sufficient heat is appbed the ignition point varies between about 300 and 600°C (65). [Pg.533]

S has been approximated for flames stabili2ed by a steady uniform flow of unbumed gas from porous metal diaphragms or other flow straighteners. However, in practice, S is usually determined less directly from the speed and area of transient flames in tubes, closed vessels, soap bubbles blown with the mixture, and, most commonly, from the shape of steady Bunsen burner flames. The observed speed of a transient flame usually differs markedly from S. For example, it can be calculated that a flame spreads from a central ignition point in an unconfined explosive mixture such as a soap bubble at a speed of (p /in which the density ratio across the flame is typically 5—10. Usually, the expansion of the burning gas imparts a considerable velocity to the unbumed mixture, and the observed speed will be the sum of this velocity and S. ... [Pg.518]

Beyond the catalytic ignition point there is a rapid increase in catalytic performance with small increases in temperature. A measure of catalyst performance has been the temperature at which 50% conversion of reactant is achieved. For carbon monoxide this is often referred to as CO. The catalyst light-off property is important for exhaust emission control because the catalyst light-off must occur rehably every time the engine is started, even after extreme in-use engine operating conditions. [Pg.488]

Ignition of a flammable dust-air mixture is more difficult than with flammable vapour-air mixtures. A larger source of heat is required, and a larger volume of fuel must be heated to the ignition point. The same range of potential ignition sources is applicable as for air-vapour mixtures. [Pg.185]

The eight pressure-time histories are shown in Figures 3 and 4, whereas the flame speed along the y-direction from the ignition point is shown in Figure 5. The largest pressure is found at location p8 in Figure 4, and it amounts to approx. 0.2... [Pg.369]

This case uses the large cloud, as in Case 2, but the ignition point is moved to the center of the process line area (IGN2). [Pg.373]

Substances tluit are not combustible but may cause ignition if combustibles (e g.. Wet calcium oxide and wet unslaked lime) are present Substances having ignition points below ordinary temperatures (e.g.. Sodium and potassium in the presence of water)... [Pg.217]

Calculate the total burning time of tlie octane pool in Illustrative Exatiiple 3. Calculate tlie peak overpressure of a 50-pound TNT explosion at a distance 200 feet from the ignition point, if tlie peak oi erpressure at 1000 feel is 0.10 psi when 150 pounds of TNT is detonated. [Pg.247]

Thallium. Ignition point 208° (Ref 12) has greatest expl effect in lead plate test when primed with MF (Ref 7). It is a useful detonator at d 1.1—1.2g/cc, but usefullness decreases at higher d (Ref 7)... [Pg.72]

Preventing fire associated with low ignition point volatile organics... [Pg.615]


See other pages where Ignition Points is mentioned: [Pg.76]    [Pg.476]    [Pg.168]    [Pg.486]    [Pg.487]    [Pg.198]    [Pg.481]    [Pg.252]    [Pg.172]    [Pg.295]    [Pg.507]    [Pg.2]    [Pg.25]    [Pg.159]    [Pg.180]    [Pg.278]    [Pg.371]    [Pg.373]    [Pg.377]    [Pg.377]    [Pg.134]    [Pg.536]    [Pg.402]    [Pg.627]    [Pg.200]    [Pg.416]    [Pg.142]    [Pg.177]    [Pg.252]    [Pg.210]    [Pg.439]    [Pg.33]    [Pg.149]    [Pg.184]   
See also in sourсe #XX -- [ Pg.101 ]

See also in sourсe #XX -- [ Pg.174 , Pg.176 ]

See also in sourсe #XX -- [ Pg.254 ]

See also in sourсe #XX -- [ Pg.292 ]




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Flammable liquid Ignition point

Fuel oils ignition point

Relaxation times near ignition and extinction points

Self-ignition point

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