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42                         CHAPTER TWO

                 50

                  0
                      C1     C2     C3    C4     C5    C6     C7    C8
                –50
               FP , °C  –100

               –150

               –200

               –250
                                         Carbon number
             FIGURE 2.6  Carbon number and flash point of natural gas hydrocarbons (up to octane, C 8 H 18 ).



             The fire point is the temperature to which the gas must be heated under the prescribed
           conditions of the method to burn continuously when the mixture of vapor and air is ignited
           by a specified flame (ASTM D92).
             From the viewpoint of safety, information about the flash point is of most significance
           at or slightly above the maximum temperatures (30 to 60°C, 86 to 140°F)) that may be
           encountered in storage, transportation, and use of liquid petroleum products, in either closed
           or open containers. In this temperature range the relative fire and explosion hazard can be
           estimated from the flash point. For products with flash point below 40°C (104°F) special
           precautions are necessary for safe handling. Flash points above 60°C (140°F) gradually
           lose their safety significance until they become indirect measures of some other quality.
             The flash point of a petroleum product is also used to detect contamination. A substan-
           tially lower flash point than expected for a product is a reliable indicator that a product has
           become contaminated with a more volatile product, such as gasoline. The flash point is also
           an aid in establishing the identity of a particular petroleum product.
             A further aspect of volatility that receives considerable attention is the vapor pressure
           of petroleum and its constituent fractions. The vapor pressure is the force exerted on the
           walls of a closed container by the vaporized portion of a liquid. Conversely, it is the force
           that must be exerted on the liquid to prevent it from vaporizing further (ASTM D323).
           The vapor pressure increases with temperature for any given gasoline, liquefied petroleum
           gas, or other product. The temperature at which the vapor pressure of a liquid, either a pure
           compound of a mixture of many compounds, equals 1 atmosphere (14.7 psi, absolute) is
           designated as the boiling point of the liquid.
             The flammable range is expressed by the lower explosive limit (LEL) and the upper
           explosive limit (UEL). The LEL is the concentration of natural gas in the air below which
           the propagation of a flame will not occur on contact with an ignition source. The LEL for
           natural gas is 5 percent by volume in air and, in most cases, the smell of gas would be
           detected well before combustion conditions are met. The UEL is the concentration of natu-
           ral gas in the air above which the propagation of a flame will not occur on contact with an
           ignition source. The natural gas UEL is 15 percent by volume in air.
             Explosions caused by natural gas leaks occur a few times each year. Individual homes,
           small businesses, and boats are most frequently affected when an internal leak builds up gas
           inside the structure. Frequently, the blast will be enough to significantly damage a building
           but leave it standing. Occasionally, the gas can collect in high enough quantities to cause a
           deadly explosion, disintegrating one or more buildings in the process.
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