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1.6. Natural Gas Properties
               1.6.1. Chemical and Physical Properties

               Natural gas is colorless, odorless, tasteless, shapeless, and lighter than air (see Table 1.1). The
               natural gas after appropriate treatment for acid gas reduction, and moisture and hydrocarbon dew
               point adjustment, would then be sold within prescribed limits of pressure, heating value, and
               possibly Wobbe Index (often referred to as the Wobbe Number).
                 One of the principal uses of natural gas is as a fuel, and consequently, pipeline gas is normally
               bought and sold on the basis of its heating value that can be produced by burning the gas. The
               heating value of natural gas is variable and depends on its accumulations which are influenced by
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               the amount and types of gases they contain.   The gas industry always uses the gross heating value
               (frequently called higher heating value) in custody transfer. Obviously, the numerical difference
               between the two net and gross heating values is the heat of condensation of water at the specified
               conditions. Heating values for custody transfer are determined either by direct measurement, in
               which calorimetry is used, or by computation of the value on the basis of gas analysis (Gas
               Processors Association, 1996). The heating value of natural gas is measured in British thermal unit
               (Btu). A British thermal unit is the energy required to raise the temperature of 1 pound of water by
               1°F. For larger industrial customers, the abbreviations MBtu (1000 Btu) or MMBtu (million Btu) are
               more commonly used. Since meters measure volume and not energy content, a conversion factor of
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               1000 Btu/ft  is commonly used by gas companies to convert the volume of gas used to its heat
               equivalent, and thus calculate the actual energy use.
                 The Wobbe Index (defined as the gross heating value of the gas divided by the square root of the
               specific gravity) gives a measure of the heat input to an appliance through a given aperture at a
               given gas pressure. Using this as a vertical coordinate and the flame speed factor as the horizontal
               coordinate, a combustion diagram can be constructed for an appliance, or a whole range of
               appliances, with the aid of appropriate test gases. This diagram shows the area within which
               variations in the Wobbe Index and flame speed factor of gases may occur for the given range of
               appliances without resulting in either incomplete combustion, flame lift, or the lighting back of
               preaerated flames. This method of prediction of combustion characteristics is not sufficiently
               accurate to eliminate entirely the need for the practical testing of new gases.
                 Since natural gas as delivered to pipelines has practically no odor, the addition of an odorant is
               required by most regulations in order that the presence of the gas can be detected readily in case of
               accidents and leaks. This odorization is provided by the addition of trace amounts of some organic
               sulfur compounds to the gas before it reaches the consumer. The sulfur compound, a chemical
               odorant (a mercaptan also called a thiol with the general formula R–SH and the odor of rotten eggs)
               is added to natural gas so that it can be smelled if there is a gas leak. The standard requirement is
               that a user will be able to detect the presence of the gas by odor when the concentration reaches 1%
               of gas in air. Since the lower limit of flammability of natural gas is approximately 5%, this
               requirement is equivalent to one-fifth the lower limit of flammability. The combustion of these trace
               amounts of odorant does not create any serious problems of sulfur content or toxicity.

               Table 1.1

               Properties of Natural Gas

                Properties                                                               Value
                Relative molar mass                                                      17–20
                Carbon content, weight%                                                  73.3
                Hydrogen content, weight%                                                23.9
                Oxygen content, weight%                                                  0.4
                Hydrogen/carbon atomic ratio                                             3.0–4.0
                Relative density, 15°C                                                   0.72–0.81
                Boiling point, °C                                                        −162
                Autoignition temperature, °C                                             540–560
                Octane number                                                            120–130
                Methane number                                                           69–99
                Stoichiometric air/fuel ratio, weight                                    17.2
                Vapor flammability limits, volume %                                      5–15
                Flammability limits                                                      0.7–2.1


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