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combusted, it produces sulfur oxides, which are a nuisance to
                    consumers. Both H 2 S and CO 2 are corrosive, especially in the
                    presence of water. Once removed, H 2 S could be commercially
                    utilized to produce sulfur.
                 3.  Heavy hydrocarbon separation: It is desirable to remove hydro-
                    carbons heavier than methane from natural gas, especially for fuel
                    gasses. Heavier hydrocarbons, specifically C þ  tend to condense,
                                                           3
                    forming two-phase flow and thus creating pipeline operating
                    problems.
                 Irrespective of the source of natural gas, the final specifications set for
            market sales requirements are usually the following [1]:


            H 2 S                    0.25–0.3 grain per 100ft 3
                                       (one grain ¼ 64.799 mg)
            Total sulfur             20 grains per 100 ft 3
            Oxygen (air)             0.2% by volume
            Carbon dioxide           2% by volume
            Liquefiable hydrocarbons  0.2 gal per 1000 ft 3
            Water content            7 lbs/MMSCF (in a 1000-psia gas line)
            Thermal heating value    1150 Btu/ft 3



                 Identification of the hydrocarbon constituents of crude oils and
            associated natural gas along with their corresponding commercial products
            are summarized in Table 1 [1].


            REFERENCE

            1. Abdel-Aal, H.K. Surface Petroleum Operations, Saudi Publishing & Distributing
               House, Jeddah, 1998.





















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