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                                                                                             1. INTRODUCTION 27
                h. 1 cp to lb/ft.h
                                                                     Operation and Management, Editions Technip, Paris,
                 i. 1 Pa · stocp        T1: IML         14:26     [15] Favennec, J. P., Petroleum Refining, Volume 5: Refinery
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                 j. 1 g/cm to lb/ft 3                                1998.
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                                    3
                         3
                    3
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                                                   ◦
                                                         ◦
                                                                     Resins, and Dipole Moment in Petroleum Fluids,” American
                  cSt.                                               Institute of Chemical Engineers Journal, Vol. 48, No. 11, 2002,
                b. Viscosity of 50 SFS at 99 C (210 F) to cSt.       pp. 2646–2662.
                                             ◦
                                       ◦
                c. Viscosity of 100 cSt at 38 C (100 F) to SUS    [18] Wauquier, J.-P., Petroleum Refining, Volume 1: Crude Oil,
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                                       ◦
                d. Viscosity of 10 cSt at 99 C (210 F) to SUS        Petroleum Products, Process Flowsheets, Editions Technip,
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            1.16. For each ton of a typical crude oil give the equivalent  Paris, 1995.
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                c. Standard cubic feet (scf) and sm of natural gas.  [20] Beck, R. J., “Demand Growth to Continue for Oil, Resume for
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