Ees nleliees show are not that the fluid property calculations described later great, however, dh...
ees nleliees show are not that the fluid property calculations described later great, however, dhe differen dne diff dhis field operating conditions ter should use the results of a separator test performed at these differences 10-3%Data from a separator test on a black oil aregiven Below. Note that the volume of separator liquid was measured at separator pressure and temperature before it was released to the stock tank. Prepare a separator test table for the reservoir fluid study Volume of oil at bubble-point pressure and reservoir temperature182.637 cc Volume of separator liquid at 100 psig and 75°F 131.588 cc Volume stock-tank oil at 0 psig 75°F = 124.773 c Volume of stock-tank oil at 0 psig and 60 F - 123.906 cc Volume of gas removed frorn separator = (0.52706 sof Volume of gas removed from stock tank - 0.07139 sef Specific gravity of stock-tank oil 0.8217 Specific gravity of separator gas -0.786 Specific gravity of stock-tank gas 1.363
ees nleliees show are not that the fluid property calculations described later great, however, dhe differen dne diff dhis field operating conditions ter should use the results of a separator test performed at these differences 10-3%Data from a separator test on a black oil aregiven Below. Note that the volume of separator liquid was measured at separator pressure and temperature before it was released to the stock tank. Prepare a separator test table for the reservoir fluid study Volume of oil at bubble-point pressure and reservoir temperature182.637 cc Volume of separator liquid at 100 psig and 75°F 131.588 cc Volume stock-tank oil at 0 psig 75°F = 124.773 c Volume of stock-tank oil at 0 psig and 60 F - 123.906 cc Volume of gas removed frorn separator = (0.52706 sof Volume of gas removed from stock tank - 0.07139 sef Specific gravity of stock-tank oil 0.8217 Specific gravity of separator gas -0.786 Specific gravity of stock-tank gas 1.363