By B. C. Craft, M. Hawkins, Ronald E. Terry
The most up-tp-date, utilized booklet out there for petroleum engineers, geologists and others operating within the improvement and creation of oil and gasoline fields and people taken with the move of flooring water, this revised version displays the advances made in reservoir engineering calculation options. various actual international examples make clear the cloth, delivering the reservoir engineer with the sensible info to make utilized calculations.
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Extra info for Applied Petroleum Reservoir Engineering (Second Edition)
To find the compressibility of a gas from thc gas deviation factor curve. Given: The gas deviation (actor curve for a gas at 150°F, Fig. 6. SoluTIoN At 1000 psia, the slope dzldp is shown graphically in Fig. 83: as — 127 I I 1(Y6) 6=llS3xlO6psi the slope dz/dp is zero, so the At 2500 psia Cg = Fig. 6. Gas compressibility from Example 1 4) compressibility is simply: = 400 X 10 the gas deviation factor versus pressure plot (Sec introduction to Reservoir Engineenng 26 At 4500 psia the slope dz/dp is positive and as shown in Fig.
00) at reservoir pressure p and temperature T by Eq. 17) The constants in Eqs. 7 psia and 60°F only, and different constants must be calculated for other standards. 00533 cu ft of space in the reservoir at 3250 psia and 213°F. Because oil is usually expressed in barrels and gas in cubic feet, when calculations are made on combination reservoirs containing both gas and oil, either the oh volume must be expressed in cubic feet or the gas volume in barrels. 000949 bbl/SCF. 7) may also be used to calculate the dcnsity of a reservoir gas.
When laboratory analyses of the reservoir fluids arc not available, it is often possible to estimate with reasonable accuracy the solution gas-oil ratio. 8%. 2. FormatIon Volume Factor, B0 It was observed earlier that the solution gas causcs a considerable increase in the volume of the crude oil. 12 shows the variation in the volume of the reservoir liquid of the Big Sandy reservoir as a function of pressure at reservoir temperature of 160°F. 333 bbl/STB at 2500 psia. Below 2500 psia this liquid expansion continues but is masked by a much larger effect: the decrease in the liquid volume due to the release of gas from solution.
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