Static gas pressure gradient estimation

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Exploring for Oil and Gas Traps
Series Treatise in Petroleum Geology
Part Critical elements of the petroleum system
Chapter Formation fluid pressure and its application
Author Edward A. Beaumont, Forrest Fiedler
Link Web page
Store AAPG Store

The static gas pressure of a gas reservoir is a function of gas density. Static gas pressure gradients can be estimated if subsurface gas density is known or has been estimated.

Subsurface gas density is dependent on the ratio of its mass to its volume. Mass is related to the apparent molecular weight of the gas. Volume is related to pressure, temperature, and the apparent molecular weight of the gas.

At atmospheric pressures and temperatures, gas density can be estimated using the Ideal Gas Law. At subsurface temperatures and pressures, gas molecules are so close to one another that they interact enough to change ideal gas behavior. A compressibility factor, z, is added to the Ideal Gas Law to correct for subsurface gas behavioral changes.

Procedure: estimating gas pressure gradient[edit]

Follow this procedure to estimate the gas pressure gradient of a gas reservoir or potential gas reservoir.

    • If data are available on gas composition and formation temperature go to step 2.
    • If no data on gas composition or formation temperature are available, estimate gas density from the average gas chart (Figure 4) and go to Step 6.
  1. Determine the apparent molecular weight of the gas mixture.
  2. Read pseudoreduced temperature and pressure from Figure 1.
  3. If not already known, estimate compressibility factor, z , from Figure 2.
  4. Using information obtained from steps 2, 3, and 4, estimate gas density from Figure 3.
  5. Estimate gas pressure gradient using the following formula:
where:
Pgas grad = gas pressure gradient
ρgas = gas density

Determining molecular weight[edit]

The apparent molecular weight of a gas mixture is equal to

where:

  • MWapp = apparent molecular weight of the gas mixture
  • MFx = mole fraction of a component of the mixture
  • MWx = molecular weight of a component of the mixture

To practice, use these values for a gas mixture:

  • Composition = 50% methane, 25% ethane, 25% propane
  • Molecular weight of carbon (C) = 12
  • Molecular weight of hydrogen (H) = 1
  • Molecular weight of methane (CH4) = 12 + 4 = 16
  • Molecular weight of ethane (C2H6) = 24 + 6 = 30
  • Molecular weight of propane (C3H8) = 36 + 8 = 44

Determining z[edit]

The gas compressibility factor, z, for the gas reservoir of interest may already be known because it was measured. In this case, use that value. If z is not known, use the figure below to determine it from the pseudoreduced temperature and pressure determined from Figure 5-8. Figure 5-9 uses values determined for Figure 1

Determining subsurface gas density[edit]

We can determine gas density from the figure below, knowing reservoir pressure, reservoir temperature, gas compressibility factor, and apparent molecular weight.

Average natural gas[edit]

According to Gerhardt-Owens (1970), average natural gas estimated by Stephens and Spencer is considered to be 84.3% methane, 14.4% ethane, 0.5% carbon dioxide, and 0.8% nitrogen. However, many natural gas wells have produced almost pure methane (99%). Others have produced up to 88% ethane, 42% propane, 99% nitrogen, and 91% carbon dioxide. Using the accompanying average gas chart (Figure 5-11) is completely satisfactory is most cases.

Estimating subsurface gas density[edit]

We can estimate gas density from Figure 4. The chart assumes an average gas composition and was made using the following:

  • Formation temperature = temperature::80°F plus 0.8° per length::100 ft of depth
  • Formation fluid pressure gradient = 0.465 psi per ft of depth
  • Supercompressibility factors used from George G. Brown, University of Michigan

The formula used to determine reduction in volume and the accompanying increase in density of a given gas (because of changes in temperature and pressure) is

where:

  • V = volume, ft3
  • V = original volume ft Pa = pressure, psia
  • Pal = original pressure, psia
  • Ta = absolute temperature, °R
  • Tal = original absolute temperature, °R
  • z = supercompressibility factor
  • z1 = original supercompressibility factor

See also[edit]

References[edit]

  1. 1.0 1.1 1.2 Schowalter, T.T., 1979, Mechanics of secondary hydrocarbon migration and entrapment: AAPG Bulletin, vol. 63, no. 5, p. 723–760.

External links[edit]

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