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Tishk International University Engineering Faculty Petroleum and Mining Engineering Department Petroleum Reservoir Engineering II Third Grade- Spring Semester 2020-2021 Lecture 10: Material Balance Equation (Gas Reservoirs) Instructor: Sheida Mostafa Sheikheh

Petroleum Reservoir Engineering II Lecture 10: Material

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Page 1: Petroleum Reservoir Engineering II Lecture 10: Material

Tishk International UniversityEngineering FacultyPetroleum and Mining Engineering Department

Petroleum Reservoir Engineering II

Third Grade- Spring Semester 2020-2021

Lecture 10: Material Balance Equation (Gas Reservoirs)

Instructor: Sheida Mostafa Sheikheh

Page 2: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  Reservoirs containing only free gas are termed gas reservoirs.

β–  Such a reservoir contains a mixture of hydrocarbons, which exists wholly in the

gaseous state.

β–  The mixture may be dry, wet, or condensate gas, depending on the composition of

the gas, along with the pressure and temperature at which the accumulation exists.

Page 3: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  If the reservoir temperature T is greater than the critical temperature 𝑇𝑐 of the

hydrocarbon fluid, the reservoir is considered as a gas reservoir.

β–  Based on the phase diagram and prevailing reservoir conditions, natural gases can

be classified into four categories:

1. Retrograde gas-condensate

2. Near-Critical gas-condensate

3. Wet gas

4. Dry gas

Page 4: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  Gas reservoirs may have water influx from a contiguous water-bearing portion of the

formation or may be volumetric (i.e., have no water influx)

β–  Volumetric Gas Reservoir: A volumetric gas reservoir is completely enclosed

by low-permeability or completely impermeable barriers and does not receive

pressure support from external sources, such as an encroaching aquifer.

β–  Non-volumetric Gas Reservoir: Gas reservoirs with water influx from an

aquifer are non-volumetric reservoirs and they produce under the pressure

support provided by the encroaching water.

Page 5: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  Most gas engineering calculations involve the use of gas formation volume factor 𝐡𝑔

and gas expansion factor 𝐸𝑔.

β€’ Gas Formation Volume Factor (𝐡𝑔): is defined as the actual volume occupied by n

moles of gas at a specified pressure and temperature, divided by the volume

occupied by the same amount of gas at standard conditions.

β€’ Gas Expansion Factor (𝐸𝑔): is simply the reciprocal of 𝐡𝑔.

Page 6: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  Through this lecture and the next lecture two approaches for estimating initial gas-

in-place G, gas reserves, and the gas recovery for volumetric and water-drive

mechanisms:

β€’ Volumetric method

β€’ Material balance approach

Page 7: Petroleum Reservoir Engineering II Lecture 10: Material

Content:

β–  The Material Balance Method

β€’ Form 1. In terms of p/z

β€’ Form 2. In terms of 𝐡𝑔

β–  Application of Material Balance Method

Page 8: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  The Material Balance Method:

β–ͺ If enough production-pressure history is available for a gas reservoir, the initial gas-

in-place G, the initial reservoir pressure 𝑝𝑖, and the gas reserves can be calculated

without knowing A, h, ΙΈ, or 𝑆𝑀.

β–ͺ This is accomplished by forming a mass or mole balance on the gas as:

𝑛𝑝 = 𝑛𝑖 βˆ’ 𝑛𝑓 βˆ’βˆ’ βˆ’ 1

Where 𝑛𝑝= moles of gas produced

𝑛𝑖= moles of gas initially in the reservoir

𝑛𝑓= moles of gas remaining in the reservoir

Page 9: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  The Material Balance Method:

β–ͺ Representing the gas reservoir by an

idealized gas container, as shown

schematically in the figure, the gas moles

in equation (1) can be replaced by their

equivalents using the real gas law to give:

𝑝𝑠𝑐𝐺𝑝

𝑅𝑇𝑠𝑐=

𝑝𝑖𝑉

π‘§π‘–π‘…π‘‡βˆ’

𝑝 𝑉 βˆ’ π‘Šπ‘’ βˆ’ π‘Šπ‘

π‘§π‘…π‘‡βˆ’βˆ’ βˆ’(2)

Page 10: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  The Material Balance Method:

𝑝𝑠𝑐𝐺𝑝

𝑅𝑇𝑠𝑐=

𝑝𝑖𝑉

π‘§π‘–π‘…π‘‡βˆ’

𝑝 𝑉 βˆ’ π‘Šπ‘’ βˆ’ π‘Šπ‘

π‘§π‘…π‘‡βˆ’βˆ’ βˆ’(2)

Where 𝑝𝑖= initial reservoir pressure 𝐺𝑝= cumulative gas production, scf

p= current reservoir pressure V= original gas volume, 𝑓𝑑3

𝑧𝑖= gas deviation factor at 𝑝𝑖 z= gas deviation factor at p

𝑀𝑒= cumulative water influx, 𝑓𝑑3 𝑀𝑒= cumulative water production, 𝑓𝑑3

T= temperature, Β°R

β–ͺ Equation (2) is essentially the general material balance equation (MBE).

Page 11: Petroleum Reservoir Engineering II Lecture 10: Material

Gas Reservoirs

β–  The Material Balance Method:

β–ͺ Equation (2) can be expressed in numerous forms depending on the type of the application

and the driving mechanism.

β–ͺ In general, dry gas reservoirs can be classified into two categories:

β€’ Volumetric gas reservoirs

β€’ Water-drive gas reservoirs

Page 12: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

β–  For a volumetric reservoir and assuming no water production, equation (2) is reduced to:

𝑝𝑠𝑐𝐺𝑝

𝑇𝑠𝑐=

𝑝𝑖

𝑧𝑖𝑇𝑉 βˆ’

𝑝

𝑧𝑇𝑉 βˆ’βˆ’ βˆ’ 3

β–  Equation (3) is commonly expressed in the following two forms:

Form 1. In terms of p/z

Form 2. In terms of 𝐡𝑔

Page 13: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

β–  Rearranging equation (3) and solving for p/z gives:

𝑝

𝑧=

𝑝𝑖

π‘§π‘–βˆ’

𝑝𝑠𝑐𝑇

𝑇𝑠𝑐𝑉𝐺𝑝 βˆ’βˆ’ βˆ’(4)

Page 14: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

β–  Equation (4) is an equation of a straight

line when (p/z) is plotted versus the

cumulative gas production 𝐺𝑝, as shown

in the figure.

β–  This straight-line relationship is perhaps

one of the most widely used relationships

in gas-reserve determination.

Page 15: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

β–  The straight-line relationship provides the

engineer with the reservoir

characteristics:

β€’ Slope of the straight line is equal to:

π‘ π‘™π‘œπ‘π‘’ =𝑝𝑠𝑐𝑇

π‘‡π‘ π‘π‘‰βˆ’βˆ’ βˆ’(5)

Page 16: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

β–  The straight-line relationship provides the

engineer with the reservoir

characteristics:

β€’ The original gas volume V can be

calculated from the slope and used to

determine the areal extent of the

reservoir from:

𝑉 = 43,560 π΄β„Žπœ‘ 1 βˆ’ 𝑆𝑀𝑖

Where A is the reservoir area in acres.

Page 17: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

β–  The straight-line relationship provides the

engineer with the reservoir

characteristics:

β€’ Intercept at 𝐺𝑝 = 0 gives ΀𝑝𝑖 𝑧𝑖

β€’ Intercept at p/z=0 gives the gas initially in

place G in scf

β€’ Cumulative gas production or gas

recovery at any pressure

Page 18: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

Example: A volumetric gas reservoir has the following production history.

The following data are also available:

ΙΈ= 13% 𝑆𝑀𝑖 = 0.52 A=1060 acres h= 54 ft T=164 Β°F

Calculate the gas initially in place volumetrically and from the MBE.

Page 19: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

Solution:

Step 1. Calculate 𝐡𝑔𝑖 from equation (1):

𝐡𝑔𝑖 = 0.02827(0.869)(164 + 460)

1798= 0.00853 𝑓𝑑3/𝑠𝑐𝑓

Step 2. Calculate the gas initially in place volumetrically by applying equation (3):

𝐺 = 43,5601060 54 0.13 1 βˆ’ 0.52

0.00853= 18.2 𝑀𝑀𝑀𝑠𝑐𝑓

Page 20: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 1. In terms of p/z:

Solution:

Step 3. Plot p/z versus 𝐺𝑝 as shown in

following figure and determine G.

G= 14.2 MMMscf

This checks the volumetric calculations.

Page 21: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 2. In terms of π‘©π’ˆ:

β–  From the definition of the gas formation volume factor, it can be expressed as:

𝐡𝑔𝑖 =𝑉

𝐺

β–  Combining the above expression with 𝐡𝑔 equation:

𝐡𝑔 =𝑝𝑠𝑐

𝑇𝑠𝑐

𝑧𝑇

𝑝= 0.02827

𝑧𝑇

𝑝

Gives:

𝑝𝑠𝑐

𝑇𝑠𝑐

𝑧𝑖𝑇

𝑝𝑖=

𝑉

πΊβˆ’βˆ’ βˆ’(6)

Page 22: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 2. In terms of π‘©π’ˆ:

𝑝𝑠𝑐

𝑇𝑠𝑐

𝑧𝑖𝑇

𝑝𝑖=

𝑉

πΊβˆ’βˆ’ βˆ’(6)

Where V= volume of gas originally in place, 𝑓𝑑3

G= volume of gas originally in place, scf

𝑝𝑖= original reservoir pressure

𝑧𝑖= gas compressibility factor at 𝑝𝑖

Page 23: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 2. In terms of π‘©π’ˆ:

β–  Combining equation (6) with equation (3):

𝑝𝑠𝑐

𝑇𝑠𝑐

𝑧𝑖𝑇

𝑝𝑖=

𝑉

𝐺

𝑝𝑠𝑐𝐺𝑝

𝑇𝑠𝑐=

𝑝𝑖

𝑧𝑖𝑇𝑉 βˆ’

𝑝

𝑧𝑇𝑉

Gives:

𝐺 =𝐺𝑝 𝐡𝑔

𝐡𝑔 βˆ’ π΅π‘”π‘–βˆ’βˆ’ βˆ’(7)

Page 24: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 2. In terms of π‘©π’ˆ:

Example: after producing 360 MMscf of gas from a volumetric gas reservoir, the pressure has

declined from 3,200 psi to 3,000 psi, given:

𝐡𝑔𝑖 = 0.005278 ΀𝑓𝑑3 𝑠𝑐𝑓

𝐡𝑔 = 0.005390 ΀𝑓𝑑3 𝑠𝑐𝑓

a. Calculate the gas initially in place.

b. Recalculate the gas initially in place assuming that the pressure measurements were

incorrect, and the true average pressure is 2,900 psi. The gas formation volume factor at

this pressure is 0.00558 ΀𝑓𝑑3 𝑠𝑐𝑓.

Page 25: Petroleum Reservoir Engineering II Lecture 10: Material

Volumetric Gas Reservoirs

Form 2. In terms of π‘©π’ˆ:

Solution:

a. Using equation (7), calculate G:

𝐺 =𝐺𝑝 𝐡𝑔

𝐡𝑔 βˆ’ 𝐡𝑔𝑖=

360 βˆ— 106(0.00539)

0.00539 βˆ’ 0.005278= 17.325 𝑀𝑀𝑀𝑠𝑐𝑓

b. Recalculate G by using the correct value of 𝐡𝑔:

𝐺 =360 βˆ— 106(0.00668)

0.00558 βˆ’ 0.005278= 6.652 𝑀𝑀𝑀𝑠𝑐𝑓