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Phase Behaviour dan Characteristics Gas
Single-component system
Two-component system
Two-component system
Multi-component system
Temperature
Pre
ssu
re liquid
gas
C
Cricondenbar
Cricondentherm
Definitions:
Cricondenbar: the pressure above which two phases can no longer exist.
Cricondentherm: the temperature above which two phases do not exist
Additional points:
Phase Diagram (Basic Definitions)
Phase Diagram (Basic Definitions)
Temperature
Pre
ssu
re
liquid
gas
100% liquid(0% gas)
80%60%
40%
20%
C
0% liquid(100% gas)
Pressure Temperature Plane
Definitions:
1. Bubble-point line: the point where the first bubble is formed during pressure decrease at constant temperature.
2. Dew-point line: the point where the first liquid drop is formed during pressure increase at constant temperature.
Note: Pure-component system can be regarded as a special case of two-component system where two-phase region shrinks to form a line.
Critical point: the point where the bubble-point line meets the dew-point line
Temperature
Pre
ssu
re
Single phaseliquid
gas
CB
ub
ble
-po
int
(pre
ssu
re)
line
Dew
-po
int
(pre
ssu
re)
line
Single phaseGas
Phase Diagram (Basic Concepts)
Temperature
Pre
ssu
re liquid
gas
C
“Retrograde condensation”
Liq
uid
-mixtu
re-gas
Path A Path B Definitions:
Retrograde condensation: phenomenon that the dew point line is crossed (i.e., from gas phase to liquid) as pressure decreases rather than increases.
Because this is the reverse of normal behaviour, it is called “retro”.
Basic definitions (cont.)
Reservoir Classification Oil reservoir
In general Tres<Tc of reservoir fluid
Gas reservoir In general,
Tres>Tc of reservoir fluid (hydrocarbon systems)
Oil Reservoir
Under-saturated oil reservoir initial reservoir
pressure, pi > the bubble-point pressure, pb of the reservoir fluid
Saturated oil reservoir pi = pb
Gas-cap reservoir or two phase reservoir pi < pb
Note The appropriate quality
line gives the ratio of volume of liquid (oil) to volume of gas
Gas ReservoirDry gas reservoir
initial reservoir temperature higher than cricondentherm temperature (light components)
even at low pressure (separator) and temperature, fluid is 100% gas
Wet gas reservoir initial reservoir temperature
higher than cricondentherm temperature
But even at low pressure (separator) and temperature, some gas condensate to liquid
Retrograde gas-condensate reservoir Reservoir temperature lies
between Tc and Tcri (Tc<Tr<Tcr)
Near critical gas-condensate Reservoir temperature is
nearly equal to critical temperature of fluid (Tr ~Tc)
Dry-gas reservoir
Wet-gas reservoir
Retrograde-gas condensate reservoir
Volatile-oil reservoir
Black-oil reservoir
Typical Hydrocarbon Mixture Compositions (mol %)
C1 88.7
C2
C3
i-C4
n-C4i-C5
n-C5
C6
C7+
6.0
3.0
0.5
0.8
0.3
0.3
0.2
0.2
96.303.00
0.40
0.07
0.10
0.02
0.02
0.02
0.00
72.710.0
6.0
1.0
1.5
0.8
1.0
2.0
5.0
66.79.0
6.0
0.8
2.5
0.8
1.2
2.0
11.0
52.65.0
3.5
0.7
1.1
0.4
0.4
0.9
27.9
DryGas
WetGas
RetrogradeGas Cond.
VolatileOil
BlackOil
Component
plus inorganics: N2, CO2, H2O, H2S
Field Identification
BlackOil
VolatileOil
RetrogradeGas
WetGas
DryGas
InitialProducingGas/LiquidRatio, scf/STB
<1750 1750 to3200
> 3200 > 15,000* 100,000*
Initial Stock-Tank LiquidGravity, API
< 45 > 40 > 40 Up to 70 NoLiquid
Color of Stock-Tank Liquid
Dark Colored LightlyColored
WaterWhite
NoLiquid
*For Engineering Purposes
Karakteristik Gas Ideal Gas Law Pada tekanan rendah, gas mengikuti persamaan Gas Ideal:
PV = nRT
Dimana: R = Universal gas constant , 10,732 psia cuft/lb-mole oR n = number of moles of the gas = m/M m = mass of gas; lb M = Molecular weight of gas lbm/lb-mol Standard conditions are generally defined as 14.7 psia and 60oF. 1 mole of any ideal gas at standard conditions occupies a volume of 379 Cu. ft. or 22.4 litres
Real Gas Persamaan gas ideal umumnya hanya berlaku untuk gas yang mendekati kondisi atmosfir. Gas di reservoir terdiri dari berbagai macam komposisi gas dan tekanan serta temperatur
tinggi; sehingga persamaan gas ideal tidak berlaku lagi. Persamaan gas nyata merupakan koreksi terhadap persamaan gas ideal
PV = z n RT.
Dimana
Sifat Fisik Gas Alam
Gas alam merupakan campuran gas dimana unsur utamanya adalah metana; terdiri dari gas hidrokarbon dan impurities.
Impurities adalah gas yang bukan hidrokarbon seperti : CO2, H2S, N2 dsb
Sifat fisik gas alam antara lain adalah: - Berat Molekul - Densitas - Specific Gravity - Faktor Deviasi gas - Viscositas Gas - Compressibilitas gas - Gas Formation Volume Factor dan Expansion Factor - Water Vapor Content - Two phase System
- API Gravity - Gas Gravity - Z factor
Berat Molekul gas
Berat Molekul gas dapat ditentukan berdasarkan persamaan:
Ma = Berat molekul gas campuran Yi = Fraksi mol gas – i Mi = Berat molekul gas –i
Contoh:
Berat molekul gas diatas adalah 17.083 lbm/lb-mol.
Densitas dan Specific Gravity Gas
Berdasarkan persamaan gas nyata : PV = n Z RT ; dimana n = m/M
Jadi PV = m ZRT/M Sedangkan densitas adalah m/V; sehingga dari persamaan diatas :
Faktor Deviasi Gas, Z
Pengukuran Z1. Di laboratorium 2. Grafik korelasi dan persamaan
Pengukuran Z di laboratorium
Penentuan Z berdasarkan Grafik Korelasi / Persamaan
Penentuan Z berdasarkan Grafik Korelasi / Persamaan memerlukan faktor pseudo reduced pressure (Ppr) dan pseudo reduced temperature (Tpr) .
Ppr dan Tpr didefinisikan sebagai
Sedang Tpc dan Ppc didefinisikan sebagai:
Apabila komposisi gas tidak diketahui, Tpc dan Ppc dapat ditentukan dari grafik dibawah ini:
Apabila kadar impurities > 5 %
Contoh
Compressibilitas
Viskositas Gas
Korelasi yang umum digunakan adalah korelasi Carr, Kobayashi
dan Burrows.
Contoh:
Tentukanlah viskositas gas reservoir pada kondisi P = 2500 psia dan T = 180 oF.
Gas Formation Volume Factor (Bg)
The gas formation volume factor (Bg) is defined as the volume of gas in the reservoir divided by the volume of gas at standard conditions.
Bg = (reservoir gas volume)/(standard conditions gas volume).
Gas Formation Volume Factor (Bg)
Jika Tekanan reservoir = 2900 psia dan Temperatur reservoir = 190 oF; tentukanlah: SG, Z, Viskositas Gas, Cg dan Bg
Komponen Fraksi MolC1 0,784C2 0,028C3 0,007i-C4 0,0008n-C4 0,0005i-C5 0,0008n-C5 0,0003C6 0,0006N2 0,005CO2 0,021H2S 0,152
Dari suatu reservoir gas diketahui SG gas = 0.7 dan terdapat impurities H2S = 5 % mole dan CO2 = 12 % mole.
Jika Tekanan reservoir = 2900 psia dan Temperatur reservoir = 190 oF; tentukanlah:
SG, Z, Viskositas Gas, Cg dan Bg
Real Gas
PV = Z n RT
Persamaan Van der Walls
Standard Units of Defined Calorific ValuesBarrel of Oil Equivalent (b.o.e.) : a hypothetical “barrel of oil” with an average heat content of 5.8 x 106 Btu gross. Ton of Oil Equivalent (t.o.e.) : a hypothetical “ton of oil” with an average heat content of 43 x 106 Btu gross. Metric Tonne Coal Equivalent (m.t.c.e.) : a hypothetical “metric tonne of coal” with an average heat content of 27.337 x 106 Btu gross, i.e. ( 12,400 Btu/lb x 2204.62 ).
Std. Fuel Units ft3 Natural Gas m3 Natural Gas
1 b.o.e. 5,800 155.50
1 t.o.e. 43,000 1152.82
1 m.t.c.e. 27,337 732.90
1 ton fuel oil equiv. 41,400 1109.92
Natural Gas Equivalents of Various Fuels