MPFM Vx Training
Vx Theory of Operation
Oct 2019
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Vx Technology Presentation
VX MAIN COMPONENTS
• Access Port
• Venturi Section :
• Detector Assembly
• Ba-133 Source Assembly
• Blind Tee
• Outlet Pipe
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Flowrates Measurement
SIMPLIFIED FLOWCHART
Total Mass Flowrate
150
100
Flowrates at Line Condi- Flowrates At Standard Condi-
50 tions 150 tions
0 150
100
PVT 100
Series 1
50
Mode 50
l
Phase Fraction 0 0
Oil Water Gas Oil Water Gas
Oil Gas Water
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Flowrates Measurement
VENTURY EQUATION
D V
P1
1
P1 + ½ r V12 = P2 + r g Hv+ ½ r V22
1
Energy conservation
(Bernoulli)
D2
V
P2 Mass conservation Qm = ¼ p D22 V2 r = ¼ p D12 V1 r
2
(Bernoulli)
b = D2 / D1
Hv
Beta Ratio
V
D P1
1
1
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Flowrates Measurement
VENTURY EQUATION
d 1
2 P P gHv ρ
2
Q C
f
4 1
total mass 1 2 mix mix
4
Applied to real multiphase flow, with some compressibility, energy losses due to turbulences
(depending on the geometry of the venturi) :
Discharge coefficient = f(viscosity, GVF)
Expansion Factor=f(rgas, rliq @ LC, GVF)
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Flowrates Measurement
GAMMA SYSTEM
When passing through matter, gamma looses energy due to collisions with atomic.
Ba133 gamma ray spectrum shows 3 energy level peaks.
d
Counts
Detector
radioactive source:
emits -ray photons Venturi 32 81 356
throat Energy Level (Kev)
N N ed
Nx: number of counts measured
No: number of counts in vacuum
d: distance X O
ν : mass attenuation
ρ: density
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Flowrates Measurement
GAMMA SYSTEM EQUATION
N X N ed
O
Oil OilOil Water WaterWater Gas GasGas
d 0le
N Xle N eO
d 0he
N Xhe N eO
d ( o . o .ole w w w
le le )
g g g
N xle Nole e
d ( o . o .ohe w w w
he he )
g g g
N xhe Nohe e
o w g 1
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Flowrates Measurement
SOLUTION TRIANGLE -1/d Ln (Nle / Nvacuumle) 0
Low Energy Linear attenuation for a triphasic fluid
aoronole+agrgngle+awrwnwle
High Energy Linear attenuation for a triphasic fluid
-1/d * Ln (Nle / N0le) =
ao.nole.ro + ag.ngle.rg + aw.nwle.rw
aoronohe+agrgnghe+awrwnwhe
-1/d * Ln (Nhe / N0he) = Gas (ag=1,aw=ao=0)
ao.nohe.ro + ag.nghe.rg + aw.nwhe.rw
-1/d Ln (Nhe / Nvacuumhe)
Any mixture of these 3 single
phases will be described by a
point within this “Solution
B
Triangle”
WLR = OA/OW
GVF = OB/OG
Oil (ao=1,ag=aw=0)
Water A
(aw=1,ag=ao=0)
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Flowrates Measurement
PVT MODEL
Line conditions Standard conditions
Density: ρo, ρw, ρg
Volume Factor: bo, bw, bg
Stock tank Gas Oil Ratio: Rst (GOR2)
Gas Phase Condensate Gas Ratio: rgmp (CGR)
Stock Tank Gas Water Ratio: Rwst
Liquid viscosity: µ
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Conclusions
The high frequency Gamma Detector measures the phase fractions, based on nuclear
linear attenuations
The Vx venturi measures the total mass rate
Primary Output:
Qmass and r mixture
Phase hold-ups
Gas Volume Fraction (GVF)
WLR
Secondary Output:
qgas at Line conditions
qoil at Line conditions
qwater at Line conditions
Final Output
Computation of flow rates from line conditions to standard conditions using VX
Fluid Properties Models
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Question ?
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Recap with
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Mixture density is at
1. Line condition
2. Standard condition
3. Separator condition
0% 0% 0%
1 2 3
0 of
10
Answer Now
15
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BSW is calculated in standard conditions?
1. True
2. False
3. Possibly
0% 0% 0%
0 of 1 2 3
10
Answer Now
17
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Which of the following is Vx primary output?
1. Flow rates at Line
condition
2. Flow rates at Standard
condition
3. WLR, GVF, hold-ups
0% 0% 0%
1 2 3
0 of
10
Answer Now
21
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