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VX Theory of Operation

The document provides information about Vx technology for multiphase flow measurement. It describes the main components of the Vx system, including the access port, venturi section, and outlet pipe. It also explains the venturi equation, gamma detection system, and how the Vx uses a venturi and gamma system to measure total mass flowrate and calculate phase fractions and flowrates at both line conditions and standard conditions.
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0% found this document useful (0 votes)
50 views15 pages

VX Theory of Operation

The document provides information about Vx technology for multiphase flow measurement. It describes the main components of the Vx system, including the access port, venturi section, and outlet pipe. It also explains the venturi equation, gamma detection system, and how the Vx uses a venturi and gamma system to measure total mass flowrate and calculate phase fractions and flowrates at both line conditions and standard conditions.
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as PPTX, PDF, TXT or read online on Scribd
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MPFM Vx Training

Vx Theory of Operation

Oct 2019
Schlumberger-Private
Vx Technology Presentation
VX MAIN COMPONENTS

• Access Port

• Venturi Section :
• Detector Assembly
• Ba-133 Source Assembly

• Blind Tee
• Outlet Pipe

Schlumberger-Private
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

Schlumberger-Private
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

Schlumberger-Private
Flowrates Measurement
VENTURY EQUATION

d 1
   2 P  P   gHv 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)

Schlumberger-Private
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 ed  
Nx: number of counts measured
No: number of counts in vacuum
d: distance X O
ν : mass attenuation
ρ: density

Schlumberger-Private
Flowrates Measurement
GAMMA SYSTEM EQUATION
N X  N ed
O
   Oil  OilOil  Water WaterWater   Gas  GasGas

 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

Schlumberger-Private
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)

Schlumberger-Private
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

Schlumberger-Private
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

Schlumberger-Private
Question ?

Schlumberger-Private
Recap with

Schlumberger-Private
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
Schlumberger-Private
BSW is calculated in standard conditions?

1. True
2. False
3. Possibly

0% 0% 0%

0 of 1 2 3
10

Answer Now
17
Schlumberger-Private
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
Schlumberger-Private

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