pipelines & flow assurance

23
Pipelines & Flow Assurance

Upload: others

Post on 08-May-2022

26 views

Category:

Documents


0 download

TRANSCRIPT

Page 1: Pipelines & Flow Assurance

Pipelines & Flow Assurance

Page 2: Pipelines & Flow Assurance

Christophe Meynet

Senior CFD Consultant,

Wood Group Kenny

Page 3: Pipelines & Flow Assurance

Using CFD To Predict Pig BehaviourChristophe Meynet, Senior CFD Consultant, Aberdeen

Page 4: Pipelines & Flow Assurance

4 - www.woodgroup.com

1. Introduction

2. CFD Modeling

3. Output and results

4. Conclusions & Way Forward

Agenda

Page 5: Pipelines & Flow Assurance

5 - www.woodgroup.com

• Pigging is necessary for various reasons:

• Cleaning

• Inspection

• Pre-commissioning

• Pigs can be made of different materials

• The main risk with pigging is the pig getting stuck

1. Introduction – About pigging

Page 6: Pipelines & Flow Assurance

6 - www.woodgroup.com

1. Introduction – Tie in location

10”

24”

34”

NEW FIELD• Added problem – 10” pig passing

through 24” then 34” pipeline

• CFD can be used to assist pig

manufacturer during design to

confirm passage of pig

Page 7: Pipelines & Flow Assurance

7 - www.woodgroup.com

1. Introduction – Design requirements – Weak link

24”

10”

24” PIG

HOT TAP CONNECTION

“LIP SHAPED” INTERSECTION

ABILITY TO SNAP IN TWO

RISK FOR THE PIG TO GET STUCK

Page 8: Pipelines & Flow Assurance

8 - www.woodgroup.com

1. Introduction – Design requirements – Density

“DEAD LEG”

PIG LIGHTER

THAN FLUID

PIG NEEDS TO BE HEAVIER THAN

CARRYING FLUID

Page 9: Pipelines & Flow Assurance

9 - www.woodgroup.com

1. Introduction – Design requirements – Onset velocity

MINIMUM FLOW RATE TO DISPLACE PIG?

Page 10: Pipelines & Flow Assurance

10 - www.woodgroup.com

1. Introduction – Design requirements – Wye pieces

?

“DEAD LEG”

Page 11: Pipelines & Flow Assurance

11 - www.woodgroup.com

1. Introduction – Design requirements – Wye pieces

?

Page 12: Pipelines & Flow Assurance

12 - www.woodgroup.com

2. CFD models – Individual pigs

VELOCITY INLET

OUTLET

Page 13: Pipelines & Flow Assurance

13 - www.woodgroup.com

2. CFD models – Wye

CAD MODEL PROVIDED

CFD MODEL

VELOCITY INLET

OUTLET

Page 14: Pipelines & Flow Assurance

14 - www.woodgroup.com

3. Results – Individual pigsF

IXE

D V

EL

OC

ITY

IN

LE

T

VELOCITY MAGNITUDE

Page 15: Pipelines & Flow Assurance

15 - www.woodgroup.com

3. Results – Individual pigs

0.0

0.2

0.4

0.6

0.8

1.0

1.2

1.4

1.6

0

10

20

30

40

50

60

0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1L

IFT

FO

RC

E [

N]

DR

AG

FO

RC

E [

N]

INLET VELOCITY [m/s]

DRAG

LIFT

FLIFT

FDRAG

FIX

ED

VE

LO

CIT

Y I

NL

ET

Page 16: Pipelines & Flow Assurance

16 - www.woodgroup.com

3. Results – Friction Theory

AXIAL FORCE

NORMAL FORCE

𝑓𝑠𝑡𝑎𝑡𝑖𝑐 = 𝛼𝑓𝑛𝑜𝑟𝑚𝑎𝑙 𝑓𝑘𝑖𝑛𝑒𝑡𝑖𝑐 = 𝛽𝑓𝑛𝑜𝑟𝑚𝑎𝑙

𝛼 >> 𝛽

Page 17: Pipelines & Flow Assurance

17 - www.woodgroup.com

3. Results – Frictions Theory

𝑓𝑛𝑜𝑟𝑚𝑎𝑙 = 𝑚𝑔 − 𝜌𝑓𝑙𝑢𝑖𝑑𝑉𝑑𝑖𝑠𝑝𝑙𝑎𝑐𝑒𝑑

G

𝑚𝑔

𝜌𝑓𝑙𝑢𝑖𝑑𝑉𝑑𝑖𝑠𝑝𝑙𝑎𝑐𝑒𝑑

Page 18: Pipelines & Flow Assurance

18 - www.woodgroup.com

3. Results – Onset velocity

𝑓𝑠𝑡𝑎𝑡𝑖𝑐 𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑠

PREDICTED ONSET VELOCITY

Page 19: Pipelines & Flow Assurance

19 - www.woodgroup.com

3. Results – Onset velocity

𝑓𝑠𝑡𝑎𝑡𝑖𝑐 𝑓𝑟𝑖𝑐𝑡𝑖𝑜𝑛𝑠

MEASURED ONSET VELOCITY

𝑓𝑠𝑡𝑎𝑡𝑖𝑐

𝛼“Static

friction factor”

Page 20: Pipelines & Flow Assurance

20 - www.woodgroup.com

3. Results – Wye

LOCAL COORDINATES

ATTACHED TO PIG COG

Page 21: Pipelines & Flow Assurance

21 - www.woodgroup.com

3. Results – Wye

-4

-3.5

-3

-2.5

-2

-1.5

-1

-0.5

0

-0.05

-0.04

-0.03

-0.02

-0.01

0

0.01

0.02

0.03

0.04

0.05

0 0.2 0.4 0.6 0.8 1 1.2 1.4F

OR

CE

[N

]

MO

ME

NT

[N

.m]

OFFSET [m]

M_x_local [N.m] M_y_local [N.m]

F_x_local [N] F_z_local [N]

VELOCITY MAG.

Page 22: Pipelines & Flow Assurance

22 - www.woodgroup.com

4. Conclusions & Way forward

• CFD was successfully used to improve knowledge on how the pig behaved when going through various piping elements

• Such study can be done in a cost efficient manner and identify potential “stuck pig” risks during pigging operations

• Testing rigs and procedures should be adapted to improve the accuracy of friction factors estimates which will improve onset velocity predictions

Page 23: Pipelines & Flow Assurance

23 - www.woodgroup.com

Thanks for listening… Any question ?