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Estimation of Burst Pressure of Corroded Pipeline Using Finite Element Analysis (FEA)

by

Mohamad Armiya bin Zahari

Dissertation submitted in partial fulfillment of the requirement for the

Bachelor ofEngineering (Hons) (Mechanical Engineering)

SEPTEMBER 2011

Universiti Teknologi PETRONAS Bandar Seri Iskandar

31750Tronoh Perak Darul Ridzuan

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CERTIFICATION OF APPROVAL

Estimation of Burst Pressure of Corroded Pipeline Using Finite Element Analysis (FEA)

Appr ved b ,

by

Mohamad Anniya bin Zahari

A project dissertation submitted to the Mechanical Engineering Programme

Universiti Teknologi PETRONAS in partial fulfillment of the requirement for the

BACHELOR OF ENGINEERING (Hons) (MECHANICAL ENGINEERING)

/

UNIVERSITI TEKNOLOGI PETRONAS TRONOH, PERAK

SEPTEMBER 2011

I

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CERTIFICATION OF ORIGINALITY

This is to certify that I am responsible for the work submitted in this project, that the original work is my own except as specified in the references and acknowledgements, and that the original work contained herein have not been undertaken or done by unspecified sources or persons.

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ABSTRACT

Pipelines are used to transmit fluid from one point to another. One major concern of maintaining pipelines integrity is failure due to corrosion defects. Corrosion is one of the common defects in pipes which can be observed externally or internally. Several methods and codes had been established to provide solutions in assessing the corroded pipes. This includes the assessment of remaining strength of the corroded pipeline which has been used for used in decades, ASME B31G. This code is referred in evaluation of metal loss in pressurized pipes and piping systems. Another code, the recommended practice DNV-RP-FlOl is used to evaluate the remaining strength of corroded pipes which has single defect, multiple defects and complex shape defects.

This study is associated with the process to estimate the burst pressure of corroded pipeline by using Finite Element Analysis (FEA). The corroded pipe undergoes UT- Scan and the thickness along the pipe's internal surface is measured and the corrosion profile is plotted. FEA is used to resemble the experimental procedure of actual burst test. Several models are built and simulated by considering defect shape, defect depth and analysis type as parameter to distinguish every simulations. All models are properly constraint and pressurized internally thus, the maximum allowable burst pressure (Ph) of corroded pipeline is determined. The result obtained by FEA is analyzed, studied and compared with the actual burst test, ASME B31G and DNV-RP-FlOl. Lastly, the best model of ANSYS simulation is determined from the simulation.

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ACKNOWLEDGEMENTS

I would like to forward my utmost gratitude to my supervisor, Dr. Saravanan Karuppanan for his weekly advices and guidance throughout the whole Final Year Project (FYP) period.

With that, this project was going smoothly as planned and successfully fmished.

My heartiest appreciation goes to my examiners for their constructive comments and criticisms, and also not to be leli behind, my parents and all my friends who had given me endless support towards completing the Final Year Project.

Thank you.

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NOMENCLATURE

FEA Finite Element Analysis FEM Finite Element Method

RSTRENG Remaining Strength of Corroded Pipe API American Petroleum Institute

UT Ultrasonic Testing

ASME American Society of Mechanical Engineer DNV-RP Det Norske Veritas- Recommended Practice SMYS Specified Minimum Yield Strength

ClVonMisses Von Mises Stress

GSMTS Specified Minimum Tensile Strength

Gaxial Axial Tension

p Internal Pressure loading

pb Burst pressure

r Radius

t Thickness

v

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TABLE OF CONTENTS

CERTIFICATION OF APPROVAL CERTIFICATION OF ORIGINALITY ABSTRACT.

ACKNOWLEDGEMENTS NOMENCLATURE

TABLE OF CONTENTS LIST OF FIGURES LIST OF TABLES •

CHAPTER 1: INTRODUCTION • 1.1 Background of study 1.2 Problem statement.

1.3 Objectives • 1.4 Scope of study

CHAPTER 2: LITERATURE REVIEW • CHAPTER3: METHODOLOGY.

3.1 Experimental data.

3.2 Codes and Equations 3.2.1 ASME B31G 3.2.2 DNV-RP-FIOI

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1 1 2

3 3

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