Materials & Corrosion and Pipeline Integrity Expert

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Full Name: KHOI TU
Current Position: Materials & Corrosionand Pipeline Integrity Expert
Date of Birth: April, 21st 1979
Nationality: Vietnamese
Email address: khoinmtu@yahoo.com
Mobile number: +84 (0) 938 591 669
Total Years of Experience: 16 years
Membership of Professional Societies:
- The Institute of Materials, Minerals and Mining (UK):
ProfGradIMMM
- NACE International (USA)
Awards
- Pipeline Engineering: UKOPA Award for Pipeline Engineering Top student
- Corrosion Protection & Material Science: The Embassy of the Socialist Republic of
Vietnam in the United Kingdom of Great Britain and Northern Ireland for Excellent PhD
student
Capabilities
- Good management, strong communication skills and HR awarenesss;
- Ability to manage limited resources to follow the project schedule;
- Leadership and expertise in matters relating to corrosion prevention for onshore and
offshore pipelines & structures;
- Training & Building up the Corrosion Protection team from different disciplines, such as
Chemical, Mechanical, Electrical & Instrumentation Engineering and Material Science;
- Good at Corrosion Assessment, Corrosion Root Cause Analysis, Risks Based Inspection,
Corrosion Control Strategy, Corrosion Management Plan and Integrity Management for
pipeline, platform and subsea structures;
- Expertise in development and design for inhibitor, anti-corrosion coating, material
selectionand cathodic protection (CP);
- Being good at development in skill and knowledge to corrosion and pipeline engineers /
designers;
- Ability to foresee disadvantages and difficulties of the project concerned issues in order to
achieve suitable solutions;
- Work under high pressure.
Education
- 2007 – 2010: PhD in Materials & Corrosion Protection: Manchester University, UK
- 2004 – 2006: MSc in Pipeline Engineering: Newcastle University, UK

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- 1997 – 2002: BEng in Chemical Engineering: University of Technology, HCM City, VN
(Link for Certificates and References )
Training Courses
- Pipeline Corrosion Integrity Management (NACE International, 2018)
- Vietnam bidding law (VN, 2018)
- T-FOET, OPITO approved (VN, 2018)
- Project Management / Hands-on Engineering Managmenet (VN, 2016)
- Safety Training for Offshore (annual refresh)
- Gas Conditioning and Processing(VN, 2014)
- T-BOSIET (OPITO approved) (VN, 2014)
- Necessary Skills and Knowledges for Middle Manager (VN, 2012)
- Nghiệp vụ Quản lý Đấu Thầu (Bidding management) (VN, 2012)
- ISO 9001:2008 - Quality Management Training (VN, 2011)
- Project management (VN, 2011)
- Research strategy and management (UK, 2008)
- Safety in laboratory and research (UK, 2007)
- Certificate of attendance, Pig Operation in Pipeline Engineering (UK, 2006)
- ACAD in design and simulation (VN, 2000)
ForeignLanguage:
- English: Fluently
Employment Record:
Duration Company Position
05/2014 - Current Cuulong Joint Operating Company
(CLJOC)
Materials & Corrosion/
Pipeline Integrity Expert
07/2013 – 05/2014 ROSEN / MACAW Engineering Ltd
Newcastle Upon Tyne, UK
Senior Corrosion & Materials
11/2010-07/2013 PVEngineering Joint Stock
Company
HCM City, VN
 Lead/Senior Corrosion
Engineer
 Deputy Manager, Pipeline
Engineering Department
 Deputy Manager, HSE
Department
01/2007-11/2010 The University of Manchester, UK Collaborator, UK government
– EPSRC commercial project

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05/2002-09/2004 HCM City University of Technology Teaching & Research assistant
Experiences
From 2011 – Current: Freelance / Part time job
 Being co-facilitator / scribe in workshop of HAZOP and HAZID;
 Visiting lecturer in Process, Pipeline Engineering, Materials and Corrosion
Protection@ the Industrial University of HCM City;
 Being supervisor for Research projects in Materials & Corrosion in Petroleum and
Petrochemicals;
 Performance the following activities for Petrovietnam Fertilizer and Chemicals
Corporation (PVFCCo)
 RBI (Risk Based Inspection) workshop Chairman / Facilitator;
 Corrosion Risk Assessment and Corrosion Management Handbook (a part of
the Asset Integrity Management System);
 Being technical advisor for Research projects in Materials and Corrosion
Management.
 Being Lead CorrosionEngineer for some offshore pipeline projects (FEED stage)
From 05/2014 – Current: Cuulong JOC
The following activities have been conducted
 Piggability engineering for Su Tu field pipelines
 Root Cause Analaysis (RCA) for defects of the 28 inch gas and 14 inch water
discharge lines on Su Tu Vang CPP
 RCA for the 10 inch discharge water line leakage on WHP-A;
 Corrosion Risk Assessment (CRA) for the topside plants and subsea pipelines (on-
going for the first 5 multiphase pipelines and planned for the next 17 pipelines);
 Develop Asset Integrity Management Program and supports local technical teams at
multiple facility locations;
 Develop the longterm inspection plan for the subsea pipelines;
 Being a key person in development and implement Risk Based Inspection (RBI)
Programs to improve asset integrity with a focus on safety and production for Su Tu
field pipelines;
 Being supevisor for the following
 Above water pipeline ends inspection (visual and NDT),
 ROV and CP inspection for subsea pipelines,
 Free span rectificationand anchor removal
 Annulus testing of the flexible risers @ FPSO

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 Deadleg inspection for topside piping (NDT including RT)
 Participate in the development and deployment of continuous improvement
programs for Topside and Pipeline Integrity Management Programs for Su Tu field;
 Act as contract owner for all integrity, inspection and monitoring contracts with
external partners;
 Acting as a lead for review, comments and approval to the reports of the following
 RBI program
 Subsea inspection with ROV and CP measurement
 Slugging issues in the condensate pipeline
 In place strength reassessment for multi-phase pipeline
 In-place free span assessment using Finite Element Analysis
 Corrosion Risk Assessment (CRA)
 Annulus testing of flexible risers @ FPSO
 NDT inspection
 Freespan rectification
From 07/2013 – 05/2014: ROSEN / MACAW Engineering Ltd
1 Root Cause Analysis and Materials Selection - Tensioner Piston Rod
Corrosion
Client: Rolls-Royce Power Engineering PLC.
Project background:
In late 2013 after around 6 months active service the owner/operator of the drill rig
contacted Rolls-Royce with concerns over the surface condition of the above piston rods.
Numerous marks, subsequently identified as corrosion pitting were observed on the outer
surface of the two new 80k riser tensioner piston rods and the new 18k guideline tensioner
piston rod. The two new compensator piston rods and the other hand did not show signs of
any surface corrosion pitting. The replacement piston rods were fabricated from
martensitic stainless steels ASTM A182 F6NM and equivalent grade DIN 1.4313.. The
martensitic stainless steel material used to fabricate the new piston rods is different to the
chrome nickel steel previously used.
The SOW for the report consists of the following
 To review the original material specification with a view to advising on the
operational suitability in the stated environment, highlighting the basis for the
individual chemical; components and their contribution to the material properties
 To clarify the suitability of the replacement piston rod materials in the current
operating conditions and environment and how the differences from the original
specification are;
 To clarify would the selected replacement piston materials be expected to corrode
in the manner and in the time frame which has been observed;

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 To comment/review the two compensator cylinder rods and the fact that there is no
apparent pitting so far;
 To advise any practical methods to minimise the corrosion / pitting risks to the rod
surface;
 Any alternative materials or rectification is required other than hard chrome plating
with a view to advising on the operational suitability in the stated environment.
Position: Senior Engineer
2 CORROSION RISK ASSESSMENT (CRA) & CORROSION CONTROL SCHEME (CCS)
Assessing corrosion risks and developing appropriate inspection and mitigation measures
forms a vital part of Asset Integrity Management System (AIMS) / Pipeline Integrity
Management System (PIMS) for operating any ageing asset / pipeline.
Corrosion related failures of processing facilities and subsea pipelines are a major
source of risk to offshore oil & gas installations and pipeline system. Corrosion threats
and their risk levels are considered based on operation parameters, inspection & sampling
reports, intelligent pigging (ILI survey), ROV survey alongside design and as-built
documents / drawings. CRA results are one of important inputs for a PIMS as shown in
Figure 1.
Figure 1: PIMS and its elements
Dr. Khoi TU has acted as Senior Corrosion Engineer and Project Manager in CRA and
CCS for the following projects / pipelines
2.1 Corrosion Risk Assessment for PL881, 16” Water Injection Pipeline -
PIPER To SALTIRE
Client: Talisman Sinopec Energy UK Limited.

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Position: Senior Engineer & Project Manager
2.2 Corrosion Risk Assessment for PL882, 10” Multiphase Production
Pipeline - SALTIRE To PIPER
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.3 Corrosion Risk Assessment for PL403, 3” Flexible Scale Squeeze Pipeline,
CLAYMORE to SCAPA
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.4 Corrosion Risk Assessment for PL1782, 30” Produced Oil, CLAYMORE to
PC Wye
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.5 Corrosion Risk Assessment for PL466 & PL11, 30” Produced Oil, PC Wye
to FLOTTA Terminal
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.6 Corrosion Risk Assessment for PL384 & PL386 (North Bundle), 10”
Production Line & 6” Test-Utility Line from SCAPA Template to
CLAYMORE
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.7 Corrosion Risk Assessment for PL383 & PL385 (South Bundle), 10”
Production Line & 6” Test-Utility Line from SCAPA Template to
CLAYMORE
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.8 Corrosion Risk Assessment for PL820, 30” Produced Oil, PIPER to PC Wye
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager
2.9 Corrosion Risk Assessment for PL726, 16” Gas Export - PIPER to
CLAYMORE Tee
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer & Project Manager

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2.10 Corrosion Risk Assessment for PL2337 3” Gas Lift, BRAE ALPHA to ENOCH
SATELLITE
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer
2.11 Corrosion Risk Assessment for PL883 Gas Lift Pipeline
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer
2.12 Corrosion Risk Assessment for PL2125 & 2126 Pipeline
Client: Talisman Sinopec Energy UK Limited.
Position: Senior Engineer
2.13 Development of Corrosion Control Strategy For TML Malaysia Platform
Topsides & Subsea Pipeline Infrastructure, KINABALU Field
Client: Talisman Malaysia Ltd.
Position: Senior Engineer
2.14 Development of Corrosion Control Strategy For TML Malaysia Platform
Topsides & Subsea Pipeline Infrastructure, PM-3 CAA North Field
Client: Talisman Malaysia Ltd.
Position: Senior Engineer
2.15 Development of Corrosion Control Strategy For TML Malaysia Platform
Topsides & Subsea Pipeline Infrastructure, PM-3 CAA South Field
Client: Talisman Malaysia Ltd.
Position: Senior Engineer
From 11/2010 to 07/2013: PVEngineering JSC
1. STV EXTENSION PLAN – STV NORTHEAST PROJECT (SVNE)
Client: Cuu Long JOC.
EPCI Contractor: Vietsovpetro Joint Venture
Design phase: FEED and Detailed Engineering Design (DED).
Project grade: I
Scope of work:
The design consists of the following
- 01 WHP-SVNE (Topside 350T and Jacket 530T);
- About 4 km of 8” Production pipeline and 4” Gas-lift pipeline;
- Modification at STV-CPP.
Position: Senior CorrosionEngineer
Reponsibilities:

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- Lead and execute design activities to provide necessary technical information,
definition and specification input to procurement of goods, materials and services
- Develop the Corrosiondesigner’s skills and knowledge;
- Manage the resources to follow the project schedule;
- Work as a Senior for the following deliverables
- Pipeline/WHP Cathodic ProtectionDesign
- Specification for Insulation coating/ anti-corrosion coating/ Field joint coating/
Painting
- Specification for CP system & CP installation
- Datasheet/MTO/MR for CP & coatings
2. RANG DONG FIELD (BLOCK 15-2) HYDROCARBON GAS - ENHANCED OIL
RECOVERY - FULL FIELD SCALE
Client: Japan Vietnam Petroleum Co., Ltd (JVPC)
Design phase: FEED.
Project grade: I
Scope of work:
The design consists of the offshore pipelines and risers & tie-in spools at NCWI, WHP-C1
and WHP-E1/E1A of Rang Dong Field HCG-EOR-FFS Project.
- About 4.0km of 6” pipeline from NCWI to WHP-E1/E1A;
- About 4.5km of 6” pipeline from subsea tie-in at WHP-E1/E1A to WHP-C1.
Position: Senior CorrosionEngineer
Reponsibilities: Covering the following deliverables
- Offshore pipeline system Cathodic ProtectionDesign
- Specification for anti-corrosion coating and Field joint coating
- Specification for CP system & CP installation
- Datasheet/MTO/TR for CP & coatings.
3. BLOCK B - OMON GAS PIPELINE PROJECT
Client: Block B - O Mon Pipeline Operating Company (BPOC)
EPC Contractor: Vietsovpetro Joint Venture
Design phase: DED
Project grade: Special
Scope of work:
This project will be implemented to transport natural gas from a proposed Central
Processing Platform (CPP) located in Block B fields to Ca Mau, O Mon and Neighboring
Industrial Zones in provinces along the pipeline route.

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The Block B-O Mon Gas Pipeline Project includes the following facilities:
- Approximately 246km subsea pipeline with DN 700 (28”)
- Mui Tram, Ca Mau Landfall station (LFS)
- Approximately 150km onshore pipeline with DN 750 (30”) from Mui Tram LFS to O
Mon GDC
- Nine Line Block Valve Stations (LBV)
- A pipeline lateral section from LBV#2 to Ca Mau GDS: approximately 400m DN 250
(10”)
- Ca Mau Gas Distribution Station (GDS)
- A pipeline section from O Mon Gas Distribution Centre (GDC) to each O Mon Power
Plant
- O Mon Gas Distribution Center (GDC)
Position: Senior CorrosionEngineer.
Reponsibilities:
- Lead and execute design activities to provide necessary technical information,
definition and specification input to procurement of goods, materials and services
- Develop monitoring technology and plan for corrosionprotection;
- Develop the Corrosiondesigner’s skills and knowledge;
- Manage the resources to follow the project schedule;
- Performance in corrosion assessment and material selection for offshore and onshore
pipelines;
- Specification for anti-corrosion coating;
- Specification for Field joint coating and infill material;
- Specification for painting;
- Specification/ Datasheets for Corrosionprobes;
- Calculation and specification of cathodic protection systems for offshore (SACP) and
onshore pipelines (SACP & ICCP), and pipings & vessels in the stations (SACP &
ICCP);
- Risk assessment and solutions for crossings between the High Voltage Transmission
Line and the Pipeline.
- Design for Remote Data Transmission systems to transfer the CP protection potential
from the Test stations and corrosion rate from Corrosion probe to the control room at
Omon GDC.
- Specification for chemical treatment during hydrotest to prevent corrosion.
- Integrity management plan for Corrosioninhibitor injection and Pigging.
- MTO & MR for Corrosionprotection systems.

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4. THAI BINH FIELD DEVELOPMENT PROJECT, BLOCK 102&106, OFFSHORE
VIETNAM.
Client: PETRONAS Carigali Overseas Sdn Bhd (PCOSB)
Design phase: Conceptual Services & FEED.
Project grade: I
Scope of work:
Thai Binh field is located approximately 20 km offshore southeast from Hai Phong port, S.
R. Vietnam in the Blocks 102&106, with a water depth of 25-30 m.
There is no existing facility nearby Thai Binh field. It is planned to have a wellhead
platform (WHP) tie back to onshore terminal at Tien Hai terminal via a 16-inch
approximately 20 km pipeline (by OTHERS).
CONTRACTOR is engaged to undertake Conceptual and FEED Engineering services for
one (01) WHP for Thai Binh project (i.e. TBDP-A). The gas evacuation from TBDP-A
will be directed to onshore terminal via a 16-inch pipeline designed and installed by
OTHERS. TBDP-A platform is anticipated to handle a maximum gas capacity of 26
mmscfd. First gas is scheduled in Quarter 3, 2013.
TBDP-A shall be a drilling platform which would accommodate four (04) conductor slots.
A dry ring main shall be provided for use during drilling. As TBDP-A is a hub for
Northern Gas Network Development, future tie-in facilities shall also be provided.
The development scheme for Thai Binh field includes:
- TPDP-A (by PCOSB)
- Riser (by PCOSB) (HOLD)
- Full wellstream (FW) pipeline from TBDP-A to an Onshore Gas Terminal (OGT) (by
OTHERS)
- OGT (by OTHERS)
Position: Senior CorrosionEngineer.
Reponsibilities: for the following
- Corrosion Design Basis Memorandum (CDBM);
- Painting Specification;
- Corrosion assessment (study) and material selection;
- Corrosion Management Plan
5. HAM RONG – THAI BINH GAS DISTRIBUTION AND GATHERING SYSTEM
PROJECT, BLOCK 102&106 – PHASE 1.
Client: PV GAS
Design phase: DED.
Project grade: I
Scope of work:

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Ham Rong & Thai Binh Gas pipeline project is designed to transport gas from 106 Ham
Rong and 102 Thai Binh fields, which belong to PETRONAS, to Thai Binh and
neighboring provinces industrial zones – in the North of Vietnam.
Phase 1 of the Project includes facilities on Thai Binh Platform, Gas Distribution Center
(GDC) and connecting gas pipelines Thai Binh field to GDC as follows:
- Platform topside facilities such as pig launcher and Corrosion Inhibitor skid.
- The 16” Tie-in point is installed for LNG export FPSO in the future.
- The 16” pipeline from Thai Binh Platform to GDC will be designed for expansion
capacity of other platform 106, 103 & 107 includes:
- Approximately 13.7 km from 102 - TB -1X to LFP at Con Vanh.
- Approximately 5.28 km from LFP to LFS.
- Approximately 5.7 km from landfall station to onshore GDC.
Position: Senior CorrosionEngineer.
Reponsibilities: for the following
- Cathodic ProtectionSystem Design Report for Offshore & Onshore Pipelines
- Corrosion ProtectionSummary
- Specification for Anti-Corrosion Coating
- Specification for Pipeline Field Joint Coating
- Specification for Onshore Pipeline Impressed Current Cathodic Protection
System
- Specification for Temporary Sacrificial Anode
- Specification for Offshore Pipeline Cathodic ProtectionSystem
- Specification for Offshore Pipeline Cathodic ProtectionSystem Installation
- Specification for Onshore Pipeline Cathodic ProtectionSystem Installation
- Specification for Monolithic Insulating Joints
- Data sheets for Test Station
- Data Sheet for Onshore pipeline Cathodic ProtectionSystem
- Drawings of CP system arrangement & Installation
- MTO & MR for coatings/ CP systems
6. THANG LONG DONG DO WHP AND INFIELD PIPELINE PROJECT
Client: LAM SON JOC.
EPCI Contractor: PTSC
Design phase: DED.
Scope of work:

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The development plan calls for a central processing facility located on an FPSO with
production from the two fields via dry trees only. As such two wellhead platforms will be
tied back; one located on Thang Long the other on Dong Do delivering full well stream
transfer to the FPSO. The FPSO will be located 2.84 km from the Thang Long WHP and
2.0 km from Dong Do WHP.
Position: Senior CorrosionEngineer – PLEM design
Reponsibilities: for the following
- Specification for painting for PLEM & PLET;
- Calculation and specification of cathodic protection systems for PLEM & PLET;
- MTO & MR for Corrosionprotection system for PLEM and PLET.
7. NAM CON SON 2 GAS PIPELINE PROJECT
Client: PV GAS SEG
Design phase: FEED.
Project grade: Special
Scope of work:
The Nam Con Son 2 Gas Pipeline Project ("NCS2" or "Project") has been initiated to
recover and process the gas reserved from the Hai Thach, Moc Tinh (Block 05.2, 05.3),
Thien Ung, Mang Cau (Block 04.3), Block 04.1 and other gas fields located within the
Nam Con Son basin. The pipeline project also considers possibilities to transport import
gas from ASEAN countries in future to provide for the growth in demand at Southeast Viet
Nam area.
Pipeline design capacity: Gas: 18.4 MMSCMD and Condensate: 1,320 ton/day, or dry gas:
20 MMSCMD (7 BMSCMY).
The NCS-2 pipeline system consists of the following items:
- Offshore pipeline is approximate 325 km to transport 2 phase gas, starts from
The Hai Thach Platform passes the Central Processing Platform of Thien Ung
field, Bach Ho and then runs to a Landfall Station at Long Hai.
- Onshore pipeline is approximate 9 km, from Long Hai Landfall Station (LFS) to
Gas Processing Plant (GPP2) at Dinh Co.
- Gas Processing Plant (GPP2) at Dinh Co.
- Onshore dry gas pipeline is approximate 30 km, from Dinh Co GPP2 to Gas Phu
My Distribution Central (GDC).
- Two liquid product pipelines (LPG & Condensate) is approximate 25 km from
outlet of Dinh Co GPP2 to transport to Thi Vai Terminal and 03 LBVs.
Position: Senior CorrosionEngineer
Reponsibilities:

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- Lead and execute design activities to provide necessary technical information,
definition and specification input to procurement of goods, materials and
services
- Develop monitoring technology and plan for corrosionprotection;
- Develop the Corrosiondesigner’s skills and knowledge;
- Manage the resources to follow the project schedule;
- Performance in corrosion assessment and material selection for raw & sale gas,
condensate and LPG pipeline;
- Specification for anti-corrosion coating;
- Specification for Field joint coating and infill material;
- Specification for paint systems;
- Calculation and specification of cathodic protection systems for offshore & riser
(SACP) and onshore pipelines & Gas processing plant (SACP & ICCP);
- MTO & MR for Corrosionprotection systems.
8. PROVISION OF BASIC DESIGN, CAPITAL INVESTMENT AND ECONOMIC
EFFICIENCY ANALYSIS FOR "DAI HUNG - NCS2 GAS GATHERING AND
TRANSPORTING SYSTEM".
Client: PV GAS.
Design phase: Feasibility Study (FS).
Project grade: Special project.
Position: Lead Corrosion Engineer.
Reponsibilities:
- Lead and execute design activities and solutions relating to corrosion protection
and interface management;
- Specification for anti-corrosion coating;
- Specification for Field joint coating and infill material;
- Calculation and specification of sacrificial anode cathodic protection systems for
offshore pipelines and riser.
9. INSTALLATION OF COROSION INHIBITOR SERVISE PUMP & SACRIFICIAL
ANODE FOR BURIED PIPELINE
Client: DVK.
Design phase: Economic-Technical Report.
Position: Lead Corrosion Engineer.
Reponsibilities:
- Lead and execute the methodology and basic design of corrosion inhibitor
injection pump;

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- Calculation and specification of sacrificial anode cathodic protection systems for
buried pipelines.
10. THANG LONG DONG DO FIELD DEVELOPMENT PROJECT
Client: Lam Son JOC.
Design phase: FEED.
Position: Lead Corrosion Engineer.
Reponsibilities:
- Provide technical leadership and execute design activities and solutions relating
to corrosionprotectionand interface management;
- Specification for anti-corrosion coating;
- Specification for thermal insulation coating;
- Calculation and specification of sacrificial anode cathodic protection systems for
Infiled pipelines and riser.
11. AS-BUILT DRAWING AND COST ESTIMATE FOR LIEN CHIEU PETROLEUM
STORAGE EXPANSION PROJECT
Client: PV Oil.
Position: Lead Corrosion Engineer.
Reponsibilities: Lead and execute design activities for Corrosionassessment.
From 2007 to 2010: The Universityof Manchester, UK.
12. ENHANCING THE PERFORMANCE OF PULSED CURRENT APPLIED
COATINGS FOR CORROSION PROTECTION, RESEARCH & DEVELOPMENT
STAGE
Client: UK Government & EPSRC.
Position: Collaborator.
Reponsibilities:
- Lead and execute survey to achieve the necessary data;
- Develop the strategy, methodology and milestones to achieve the research target;
- Work as a supervisor of the Research & Development team;
- From the research results, develop site application to protect the steel structures
from corrosionin sea water;
- Complete the Economical Technical Report.
From 2005 to 2006: Newcastle University, UK

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13. DETAIL DESIGN FOR CORROSION CONTROL DESIGN AND INTEGRITY
MONITORING FOR A PIPELINE TO COMPLY WITH THE LATEST ISO CODE
(ISO/FDIS 15589-1)
Position: Corrosion Engineer
Reponsibilities: Develop and carry out Detailed Engineering Design for a CP system to
protect the onshore pipeline from corrosion in various condition of swamps, hills and
mountain along the pipeline route.
From 2002 to 2004: HCM City University of Technology, VN
Position:Teaching & Research Assistant
14. RESEARCH & DEVELOPMENT FOR USING MMT ADDITIVE IN MAKING UP
NON-LEAD GASOLINE DERIVING FROM BACH-HO CONDENSATE –
VIETNAM
Reponsibilities: Develop a strategy to develop a process in order to increase RON for Bach
Ho condensate.
15. DOING RESEARCH FOR PETROCHEMICALS PROJECTS – HCM CITY
UNIVERSITY OF TECHNOLOGY PROJECT
16. RESEARCH AND DEVELOPMENT FOR THE CASHEW NUT PROCESSING –
HCM CITY PROJECT
Reponsibilities:
- Working as a leader or member of research groups to develop new technologies
in chemical engineering; especially in petrochemicals;
- Being tutor or teaching assistant in petrochemicals.
Publication:
- Khoi Tu and R.A. Cottis, “Controlling the Components of Calcareous Deposit to
Protect Steel Structures from ALWC with DC and Pulse Current”, in NACE
2009, USA, Paper No. 09008
- Khoi Tu and R.A. Cottis, “The influence of waveform on calcareous deposit”, in
ACA Corrosion & Prevention 2009, Australia, Paper No. 018
- Khoi Tu and R.A. Cottis, “Enhancing the protection of marine structures from
ALWC by understanding the components of calcareous deposit in cathodic
protection”, in The 14th International Congress on Marine Corrosion and
Fouling 2008, Japan
- Khoi Tu and R.A. Cottis, “The effect of applied potential on components of
calcareous deposit in seawater”, in The 6th Scientific Conference of Vietnam
National University 2008, HCMC, VN, Paper No. IX-O-1.3
- Khoi Tu, Tan Phan and Long Nguyen, “Research into using MMT additive in
making up non-lead gasoline deriving from Bach-Ho condensate” (in
Vietnamese), HCMC Vietnam National University - Science & Technology
Development Journal, 2004

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Certification:
The undersigned certifies the above information is true and correct and will be responsible
for any false statement discovered.
HCM City (VN), 16th January 2019
Khoi TU