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Petroleum-engineer-CDR-Sample

Career Episode 2 on CDR Sample Petroleum Engineer

INTRODUCTION

Time duration Jan 2015 to Apr 2015
Location
Organization NGL Tech Sdn Bhd (www.ngltech.com)
Project Development of Crude Separation System for Wahoo Field FPSO
Position Process Engineer (Intern)

[CE 2.1]

This career episode is about my project titled “Development of Crude Separation System for Wahoo Field FPSO’’. This project was carried out during my tenure at NGL Tech as an Internee Engineer from ……………..to ……………… .

BACKGROUND

[CE 2.2]

Nowadays most of the companies use FPSOs for their production facilities. One of the most important parts of the production facility is the inlet separation system. This system separates oil, water and gas from the crude. As soon as they are separated, the products are stored in a storage facility. To make sure that the carry over liquid in the gas is low and vice versa, an efficient inlet separation system is needed. This system should have the ability to get rid of the water from the crude. The Wahoo field was discovered in Campos Basin by APC (Anadarko Petroleum Corporation). In order to develop the field, the option of an FPSO with a wet tree is considered. Enough drilling has been done to follow the defining of this concept for the support development by the host facility. This local host facility needs to support several wet trees for the production wells in vicinity of the floater. It will also support risers for the satellite wells of the subsea at remote locations from the host. Produced oil will be stored in the FPSO then exported through the shuttle tankers by offloading. Depth of the water around the prospect ranges between 4430 and 5085 feet. For the floaters they will be located at the depth of 4650 feet.

[CE 2.3]

This field is expected to produce for at least seven years. Thus, the FPSO will be designed for 15 years without the dry docking as it will not be needed. The facilities such as piping systems and tanks will be also designed for the span of 15 years with a few routine inspections and maintenance.

[CE 2.4]

During my tenure at NGL Tech Sdn Bhd which lasted for 8 months from the period September 2014 to April 2015, I took part in several projects for numerous clients. However, I was required by Universiti Teknologi PETRONAS to produce a wide-ranging report on one major project for partial fulfillment of the Student Industrial Project course for my bachelor’s degree.

[CE 2.5]

The project hierarchy is given below -

Petroleum Engineer CDR report

[CE 2.6]

The project was aimed at developing a crude separation system for a client operating a FPSO in the Wahoo field. It was at the proposal and project bidding stage which encompassed activities such as preparing process flow diagrams (PFDs) for the topside of the FPSO as well as simulating the design on ASPEN HYSYS. It also involved weight sizing for the equipment and pipeline sizing.

Development of PFDs, HYSYS simulation of the design, equipment sizing, weight sizing, process design and unit operation, process and instrumentation control, plant process and maintenance, process analysis, production planning, computer applications, HSE, and research & development.

PERSONAL ENGINEERING ACTIVITY

[CE 2.7]

I did the Project management of the system which involved the modularization of the project in to definite number of stages & created a sequence of the activities to be performed. I planned the entire project in two stages.

  • Developing the Process Flow Diagrams (PFDs) for the system of the topside. This was based on certain specifications prescribed by the client.
  • Meeting the client with my manager to discuss the feasibility of the several proposed PFDs and implementing the client’s recommendation into a final PFD and accordingly seeking their approval.
  • Conducting stage two simulations of the system using ASPEN HYSYS
  • Processing the simulation data such capacity, temperature, density and pressure in order to facilitate the sizing design procedures of the separator and scrubber.
  • Researching for vendors that can do the sizing of the heat exchanger, pumps and compressors within allocated deadlines and the client’s standards.
  • Conducting the line sizing using the company’s template of Microsoft Excel Sheets that are designed based on API and PTS (Petronas Technical Standards).
  • Performing weight sizing via the provided template by entering data such as the size of the vessel and the class of material to estimate the weight of the vessel needed.

[CE 2.10]

The first issue was during the first meeting with the client. The client declined the proposed designs commenting that the system was not meeting the weight requirement. This required me to change the line sizing. To accomplish that, I sought insights from my manager on how to achieve this within the designated deadline and requirements advised by the client. I had to run the sizing process a couple of time using predefined spreadsheets prepared by the company’s engineers. However, this required thorough and in-depth reading of materials related to sizing so as to achieve the desired pressure dropdown asked for by the client in accordance to their set technical standards.

[CE 2.11]

After thorough understanding of the components that crude separator system comprises of; I designed the Process Flow Diagram (PFD) which included a production header, slug catcher, test separator, crude stabilizer, crude dehydrator, produced water treatment, gas dehydration system, and high pressure gas compression system. The design served as an input for the ASPEN HYSYS simulation to determine the working conditions for each component in the system. The adopted method for designing the PFD was with the aid of previous PFD designs from the company’s database and I tested the feasibility of the design on the HYSYS simulation. The software used to come up with the PFD was AutoCAD.

[CE 2.12]

I worked on designing the length and diameter of the pipeline. This was achieved using existing templates by altering the class of material used and the lengths to achieve the desired pressure dropdown. The templates adopt Microsoft Excel Spreadsheets designed by the company’s engineers.

[CE 2.13]

I performed the ASPEN HYSYS simulation in order to test the proposed PFD design with the operating conditions provided by the client. I performed two simulations. The first was Max Oil Case which had a flow rate of 50,000 BOPD, 15,000 BWPD, and 70 MMSCFD of gas. The second was Max Water Case which had a flow rate of 20,000 BOPD, 45,000 BWBP, and 70 MMSCFD of gas.

[CE 2.14]

I arranged meeting every week discussing status of the upcoming works, remaining clearances and resources allocation. Taking an essence of the previous completed works and made prior documentation for approval from authorities in order to perform seamless project proceedings.

[CE 2.15]

I was also accountable for the groundwork of feasibility study which included technical & economic consideration of this project. I calculated the whole project cost scrutiny and presented it to the authorities as well. My feasibility report was given weightage and it was used to finalize the approach towards project execution.

[CE 2.16]

Summary

This project was a good chance to develop my knowledge regarding Crude Separation System and deepen my expertise in the design of Separation Systems. Moreover, I have this chance to excel my planning, analysing and execution skills. This project has elevated my project management, planning, analysis and implementation skills. The crude separation system was successfully implemented without any delay in project envisioned deadline. My role in every aspect of project was highly admired by the executives of the company.

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