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Ir. Fadhli Halim ST IPM ACPE AE

Senior Process Engineer at British Petroleum

Johor Bahru, Malaysia

Work Experience

  • Senior Process EngineerFull Time

    British Petroleum

    Feb 2021 - Present -4 yrs, 2 months

    • Job Details:a. Acting as Project PIC b. As Coordinator and interface lead with Engineering Company, Engineering Sub Contractor, Engineering EPC Company and Vendor Company. c. As Coordinator and interface lead with bp engineers. d. As lead to define the concept. e. As lead to define SOR (Statement of Requirement). f. As lead to define Project Basis of Design. g. Coordinating internal and external disciplines and contractors / vendors. h. Preparation or review Concept Selection Report. i. Preparation or review Process Drawings (i.e. PFD, PID, Schematic, etc). j. Review Process Simulations (i.e. Flarenet), including determine process simulation case. k. Preparation or review SOR (Statement of Requirement). l. Review Contractors / Vendor documents (Reports, Equipment’s Sizing, Lines Sizing, etc.) m. Review Contractor CTR (Cost Time Resource) n. Monitoring Contractor Schedule.

  • Process EngineerFull Time

    Worleyparsons

    May 2019 - Jul 2020 -1 yr, 2 months

    Oman

    • Job Details:a. Coordinating internal and external disciplines. b. Preparation or review of Process Drawings (i.e. PFD, PID, SAFE Chart, Cause and Effect, Schematic). c. Preparation of Process Simulations. d. Preparation process documents (Reports, Equipment’s Sizing, Utility Consumptions, Lines Sizing, PSV Sizing, etc.) e. Preparation of Design Review (DR document) including presentation, and DR meeting with client. f. Preparation of HAZOP (HAZOP Report and HAZOP Close out Report) including presentation, and HAZOP meeting with client. g. Monitoring Project Schedule. h. Provide process data for other disciplines i. Attend site survey

  • Process EngineerFull Time

    Chiyoda Almana

    Sep 2018 - May 2019 -8 months

    Qatar

    • Job Details:a. Coordinating internal and external disciplines. b. Preparation or review Process Drawings (i.e. PFD, PID, HMB, Schematic, etc). c. Review Process Simulations (i.e. Promax, Hysys, Pro II), including determine process simulation case. d. Preparation process documents (Reports, Equipment’s Sizing, Hydraulic Simulation, Utility Consumptions, Blowdown, Flare network, Lines Sizing, PSV Sizing, etc.) e. Preparation or review Concept Selection Report. f. Provide process data for other disciplines g. Attend site survey

  • Sr. Process EngineerFull Time

    Singgar Mulia

    Mar 2014 - Mar 2016 -2 yrs

    Indonesia , Jakarta

    • Job Details:Few Examples of Projects: 1. Successfully part of engineering proposal team which win many proposals (small to large-scale project). Example win of proposal: HCML EPCI project, the project is to install two (2) new wellhead platforms (110 MMSCFD MDA Platform, and 55 MMSCFD MBA Platform). 2. Successfully responsibilities to control (act as lead) the 3th party company and process engineers for new 365 MMSCFD gas processing facility in the Tiung Biru project. Process Engineers and 3th party company success issue around hundreds of Shutdown Hierarchy and Cause and Effect less than 1 month. The Shutdown Hierarchy and Cause and Effect cover Separation unit, Acid Gas Removal unit, Gas Dehydration Unit, Sulphur Removal and Recovery Unit, Tail Gas Unit, Thermal Oxidizer, Condensate Stabilization unit and any utilities. 3. Successfully complete to recommend for PCI BCD5 project: a) Complete recommend for all recommendation to modify in the power point form. b) Complete recommend for MEG is injected to prevent hydrate during normal operation. c) Complete recommend to install new MEG injection and new MEG regeneration unit to suppress the hydrate, since the existing Glycol reconcentration system package is insufficient for additional new Geragai Receiving facilities with a new operating condition in JT and Hammilton plant in the FEED Geragai Modification for BCD-5. The recommendation is selected based on reliability (weight factor 40%), CAPEX & OPEX cost (weight factor 30%) and Maintainability & constructability (weight factor 30%). d) Complete recommend to utilize the existing glycol regeneration as a backup of new MEG regeneration. e) Complete estimate the cost of new MEG injection and MEG regeneration is USD 620,535. f) Complete recommend to modify the JT Plant and Hammilton Plant to reach C3+ recovery 65% (JT Plant) - 70% (NGL Plant) and gas dew point is decrease to -20 C. the example of modification are: i. Recommend to install a new Chiller, new refrigerant unit and new separator in the downstream of Low Temperature Separator (JT Plant) ii. Recommend to replace the existing HE in JT Plant.Recommend to install new Chiller and new refrigerant unit (NGL Plant) iii. Complete estimate the cost modification for liquid recovery around US$ 1,168,677. g) Complete recommend flare design flowrate is 50.6 MMSCFD. 4. Successfully complete to response, closed and implemented all HAZOP response sheet in the PID and any related documents in the HAZOP/HAZID Follow Up. The example case of hazop response is: Complete to recommend to install a new LLLL and a new SDV at Production Separator liquid outlet to prevent potential loss of level and potential gas blowby in case liquid control valve stuck open. It is recommended the location of new SDV shall be as closed as the Production Separator liquid outlet nozzle and level setting of LLLL shall be follow company criteria and shall consider for the operator response time between low level alarm and LLLL.

    • Achievements

    8 times earned the first rank and 1 time earned the second rank of a total of 9 quarterly during Senior High school

    Skills

    Languages

    • Malay

      Advanced

    • English

      Intermediate
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