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CV Control Room Operator in Total Sirrie Abu Dhabi Offshore, Persian Gulf CNPC, PETRONAS, ONGC, SUDAPET

 
Control Room Operator in Total Sirrie Abu Dhabi Offshore, Persian Gulf CNPC, PETRONAS, ONGC, SUDAPET

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CV/Resume ID no.: 100051

Location (Residence): Trunelvelli, India
Citizenship: India
 
Languages:
  Native: Urdu
  Other: Gujarati
 
Education & Experience: Work Authorization & Relocation:
Education:
  Bachelors in Diploma IN mechanical engineering

Years of Experience: 20 years
Authorized to work in:
   Nigeria
Present Location:
   Sudan, Heglig
Relocation:
   Anywhere (International)
 
Expertise
Category Subcategory Ability Experience
Operations Control Room Operator Basic 27 years
Operations Control Room Operator Experienced 1 year
Operations Control Room Operator Basic 9 years
Operations Control Room Operator Basic 9 years
Plant (Refinery, Gas...) Gas Plant Experienced 2 years
Operations Control Room Operator Basic 25 years
 
CV/Resume Details
 
1. Summary (Cover Letter) - CV/Resume Part 1 [Mandatory]

TOTAL OIL & GAS EXPERIENCE
14YEARS plant commissioning

2. Work Experience - CV/Resume Part 2 [Mandatory]

Total Sirrie (Abu Dhabi Offshore, Persian Gulf) June 1998 to May 1999.
GREATER NILE PETROLEUM OPERATING COMPANY LTD, SUDAN (Consortium of CNPC, PETRONAS, ONGC, SUDAPET).

Responsibilities
1. Neem FPF( GNPOC `SUDAN) Since from June 2006.
Position Held: Production Forman as a Control Room operator
Responsibilities:
DCS,SCDA and PLC system operation –safety system honey well-during commissioning carry out all ESD LOOP function test-train shout down loop-vessels LALL &LAHH activation test-checking the switch and controller transmitter variation -control vale functioning-if it is stuck up open bypass and maintain the vessel level avoid the liquid carry over to flare system-maintain the interface level –vessel water out let sample collecting for PPM measurement –adjust the chemical dosing-regulating the preheating temperature by heater treater with Heat exchanger row liquid controlling-collecting gas sample for H2 S concentration and CO2 %-safety system calibration each 3moth –gas detector ,fire detector UV –test with over ride mode-faulty sensor changing-Reporting daily production, down time with reason, system down graded and inhibited to the Supervisor, controlling the inventory of chemicals and consumable. Responsible for Isolations and enhance the PTW in a safe manner, Conducting weekly, monthly safety meeting and reinstate the minutes to the operation. Identify the potential hazards and preparing MOCs for the management changes. Planning and implement the front lime maintenance as well as planed maintenance. Coordinate with the Maintenance team and Minimize the down time by proper planning. Assist Production Supervisor for deputing management meeting. Control the process of 80,000 Bpld crude 42 API and 40 MMSCFD Gas with CO2 by Emerson DeltaV process controller and Honeywell F&G system.

2. ALL FPFs&EPFs (GNPOC- SUDAN) June 1999 to June 2006
Position Held: Control Room Operator
Responsibilities:
1. Controlling and trouble shooting the process and F&G systems of
1.Heglic CPF - Capacity 140000Bbls/d Honeywell TPS/ Allan Broadley/
2, Munga FPF. Capacity 40000 Bpld/ Honeywell-Hima
3,Unity FPF Capacity 1,00,000 Bpld/Honeywell- Hima
4, Elnar Capacity 25,000 Bpld /Emerson Delta V
5, Elthoor Capacity 15,000 Bpld
6, Toma South Capacity 60.000
7, Bamboo Capacity 40,000 bpld
8, Diffra Capacity 40,000 Bpld with22 MMSCFD GAS by Honey well control system- 3train- 2 Nos plat type heat exchanger -Three face process - freione water knock out drum Heater Treater with direct fire system by Fuel gas and Diesel –Nalco burner temperature control system-up to 111oC can increase the temp depending on crude separation and viscosity (emulsion )-Gas handling Capacity 40mmscf/d- Determine by US meter-Flare knock out drum-condensate removed and come back inlet header by pump – smokeless flare stack with blower and velocity seal for prevent air from infiltrating to the flare system-- ignition panel-fuel gas filter separator- from fuel gas filter we shall use gas for –pilot gas-fuel gas-blanket gas-power plant Fuel gas compressor-Nitrogen compressor-for inert gas purging system -Auto sampler operation-Crude storage tank PCV operation- Produced water tank water box system –closed drain skimming system-CPI separator operation- Export centrifugal & screw pump operation-chemical pump injection calibration-Export micro motion meter density calibration-Temperature zero calibration.. Flame detector system-gas detector system-smoke detector system.
3.Total Sirrie (Abu Dhabi Offshore, Persian Gulf) June 1998 to May 1999.
Position Held: Production Operator
Responsibilities:
Three field WPE 1, WPE 2, WPE 3 – Total 16 wells – Production 1.5 lacks barrels per day – WPE 2 & WPE 3 unman Platform, WPE 1 as process platforms (PPE)Total 7 Wells – Brisco Panel board – ESD Loops – Fusible Plug (1050C) – Hydraulic valves ‘X’ mas tree – checking the Brisco Panel board hydraulic tank oil level (70%) & check the banal board instrument air pr. (7 bar). Wing value hydraulic pressure 280 bar). Master valve 500bar) & Down hole safety valve (310 bar). Hydraulic pressure in banal gauge & Low – high Pilot indication (25 & 52 bar) Dead weight pressure gauge: check well head pressure & DCS pressure (difference) Fully Pneumatics control valves system Panel board. ESD level 3.1 – PSHH pressure 54 bar close SDV (inlet & outlet valves close) & blow down valve open- (PSV- auto open)- LSHH 72% SDV close (inlet & outlet liquid valves close) Antifoam injection pump stop – by pass valve open. Reset ESD level – again reopen test sep. – Flushing time – close drain – open drain. Two Sep. – Capacity 77.3 mtr3 ESD – 3.4 LSHH & PSHH – close SDV (inlet & outlet valves) – open blow down valve (BDV) – LSLL & close SDV outlet oil. Pig launching & receiving – ESD failed 9line pr. 8 bar) well head safety cabinet (WHSC) CP0102 Test Sep. Gas flare – fuel gas system – knock drum, - drain Oil goes to closed drain – closed & open drain joint to production separator inlet. Fusible plug (1050C), connect to ESD system – UV + IR – detectors (Ultra violet & infrared sensor) – deluge system, (Auto realized & fire detection) – MANUAL CALL POINT – control & Electrical rooms are composed of thermostatic heat detection loop (HDL) – ionization type smoke detection loop (SDL) – F & G logic – gas detection – CO2 realized system (Local mode).

•

4, Oil India Limited May 1996 to May 1998.
Position Held- Process Operator

Operation Units and Systems
• Utility system, sea water system

Responsibilities :
.
Responsibilities:
GLYCOL DEHDRATION UNIT – INDIAN FIELD EXPERIENCE
SCADA” system – summary of daily Report – Plant Status – Tot flow – Current Flow – Hourly report – 12 & 24 hours Report.” PROCESS UNIT” – Manifold – PRODUCTION SEP – Test Separator – COLESCER SEP – Glycol Heat Exchanger – Glycol scrubber – CTM (Custody Transfer meter) – DEW Point (Kahn sensor) – MP & LP Flash drum – Drain sum (Water and Condensate) – EVAPORATOR PIT _ Condensate Storage Tank – Booster Pump – Ground Flare System – Cold vent System – Water Seal.“GLYCOL DEHDRATION UNIT” – Wet gas to Dry gas – Glycol contractor (8 Carbon Steel bubble cap type trays, Plugged trays) – Glycol Scrubber, (reduce to the glycol losses)“REBOILER UNIT” – Gas condensate – Glycol separator (G.C.G. Sep) Cartridge Filter – charcoal filter (absorb hydrocarbons, show differential pressure) – plate type exchange (1040C up to 1100C, to heat rich glycol, to cool lean glycol) – Storage Tank (128 cub feet) – check PH value – Add NACAP (33.38 kg. Do not add more than 5 litters) – Still column (tem 212 – 2150F ) – The Reboiler (T.E.G 360 – 3750F) – THERMAL COMPOSITION – Stripping gas – Pilot gas – Fuel gas – Blanket gas – Reflux coil – Three way valve – Glycol Pump – Flow stabilizer – Glycol circulation rate (around 3 gallon of glycol per pound of water)“GAS GATHERING STATION” – Test separation – Panel Board operation – Local Controller – Flow line – Pig launching.” WELL HEAD” – Master valve, Wing valve, Double Arm valve, Beam housing (Using different bean size)
Equipment Experienced:
• Horizontal & Vertically Suspended Centrifugal Pumps- for boiler feed water, hydrocarbon, sea water and utility services make- KSB, Kirloskar, Ingersoll Rand, Nuovo pignone, Worthington, Sulzer, Nigata , Turbo, Ebara
• Positive displacement pumps- plunger, screw, gear make- Milton Roy, Ingersall Rand, Allweiler, Union, IMO pumps.
• Reciprocating compressor of Thomosan , Ingersoll Rand
• Centrifugal compressor of Dresser, Sulzer, Elliot.
• Screw compressor of Atlas Copco, Bauer
• Steam Turbines of Coppus, Terry, Elliot, Siemens SST-150- 19.5MW & SST-300- 30MW.
• Gas Turbine of GE Frame MS5001

1997 to 2003 Oil and Natural Gas Corporation Ltd India, Sept 1994 -1996.
Position Held: Production/ Utility Operator
Responsibilities:
Operation of Christmas tree and Flow line check-ups. Storm Choke, Lower & Upper tubing master valves, wing valves, free size choke (at high pressure) & (Multiple Orifice, Rotary, Adjustable), Swab valve, safety valves, (Safomatic, Manumatic, Baker Submersible, Cameron Type FC), Check Valve, Top Adaptor, Flow line Pressure looses, Abnormal Pressure Variations, Flow line Protection, Flow line Inspection & Servicing, Pig (or) Scrapper Launching & receiving. Arrival manifold, Collector Equipment, Pressure Relief Valves, Safety Shut Down Valves (S.S.V.) (Gas or instrument air system 100 PSI) normal Re-opening, Sub surface safety valve (S.S.S.V.) (Hydraulic Oil Pressure 3600 PSI), CHEVERON, BALL VALUE, FLAPER VALUE. S.S.S.V. & S.S.V. Auto & manual switch, emergency shout down (ESD), Fire shout down (FSD), Pressure gauges, Pilot control (Low & High), Control line Ύ”, S.S.V. bleeding line ½”, Types of Panel Board AUTOCON, BRISCO, BAKER, Pilot SENSINGLINE, Panel Board instrument Air system, Hydraulic Oil, Sea 100, Toeless 32.
Satellite Field, 6” line Bulk Manifold, 10” line bulk manifold, 6” line Test manifold. Separator checklist, separator start-up, handling various Types of valves, P.C.V.,L.C.V.,F.C.V.,T.C.V., Fisher Controller, Joucovier Pilot Operated, Norbo Actuators, Gas Detectors, U.V.Detectors, Foxboro Chart, Microns and Honey well Orifice Plate select, separator Max pressure 100 BAR, Max. Tem. 100C”. Lift gas injection system, stabilization of Annuals Pressure, measurement Orifice (M.O. =25mm) & Restrict Orifice (R.O.=6mm) & Differential Pressure. Take sample, water cut (Ag No3), Demulsifier Gas gravity, Salinity, Ph of water, H2S concentration, Gas oil ratio (G.O.R.), Flow line Tubing Head Pressure (F.T.H.P.20 Kg/cm2) Mainline tem M.L.T.88 C). Mainline pressure (M.L.P.19 Kg/cm2). Main water line pressure (MWLP 130 Kg/cm2). Main Gas line pressure (K.G.L.P.106 Kg/cm2). Particular well lift Gas injection (1250 PSI). Single Completion, Dual Completion, Using WORLDWIDE OIL FIELD MACHANICS, BREDA, FMC’XMAS’ TREE, Single Straddle Completion Perforation, BOP, Tale Pipe, Seal Assembly, Permanent Packers (Alpha, pengo, Baker, Arrow, Jam), Landing Joint, Dual (or) single hydraulic packers, Mechanical packer, sliding sleeve, side pocket mandrel, Gas lift valve fitting, Expansion joint, S.S.S.V. & control line fitting, casing hanger, S.S.S.V. needle valve fitting. Acid job (HCL 15% per meter of perforation). Control, Choke manifold, Separator, Burner, Well Killing, Brain Solution, Sea water, Mud Cementing, Perforation. (T.C.P).
Stabilized flow rates through 32/60” choke, flowing bottom hole pressure (F.B.H.P.), Shutting bottom hole study (S.B.H.P.) CHOKE SIZE Ό” = 16/64”, ½” = 32/64”, Ύ” = 48/64”, 1” = 64/64”, 5/8”=40/64”, 3/8”=24/64”, EACH SHOULD BE FOR 6 TO 8 HOUS STABILISATION. During the flow studies, well head and separator pressure, up stream, down stream, temperature & Production rates of oil, Gas & Water may be record at half on hour interval. Tubing’s, Tubing threads (Eu-External up set), Iu-Internal Upset Warm thread, NPT – Nation Pipe Thread, UNC – Unified National Cave, UNF – UNIFIED National Gave. Elevator, Slip, Tang, Tergue, Scrapper. ‘X’ over, Seal Assembly Packer, Packer Setting Kit, Shear Stud. Milling tool, breaking tools, control head, Pipe joint, tungsten carbide. Acid, Chock manifold, needle valves, Pressure gauges, Temperature Gauge, S.S.S.V.F;a[[er valve (CP,CP), (4500 PSI), G.L.V. Mandrel. Bop method, Ball, landing method standing valve (or) Balking Plug & Seawater Pressurize at 2000 PSI to 10,000 PSI.


3. Education & Training - CV/Resume Part 3 [Mandatory]

HIGHEST EDUCATION LEVEL
Diploma in Mechanical Engineering
Board OF Tamil Nadu Govnt, INDIA


4. Computer Skills - CV/Resume Part 4 [Mandatory]
MS Office, Excel, Foxbro, C – Language
Diploma in Mechanical Engineering
5. Other Skills - CV/Resume Part 5 [Optional]
-
6. Additional Information - CV/Resume Part 6 [Optional]
-


 

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Control Room Operator in Total Sirrie Abu Dhabi Offshore, Persian Gulf CNPC, PETRONAS, ONGC, SUDAPET
CV/Resume ID no.: 100051

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