1. CURRICULUM VITAE
Name: ERNESTO N. VALERIO
Address:BLK. 20 LOT 18 C-63 PHASE 1, VILLA DE CALAMBA,
LAMESA,CALAMBACITY4027,LAGUNA, PHILIPPINES
E-mail address: envalerio@yahoo.com
Philippinespassportno.: EB 1844901
Date of issue: FEBRUARY2, 2011
Valid until: FEBRUARY1, 2016
Telephoneno.: 0063-49-5453754
Cellphone no.:0063-9155007999
Date of birth: DECEMBER28,1956
Nationality:FILIPINO
Marital status: MARRIED
Educational attainment:BACHELOROF SCIENCE IN MECHANICAL
ENGINEERING
Position applyingfor: PRODUCTIONOPERATOR
Work experiences:
1.Wood Group Equatorial Guinea Limited - Offshore Operator
ALBA FIELD PLATFORM -from OCT.2005 to MAR. 2012

2. Responsiblefor start up / shut down of Production Separator,Test
Separator, Coalescer, HP Degasser,LP Degasser, Flare Scrubber,Fuel
Gas Scrubber, Gas Compressor, Gas Injection, Glycol Dehydration Unit,
Glycol Contactor, Air Compressor,and R.O. Unit. Check valve setting
prior start up of Process Unit. Monitor Process Unit Parametersuch as
Flow, Level,Pressure, Temperature,and makes necessaryadjustment/
setting as required.Perform line pigging, and well test. Check chemical
injection rate to ensure correct chemical dosage.Toppingup chemical
on it’s specified storage tank such as Anti Foulant,Corrosion Inhibitor,
Demulsifier,Hydrate Inhibitor,Methanol,and Water Clarifier. Conduct
laboratoryanalysis such as BS&W, Oil Content,and Free Chlorine
Content. Perform Draining,De-Pressurizing,Purging,and Ventingon
Process Unit prior maintenance job.Perform minor maintenance such
as bolt tightening, pump strainer cleaning,and toppingup oil on
rotating equipment.
2. MODEC International LLC- Process Technician
FPSO FLUMINENSE,BRAZIL - from JAN. 2003 to JUN. 2005
Responsiblefor start up / shut down of Production Separator,Test
Separator,IP Separator, Treater,Heater, Heat Exchanger,Waste Heat
RecoveryUnit, Flash Gas Compressor,BoosterGas Compressor,Gas
Lift, Gas Inlet Separator,VaporRecovery Unit, Fuel Gas Scrubber,
Glycol Reboiler,Glycol Contactor,LP Flare Scrubber,HP Flare
Scrubber, WaterInjection Pump,De-Oxidizer,R.O. Unit, Air
Compressor,and Nitrogen Generator.Checkvalve setting prior start up
of Process Unit. MonitorProcess Unit Parametersuch as Flow, Level,
Pressure, Temperature,and makes necessaryadjustment/ setting as
required.Perform line pigging, and well test. Check chemical injection
rate to ensure correct chemical dosage.Toppingup chemical on it’s
specified storage tank such as Corrosion Inhibitor, Defoamer,
Demulsifier,Methanol,Scale Inhibitor,Biocide,and Oxygen Scavenger.
Conductlaboratoryanalysis such as BS&W, RVP,Oxygen Content,and
Conductivity.Perform Draining,De-Pressurizing,Purging,and Venting

3. on Process Unit prior maintenance job.Perform minor maintenance
such as bolt tightening, pump strainer cleaning,and toppingup oil on
rotating equipment.
3. IPEDEXProduction LLC - Production Operator
EAST SHABWA BLOCK,YEMEN- from OCT. 2000 to NOV. 2001
Responsiblefor start up / shut down of Early Production Facility
such as Surge Separator,Test Separator,Hydrogen Sulphide Stripper,
Flare Scrubber, Crude Oil Storage Tank,and Centrilift Pump. Check
valve setting prior start up of Process Unit. MonitorProcess Unit
Parametersuch as Flow, Level, Pressure, Temperature,and makes
necessaryadjustment/ setting as required.Perform well test. Check
chemical injection rate to ensure correct chemical dosage.Toppingup
chemical on it’s specified storage tank such as Corrosion Inhibitor,and
Demulsifier. Conductlaboratoryanalysis such as BS&W. Perform
Draining,De-Pressurizing,Purging, and Venting on Process Unit prior
maintenance job. Perform minor maintenance such as bolt tightening,
pump strainercleaning,and topping up oil on rotating equipment.
4. SBM Offshore Contractor Inc. - Production Operator
FPSO KUITO, ANGOLA - from JAN. 2000 to JUL. 2000
Responsiblefor start up / shut down of Production Separator,Test
Separator,Treater, Degasser,Heat Exchanger, BoosterGas
Compressor,Main Gas Compressor,Gas Lift, Gas Filter Separator,
Glycol Reboiler,Glycol Contactor,Fuel Gas Scrubber, LP Flare Knock
Out Drum, HP Flare Knock Out Drum, Water Injection Pump,and R.O.
Unit. Check valve setting prior start up of Process Unit. Monitor
Process Unit Parametersuch as Flow, Level, Pressure, Temperature,
and makes necessaryadjustment/ setting as required.Perform line
pigging, and well test. Check chemical injection rate to ensure correct
chemical dosage. Toppingup chemical on it’s specified storage tank
such as Corrosion Inhibitor,Defoamer,Demulsifier,Methanol,Scale

4. Inhibitor,Biocide,and Oxygen Scavenger. Conductlaboratoryanalysis
such as BS&W, RVP, Oxygen Content,and Conductivity. Perform
Draining,De-Pressurizing,Purging, and Venting on Process Unit prior
maintenance job.Perform minor maintenance such as bolt tightening,
pump strainercleaning,and topping up oil on rotating equipment.
5. Alliance Marine Services - Lead Production Operator
MOPU TCHATAMBAA, GABON - from JAN. 1998 to NOV. 1999
Responsiblefor start up / shut down of Production Separator,Test
Separator,Treater, Water Skimmer, FloatationCell,Heat Exchanger,
Flare KnockOut Drum, Surge Tank, R.O. Unit, and Air Compressor.
Check valve setting prior start up of Process Unit. MonitorProcess Unit
Parametersuch as Flow, Level, Pressure, Temperature,and makes
necessaryadjustment/ setting as required. Perform line pigging, and
well test. Checkchemical injection rate to ensure correct chemical
dosage.Toppingup chemical on it’s specified storage tank such as
Corrosion Inhibitor,Defoamer,Demulsifier,and Scale Inhibitor.
Conductlaboratoryanalysis such as BS&W, RVP,and Conductivity.
Perform Draining,De-Pressurizing,Purging, and Ventingon Process
Unit prior maintenance job.Perform minor maintenance suchas bolt
tightening,pump strainer cleaning,and topping up oil on rotating
equipment.
6. Saudi Arabian Oil Company - Utilities Operator
RABIGH,K.S.A. - from OCT. 1989 to DEC. 1996
Responsiblefor start up / shut down of Waste Water Treatment
Plant such as BallastSeparator,Process Separator,Ballast Polishing
Pond,Process PolishingPond,Aerator, Clarifier, Filtration Unit, and
Sludge Basin. Checkvalve setting prior start up of Process Unit. Check
chemical injection rate to ensure correct chemical dosage.Toppingup
chemical on it’s specified storage tank such as Aluminum Sulphate,
Caustic Soda, Demulsifier,Ferrous Sulphate, PhosphoricAcid,

5. SulphuricAcid, and Urea. Conductlaboratoryanalysis such as
Biological Oxygen Demand,Chemical Oxygen Demand,Conductivity,
and Sludge Volume Index.Skimmed oil on BallastSeparator,and
Process Separator,and then pumped out to crude oil storage tank.
Responsiblefor start up / shut down of DesalinationPlantsuch as Meco
Distillation Unit, ElectrolizerUnit, Chlorine Unit, and Potable Water
Production Unit. Check valve setting prior start up of Process Unit.
Check chemical injection rate to ensure correct chemical dosage.
Toppingup chemical on it’s specified storage tank such as Calcium
Chloride,Sodium Chloride,CausticSoda, and SulphuricAcid. Conduct
laboratoryanalysis such as Chlorine,Conductivity,and PH. Perform
minor maintenance such as bolttightening,pump strainercleaning,
and toppingup oil on rotating equipment.
7. Star EnergyResources Ltd. - Terminal Supervisor
DUBAI,UNITED ARAB EMIRATES - from SEP. 1987 to SEP. 1989
Supervise loading/ unloadingof petroleum product on oil tanker,
line blending, and line pigging, Check valve setting prior loading/
unloadingof petroleum product on oil tanker. Check shore tank ullage
prior receivingof petroleum product to preventshore tank overflow.
Calculate shore tank received / discharged quantity,and oil tanker
received / discharged quantity.Check possible cause of abnormal gain /
loss on petroleum productshipment.Check job site for safety prior
issuance of permit to work. Appraise operatorperformance.
8. Mobil Oil Philipines - Process Operator/ Oil MovementOperator
MANILA,PHILIPPINES -from JUL. 1979 to JUL. 1987
Monitorcondition of equipmenton Crude Distillation Unit to ensure
safe, efficient, and continuousoperation.Carry out Control Room
Operatorinstruction during upsetor emergency,start up / shut down,
and on operational change of Crude Distillation Unit. Take sample, and
perform analysis to be made on Crude Distillation Unit such as API

6. gravity. Drain accumulated wateron vessel.Adjust heateroperation
such as changingburner, correcting draft, improve flame by
manipulatingair register, and atomizingsteam. Adjustammonia
injection rate to obtain desired PH of 6.5 on Naptha accumulatordrain,
and to neutralize acid formed on atmospheric column overhead vapor
line, and Kerosene stripper vaporreturn line. Set Caustic injection rate
at 7.5 gallons per thousand barrels crude oil feed on furnace crude inlet
lines in order to neutralize mostof the HCL formed by the
decomposition of salt. Adjust Organic InhibitorNALCO 165 AC, and
Kerosenemixture injection rate on atmosphericcolumn overhead vapor
line in order to protect Naptha condenser,and downstream equipment
from H2S attack. Set Phosphateinjection rate on steam drum to react
with ions to minimize scale formation.Operate side stream to produce
Keroseneor Jet A distillate specification.Correct a low 10% point on
distillation by increasingvapor line temperature. Correct a high 10%
point on distillation by reducing vaporline temperature.Correct a low
90% pointon distillation by increasingKerosene rate to storage. Correct
a high 90% on distillation by reducing Kerosenerate to storage.
Increase stripping steam rate to increase flash point. Decrease stripping
steam rate to decrease flash point. Operate side stream to produce
Diesel distillate specification.Correct a low 90% pointon distillation by
increasingDiesel rate to storage.Correct a high 90% point on
distillation by reducing Diesel rate to storage. Perform Draining,De-
Pressurizing,Purging, and Ventingon Process Unit prior maintenance
job. Perform minor maintenance such as bolt tightening,pump strainer
cleaning,and toppingup oil on rotating equipment. Take openinggauge
/ closing gauge, and sample of petroleum producton shore tank prior
receiving / discharging,and after receiving/ discharging of petroleum
product. Inspect / take gauging,and sample of petroleum product on
Cargo Oil Compartmenton oil tanker prior loading/ unloading,and
after loading / unloading of petroleum product. Valve, and line setting
on shore tank prior receiving / dischargingof petroleum product. Take
midnightinventory of petroleum product on shore tank.