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CV Production Technician

 
Production Technician

Resume built for oil and gas job opportunities by a jobseeker with experience in Production Technician - would you like to offer this candidate a job/contract employment?

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CV/Resume ID no.: 89186

Location (Residence): TUTICORIN, India
Citizenship: India
 
Languages:
  Native: Tamil
  Other: English
 
Education & Experience: Work Authorization & Relocation:
Education:
  High School in PHYSICS,CHEMISTRY,BOTONY,ZOOLOGY

Years of Experience: 4 years
Authorized to work in:
   Australia, Canada, Hong Kong, Kuwait, Mexico, Nigeria, Oman, Qatar, Saudi Arabia, Singapore, South Africa, Sudan
Present Location:
   INDIA, TUTICORIN
Relocation:
   United States, Australia, Bahrain, Bhutan, Hong Kong, Jordan, Kuwait, Malaysia, Mexico, Nigeria, Oman, Qatar, Saudi Arabia, Singapore, Sudan, United States
 
Expertise
Category Subcategory Ability Experience
Technician Level Production Experienced 3 years
Technician Level DCS Experienced 1 year
 
CV/Resume Details
 
1. Summary (Cover Letter) - CV/Resume Part 1 [Mandatory]

I have completed B.Sc CHEMISTRY with academic excellence and I am technically competent. I have completed DIPLOMA IN INDUSTRIAL SAFETY with second class. I wish to apply for the above-mentioned post in your esteemed organization. I am working in Southern Petrochemical Industries Corporation Ltd., Tuticorin. I have rich experience in the operation of Ammonia Plant and Power plant.

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

Experience

Name of the Employer : M/s. Southern Petrochemical Industries Corporation Ltd., Tuticorin - 628 005

Duration : 08¬¬-02-2006 onwards

Designation held : PRODUCTION TECHNICIAN

Previous experience

Institutional training : M/S Suguna Poultry farm Ltd,
Bangalore

Designation held : LAB CHEMIST

Period : One year


Professional Qualification : Working as PRODUCTION TECHNICIAN(Plant Operator) in Ammonia Plant in SOUTHERN PETROCHEMICAL INDUSTRIES CORPORATION LTD. (SPIC);

a large Naphtha based Petrochemical Complex in India.

i. Operating Experience in I.C.I. Steam Naphtha Reforming Process Ammonia plant of capacity 1260 TPD,

ii. Operation of various Rotary equipments like STEAM TURBINE, POSITIVE DISPLACEMENT COMPRESSORS, MULTISTAGE CENTRI-FUGAL PUMPS and HIGH PRESSURE POSITIVE DISPLACEMENT PUMPS.

iii. Operating experience in Furnace oil fired high pressure boiler, capacity of 90 TPH & pressure of 106 Kg /Cm2

iv. Operation of Catalyst beds, Absorbers, Regenerators, Stripper column, Distillation column, Dryer and various types of filters.

v. Operation, cleaning, Leak checking and pressure testing of Heat exchangers.

vi. DCS Operations.

vii. Operation of all types of fire extinguishers and personal protecting equipments.

Course Attended :
i. Attended a course on SAFETY AND FIRE FIGHTING conducted by our company.

ii. Attended a FIRST AID COURSE conducted by St. JOHN AMBULANCE ASSOCIATION.

iii Attended a course on HUMAN RELATIONS conducted by our company

project work
(Diploma in industrial safety) : Safety in naphtha tank
maintenance


EXPERIENCE DETAILS

HYDRO DESULPHURISATION OR HYDRO FINING UNIT
The Naphtha Hydro-desulphurization Unit (Hydro fining Unit) is based on HP / IFP process and is designed to produce 26.793 T/hr of desulphurised naphtha product. The sulphur content in raw naphtha is reduced from 1500 ppm to 5 ppm in this unit. And the desulphurised naphtha (sweet naphtha) is stored in sweet naphtha tank having a storage capacity of 8800 m3.
Feed stock naphtha pumped from raw naphtha tanks is mixed with hydrogen rich gas from hydrogen gas compressor (Reciprocating type) is vapourised and preheated to 355°C in the Raw naphtha vaporizer. The Vapourised naphtha is passed through the hydrofiner catalyst vessel which is packed with Cobalt molybdenum (Comox) catalyst. The sulphur in the naphtha reacts with Hydrogen in the present of catalyst at 330~350°C and is converted to Hydrogen Sulphide. The effluent gas from the catalyst vessel is condensed and the condensed naphtha is stripped free of H2S in the stripper, a tall vessel containing 30 trays of Stainless steel valve plate trays and a reflux condenser. The heat required for gases from the catalyst vessel, the naphtha from the stripper is cooled and sent to sweet naphtha storage tank, contains sulphur less than 5 ppm.
The Sweet Naphtha containing less than 5 ppm sulphur is pumped and mixed with recycle hydrogen and vapourised to 375 - 390°C in the process naphtha vapouriser and is passed through the Desulphurisation vessel, this vessel is provided with Cobalt molybdenum catalyst and bottom two beds packed with Zinc Oxide catalyst. The sulphur reacts with hydrogen in presence of COMOX catalyst and is converted to Hydrogen Sulphide. And thus the sulphur in Feed Stock Naphtha is reduced to less than 0.5 ppm.
FIRED HEATERS
The Raw Naphtha and Sweet Naphtha Vapouriser are Natural Draft fired heaters fueled by the fuel gas and Naphtha using 4 AIROIL Burners each. The furnace is refractory lined. Flame is sensed by two Flame Scanners and the skin temperatures of radiation coils measured. Each Burner is fixed with an Ignitor for the light up and safety measures are provided.
REGENERATION AND DECOKING
Catalyst vessels (Desulphuriser) Regeneration of catalyst and Fired heater Vapouriser tube’s Decoking are known
HYDROFINING OF NAPHTHA
REFORMING
This unit is based on ICI Steam - Naptha reforming process. Vapourised sweet Naptha with 0.5 ppm of Sulphur is mixed with superheated steam and enters the reformer tubes at a temperature of 457 degree. There are totally 264 tubes packed with ICI 46-3 & 46-6 catalyst. Material of construction of catalyst tube is HK 40.
Reformer furnace in top fired, negative pressure (-1.27 mm of H20). Exit gas after primary reformer leaves the outlet pigtails (Incoloy 800) at 787 degrees. There are totally 90 burners fuelled with fuelgas & Naptha. Furnace pressure is maintained with the help of two sets of induced & forced draft fans.
Flue gas heat is recovered in clock chapman joule thomson waste heat recovery system which is used to generate 106 KSC steam & Superheating of reforming steam.

SECONDARY REFORMING
This unit is provided to reduce methane content form 9.25% to 0.25% at the exit by burning part of process gas with process air. The other advantage is, N2 required for synthesis reaction later is met here.
Catalyst for secondary reformer are of nickel high alumina & silica type (ICI 54.8). Gas at the exit is at 972 degree and enters RGB where the heat energy available is used to generate 149 tonnes of 106 KSC steam.


TANK FARM:-
The feed stock and the fuels used in Ammonia Plant are received from IOC. Naphtha and fuel oil are transferred through pipe lines to our tanks.

In our tank from five floating roof naphtha tank’s of capacity 8750KL and two fuel oil tanks of capacity 3800 KL are there. Raw naphtha pumped to HF though multistage centrifugal motor driven pump. Where as sweet naphtha and fuel naphtha pumped thru Back Pressure turbine driven Pump.
The storage facilities of Naphtha and furnace Oil are done here
Two Raw Naphtha Tank 8750 NM3
Two High Aromatic Naphtha Tan 6150 NM3
One Sweet Naphtha Tank 8750 NM3
Two Furnace Oil Tanks 3800 NM3

Naphtha Tanks are having “Floating Roof Pontoon Type with NEOPRENE seal Breather vent, rim vent, flame traps, Roof drains are located in the roof. Fire water, Foam Pourer System also is there.


Inert Gas Plant
This plant produces Hydrogen / Nitrogen using NH3 as raw material. It has vopourisers, dissociators, direct contact coolers and compressors.
‘Safety & Fire Fighting
Attended Safety and Fire Fighting training classes conducted by our safety dept. and faced many emergency situations, handled them very efficiently and got appreciation from management.
I am actively involved in getting FIVE STAR SAFETY AWARD BY BRITISH SAFETY COUNSIL.
Rogenated gas.
I have received best safety coordinator award by our company. I am actively participated in the plant safety committee and central safety committee
Instrument Air System
Instrument air is the first requirement and critical to process plant. The air required for this was supplied by 3 Reciprocating Compressors 800 NM3/hr. Normally during normal course of running air is supplied from Process Air Compressor. Here is wet air is dried in the Drying Unit which contain Silica Gel bed. The Dried air is filtered and stored in instrument Air Receiver and then supplied to process. The unit capacity is 2000 NM3/hr.
The unit consists of Auto Start and auto loading / unloading facility to Compressors, High Pressure Alarm, Low Pressure Alarm, Adsorption and Reactivation of Drying unit
I am having rich experience in the above said areas during normal operation, shut-down, start-up and during emergencies. Added to this, I have exclusive experience in annual Turnaround exercises


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

S.S.L.C Government Higher Secondary School
T.Vadipatti
March 1998 72%
H.Sc., Government Higher Secondary School
T.Vadipatti
March 2001 77%

B.Sc(Chemistry) Thiagarajar College
Madurai-625009 April 2004 65.21%

Dip.in industrial Safety Annamalai University
Chidambaram 2007-2008 53.0%


4. Computer Skills - CV/Resume Part 4 [Mandatory]
-
5. Other Skills - CV/Resume Part 5 [Optional]
PLAYING TENNIS,CRICKET AND READING BOOKS
6. Additional Information - CV/Resume Part 6 [Optional]
I HAVE OPERATE PETROCHEMICAL PLANT IS VERY WELL.


 

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Production Technician
CV/Resume ID no.: 89186

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