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[QUOTE=kuttytac1147@gmail.com;282258]T.kuttidurai [b][u]Email [/u][/b]:kuttytac1147 AT gmail.com [b][u]Sub [/u][/b]: Application for the post of FIELD OPERATOR Respected Sir, I would like to apply for the post of “FIELD OPERATOR” I am B.Sc Chemistry Degree holder and additionally studied in petroleum refining engineering course. Having totally 8 years experience presently working as an an utility operator in TAC LTD and in naphtha based Ammonia Plant in Spic Ltd (on deputation)Tuticorin, India. I herewith submit my detailed resume for your kind perusal and favorable consideration. Thanking you, [b][u]Place [/u][/b]: Tuticorin yours truly, [b][u]Date [/u][/b]: 06/05/2013 (T. KUTTIDURAI) [b][u]Personal details [/u][/b]: [b][u]Educational Qualification [/u][/b]: B.Sc (Chemistry), first class First class, diploma in petroleum Refining engineering. [b][u]Father’s Name [/u][/b]: m.thatchinamoorthi [b][u]Date of Birth and Age [/u][/b]: 06/03/1984, 29 years [b][u]Nationality [/u][/b]: Indian [b][u]Marital Status [/u][/b]: Married [b][u]ADDITIONAL QUALIFICATIONS AND TRAINING COURSES [/u][/b]:- DIPLOMA IN PETROLEUM REFINING ENGINEERING I have complete knowledge of the following production and composition of Sources, exploitation and composition of petroleum-refinery products and Test methods,astm distillation, Thermal and catalytic cracking ,vacuum Distillation, thermalreforming, wax, asphalts, and testing experience of Petroleum products like flashpoint, firepoint, cloudpoint, pourpoint, anilinepoint, dieselindex, smokepoint.etc. [b][u]PROFILE [/u][/b]: [b][u]Presently employed in [/u][/b]: TUTICORIN ALKALI CHEMICALS AND FERTILIZERS LIMITED. (GROUP OF COMPANY OF SPIC LTD) [b][u]Previously Employed in (41/2yrs) SOUTHERN PETRO CHEMICAL [/u][/b]: INDUSTRIES CORPORATION LTD (On deputation basis) Production Plant (Ammonia Operator) [b][u]Known areas in Ammonia Plant [/u][/b]: (i) COMPRESSOR HOUSE (ii) NAPTHA TANKFARM (iii) HYDROFINING –HYDRO DESULPHURIZATION (iv) STEAM NAPTHA REFORMING (v) SHIFT CONVERSION & METHANATION (vi) DCS (vii) AMMONIA IMPORTATION SYSTEM (viii) INERT GASPLANT [b][u]EXPERIENCE IN DETAIL [/u][/b]: [b][u]ABOUT THE ORGANISATION [/u][/b]: Southern Petrochemical Industries Corporation Ltd, short - named SPIC, is a giant petrochemical Complex in Southern part of India producing 1600 TPD of UREA, 1260 TPD of Ammonia and 1500 TPD of Di-Ammonium Phosphate (DA.P). This Complex also consists of process plant like Sulphuric Acid, Phosphoric Acid Aluminum Fluoride plant and utilities like Captive Power Plants ( capacity 22 MW ), Storage and handling facility of imported LPG(Capacity 8500 MT) and imported Ammonia (10000 MT ) etc. [b][u]ABOUT THE PLANT [/u][/b]: I am working as Field Operator for the past 41/2 years in the Naphtha based Ammonia Plant, is designed to produce Anhydrous Ammonia on total energy concept using Steam-Naphtha reforming process with the capacity of 1260 T/Day, in which I am having diversified experience in the following areas. TANK FARM The handling and storage facilities of naphtha and furnace oil are coming under this unit which consists of the following tanks. Capacity in KL 1. Two Raw Naphtha Tanks 8700 2. Two High Aromatic Naphtha Tanks 6250 3. One Sweet Naphtha Tank 8750 4. Two Furnace Oil Tanks 3800 Naphtha Tanks are having "Floating roof Pantoon Type with Neoprene Seal" Breathers, Roof drains are located in the roof. Foam pourer and Water sprayers are provided for Safety. [b][u]HYDRO DE-SULPHURISATION OF NAPHTHA SECTION [/u][/b]: This unit is an oil-processing Unit where the sulphur content is reduced from 1500 ppm to 0.5 ppm based on IIP-IFP Process. I have the operating experience of this unit, where we have two natural draft FIRED HEATERS fuelled by fuel gas and naphtha using 4 AIROIL burners, COMOX-ZnO catalyst reactors, Two reciprocating Hydrogen Compressors, Stripping Column and necessary pumps and heat exchangers. The desulphurised naphtha is called as sweet naphtha which stored in the respective tank for the supply to reforming section. [b][u]Fired heaters (Naphtha vaporizer) [/u][/b]: This vaporizer contains two natural draft fired heaters fuelled by 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 the radiation coils are measured. Each burner is fixed with an igniter for the light up. Remote fuel isolation valve is given for the safety measure. [b][u]Reactor [/u][/b]: The COMOX catalyst reactor is operated at 350ºC at 21 KSG pres. Over the COMOX CATALYST Alumina balls are packed to avoid the direct impingement of the gas over the naphtha feed and H2S is formed in this vessel. Six thermocouples were installed along the catalyst bed to monitor the bed temperatures. COMOX - ZnO reactor operates at 400ºC at KSC pressure. [b][u]Stripping column [/u][/b]: The Stripper is a separating column which strips out H2S which is in dissolved state in naphtha. It is having reboiler at the bottom and reflux unit with condenser at the top. It contains 30 ballast type single pass trays where feed enters at the 21st tray from the bottom. The sour gas at the top is used for firing in the fired burners, through pressure control valve. This stripping column operates at a pressure of 14.2 KSC. [b][u]CATALYTIC REFORMING UNIT [/u][/b]: This unit based on ICI-STEAMNAPHTHA REFORMING PROCESS Primary reformer unit is having 90 no of top fired burners and a furnace, 264 HP-NB-MICROALLOY TUBES, two sets of Induced and Forced draft fans and four no of fuel gas waste heat recovery boilers and super heaters. Vapour Naphtha is mixed with steam and enters at 457ºC to a Nickel Catalyst bed. Primary reformer outlet temperature is 765°C.The outlet gas contains CO, CO2, H2 H20 and CH4.Flare system is available. Routine observation of skin temperature, gun cleaning and explosive check is done here [b][u]SECONDARY REFORMING UNIT [/u][/b]: In Secondary Reforming CH4 content is reduced from 9.25% to 0.25% at the exit by burning process gas with process air. Other advantage is N2 required for synthesis section is introduced at this section. Catalyst for secondary reformer is of nickel high alumina and silica type (ICI 54.8). Gas at the exit is at 946°C and enters RGB where the heat energy available is used to generate 150 tones of 106-ksc steam. The exit gas is sent to high temperature shift converter. Compressor House [b][u]SYNTHESIS GAS COMPRESSOR [/u][/b]: Delivered Synthesis gas at 200 Ksc, to Ammonia Converter. It is a multistage centrifugal compressor and having three barrel (vertically split) machine with anti surge control system. [b][u]Driver [/u][/b]: Extraction cum condensing turbine powered by 106 ksc, steam At 475oC developing 19,035 KW at 10,309 RPM [b][u]Capacity [/u][/b]: 1, 30, 522 NM3 /hr [b][u]Make [/u][/b]: MITSUBISHI [b][u]Auxiliaries [/u][/b]: Lube oil and Seal oil system [b][u]PROCESS AIR COMPRESSOR [/u][/b]: It is a multistage centrifugal compressor driven by 12 KSC, condensing type turbine with anti-surge control system and delivered process air to secondary reformer. [b][u]Capacity [/u][/b]: 45,000 NM3 / hr [b][u]Make [/u][/b]: HITACHI [b][u]LOOP REFRIGERATION COMPRESSOR [/u][/b]: The Compressor is a single casing, two stage centrifugal machine driven by a 45 Ksc, condensing type turbine. This compressor handling Ammonia and contains compact seal oil and Surge control system. [b][u]Capacity [/u][/b]: 50,000 NM3 / hr INERT GAS PLANT We have produced N2 and cracked gas ( N2+H2) by cracking of ammonia [b][u]Capacity [/u][/b]: 950 NM3 of nitrogen, 1200nm3 of cracked gas. AMMONIA IMPORTATION SYSTEM We have received from AIT Ammonia temperature of -33cand stored in the Horton sphere 3.5Ksc and 0 oC [b][u]Capacity [/u][/b]: 3000MT [b][u]OPERATING EXPERIENCE [/u][/b]: ** Regular visual checkup of furnace for uniform firing, flame geometry, reformer tube conditions etc., and remedy action. ** Gun cleaning and catalyst reduction. ** I have known about Reformer, Catalyst Charging. ** Boiler feed water treatment, hydro test and Deaerator operation. ** Fired heater and furnace refractory curing. ** Multistage turbine driven mega capacity centrifugal compressor startup, shutdown, trouble shooting and antisurge control operation. ** Lube oil, seal Oil, and Sour oil system. ** Silica washing and Heat exchanger cleaning. ** Various start up & shutdown ** Inert gas plant operation ** Cooling tower operation UTILITIES; BOILERS [b][u]There are two boilers each having capacity [/u][/b]: 90TPH and 120TPH [b][u]Type [/u][/b]: vertical water tube two drum natural circulation oil fired boiler [b][u]Make; M/S thermax ltd, Pressure [/u][/b]: 106 KSC, temperature: 482 c ** Well experienced in the operation of High pressure boilers both in the Field and Control room. ** Well experienced in start up, shutdown, trip systems. WATER TREATMENT PLANT [b][u]Type [/u][/b]: Ion exchange process [b][u]Make [/u][/b]: Demineralised water: 6500 m3/day [b][u][/u][/b]: Polished water : 6500 m3/day [b][u][/u][/b]: Mixed bed design capacity: 12,600M3/hr ** Conversant with sand filter operation ** Production of soft water and demineralised water by ION EXCHANGE process. ** Conversant with above unit operation, regeneration of exhausted units etc. ** Water analysis ** Conversant with operation of resin organic fouling treatment. ** Conversant with operation of mixed bed units. PROCESS AIR COMPRESSOR & DRYING UNIT [b][u]Supplier; khosla-crepelle [/u][/b]: Capacity: 1085.7m3/hr, discharge pressure: 9ksc [b][u]Type [/u][/b]: horizontal balanced opposed non-lubricated double acting, double stage Reciprocating Compressor. ** Conversant with operation of Instrument air compressor ** Conversant with operation of Startup, shut down and trip systems. INSTRUMENT AIR DRYING UNIT [b][u]Make [/u][/b]: Indicon pvt ltd pressure: 9ksc [b][u]Capacity [/u][/b]: 1000m3/hr dew point: -40c [b][u]Dessicantype [/u][/b]: Heated activated alumina & silica gel absorbent dryer ** Conversant with operation of Instrument air drying unit. ** Conversant with trip systems & trouble shooting ** Conversant with startup & shut down of drying system ** Hydrogen gas compressor [b][u]** Type [/u][/b]: single stage, double acting reciprocating compressor [b][u]** Make[/u][/b]: peter brother hood ltd ,England, capacity : 5690 nm3/hr [b][u]** Max.pressure [/u][/b]:29.5 ksc , max temperature :80c Turbines [b][u]Type [/u][/b]: back pressure turbines and condensing turbines [b][u]Make[/u][/b]: Hitachi ** Conversant with operation of back pressure and condensing type turbines. [b][u]** Conversant with trip systems & trouble shooting of back pressure and condensing type turbines Coppus turbine[/u][/b]: single stage impulse type, fuel and process naphtha pumps are Back pressure turbines. [b][u]SAFETY AND FIRE FIGHTING [/u][/b]: Periodically we are given both theoretical and practical refresher training in safety and Fire Fighting by our Safety Department. We are given training in using various types of Fire Extinguishers and I am also conversant to use all types of Safety appliances including personal protective appliances. Mock drill will be conducted once in every month to check the emergency preparedness of the individuals. I have fully participated and handled them efficiently. [b][u]Special Skills [/u][/b]: - Good Training In Fire Fighting, Safety. Now Being an Active Safety Committee Member In Ammonia Plant. - Hands on Experience In SCBA, Gas Meters, LEL Meters, Oxygen Meters And Other Safety Apparatus. - Actively Involved In Emergency Mock Drills in Ammonia Plant. - Trained in First Aid by St John’s Ambulance Association. - I have experience in decoking operation of natural draft fired heater. - Actively involved in annual turn around in ammonia plant which undergoes major modifications. - I have experienced in decommissioning of floating roof naphtha tank. - Basic computer knowledge. - DCS Operation in Ammonia Plant [b][u]ACIEVEMENTS [/u][/b]: - Quickest startup one of the Team member - I got the second rank in our batch in spic [b][u]DECLARATION [/u][/b]: With an experience of about 41/2years in ammonia plant desulphurization and reforming plant and 31/2yrs experience in utility plants and having a good background of a degree in Bachelor of Science (Chemistry)aswellas diploma in petroleum refining engineering course I assure that I can operate any oil or gas refining plant. Also I assure that I am always conscious about the safety, environmental protection and productivity. Thanking you Yours faithfully (T.KUTTI DURAI)[/QUOTE]
